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Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

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Форма поиска

Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 1795. Отображено 100.
09-02-2012 дата публикации

Method and apparatus for compacting coal for a coal coking process

Номер: US20120030998A1
Автор: John Sanor, Michael P. Barkdoll, Richard C. Retort
Принадлежит: Sun Coke Co

Relatively high speed methods for increasing the bulk density of coal particles without impacting the coal particles and an apparatus for compacting coal for making metallurgical coke. The method includes depositing coal particles onto a charging plate external to a coking oven. The charging plate has side walls, and at least one movable end wall to provide an elongate bed of dry, uncompacted coal having an upper surface on the charging plate. The uncompacted coal is compacted by passing a vibratory cylindrical compactor along a length of the uncompacted coal for a number of passes sufficient to decrease a thickness of the bed of coal to less than about 80 percent of an original thickness of the uncompacted coal. The vibratory cylindrical compactor has a length to diameter ratio ranging from about 1.4:1 to about 2:1.

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Номер записи: 1
06-09-2012 дата публикации

Sealing device for a coking plant charged with a coal cake

Номер: US20120222950A1
Автор: Joachim Berger, Norbert Peter, Ralph Eiden
Принадлежит: Individual

Disclosed is a device for sealing an oven chamber of a coking plant, wherein a sealing frame can be placed against an inlet opening of the oven chamber during charging with a coal cake, from which, on oppositely disposed legs, sealing flaps protrude, which can be swiveled inward by the coal cake, the free end edges of the flaps grazing the coal cake.

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Номер записи: 2
25-04-2013 дата публикации

DROPLET GENERATION SYSTEM AND METHOD

Номер: US20130101500A1
Автор: Chang Han Kwon, Jang Hee Dong, Lim Kok Seng, Nikolov Jonian
Принадлежит:

A droplet generation system includes a first nozzle configuration structured to receive a liquid and a gas under pressure in a controllable feed ratio, and to merge the liquid and gas to form an intermediate stream that is a mixture of the gas and of a dispersed phase of the liquid. A second nozzle configuration is connected to receive the intermediate stream from the first nozzle configuration and has a valve mechanism with one or more controllable operating parameters to emit a stream of droplets of the liquid. The mean size of the droplets is dependent on the controllable feed ratio of the liquid and gas and the flow rate of the stream of droplets is dependent on the controllable operating parameter(s) of the valve mechanism. A corresponding method is disclosed, as is the application of the system and method to the production of nanoparticles in a thermochemical reactor. 1. A droplet generation system , comprising:a first nozzle configuration structured to receive a liquid and a gas under pressure in a controllable feed ratio, and to merge the liquid and gas to form an intermediate stream that is a mixture of the gas and of a dispersed phase of the liquid; anda second nozzle configuration that is connected to receive the intermediate stream from the first nozzle configuration and has a valve mechanism with one or more controllable operating parameters to emit a stream of droplets of said liquid;wherein the mean size of the droplets is dependent on said controllable feed ratio of the liquid and gas and the flow rate of the stream of droplets is dependent on the controllable operating parameter(s) of the valve mechanism.2. The system according to wherein the controllable operating parameter of the valve mechanism is its duty cycle.3. The system according to wherein the controllable operating parameter of the valve mechanism is its frequency of opening and the period for which it is open.4. The system according to wherein the first nozzle configuration includes a ...

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Номер записи: 3
20-06-2013 дата публикации

COKER INLET DESIGN TO MINIMIZE EFFECTS OF IMPINGEMENT

Номер: US20130153466A1
Автор: AXNESS Jay T., GANDHI Ramesh, MOLONEY Mitchell J., Nadarajah Chithranjan, SINCLAIR David S.
Принадлежит: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Coke drum assembly is provided with a vessel having a body portion defining an interior, a central axis, and having a lower portion including a sidewall, and at least one feed inlet coupled with the lower portion in fluid communication with the interior of the vessel. The at least one feed inlet is directed toward the central axis of the vessel, and angled upwardly at a feed inlet angle relative to the central axis. At a location opposite the feed inlet, the side wall of the lower portion is angled upwardly at an opposing wall angle relative to the central axis, wherein the feed inlet angle is less than or equal to the opposing wall angle. Method also is provided for delayed coking using the coke drum assembly disclosed herein. 2. The coke drum assembly of claim 1 , wherein the feed inlet angle is approximately equal to the opposing wall angle.3. The coke drum assembly of claim 1 , wherein the opposing wall angle is equal to or greater than about 45° relative to the central axis and the feed inlet angle is equal to or less than about 45° relative to the central axis of the vessel.4. The coke drum assembly of claim 1 , wherein the at least one feed inlet includes at least two feed inlets evenly spaced about the lower portion around the central axis of the vessel.5. The coke drum assembly of claim 4 , wherein the at least two feed inlets are generally directed toward a common focal point in the interior of the vessel.6. The coke drum assembly of claim 5 , wherein the common focal point is located along the central axis of the vessel.7. The coke drum assembly of claim 1 , further comprising a feed pipe system in fluid communication with the at least one feed inlet.8. The coke drum assembly of claim 8 , wherein the at least one feed inlet includes at least two feed inlets spaced about the lower portion of the vessel claim 8 , the feed pipe system including a primary feed pipe and a plurality of branch feed pipes extending from the primary feed pipe claim 8 , each branch ...

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Номер записи: 4
10-10-2013 дата публикации

PROCESS FOR PRODUCTION OF HYDROCARBON CHEMICALS FROM CRUDE OIL

Номер: US20130267745A1
Автор: Petzny Wilfried J., Schrod Heinrich Manfred
Принадлежит: SAUDI BASIC INDUSTRIES CORPORATION

An integrated process comprising to convert crude oil, comprising: converting crude oil () in a feed preparation facility () by separating the crude oil to a gas fraction (), liquid fraction (), and first residuum fraction in an atmospheric distillation unit (); separating the 1residuum to a vacuum gas oil fraction () and a second residuum () in a vacuum distillation unit (); converting the vacuum gas oil fraction to a CU gas fraction (), a CU liquid fraction (), and an CU higher boiling fraction () in a cracking unit (); and processing the second residuum fraction to DCU gas oil/lighter fraction () in a coking unit (); and steam cracking at least one of the gas fraction (), liquid fraction (), CU gas fraction (), and DCU gas oil/lighter fraction () to the hydrocarbon products (). 1. An integrated process comprising to convert crude oil into fractions suitable for conversion to chemicals , comprising:{'b': 10', '800, 'claim-text': [{'b': 101', '102', '100, 'separating the crude oil to a gas fraction (), liquid fraction (), and first residuum fraction in an atmospheric distillation unit ();'}, {'sup': 'st', 'b': 202', '201', '200, 'separating the 1residuum to a vacuum gas oil fraction () and a second residuum () in a vacuum distillation unit ();'}, {'b': 301', '401', '302', '303', '402', '300', '400, 'converting the vacuum gas oil fraction to a CU gas fraction (,), a CU liquid fraction (), and an CU higher boiling fraction (,) in a cracking unit (,); and'}, {'b': 501', '502', '500, 'processing the second residuum fraction to DCU gas oil/lighter fraction () and coke () in a coking unit (); and'}], 'converting crude oil () in a feed preparation facility () by'}{'b': 800', '920', '900, 'claim-text': {'b': 101', '102', '301', '401', '501, 'steam cracking at least one of the gas fraction (), liquid fraction (), CU gas fraction (,), and DCU gas oil/lighter fraction () to hydrocarbon products.'}, 'converting feedstock products from the feed preparation facility () into ...

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Номер записи: 5
24-10-2013 дата публикации

METHOD FOR PRODUCING A COKING ADDITIVE BY DELAYED COKING

Номер: US20130276587A1
Автор: "Sukhov Sergei Vitalevich", "Valyavin Konstantin Gennadevich", Bidilo Igor Viktorovich, Mamaev Mikhail Vladimirovich, Stukov Mikhail Ivanovich, Valyavin Gennady Georgirvich, Vetoshkin Nikolai Ivanovich, Zagainov Vladimir Semenovich, Zaporin Victor Pavlovich
Принадлежит:

This invention relates to the field of oil refining and, in particular, to a delayed coking process that produces coke with a volatile substances content of 15-25% for use as a coking additive in a coal coking charge in the production of metallurgical coke. The invention is directed towards increasing the content of volatile substances in coke and increasing the efficiency of a plant. The method comprises preheating a primary raw material, mixing the latter with recycle in a tank in order to form a secondary raw material, heating the secondary raw material to 455-470° C. and supplying the latter to a coking chamber, and coking to form a coking additive. It is expedient to feed an antifoaming additive into the coking chamber 3-5 hours before coking is finished. It is preferable to feed in the antifoaming addition agent at two-four points around the perimeter of the coking chamber. 13-. (canceled)4. A method of producing a coking additive in delayed coking , comprising:heating a primary charge to 270-330° C.;mixing the primary charge with a recirculate in a tank to form a secondary charge;heating the secondary charge and introducing it into a coking chamber; andcoking to form a target product;wherein the secondary charge is introduced into the coking chamber at 455-470° C.5. The method according to claim 4 , further comprising introducing an anti-foaming dope into the coke chamber 3-5 hours before the end of coking.6. The method according to claim 5 , wherein the anti-foaming dope is introduced into 2-4 areas around a perimeter of the coking chamber. This invention relates to oil refining, in particular to delayed coking that produces coke containing 15-25% of volatiles substances, which can be used as a coking additive in a coal coking charge for metallurgical coke production.Oil coke with more than 14% but less than 25% volatiles is capable not only of replacing the K-brand (coking) coal, which is in short supply, in coal coking charges, but also of improving the ...

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Номер записи: 6
21-11-2013 дата публикации

Apparatus and Method for Nanoflow Liquid Jet and Serial Femtosecond X-ray Protein Crystallography

Номер: US20130308756A1
Автор: Bogan Michael J., Laksmono Hartawan, Sierra Raymond G.
Принадлежит: THE BOARD OF TRUSTEES OF THE LELAND STANFORD JUNIOR UNIVERSITY

Techniques for nanoflow serial femtosecond x-ray protein crystallography include providing a sample fluid by mixing a plurality of a first target of interest with a carrier fluid and injecting the sample fluid into a vacuum chamber at a rate less than about 4 microliters per minute. In some embodiments, the carrier fluid has a viscosity greater than about 3 centipoise. 1. A method comprising:providing a sample fluid by mixing a plurality of a first target of interest with a carrier fluid; andinjecting the sample fluid into a vacuum chamber at a rate less than about 4 microliters per minute.2. A method as recited in claim 1 , wherein injecting the sample fluid into the vacuum chamber further comprises injecting the sample fluid into the vacuum chamber at a rate less than about 1 microliters per minute.3. A method as recited in claim 1 , wherein providing the sample fluid further comprises providing the sample fluid by mixing a plurality of nanoscale crystals of the first target of interest with the carrier fluid.4. A method as recited in claim 3 , wherein the nanoscale crystals are each smaller than about 500 nanometers in a largest dimension.5. A method as recited in claim 1 , wherein:the carrier fluid is electrically conductive; andinjecting the sample fluid into the vacuum chamber further comprises injecting the sample fluid into the vacuum chamber by applying a first voltage to the sample fluid and a different second voltage to a counter electrode in the vacuum chamber.6. A method as recited in claim 5 , wherein:the counter electrode has a shape that is axially symmetric and has a first end closest to an axis of symmetry and a second edge farthest from the axis; andthe counter electrode is disposed in the vacuum chamber with the axis aligned with the flow of the sample fluid in the vacuum chamber and with the first edge closer than the second edge to an injection point where the sample fluid is injected into the vacuum chamber.7. A method as recited in claim 1 , ...

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Номер записи: 7
26-12-2013 дата публикации

Efficient Method for Improved Coker Gas Oil Quality

Номер: US20130341248A1
Автор: John D. Ward, Kevin Sitton, Linda M. Strassle
Принадлежит: Bechtel Hydrocarbon Technology Solutions Inc

An efficient delayed coking process improvement for producing heavy coker gas oil of sufficient quality to be used as hydrocracker feedstock.

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Номер записи: 8
20-02-2014 дата публикации

METHOD AND APPARATUS FOR REDUCING FILLING GAS EMISSIONS WHEN CHARGING OVEN CHAMBERS OF A COKING-OVEN BATTERY WTIH SLUGS OF COMPRESSED CARBON

Номер: US20140048403A1
Автор: Reinke Martin, Thielert Holger, Worberg Rainer
Принадлежит:

The invention relates to a method of reducing emissions of byproduct gas when charging oven chambers of a battery of coking ovens, on the proviso that the oven chamber () to be charged is opened on the machine side (MS) of the battery of coking ovens, and a block of compressed coal () is introduced into the opened oven chamber (). Byproduct gases released during introduction of the block of compressed coal () into the hot oven chamber (), are discharged through a byproduct-gas manifold () attached to the oven chamber () and are then preferably freed of dust and incinerated. Crude gases formed in the closed oven chambers during coking are discharged through a crude-gas manifold () attached to the oven chambers () and are passed on for treatment by at least one gas scrubber. According to the invention, conduits connecting the crude-gas manifold () and the byproduct-gas manifold () to the oven chambers () are alternately opened and closed such that the byproduct gases that form during the charging of the oven chambers () are admitted only into the byproduct-gas manifold (), and that the crude gases that form during coking in the closed oven chambers are fed only into the crude-gas manifold (). 1. A method of reducing byproduct-gas emissions when charging oven chambers of a battery of coke ovens with compressed-coal blocks , the method comprising the steps of:opening the oven chamber to be charged on the machine side of the battery of coke ovens and introducing a block of compressed coal into the opened oven chamber such that byproduct gases are released, the block is coked, and crude gases are formed,conducting the byproduct gases released during the introduction of the block of compressed coal into the hot oven chamber conducted to a byproduct gas manifold connected to the open chamber,conducting crude gases formed during a the coking process inside the closed oven chambers by a crude-gas manifold to the oven chambers to a gas-treatment system that has at least a gas ...

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Номер записи: 9
20-02-2014 дата публикации

Method and apparatus for volatile matter sharing in stamp-charged coke ovens

Номер: US20140048404A1
Автор: John F. Quanci, Vince G. Reiling
Принадлежит: SunCoke Technology and Development LLC

A volatile matter sharing system includes a first stamp-charged coke oven, a second stamp-charged coke oven, a tunnel fluidly connecting the first stamp-charged coke oven to the second stamp-charged coke oven, and a control valve positioned in the tunnel for controlling fluid flow between the first stamp-charged coke oven and the second stamp-charged coke oven.

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Номер записи: 10
10-04-2014 дата публикации

Center feed system employing removable inserts in a retractable injection nozzle

Номер: US20140097268A1
Автор: Gary Larsen, Kenneth Krause, Ruben F. Lah
Принадлежит: Individual

The present invention extends to a center feed system that allows residual byproduct to be injected into a vessel from within the center of the vessel. The center feed system can include an inlet sleeve that is attached to the vessel and a retractable injection nozzle that extends into the vessel to inject residual byproduct into the vessel and that retracts into the inlet sleeve after injecting the residual byproduct. A retractable injection nozzle in accordance with one or more embodiments of the invention may include one or more openings that each includes an insert that can be removed from the opening. The inserts can therefore be replaced to customize the functionality of the nozzle or to replace the inserts when they have become worn.

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Номер записи: 11
07-01-2016 дата публикации

APPARATUSES FOR DISTRIBUTING FLUIDS IN FLUIDIZED BED REACTORS

Номер: US20160001245A1
Автор: Sprague Robert T.
Принадлежит:

A fluid distribution apparatus is disposed in a fluidized bed reactor and includes a distributor pipe configured to carry a fluid and a centerpipe fluidly connected to the distributor pipe and enclosing an annular space for receiving the fluid from the distributor pipe. The annular space is defined by an interior radius including a cylindrical plug disposed concentrically within the centerpipe, an exterior radius including the centerpipe, an upper end including an upper circular plate, and a lower end including a lower circular plate. The fluid distribution apparatus further includes a plurality of inlet nozzles fluidly connected to the annular space and disposed through the centerpipe for distributing the fluid from the annular space to a bed of the fluidized bed reactor. 1. A fluid distribution apparatus disposed in a fluidized bed reactor comprising:a distributor pipe configured to carry a fluid;a centerpipe fluidly connected to the distributor pipe and enclosing a conical distributor comprising a conical shape for receiving the fluid from the distributor pipe, wherein the conical distributor is defined by an exterior radius comprising the centerpipe, an upper end comprising an upper angled, circular plate, and a lower end comprising a lower circular plate; anda plurality of inlet nozzles fluidly connected to the conical and disposed through the centerpipe for distributing the fluid from the conical distributor to a bed of the fluidized bed reactor.2. The apparatus of claim 1 , wherein each of the plurality of inlet nozzles comprises a reducer portion that is proximate to a connection point between the centerpipe and each such inlet nozzle.3. The apparatus of claim 1 , wherein the distributor pipe comprises a reducer portion that is proximate to a connection point between the centerpipe and the distributor pipe.4. The apparatus of claim 3 , wherein the reducer portion is an eccentric increase in the diameter of the distributor pipe.5. The apparatus of claim 1 , ...

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Номер записи: 12
06-01-2022 дата публикации

Multiport Valve

Номер: US20220003327A1
Автор: Anderson Alfred Lewis, Inman Phillip M., Kassab Asmaa Sadek
Принадлежит:

Multiport valve with outlets transverse to the inlet useful as a coker switch valve. A sealed lower sleeve assembly provides semi-trunnion ball support. An upper part of the outlet seat recesses is formed in the bonnet, and a lower part in the valve body, which together bias a resilient member to load the seats, independently of end connections. Before bonnet assembly, when the ball is rotated to face a body outlet, there is sufficient space in the seat recesses to insert the seat, slide the seat onto the ball, and then insert the resilient member. When all the seats and resilient members are in place, engagement of the bonnet biases the upper part of the resilient members to load the seat. In valve operation, an enlarged ball outlet bore can straddle two outlet ports and maintain process media flow during switching. Also, methods of assembling, operating, and servicing the valve. 1. A multiport valve , comprising:a valve body comprising a body inlet coaxial to a first axis and a plurality of body outlets each oriented at an angle transverse to the first axis;a spherical flow control element disposed within a cavity of the valve body in a sealed semi-trunnion arrangement to support the spherical flow control element;wherein the valve body comprises a lower main body sealingly engaged with an upper bonnet;a lower part of a respective outlet seat recess formed in the lower main body of the valve;an upper part of the respective outlet seat recess formed in the bonnet;wherein the bonnet and body together bias a respective resilient member to load the seat, maintaining alignment of the ball and equalizing stresses, independently of end connection loads.2. The multiport valve of claim 1 , wherein the resilient member comprises a Belleville resilient member.3. The multiport valve of claim 1 , wherein an outlet of the spherical flow control element has a larger bore than an inlet of the spherical flow control element.4. The multiport valve of claim 1 , wherein the spherical ...

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Номер записи: 13
02-01-2020 дата публикации

Petroleum Coking Additive

Номер: US20200002618A1
Автор: LYSENKO Aleksei V., MAMAEV Mikhail V., STUKOV Mikhail I., ZAPORIN Viktor P.
Принадлежит:

The quality of coke is improved by increasing the coking properties of a component of a coking feedstock (a coking additive) and by ensuring stability of the coking properties of a component when the coking additive constitutes up to 99% of the total volume of the coking feedstock. The result is an increase in the stability of a coking additive and in the coking properties of said coking additive. It is achieved by a petroleum coking additive consisting of a product of the delayed low temperature carbonization of heavy petroleum residues at temperatures of up to 500° C., said product being characterized by a 14 to 28% volatile substance content, the product of the delayed low temperature carbonization of heavy petroleum residues obtained at a recycle ratio of from 1.05 to 1.2 in the coking chamber is characterized by coking properties of not less than G on the Gray-King scale. 1. A petroleum coking additive comprising a product of a delayed low temperature carbonization of heavy petroleum residues at temperatures of up to 500° C., the product having a content of volatile substances from 14% to 28%, the product being obtained in the coking chamber at a recycle ratio from 1.05 to 1.20 and having a coking property of no less than G on a Gray-King scale. This Application is a Continuation Application of International Application PCT/RU2017/000020, filed on Jan. 18, 2017, which in turn claims priority to Russian Patent Applications RU2016143290, filed Nov. 2, 2016, both of which are incorporated herein by reference in their entirety.The invention relates to the by-product coke industry, specifically, to technologies of producing of furnace coke from feedstock which includes petrochemical products; the invention can be used in metallurgy, in particular, at by-product coke industry plants.From RU Patent No. 2400518, a method of producing a coking feedstock by delayed carbonisation is known which includes feeding of a heated stock into a coking chamber, coking of the ...

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Номер записи: 14
20-01-2022 дата публикации

Reactor for a Chemical Reaction and Method for Controlling the Chemical Reaction

Номер: US20220016588A1
Автор: Anton Ledwon, Waldemar Lewtschenko
Принадлежит: Heion GmbH

The invention relates to a reactor (1) for a chemical reaction, comprising a housing (10) and a reaction chamber (3), a nozzle member (30) with an inlet (32) for letting at least one reactant flow into the reaction chamber (3), wherein the nozzle member (30) is mounted in a movable manner relative to the housing (10), a sensor device (80) by means of which at least one measuring quantity can be detected during the chemical reaction, and an adjusting device (50) by means of which at least one mounting parameter influencing the movement of the nozzle member (30) can be adjusted, a control unit (70) configured for receiving from the sensor device (80) a measurement signal of the sensor device (80) based on the measuring quantity and generating a control signal for the adjusting device (50) depending on the measurement signal. The invention further relates to a method for controlling the chemical reaction.

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Номер записи: 15
14-01-2021 дата публикации

CATALYTIC CRACKING SYSTEM WITH BIO-OIL PROCESSING

Номер: US20210008517A1
Автор: Boatman Digna, Gbordzoe Eusebius Anku, Patel Bandish
Принадлежит:

A catalytic cracking system in which liquid hydrocarbon and bio-oil are directed into a reactor riser of a fluid catalytic cracking unit by separate feed spray nozzle assemblies. To protect liquid bio-oil directed through the liquid bio-oil feed nozzle assembly from high temperature degradation, an insulating layer is provided between a central bio-oil feed tube in a concentrically surrounding atomizing gas passageway. Cooling channels also may be provided in the spray tip of the bio-oil feed nozzle assembly. 1. A catalytic cracking system comprising:a catalytic cracking reactor;a riser communicating upwardly to said catalytic cracking reactor;a supply of a liquid hydrocarbon;a first feed spray nozzle assembly mounted in and extending through a wall of said riser and having a spray tip at a downstream end, said first feed spray nozzle assembly having an upstream end coupled to a supply of liquid hydrocarbon and a supply of atomizing gas such that liquid hydrocarbon directed through said first feed spray nozzle assembly is atomized by the atomizing gas and discharged from said spray tip into riser as a finely atomized liquid hydrocarbon spray;a second feed spray nozzle assembly comprising an elongated nozzle body mounted in and extending through the wall of said catalytic cracking riser and having a spray tip at a downstream end;a bio-oil feed tube supported within the elongated nozzle body having an upstream end connected to a supply of a liquid bio-oil for directing liquid bio-oil through bio-oil feed tube to said spray tip;said elongated nozzle body defining an annular atomizing gas passage in surrounding relation to said bio-oil feed tube; said annular atomizing gas passage being connected to a supply of atomizing gas for direction through said annular atomizing gas passage for atomizing liquid bio-oil discharging from the liquid feed tube and spray tip into a fine particle liquid bio-oil spray; andan annular insulating layer between said bio-oil feed tube and ...

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Номер записи: 16
14-01-2021 дата публикации

METHOD AND APPARATUS FOR PROCESSING OF MATERIALS USING HIGH-TEMPERATURE TORCH

Номер: US20210009412A1
Автор: DiNicolantonio Arthur R., Howard Erik M., Knight Clifton T., Poteet Darrell, Stell Richard C.
Принадлежит:

A method and apparatus for reforming carbonaceous material into syngas containing hydrogen and CO gases is disclosed. In one embodiment, a hydrogen rich torch reactor is provided for defining a reaction zone proximate to torch flame. One input of the reactor receives input material to be processed. Further inputs may be provided, such as for example to introduce steam and/or gases such as methane, oxygen, hydrogen, or the like. 1. An apparatus for processing input material , comprising:a reactor vessel defining a combustion zone; the reactor vessel further having at least one input port for receiving the input feedstock, the input feedstock being directed proximally to the at least one flame;', 'the reactor vessel further having an output for discharging a primary reactor output stream;', 'at least one cooler coupled to receive the primary reactor output stream and operable to cool the primary reactor output stream and generate a secondary output stream;, 'the reactor vessel having at least one input for a combustible torch fuel to at least one torch nozzle, the at least one torch nozzle being adapted to generate at least one flame within said reactor;'}a scrubber, coupled to receive the secondary output stream from the cooler/separator, the scrubber being operable to further extract at least one gas from the secondary output stream.2. An apparatus in accordance with claim 1 , wherein the reactor vessel further has an input for receiving a supply of steam.3. An apparatus in accordance with claim 1 , wherein the combustible torch fuel comprises hydrogen.4. An apparatus in accordance with claim 2 , wherein the combustible torch fuel further comprises methane.5. An apparatus in accordance with claim 1 , wherein the combustible torch fuel is combined with oxygen.6. An apparatus in accordance with claim 1 , wherein the combustible torch fuel comprises acetylene.7. An apparatus in accordance with claim 1 , wherein the reactor vessel further having at least one input port ...

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Номер записи: 17
21-01-2021 дата публикации

DELAYED COKER CONTROLLED DISPERSION MODULE

Номер: US20210017451A1
Автор: Perilla Miguel A.
Принадлежит:

A controlled dispersion module includes a distal end coupled to an effluent feed. A proximal end having at least one baffle is disposed within the controlled dispersion module. The proximal end is fluidly coupled to the coke drum. In various embodiments, the proximal end is curved to match a curvature of the coke drum. In various embodiments, the at least one baffle includes a plurality of baffles. 1. A controlled dispersion module for use with a coke drum , the controlled dispersion module comprising:a distal end coupled to an effluent feed;a proximal end having at least one wedge disposed therein, the proximal end being fluidly coupled to the coke drum, the proximal end having a flared profile relative to the distal end; andwherein the flared profile decreases a velocity of an effluent within the controlled dispersion module and facilitates vectoring of the effluent by the at least one wedge.2. The controlled dispersion module of claim 1 , wherein the proximal end is curved to match a curvature of the coke drum.3. The controlled dispersion module of claim 1 , wherein the at least one wedge comprises a plurality of baffles.4. The controlled dispersion module of claim 3 , wherein the plurality of baffles comprise:a first inboard baffle;a first outboard baffle;a second inboard baffle; anda second outboard baffle.5. The controlled dispersion module of claim 4 , wherein the first inboard baffle and the second inboard baffle are arranged about a center line of the controlled dispersion module.6. The controlled dispersion module of claim 5 , wherein the first outboard baffle and the second outboard baffle are arranged generally parallel to the first inboard baffle and the second inboard baffle claim 5 , respectively.7. The controlled dispersion module of claim 5 , wherein the first inboard baffle claim 5 , the second inboard baffle claim 5 , the first outboard baffle claim 5 , and the second outboard baffle direct effluent towards a periphery of the coke drum.8. The ...

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Номер записи: 18
02-02-2017 дата публикации

INTEGRATED EBULLATED-BED HYDROPROCESSING, FIXED BED HYDROPROCESSING AND COKING PROCESS FOR WHOLE CRUDE OIL CONVERSION INTO HYDROTREATED DISTILLATES AND PETROLEUM GREEN COKE

Номер: US20170029724A1
Автор: KOSEOGLU Omer Refa
Принадлежит:

A system and process for upgrading a whole crude oil feed in an integrated ebullated-bed and hydrotreater is provided in which the whole crude oil is flashed into a flashed straight run distillates fraction and an atmospheric residue fraction. The atmospheric residue fraction is hydroprocessed in an ebullated-bed reaction zone, while the flashed straight run distillates fraction and the products fraction produced from the ebullated-bed reaction zone are hydrotreated in a fixed-bed reaction zone. The unconverted residue fraction from the ebullated-bed reaction zone is processed in a coker unit to produce high quality petroleum green coke. 1. A method for upgrading a crude oil feed to reduce the content of undesired hetero atom compounds containing metals , sulfur and nitrogen , the method comprising:a. heating the crude oil feed and flashing the heated crude oil feed to produce a flashed straight run distillate fraction and an atmospheric residue fraction;b. hydroprocessing the atmospheric residue fraction in an ebullated-bed reaction zone in the presence of hydrogen and an ebullated-bed reactor catalyst to produce a desulfurized and demetallized ebullated-bed reactor effluent stream, wherein make-up hydrogen is introduced as needed;c. separating the ebullated-bed reactor effluent stream into a hydroprocessed products stream containing hydrogen, a recycle oil stream and an unconverted residue stream;d. hydrotreating in a fixed bed hydroprocessing zone a combined stream of the hydroprocessed products stream containing hydrogen and the flashed straight run distillate fraction in the presence of a hydrotreating catalyst in a hydrotreater to produce a hydrotreated effluent, wherein hydrogen from the hydroprocessed products stream forms at least a portion of the requisite hydrogen for hydrotreating reactions;e. separating the hydrotreated effluents to produce a light gas stream and a hydrotreated distillate stream;f. purifying the light gas stream and recycling the ...

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Номер записи: 19
30-01-2020 дата публикации

METHOD AND DEVICE FOR THE HYDROLYSIS OF A COMPOUND

Номер: US20200030769A1
Автор: Hofmann Albert, Klose Göran, Maier Helene
Принадлежит:

The subject matter of the invention is a device for the hydrolysis of at least one compound. The device comprises a first cylindrical section having a diameter D, a central duct, an outer duct which surrounds the central duct coaxially, an outlet having a diameter D, and a second section which tapers towards the outlet and into which the ducts issue. The second section has, in cross-section along a longitudinal axis Aof the device, a profile which is described by two radii R1 and R2 which merge tangentially into each other, where 0.2 Подробнее

Номер записи: 20
08-02-2018 дата публикации

METHOD AND SYSTEM FOR UTILIZING MATERIALS OF DIFFERING THERMAL PROPERTIES TO INCREASE FURNACE RUN LENGTH

Номер: US20180037821A1
Автор: Myszka Ronald T., Young Bruce T.
Принадлежит: AMEC FOSTER WHEELER USA CORPORATION

In one aspect, the present invention relates to a furnace having a heated portion arranged adjacent to an unheated portion. A plurality of straight tubes are formed of a first material and are at least partially disposed in the heated portion. A plurality of return bends are operatively coupled to the plurality of straight tubes. The plurality of return bends are formed of a second material and are at least partially disposed in the unheated portion. The first material exhibits a maximum temperature greater than the second material thereby facilitating increased run time of the furnace. The second material exhibits wear-resistance properties greater than the first material thereby facilitating wear-resistance of the furnace. 1. A method of manufacturing a heater process coil , the method comprising:forming a plurality of straight tubes from a first material;forming a plurality of return bends from a second material;joining the plurality of straight tubes to the plurality of return bends;orienting the plurality of straight tubes and the plurality of return bends within a furnace such that the plurality of straight tubes are at least partially disposed within a heated portion and the plurality of plug headers are at least partially disposed within an unheated portion;wherein the first material exhibits a maximum temperature greater than the second material thereby facilitating increased run time of the furnace; andwherein the second material exhibits wear-resistance properties greater than the first material facilitating wear resistance of the furnace.2. The method of claim 1 , comprising forming a plurality of plug headers from the second material.3. The method of claim 1 , wherein the joining comprises joining opposite ends of the plurality of straight tubes to the plurality of return bends.4. The method of claim 1 , wherein the forming the plurality of return bends comprises forming a plurality of 180 degree bends.5. The method of claim 1 , wherein the first ...

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Номер записи: 21
14-02-2019 дата публикации

Delayed coke drum quench systems and methods having reduced atmospheric emissions

Номер: US20190048265A1
Автор: John D. Ward, Richard Heniford, Scott Alexander
Принадлежит: Bechtel Hydrocarbon Technology Solutions Inc

Systems and methods for reducing atmospheric emission of hydrocarbon vapors by flashing off hydrocarbon vapors in an overflow drum where the pressure is ultimately reduced to 0 psig and then flashing off any remaining hydrocarbon vapors in an overflow tank wherein the pressure in the overflow tank is reduced to 0 psig by an overflow ejector.

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Номер записи: 22
10-03-2022 дата публикации

INJECTION DEVICE FOR DISCHARGING A GAS, PROCESS GAS SYSTEM FOR SUPPLYING A PROCESS GAS, AND DEVICE AND METHOD FOR THE THERMAL OR THERMO-CHEMICAL TREATMENT OF MATERIAL

Номер: US20220072496A1
Автор: Esfehanian Arian, Hipp Daniel
Принадлежит:

Injection device () for discharging a gas (), in particular a process gas (), onto a material (), in particular onto a battery cathode material () that is to be calcined, having at least one inlet () through which the gas () can be supplied to the injection device (), and at least one outlet () through which the gas () can be discharged from the injection device (), the inlet and outlet being connected to one another by a flow path () for the gas (). According to the invention, the flow path () has a heat exchanger () with a heat exchanger housing () which is accessible from the outside for an ambient atmosphere () and in which a duct arrangement () is integrated. The duct arrangement () comprises a first flow duct () and a second flow duct () between which there is formed a redirection region () such that the gas () can flow through the first and second flow duct () in different main flow directions. The invention further relates to a process gas system () for supplying a gas () and to a device () and a method for the thermal or thermo-chemical treatment of material. 1. An injection device for supplying a gas to a material to be calcined , the injection device comprising ,a) at least one inlet through which the gas can be fed to the injection device and at least one outlet through which the gas can be supplied from the injection device, which are connected to one another by a flow path for the gas;whereinb) the flow path has a heat exchanger having a heat exchanger housing which is accessible to an ambient atmosphere from the outside and in which a channel arrangement is accommodated; andc) the channel arrangement comprises a first flow channel and a second flow channel between which a diversion region is formed in such a way that the gas can flow with different main flow directions through the first and second flow channels.2. The injection device of claim 1 , wherein the channel arrangement has a third flow channel claim 1 , with a second diversion region being ...

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Номер записи: 23
03-03-2016 дата публикации

COKE OVEN CHARGING SYSTEM

Номер: US20160060534A1
Автор: Ball Mark Anthony, Choi Chun Wai, Mounts Dexter Junior, Quanci John Francis, Sparling Danny E.
Принадлежит:

The present technology is generally directed to coal charging systems used with coke ovens. In some embodiments, a coal charging system includes a charging head having opposing wings that extend outwardly from the charging head, leaving an open pathway through which coal may be directed toward side edges of the coal bed. In other embodiments, an extrusion plate is positioned on a rearward face of the charging head and oriented to engage and compress coal as the coal is charged along a length of the coking oven. In other embodiments, charging plates extend outwardly from inward faces of opposing wings. 1. A coal charging system , the system comprising:an elongated charging frame having a distal end portion, proximal end portion, and opposite sides; anda charging head operatively coupled with the distal end portion of the elongated charging frame; the charging head including a planar body residing within a charging head plane and having an upper edge portion, lower edge portion, opposite side portions, a front face, and a rearward face;the charging head further including a pair of opposing wings having free end portions positioned in a spaced-apart relationship from the charging head, defining open spaces that extend from inner faces of the opposing wings through the charging head plane.2. The coal charging system of wherein the opposing wings are positioned to extend forwardly from the charging head plane.3. The coal charging system of wherein the opposing wings are positioned to extend rearwardly from the charging head plane.4. The coal charging system of further comprising:a pair of second opposing wings having free end portions positioned in a spaced-apart relationship from the charging head, defining open spaces that extend from inner faces of the opposing wings through the charging head plane;the second opposing wings extending from the charging head in a direction opposite to a direction in which the other opposing wings extend from the charging head.5. The ...

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Номер записи: 24
20-02-2020 дата публикации

FLUID DISTRIBUTION SYSTEM FOR A REACTOR VESSEL

Номер: US20200055008A1
Автор: Maier William C., Wisler Scott David
Принадлежит:

A fluid distribution system () is provided for a reactor vessel () defining a reaction chamber (). The fluid distribution system () may include a radial distribution component () positionable within the reaction chamber () and adjacent a vessel inlet () at an end portion of the reactor vessel (). The radial distribution component () may include one or more annular distribution conduits () configured to receive a fluid mixture provided to the reactor vessel (). The fluid distribution system () may also include an axial distribution component () positionable within the reaction chamber () to extend from the radial distribution component () along a longitudinal axis of the reactor vessel (). The axial distribution component () may include a plurality of helical conduits () fluidly coupled with the one or more annular distribution conduits () and configured to receive the fluid mixture from the one or more annular distribution conduits () and to disperse the fuel mixture uniformly within the reaction chamber (). 1208200202. A fluid distribution system () for a reactor vessel () defining a reaction chamber () , comprising:{'b': 224', '202', '212', '200', '224, 'claim-text': [{'b': 228', '212', '200, 'a fluid distribution system inlet () configured to couple with the vessel inlet () and receive a fluid mixture provided to the reactor vessel (); and'}, {'b': 230', '228', '208, 'one or more annular distribution conduits () fluidly coupled with the fluid distribution system inlet () and configured to receive the fluid mixture provided to the fluid distribution system (); and'}], 'a radial distribution component () positionable within the reaction chamber () and adjacent a vessel inlet () at an end portion of the reactor vessel (), the radial distribution component () comprising'}{'b': 226', '202', '224', '200', '226, 'claim-text': {'b': 236', '230', '230', '202, 'a plurality of helical conduits () fluidly coupled with the one or more annular distribution conduits () and ...

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Номер записи: 25
10-03-2016 дата публикации

GAS DISTRIBUTOR FOR A SIEMENS REACTOR

Номер: US20160067663A1
Автор: KUTZA Christian, POPP Friedrich, ROECKL Martin, WEISS Tobias
Принадлежит:

A gas distribution system for a polysilicon deposition reactor eliminates or mitigates the problems associated with prior art distribution systems employs at least two segments which are gas-tightly connected to one another by readily detachable fasteners, with at least one gas inlet opening and one gas outlet opening, the gas distributor of the system being mounted by readily detachable fasteners to the polysilicon reactor. 112-. (canceled)13. A gas distributor in which gases can be transported , comprising at least two segments which are gas-tightly connected to one another by detachable fasteners , and comprising at least one gas inlet opening and at least one gas outlet opening , wherein the gas distributor is mounted by means of detachable fasteners to a reactor for deposition of polycrystalline silicon , whereina) the at least one gas outlet opening of the gas distributor is communicatingly connected to at least one gas inlet opening of the reactor, and/or wherein the at least one gas inlet opening of the gas distributor is communicatingly connected to at least one gas feed line of a media supply of the reactor, orb) the at least one gas inlet opening of the gas distributor is provided for the feeding of off-gas from the reactor and is connected to at least one off-gas opening of the reactor, wherein the at least one gas outlet opening of the gas distributor serves for removing the off-gas from the gas distributor.14. The gas distributor of claim 13 , which claim 13 , in embodiment a) claim 13 , is suitable for introducing gas into the reactor claim 13 , wherein the at least one gas inlet opening is provided for the feeding of gas and is connected to a gas feed line claim 13 , wherein the at least one gas outlet opening serves for feeding gas to reactor nozzles.15. The gas distributor of claim 13 , wherein in embodiment a) claim 13 , the detachable fasteners are flange connections.16. The gas distributor of claim 14 , wherein in embodiment a) claim 14 , the ...

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Номер записи: 26
27-02-2020 дата публикации

Gas Injection Element for a Fluid Catalytic Cracking Unit and Gas Distribution System Equipped with this Injection Element

Номер: US20200061567A1
Автор: Lesage Romain
Принадлежит:

A gas injection element () for a system for distributing a gas inside a chamber of a fluid catalytic cracking unit. This injection member comprises a passage () extending entirely therethrough, and —an inner ceramic member () having an inner surface () that entirely delimits the through-passage (); and —a hollow metal sleeve (), inside which at least a portion of the inner member () is received, the sleeve () and the inner member () respectively having an inner surface () and an outer surface () with matching shapes allowing the inner member () to move relative to the sleeve () in a direction parallel to an axis (X) of the passage (), the outer () and inner surfaces () being provided with fastening elements () that engage to reversibly fasten the sleeve and the inner member. 110.-. (canceled)12. The gas injection element as claimed in claim 11 , characterized in that the external surface of the internal element and the internal surface of the sleeve are surfaces of revolution claim 11 , notably cylinders of revolution claim 11 , having an axis of revolution coincident with or parallel to the axis (X) of the through-passage.13. The gas injection element as claimed in claim 12 , characterized in that the fixing elements comprise lugs or notches collaborating respectively with grooves or ribs of a suitable shape to allow the sleeve and the internal element to move between a fixed state and a freed state following movements in translation in a direction parallel to the axis of revolution and in rotation about the axis of revolution.14. The gas injection element as claimed in claim 11 , characterized in that the sleeve is of cylindrical shape.15. The gas injection element as claimed in claim 11 , characterized in that the internal element has claim 11 , at one of its ends claim 11 , a flange bearing claim 11 , in the fixed state claim 11 , against one end of the sleeve in the direction of the axis of the through-passage.16. The gas injection element as claimed in claim ...

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Номер записи: 27
09-03-2017 дата публикации

INTEGRATED PROCESS FOR PRODUCING ANODE GRADE COKE

Номер: US20170066971A1
Автор: KOSEOGLU Omer Refa
Принадлежит:

The invention relates to processes for producing anode grade coke from whole crude oil. The invention is accomplished by first deasphalting a feedstock, followed by processing resulting DAO and asphalt fractions. The DAO fraction is hydrotreated or hydrocracked, resulting in removal of sulfur and hydrocarbons, which boil at temperatures over 370° C., and gasifying the asphalt portion in one embodiment. This embodiment includes subjecting hydrotreated and/or unconverted DAO fractions to delayed coking. In an alternate embodiment, rather than gasifying the asphalt portion, it is subjected to delayed coking in a separate reaction chamber. Any coke produced via delayed coking can be gasified. 1. A method for producing anode grade coke , comprising:(i) solvent deasphalting said feedstock to produce an asphalt fraction and a deasphalted rail (DAO) fraction, in a first reaction chamber;(ii) processing said DAO fraction and asphalt fraction in separate, second, third, and fourth reaction chambers;(iii) hydrotreating or hydrocracking said DAO fraction in said second reaction chamber to remove sulfur and nitrogen therefrom and to distill any hydrocarbons contained in said DAO which have a boiling point over 370° C.;(iv) subjecting any hydrotreated or unconverted DAO fraction to delayed coking in a third chamber, and(v) gasifying, said asphalt fraction via combining it with oxygen and steam, in said fourth reaction chamber, to produce hydrogen therefrom.2. The method of claim 1 , further comprising gasifying any coke produced in step (iv).3. The method of claim 1 , comprising introducing said hydrogen produced in said third reaction chamber into said second reaction chamber.4. The method of claim 1 , wherein said solvent deasphalting comprises mixing claim 1 , said crude oil with a paraffinic solvent containing C-Ccarbon atoms claim 1 , at a temperature and a pressure below critical temperature and critical pressure of said solvent.5. The method of claim 4 , wherein said ...

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Номер записи: 28
11-03-2021 дата публикации

REACTION CHAMBER AND ASSEMBLY METHOD

Номер: US20210071085A1
Автор: MOZZARDI Fabrizio, TOSTO Luca
Принадлежит: WALTER TOSTO SPA

Described is a reaction chamber () configured to house coking reactions comprising a main body () with a base portion (B) and a head portion (S), wherein the base portion (B) and the head portion (S) are joined together at their respective joint edges, characterised in that the walls of the main body () are made of stainless steel in such a way as to allow a joint between the base portion (B) and the head portion (S), of the main body (), by welding only the base sheet since no plating is present on the sheet itself and in such a way as to allow the construction of the base portion (B) and the head portion (S), when constructed by coupling and welding a plurality of sheets, by welding only the base sheet since no plating is present on the sheet itself. 1100. A reaction chamber () configured to house coking reactions comprising:{'b': '90', 'a main body () having a base portion (B) and a head portion (S), wherein said base portion (B) has a conical conformation for conveying the reaction products and wherein said head portion (S) has a substantially cylindrical conformation delimited at the top by a closing cap, said base portion (B) and said head portion (S) being jointed to each other by a plurality of welded joints at respective junction edges,'}{'b': '90', 'characterized in that said portions of said main body () are made of stainless steel in such a way as to allow a junction between sheets forming the three aforementioned portions and the junction between said portions by means of a single welded junction line, so avoiding the plating restoration operation required for clad sheet metal not characterized by carbon and/or low alloy steel metal sheet.'}2100. The reaction chamber () according to claim 1 , wherein said stainless steel comprises a balanced percentage of ferritic steel wherein the remaining percentage is austenitic steel.310090. The reaction chamber () according to claim 1 , wherein said main body () comprises a substantially cylindrical lateral casing ...

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Номер записи: 29
12-03-2020 дата публикации

METHOD AND SYSTEM FOR UTILIZING MATERIALS OF DIFFERING THERMAL PROPERTIES TO INCREASE FURNACE RUN LENGTH

Номер: US20200080002A1
Автор: Myszka Ronald T., Young Bruce T.
Принадлежит: AMEC FOSTER WHEELER USA CORPORATION

In one aspect, the present invention relates to a furnace having a heated portion arranged adjacent to an unheated portion. A plurality of straight tubes are formed of a first material and are at least partially disposed in the heated portion. A plurality of return bends are operatively coupled to the plurality of straight tubes. The plurality of return bends are formed of a second material and are at least partially disposed in the unheated portion. The first material exhibits a maximum temperature greater than the second material thereby facilitating increased run time of the furnace. The second material exhibits wear-resistance properties greater than the first material thereby facilitating wear-resistance of the furnace. 19-. (canceled)10. A furnace comprising:a plurality of straight tubes formed of a first material and at least partially disposed in a heated portion;a plurality of return bends coupled to the plurality of straight tubes, the plurality of return bends formed of a second material and at least partially disposed outside of the heated portion;a plurality of plug headers coupled to the plurality of straight tubes at an end opposite the plurality of return bends, the plurality of plug headers formed of the second material;wherein the first material exhibits a design-maximum tube-metal temperature greater than the second material thereby facilitating increased run time of the furnace; andwherein the second material exhibits wear-resistance properties greater than the first material facilitating wear resistance of the furnace.11. The furnace of claim 10 , wherein the plurality of plug headers are at least partially disposed outside of the heated portion.12. The furnace of claim 10 , wherein the first material is an austenitic material.13. The furnace of claim 10 , wherein the second material is a ferritic material.14. The furnace of claim 10 , wherein the first material is TP347H.15. The furnace of claim 10 , wherein the second material is 9Cr-1Mo.16. ...

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Номер записи: 30
01-04-2021 дата публикации

Predictive control systems and methods with offline gains learning and online control

Номер: US20210096518A1
Автор: Elhanan Ilani, Nadav Cohen
Принадлежит: Imubit Israel LTD

A controller for a plant that exhibits nonlinear dynamics includes one or more processors and memory storing instructions that cause the one or more processors to perform operations. The operations include training a neural network model during an offline learning period using historical plant data representing a plurality of different historical states of the plant and using the neural network model during online operation of the plant to generate a linear predictor as a function of a current state of the plant, the linear predictor defining a linearization of the nonlinear dynamics localized at the current state of the plant. The controller controls equipment that operate to affect the current state of the plant by performing a predictive control process that uses the linear predictor to generate values of one or more manipulated variables provided as inputs to the equipment.

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Номер записи: 31
06-04-2017 дата публикации

THERMAL PROCESSING REACTOR FOR MIXTURES, FABRICATION OF THE REACTOR, PROCESSES USING THE REACTORS AND USES OF THE PRODUCTS OBTAINED

Номер: US20170095790A1
Автор: WHEELER Lucie B.
Принадлежит:

A reactor and its internals used for the thermal processing of a liquid mixture. The reactor comprises plates and at least part of the surface of said plates is used to perform the thermal processing. The reactor and its internals are used for the thermal processing of various liquid mixtures containing organic compounds. The processes, for thermal processing the mixture comprising organic compounds, comprising the steps of feeding the reactor and its internals and being useful for treating wastes oils and/or for destroying hazardous and/or toxic products; and/or for reusing waste products in an environmentally acceptable form and/or way, and/or for cleaning contaminated soils or beaches, and/or cleaning tar pits, and/or use in coal-oil co-processing, and/or recovering oil from oil spills, and/or PCB free transformed oils. A process for fabricating the reactor and its internals is also proposed. 1. A reactor and internals of said reactor for thermal processing of a liquid mixture comprising at least one member chosen from a used oil , a waste oil , an heavy oil , and Marpol , said reactor comprising:a. a rotating kiln;b. a heating system;c. at least one shelf on a wall of the rotating kiln;d. a charge of plates of consistent shapes, at least a portion of said plates being held by said at least one shelf against said reactor wall so as to heat a surface of said plates for a time until rotation of said kiln causes said plates to flip and fall so as to present said heated surface of said plates to said liquid mixture to be thermally processed;e. means for bringing the liquid mixture to be thermally processed on the surface of at least part of the plates;f. means for removing the solids, produced in the reactor during the thermal processing, from the rotating kiln;g. means for recovering reaction and straight run products produced in the reactor during the thermal processing; andh. means for venting gas, obtained by the thermal processing, outside the zone defined by ...

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Номер записи: 32
19-04-2018 дата публикации

ELIMINATION OF POLYMER FOULING IN FLUIDIZED BED GAS-PHASE FINES RECOVERY EDUCTORS

Номер: US20180105613A1
Автор: Hendrickson Gregory G., Lowell Jeffrey S., Price Ralph J.
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

An eductor, a process and apparatus for gas phase polymerization of olefins in a polymerization reactor are disclosed. The process and apparatus employ an eductor which has an inlet which makes a bend of less than about 90° toward the outlet after entering the mixing chamber of the eductor. 1. An eductor comprising: a first inlet and a first outlet spaced apart from the first inlet along a central axis, and', 'a sidewall circumscribing the central axis and defining a mixing chamber; and, 'a first tubular body having a hollow interior and comprising'}a second tubular body having a hollow interior and comprising a second inlet and a spaced apart second outlet wherein the second tubular body extends into the mixing chamber through the sidewall of the first tubular body between the first inlet and the first outlet,wherein the second inlet is oriented substantially perpendicular to the axis of the first tubular body,wherein the second tubular body comprises a first bend of less than 90° from perpendicular toward the first outlet before extending into the mixing chamber, andwherein the second tubular body comprises a second bend of less than 90° toward the first outlet after extending into the mixing chamber.2. The eductor of claim 1 , wherein the second tubular body makes a first bend of about 45° from perpendicular toward the first outlet before entering the mixing chamber and a second bend of about 45° toward the first outlet after entering the mixing chamber.3. The eductor of claim 1 , wherein the second tubular body is substantially parallel to the central axis at the second outlet.4. The eductor of claim 1 , wherein the first inlet is a solid fines inlet and the second inlet is a motive gas inlet.5. The eductor of claim 1 , wherein the first inlet is a motive gas inlet and the second inlet is a solid fines inlet.6. The eductor of claim 1 , wherein the first tubular body and the second tubular body below the second bend after entering the mixing chamber are coaxial.7 ...

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Номер записи: 33
27-04-2017 дата публикации

METHOD AND SYSTEM FOR IMPROVING SPATIAL EFFICIENCY OF A FURNACE SYSTEM

Номер: US20170114278A1
Автор: Myszka Ronald T., Young Bruce T.
Принадлежит: Foster Wheeler USA Corporation

A furnace system includes at least one lower radiant section having a first firebox disposed therein and at least one upper radiant section disposed above the at least one lower radiant section. The at least one upper radiant section has a second firebox disposed therein. The furnace system further includes at least one convection section disposed above the at least one upper radiant section and an exhaust corridor defined by the first firebox, the second firebox, and the at least one convection section. Arrangement of the at least one upper radiant section above the at least one lower radiant section reduces an area required for construction of the furnace system. 1. A furnace system comprising:at least one lower radiant section comprising a first firebox disposed therein;at least one upper radiant section disposed above the at least one lower radiant section, the at least one upper radiant section comprising a second firebox disposed therein, the at least one upper radiant section and the at least one lower radiant section being controlled independently from each other;at least one convection section disposed above the at least one upper radiant section;an exhaust corridor defined by the first firebox, the second firebox, and the at least one convection section; andwherein arrangement of the at least one upper radiant section above the at least one lower radiant section reduces an area required for construction of the furnace system.2. The furnace system of claim 1 , wherein the at least one convection section is offset from the at least one upper radiant section and the at least one lower radiant section.3. The furnace system of claim 1 , wherein the at least one convection section comprises a convection inlet and a convection outlet.4. The furnace system of claim 3 , wherein the convection inlet receives a residual oil feed.5. The furnace system of claim 3 , wherein the at least one lower radiant section comprises a first radiant inlet and a first radiant outlet ...

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Номер записи: 34
13-05-2021 дата публикации

Coker switch valve operating system and method

Номер: US20210140561A1
Автор: Alfred Lewis Anderson, Asmaa Sadek KASSAB, Phillip M. Inman
Принадлежит: Mogas Industries Inc

An operating system for switching a coker switch valve to drum A, drum B, and bypass. The system has a shear pin linkage between the actuator and the valve stem and a position indicator independent of the actuator, to maintain functionality in the event of shear pin failure; and/or lockout functionality to prevent an inadvertent switch to bypass when switching between drum A and drum B and to lock down bypass mode to prevent an inadvertent switch from bypass to an open drum.

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Номер записи: 35
03-05-2018 дата публикации

Automated Batch Control of Delayed Coker

Номер: US20180119018A1
Автор: Lucas Richard
Принадлежит: BP CORPORATION NORTH AMERICA INC.

An automatic batch sequence computer control system is configured to automatically operate process valves in a delayed coker for a complete coke drum cycle. Double verification of the movement of the process valves is used to confirm advancing to the next step. Primary verification is achieved by using position sensors on the valves. Secondary verification is achieved by using monitored process conditions and confirming the measured conditions correlate with expected process conditions for an arrangement of valve positions at a given sequence in the coke drum cycle. A safety interlock system may be integrated with the control system. 14-. (canceled)5. A method for automatic operation of a delayed coker comprising one or more pairs of coke drums , the method comprising:operating the one or more pairs of coke drums in alternating cycles of filling a first drum of a pair with heated feed material while emptying a second drum of the pair;initiating an automatic batch sequence computer control system configured to automatically operate one or more sets of double block valves, each set of double block valves including a first valve and a second valve positioned along process piping between the first drum of the pair and the second drum of the pair, wherein the process piping connects the one or more pairs of coke drums with additional components of the delayed coker through a sequence of steps for a complete coke drum cycle; andin one step of the cycle:transmitting a command to close a set of the double block valves;monitoring position sensors on the set of double block valves as a primary verification to confirm the double block valves are both closed;monitoring a pressure at a valve isolation point between the set of double block valves to confirm the pressure between the double block valves has increased above a predetermined threshold as a secondary verification to confirm the double block valves are both closed;confirming that the double block valves are both closed ...

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Номер записи: 36
25-08-2022 дата публикации

LOW-CTE, LOW-PUFFING NEEDLE COKE

Номер: US20220267151A1
Автор: Hada Kyohei
Принадлежит: NIPPON STEEL CHEMICAL & MATERIAL CO., LTD.

To provide low CTE and low puffing needle coke more stably while dealing with changes in the properties of a feedstock. The low CTE and low puffing needle coke is obtained by mixing and coking a needle coke main feedstock of a coal tar-based heavy oil or petroleum-based heavy oil having a weak hydrogen donating property with a PDQI value expressed by equation (1) of less than 5.0, with a secondary feedstock having a strong hydrogen donating property with a PDQI value expressed by equation (1) of 5.0 or more, and calcining the obtained raw coke. [Equation (1)] PDQI=H %×10×(HNβ/H), wherein H % is a hydrogen amount (% by weight) obtained by elemental analysis, and HNβ/H is a ratio of β naphthenic hydrogen to total hydrogen measured by H-NMR. 1. Low CTE and low puffing needle coke , obtained by mixing and coking 100 parts by weight of a needle coke main feedstock of a coal tar-based heavy oil or petroleum-based heavy oil having a weak hydrogen donating property with a PDQI value expressed by equation (1) of less than 5.0 , with 10 to 80 parts by weight of a secondary feedstock having a strong hydrogen donating property with a PDQI value expressed by equation (1) of 5.0 or more , and calcining the obtained raw coke:{'br': None, 'PDQI=H %×10×(HNβ/H) \u2003\u2003[Equation (1)]'}{'sup': '1', 'wherein H % is a hydrogen amount (% by weight) obtained by elemental analysis, and HNβ/H is a ratio of β naphthenic hydrogen to total hydrogen measured by H-NMR.'}2. Low CTE and low puffing needle coke , having a CTE-related structure index (NCSIC) expressed by equation (2) of more than 25.0 , and a puffing-related structure index (NCSIP) expressed by equation (3) of more than 5.0:{'br': None, 'i': 'Lc/d', 'NCSIC=((002)+(open pore ratio))/(σ(θ)) \u2003\u2003[Equation (2)]'} {'br': None, 'NCSIP=(open pore amount/closed pore amount)+(HIT/1000)/EIT \u2003\u2003[Equation (3)]'}, 'wherein Lc represents a crystallite size, d002 represents an interplanar spacing, and σ(θ) represents a ...

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Номер записи: 37
14-05-2015 дата публикации

Thermal cracking additive compositions for reduction of coke yield in delayed coking process

Номер: US20150129460A1
Автор: Biswapriya DAS, Brijesh Kumar, Debasis Bhattacharyya, Eswar Prasad Dalai, Gautam THAPA, Jagdev Kumar Dixit, Parkash Om, Ponoly Ramachandran Pradeep, Rajesh, Ram Mohan Thakur, Ravinder Kumar Malhotra, Samik Kumar HAIT, Santanam Rajagopal, Satyen Kumar Das, Terapalli Hari Venkata Devi Prasad
Принадлежит: Indian Oil Corp Ltd

The present invention is directed to novel thermal cracking additive compositions for reduction of coke yield in Delayed Coking process and method for preparing the same. The present invention also provides that the thermal cracking additive compositions of the present invention are in micron-size and nano-size. Further, the present invention provides a process of thermal cracking of heavy petroleum residue used in petroleum refineries using Delayed Coking process to produce petroleum coke and lighter hydrocarbon products with decreased coke yield and increased yield of liquid and/or gaseous products.

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Номер записи: 38
10-05-2018 дата публикации

Cyclonic Injector And Method For Reagent Gasification And Decomposition In A Hot Gas Stream

Номер: US20180126332A1
Автор: Eric Lindemann, James M. Valentine, Jeffrey Michael Broderick, Saiprasad Jangiti, Thomas V. Eldredge
Принадлежит: Peerless Manufacturing Co

A system for vaporizing and optionally decomposing a reagent, such as aqueous ammonia or urea, which is useful for NOx reduction, includes a cyclonic decomposition duct, wherein the duct at its inlet end is connected to an air inlet port and a reagent injection lance. The air inlet port is in a tangential orientation to the central axis of the duct. The system further includes a metering valve for controlling the reagent injection rate. A method for vaporizing and optionally decomposing a reagent includes providing a cyclonic decomposition duct which is connected to an air inlet port and an injection lance, introducing hot gas through the air inlet port in a tangential orientation to the central axis of the duct, injecting the reagent axially through the injection lance into the duct; and adjusting the reagent injection rate through a metering valve.

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Номер записи: 39
10-05-2018 дата публикации

APPARATUS FOR INTRODUCTION OF DROPLETS INTO A REACTOR

Номер: US20180126351A1
Автор: Bayer Robert, Freiberg Juergen, Gampfer Oliver, Krueger Marco
Принадлежит: BASF SE

The invention relates to an apparatus for introduction of droplets into a reactor, comprising a holder for at least one dropletizer unit, where the dropletizer unit has a feed for a liquid to be dropletized and a dropletizer plate and the dropletizer plate has holes through which a liquid to be dropletized is introduced into the reactor, where the holder for the at least one dropletizer unit can be pushed into the reactor or pulled out of the reactor through an opening in the shell of the reactor. At least one rail is accommodated within the reactor and is used to guide the holder for the at least one dropletizer unit along it. 113161616567676913161113714513161. An apparatus for introduction of droplets into a reactor () , comprising a holder () for at least one dropletizer unit () , where the dropletizer unit () has a feed () for a liquid to be dropletized and a dropletizer plate () and the dropletizer plate () has holes () through which a liquid to be dropletized is introduced into the reactor () , where the holder () for the at least one dropletizer unit () can be pushed into the reactor () or pulled out of the reactor () through an opening () in the shell of the reactor () , wherein at least one rail () is accommodated within the reactor () and is used to guide the holder () for the at least one dropletizer unit () along it.23161. The apparatus according to claim 1 , wherein the holder () for the at least one dropletizer unit () being guided is suspended on the rail.33145. The apparatus according to claim 1 , wherein the holder () being guided within the reactor rests on two rails ().445413161. The apparatus according to claim 3 , wherein the rails are two contact surfaces () on a pipe () which is open at the bottom and on which the holder () for the at least one dropletizer unit () rests.5454341. The apparatus according to claim 4 , wherein the contact surfaces () run parallel to the opening () at the base of the pipe ().6454341. The apparatus according to ...

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Номер записи: 40
03-06-2021 дата публикации

BURN PROFILES FOR COKE OPERATIONS

Номер: US20210163822A1
Автор: Brombolich Jeffrey Scott, Chun Ung-Kyung, FERNANDEZ Mayela Carolina, Glass Edward A., Kandula Rajesh Kumar, Kesavan Parthasarathy, Mrozowick Richard Alan, Quanci John Francis, Vichitvongsa Khambath
Принадлежит:

The present technology is generally directed to systems and methods for optimizing the burn profiles for coke ovens, such as horizontal heat recovery ovens. In various embodiments the burn profile is at least partially optimized by controlling air distribution in the coke oven. In some embodiments, the air distribution is controlled according to temperature readings in the coke oven. In particular embodiments, the system monitors the crown temperature of the coke oven. After the crown reaches a particular temperature range the flow of volatile matter is transferred to the sole flue to increase sole flue temperatures throughout the coking cycle. Embodiments of the present technology include an air distribution system having a plurality of crown air inlets positioned above the oven floor. 128-. (canceled)29. A method of controlling a burn profile of a coke oven , the method comprising:charging a bed of coal into an oven chamber of a coke oven, the oven chamber being at least partially defined by an oven floor, opposing oven doors, opposing sidewalls that extend upwardly from the oven floor between the opposing oven doors, and an oven crown positioned above the oven floor, wherein the oven chamber is in fluid communication with an exterior environment via an air inlet;creating a negative pressure draft on the oven chamber such that air is drawn into the oven chamber through the air inlet, the negative pressure draft causing volatile matter from the coal bed to mix with the air and at least partially combust within the oven chamber and thereby generate heat within the oven chamber;based on a plurality of temperature increases detected in the oven chamber, reducing the flow of air into the oven chamber until the temperature in the oven chamber reaches a predetermined peak temperature; anddirecting the volatile matter from the oven chamber to a sole flue beneath the oven floor, thereby preheating the coke oven for a subsequent coke oven charge.30. The method of claim 29 , ...

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Номер записи: 41
17-05-2018 дата публикации

Method and Device for Making Polymer Microparticles

Номер: US20180133685A1
Автор: Chen Lin, Gao Jie, Lu Lianghua, PAN Zhida, Peng Wenqing, Soderman Tobias E.
Принадлежит: GENERAL ELECTRIC COMPANY

A method includes spraying a liquid including polymer and a gas substantially inert to the liquid respectively from a first and second orifice of a nozzle into air to form mist of beads. The beads then are collected with a collecting medium at a temperature in a range from about −10° C. to about 80° C. The collecting medium includes at least one of water and alcohols. 1. A method , comprising:spraying a liquid comprising a polymer and a gas, substantially inert to the liquid, respectively from a first and second orifice of a nozzle into air to form a mist of beads; andcollecting the beads with a collecting medium at a temperature in a range from about −10° C. to about 80° C., the collecting medium comprising water, alcohol, or a combination thereof.2. The method according to claim 1 , wherein the liquid is an aqueous solution of the polymer.3. The method according to claim 1 , wherein the polymer comprises a polysaccharide.4. The method according to claim 3 , wherein the polysaccharide comprises agarose claim 3 , dextran claim 3 , cellulose claim 3 , or combinations thereof.5. The method of claim 3 , wherein the polysaccharide comprises native or derivatised agarose or agar.6. The method according to claim 1 , wherein the collecting medium is water or an aqueous solution comprising at least 80 or 90 wt. % water.7. The method according to claim 1 , further comprising feeding the liquid into the nozzle at a temperature in a range from about 65° C. to about 100° C.8. The method according to claim 1 , wherein the nozzle is a two-phase spray nozzle configured to atomize the liquid by causing interaction of the liquid and gas from the first and second orifices respectively.9. The method according to claim 1 , wherein the nozzle is configured to produce a substantially conical spray pattern with a spray angle of less than 90 degrees claim 1 , such as less than 45 degrees.10. The method according to claim 1 , wherein the liquid and gas are fed into the nozzle under ...

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Номер записи: 42
04-06-2015 дата публикации

DELAYED COKING PROCESS

Номер: US20150152334A1
Автор: Arora Ajay Kumar, Bhattacharyya Debasis, DEVI PRASAD Terapalli Hari Venkata, Dixit Jagdev Kumar, Kumar Brijesh, Malhotra Ravinder Kumar, PURI Suresh Kumar, Rajagopal Santanam, RAJESH , RAMACHANDRAN Pradeep Ponoly, Thakur Ram Mohan
Принадлежит:

The present invention provides a delayed coking process comprising a step of subjecting a mixed feed comprises residual heavy hydrocarbon feedstock and bio oil obtained from fast pyrolysis of lignocellulosic biomass of one or more of Jatropha, Cashew nut, Karanjia and Neem to a delayed coking process and a system for the delayed coking process. 1. A delayed coking process comprising a step of subjecting a mixed feed comprising residual heavy hydrocarbon feedstock and bio oil obtained from fast pyrolysis of lignocellulosic biomass of one or more of Jatropha , Cashew nut , Karanjia and Neem to a delayed coking process.2. The process as claimed in claim 1 , wherein the residual heavy hydrocarbon feedstock has boiling point in the range of 400° to 700° C.3. The process as claimed in claim 1 , wherein the bio oil has boiling point in the boiling range of about 200° to 620° C.4. The process as claimed in claim 1 , wherein the residual heavy hydrocarbon feedstock has Conradson carbon residue content of 15 to 27 wt % and the bio oil has Conradson carbon residue content of 7 to 10 wt %.5. The process as claimed in claim 1 , wherein the lignocellulosic biomass are selected from the group comprising of routes claim 1 , stems claim 1 , leaves and seeds or combination thereof.6. The process as claimed in claim 1 , wherein the mixed feed is obtained by:(a) mixing residual heavy hydrocarbon feedstock and bio oil to obtain a mixture;(b) feeding the mixture thus obtained in step (a) to a bottom of a fractionator along with a condensed recycle oil; and(c) withdrawing the mixed feed from the bottom of the fractionator.7. The process as claimed in claim 1 , wherein the mixed feed is obtained by:(a) feeding the residual heavy hydrocarbon feedstock to a bottom of a fractionator along with a condensed recycle oil;(b) withdrawing a bottom fraction from the bottom of the fractionator; and(c) mixing bio oil with the bottom fraction thus obtained in step (b) to obtain the mixed feed.8. The ...

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Номер записи: 43
25-05-2017 дата публикации

COKE DRUM WITH AIR INJECTION SYSTEM FOR SKIRT JUNCTION

Номер: US20170145319A1
Автор: Araque Vivas Egler Dubín, Specht María Isabel, Vivas Chacón Gabriel Arcángel
Принадлежит: Intevep, S.A.

A coke drum includes a coke drum vessel having a substantially cylindrical wall and a conical bottom portion; a skirt downwardly depending from a transition of the cylindrical wall into the conical bottom portion, an inner annular space being defined between the skirt and the conical bottom portion; and a fluid injection system communicated with the inner annular space for injecting fluid at a desired temperature to heat or cool the inner annular space. The fluid injection system allows the inner annular space and junction of the skirt with the coke drum vessel to be heated or cooled to minimize temperature difference between these areas and a batch of coke to be introduced into the drum. 1. A coke drum , comprising:a coke drum vessel comprising a substantially cylindrical wall and a conical bottom portion;a skirt downwardly depending from a transition of the cylindrical wall into the conical bottom portion, an inner annular space being defined between the skirt and the conical bottom portion; anda fluid injection system communicated with the inner annular space for injecting fluid at a desired temperature to heat or cool the inner annular space.2. The coke drum of claim 1 , wherein the fluid injection system comprises a toroid tube in the inner annular space and communicated with a source of the fluid.3. The coke drum of claim 1 , wherein the fluid injection system has a fluid inlet and a fluid outlet claim 1 , and at least one baffle in the inner annular space between the fluid inlet and the fluid outlet.4. The coke drum of claim 1 , further comprising a bottom wall section connected between the skirt and the conical bottom portion and closing off the inner annular space.5. The coke drum of claim 1 , wherein the fluid injection system comprises a first toroid tube defining a fluid inlet claim 1 , a second toroid tube defining a fluid outlet claim 1 , and a series of baffles in the inner annular space between the first toroid tube and the second toroid tube.6. The ...

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Номер записи: 44
07-05-2020 дата публикации

APPARATUSES FOR MIXING OF STAGED METHANOL INJECTION

Номер: US20200139327A1
Автор: II Richard A., Johnson, Montalbano Joseph A., Senetar John J.
Принадлежит:

This present disclosure relates to apparatuses for methylation of aromatics in an aromatics complex for producing a xylene isomer product. More specifically, the present disclosure relates to apparatuses for producing para-xylene by the selective methylation of toluene and/or benzene in an aromatics complex using processed toluene instead of crude toluene. 1. A riser reactor , comprising:a cylindrical riser comprising an outer wall and an inner wall;at least one baffle affixed to the inner wall extending into the riser; andat least one distributor configured to inject methanol into the riser, wherein the at least one distributor is located above the at least one baffle, below the at least one baffle, extends through the at least one baffle and into a different radial location within the riser reactor, or a combination thereof2. The riser reactor of claim 1 , wherein the at least one baffle extends around the entire inner wall of the riser reactor.3. The riser reactor of claim 1 , wherein the at least one distributor is angled from 30 degrees to 120 degrees relative to the inner wall.4. The riser reactor of claim 1 , further comprising a second distributor claim 1 , wherein the distributors are located at two different axial locations within the riser reactor.5. The riser reactor of claim 1 , wherein there are at least two rows of baffles.6. The riser reactor of claim 1 , further comprising a plurality of baffles and wherein the baffles are arranged symmetrically around the inner wall of the riser.7. The riser reactor of claim 1 , further comprising a plurality of baffles and wherein baffles cover substantially a circumference of the riser.8. The riser reactor of claim 1 , wherein the riser reactor is a toluene methylation riser reactor. This application is a continuation of U.S. Ser. No. 15/849,529 filed on Dec. 20, 2017, the entirety of which is incorporated herein by reference.This present disclosure relates to apparatuses for methylation of aromatics in an ...

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Номер записи: 45
11-06-2015 дата публикации

Automated Batch Control of Delayed Coker

Номер: US20150159090A1
Автор: Lucas Richard E.
Принадлежит: BP CORPORATION NORTH AMERICA INC.

An automatic batch sequence computer control system is configured to automatically operate process valves in a delayed coker for a complete coke drum cycle. Double verification of the movement of the process valves is used to confirm advancing to the next step. Primary verification is achieved by using position sensors on the valves. Secondary verification is achieved by using monitored process conditions and confirming the measured conditions correlate with expected process conditions for an arrangement of valve positions at a given sequence in the coke drum cycle. A safety interlock system may be integrated with the control system. 2. The method of claim 1 , further comprising:identifying a plurality of valves as hydrocarbon isolation points;identifying a plurality of valves as an atmosphere isolation points;confirming that all valves on a hydrocarbon isolation point are closed before transmitting a signal to open a valve on an atmospheric isolation point; andconfirming that all valves on an atmospheric isolation point are closed before transmitting a signal to open a valve on a hydrocarbon isolation point.3. The method of claim 2 , wherein confirming that all valves on a hydrocarbon isolation point are closed comprises receiving the primary verification and the secondary verification associated with the valve.4. The method of claim 2 , wherein:a main feed isolation valve, drum condensation double block valves, antifoam double block valves, overhead quench double block valves, overhead vapor double block valves and blowdown double block valves are identified as valves on the hydrocarbon isolation points; anda top head valve, a bottom head valve, and overhead vent double block valves are identified as valves on the atmospheric isolation points.5. A method for automatic operation of a delayed coker comprising:initiating an automatic batch sequence computer control system configured to automatically operate process valves in a delayed coker through a sequence of ...

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Номер записи: 46
08-06-2017 дата публикации

INLET DISTRIBUTOR FOR SPHERICAL REACTOR

Номер: US20170157584A1
Автор: Palmer Brad P.
Принадлежит: Phillips 66 Company

The invention relates to distributing reactants more evenly across the interior space of a reactor vessel utilizing a distributor at the inlet end that initially directs the flow of reactants through a series of circumferential nozzles. The nozzles are physical spaced such that the first nozzle provides the reactants into the vessel to spread radially and broadly outwardly into the vessel and each successive circumferential nozzle to deliver reactants in a less broadly distribution or dispersion where the interior space is filled with reactants without broadly diverse velocities that may create hot spots within the catalyst bed. 1. A reactor inlet distributor for delivering a feedstream of reactants into a reactor vessel comprising:a) a generally cylindrical body having an inlet end and an outlet end;b) a first deflector ring with an integrally attached first neck attached to but spaced from the outlet end of the generally cylindrical body by stanchions such that a circumferential nozzle is defined between the deflector ring and the outlet end of the generally cylindrical body and the neck extends from the first deflector ring away from the generally cylindrical body;c) at least one additional deflector ring with an integrally attached additional neck attached to but spaced from the first neck by stanchions such that an additional circumferential nozzle is defined between the additional deflector ring and the first neck; andd) a deflector plate attached to said additional deflector ring by stanchions, but spaced from said additional neck to define a last circumferential nozzle.2. The reactor inlet distributor set forth in wherein the deflector rings include through holes to allow reactants to pass through.3. The reactor inlet distributor set forth in wherein the deflector plate includes through holes to allow reactants to pass through.4. The reactor inlet distributor set forth in wherein the necks include through holes to allow reactants to pass through.5. The ...

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Номер записи: 47
08-06-2017 дата публикации

CRUDE BIO OIL PRETREATMENT AND UPGRADING

Номер: US20170158967A1
Автор: BILLIMORIA Rustom M., Borghard William G., Buchanan John S., Lewis William E., Reiner Virginia M.
Принадлежит:

Systems and methods are provided for pretreatment and upgrading of crude bio oils for further processing and/or use as fuel products. Crude bio oils can be treated by one or more of flash fractionation and thermal cracking to generate fractions suitable for further processing, such as further hydroprocessing. Blending of crude bio oil fractions with mineral feeds can also be used to reduce metals contents to levels suitable for refinery processing. 1. A method for upgrading a crude bio oil fraction , comprising:thermally cracking a feedstock comprising a first crude bio oil fraction, the first crude bio oil fraction having a metals content of at least about 500 wppm and a T95 boiling point of about 600° C. or less, under effective thermal cracking conditions comprising a temperature of about 300° C. to about 500° C. and a pressure of about 50 kPaa to about 1000 kPaa, to form at least a liquid product and coke product, the coke product comprising metals in an amount of at least about 80 wt % of the metals content of the crude bio oil, phosphorus in an amount of at least about 80 wt % of a phosphorus content of the crude bio oil, or a combination thereof.2. The method of claim 1 , further comprising:fractionating a second crude bio oil fraction to form a fraction having a T5 boiling point of about 280° C. to about 360° C., the first crude bio oil fraction comprising at least a portion of the fraction having a T5 boiling point of about 280° C. to about 360° C.3. The method of claim 1 , further comprising:hydroprocessing at least a portion of the liquid product under effective hydrotreating conditions to form a hydroprocessed liquid product.4. The method of claim 3 , wherein hydroprocessing at least a portion of the liquid product further comprises hydroprocessing a first mineral feed with the at least a portion of the liquid product claim 3 , the at least a portion of the liquid product comprising at least about 5 wt % of a combined weight of the at least a portion of ...

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Номер записи: 48
30-05-2019 дата публикации

METHOD AND SYSTEM FOR IMPROVING SPATIAL EFFICIENCY OF A FURNACE SYSTEM

Номер: US20190161681A1
Автор: Myszka Ronald T., Young Bruce T.
Принадлежит: AMEC FOSTER WHEELER USA CORPORATION

A furnace system includes at least one lower radiant section having a first firebox disposed therein and at least one upper radiant section disposed above the at least one lower radiant section. The at least one upper radiant section has a second firebox disposed therein. The furnace system further includes at least one convection section disposed above the at least one upper radiant section and an exhaust corridor defined by the first firebox, the second firebox, and the at least one convection section. Arrangement of the at least one upper radiant section above the at least one lower radiant section reduces an area required for construction of the furnace system. 1. A furnace system comprising:at least one lower radiant section comprising a first firebox disposed therein;at least one upper radiant section disposed above the at least one lower radiant section, the at least one upper radiant section comprising a second firebox disposed therein, the at least one upper radiant section and the at least one lower radiant section being controlled independently from each other;at least one convection section disposed above the at least one upper radiant section; andan exhaust corridor defined by the first firebox, the second firebox, and the at least one convection section.2. The furnace system of claim 1 , wherein the at least one convection section is offset from the at least one upper radiant section and the at least one lower radiant section.3. The furnace system of claim 1 , wherein the at least one convection section comprises a convection inlet and a convection outlet.4. The furnace system of claim 3 , wherein the convection inlet receives a residual oil feed.5. The furnace system of claim 3 , wherein the at least one lower radiant section comprises a first radiant inlet and a first radiant outlet.6. The furnace system of claim 5 , wherein the at least one upper radiant section comprises a second radiant inlet and a second radiant outlet.7. The furnace system of ...

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Номер записи: 49
21-05-2020 дата публикации

BURN PROFILES FOR COKE OPERATIONS

Номер: US20200157430A1
Автор: Brombolich Jeffrey Scott, Chun Ung-Kyung, FERNANDEZ Mayela Carolina, Glass Edward A., Kandula Rajesh Kumar, Kesavan Parthasarathy, Mrozowicz Richard Alan, Quanci John Francis, Vichitvongsa Khambath
Принадлежит:

The present technology is generally directed to systems and methods for optimizing the burn profiles for coke ovens, such as horizontal heat recovery ovens. In various embodiments the burn profile is at least partially optimized by controlling air distribution in the coke oven. In some embodiments, the air distribution is controlled according to temperature readings in the coke oven. In particular embodiments, the system monitors the crown temperature of the coke oven. After the crown reaches a particular temperature range the flow of volatile matter is transferred to the sole flue to increase sole flue temperatures throughout the coking cycle. Embodiments of the present technology include an air distribution system having a plurality of crown air inlets positioned above the oven floor. 115-. (canceled)16. A system for controlling a horizontal heat recovery coke oven burn profile , the method comprising:a horizontal heat recovery coke oven having an oven chamber being at least partially defined by an oven floor, opposing oven doors, opposing sidewalls that extend upwardly from the oven floor between the opposing oven doors, an oven crown positioned above the oven floor, and at least one sole flue, beneath the oven floor, in fluid communication with the oven chamber;a temperature sensor disposed within the oven chamber;at least one air inlet, positioned to place the oven chamber in fluid communication with an environment exterior to the horizontal heat recovery coke oven;at least one uptake channel having an uptake damper in fluid communication with the at least one sole flue; the uptake damper being selectively movable between open and closed positions;the negative pressure draft is reduced over a plurality of flow reducing steps by; anda controller operatively coupled with the uptake damper and adapted to move the uptake damper through a plurality of increasingly flow restrictive positions over the carbonization cycle, based on the plurality of different ...

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Номер записи: 50
15-07-2021 дата публикации

SLURRY PHASE REACTOR WITH INTERNAL VAPOR-LIQUID SEPARATOR

Номер: US20210214624A1
Автор: Piotter Douglas, Schoessow Cassandra
Принадлежит: Kellogg Brown & Root LLC

A system for processing a hydrocarbon feed has a final stage reactor and internal separator that forms a substantially gas stream and a substantially non-gas stream. The substantially gas stream is sent directly from the final stage reactor to a separator or for other processing. 1. A system for processing a hydrocarbon feed , comprising: a vessel body,', 'an inlet formed in the vessel body for receiving the hydrocarbon feed,', 'a reactor section formed in the vessel body, the reactor section receiving the hydrocarbon feed via the inlet;', 'a separator section formed in the vessel body, the separator section configured to form a substantially gas stream and a substantially non-gas stream;', 'a nozzle separating the reactor section from the separator section, the nozzle having an opening directing the hydrocarbon feed, hydrogen, and reaction products from the reactor section to the separator section;', 'a first outlet formed in the vessel body receiving the substantially non-gas stream;', 'a second outlet formed in the vessel body, the second outlet receiving the substantially gas stream; and, 'a plurality of serially aligned reactors, the plurality of reactors including a final stage reactor, the final stage reactor includinga separator receiving the substantially gas stream from the second outlet.2. The system of claim 1 , further comprising a deflector positioned in the separator section claim 1 , the deflector obstructing axial flow of the hydrocarbon feed in the separator section.3. The system of claim 2 , wherein the deflector is a plate.4. The system of claim 2 , wherein the deflector is a curved tubular member connected to the second outlet.5. The system of claim 1 , further comprising a quench inlet formed in the vessel body claim 1 , the quench inlet receiving at least one of: a cooled hydrogen claim 1 , a vacuum gas oil claim 1 , a cool hydrocarbon stream.6. The system of claim 1 , wherein the plurality of serially aligned reactors further includes a first ...

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Номер записи: 51
19-07-2018 дата публикации

GAS JETTING APPARATUS

Номер: US20180200687A1
Автор: Nishimura Shinichi, Tabata Yoichiro, Watanabe Kensuke
Принадлежит: TOSHIBA MITSUBISHI-ELECTRIC INDUSTRIAL SYSTEMS CORPORATION

A gas jetting apparatus capable of uniformly jetting, even onto a treatment-target object having a high-aspect-ratio groove, a gas into the groove. The gas jetting apparatus includes a gas jetting cell unit for jetting a gas toward a treatment-target object. The gas jetting cell unit includes a first cone-shaped member and a second cone-shaped member. A gap is formed between a side surface of a first cone shape and a side surface of the second cone-shaped member. Apex sides of the cone-shaped members face the treatment-target object. 1. A gas jetting apparatus comprising:a vessel unit;a gas supply unit for supplying a gas to said vessel unit; anda gas jetting cell unit provided in said vessel unit to jet the gas toward a treatment-target object, wherein a first cone-shaped member; and', 'a second cone-shaped member disposed to surround said first cone-shaped member in a side surface direction so that a gap is formed with a side surface of said first cone-shaped member,, 'said gas jetting cell unit includesan apex side of said first cone-shaped member and an apex side of said second cone-shaped member face said treatment-target object,the gas supplied from said gas supply unit enters from a bottom surface side of said first cone-shaped member and a bottom surface side of said second cone-shaped member into said gap, passes through said gap, and is jetted from the apex side of said first cone-shaped member and the apex side of said second cone-shaped member toward said treatment-target object.2. The gas jetting apparatus according to claim 1 , whereina portion of said first cone-shaped member which faces said gap and a portion of said second cone-shaped member which faces said gap are made of sapphire or quartz.3. The gas jetting apparatus according to claim 1 , whereina distance between a side surface of said first cone-shaped member and a side surface of said second cone-shaped member in said gap is a value in a range from 0.3 mm to 3 mm inclusive, andgas pressure ...

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Номер записи: 52
19-07-2018 дата публикации

INSULATED COKE DRUM, INSULATION SYSTEM THEREFORE, AND METHOD OF INSTALLING SAME

Номер: US20180201839A1
Автор: MCBRIDE JONATHAN
Принадлежит: INSULTHERM, INC.

An insulated pressure vessel, such as a coke drum, having an insulation system installed thereon. The insulation system includes an insulation support system comprising either a floating ring type support system, or a cage type support system including a plurality of vertically spaced insulation support rings each having a diameter greater than the external diameter of the coke drum. A plurality of insulation panels are secured to the support rings, each panel including insulation material and an exterior metal jacket. The panels are secured to horizontally adjacent insulation panels with standing seams. Weather shields may be provided over the top of the seams. Tensioned insulation securing cables, corresponding in number to the insulation support rings, are routed through horizontally aligned eyelets in each standing seam. 1. An insulated coke drum comprising (or consisting essentially of , or consisting of):(a) a coke drum having an external diameter, an exterior surface, and a longitudinal axis; i) an insulation support system comprising a series of spaced apart weldments (preferably vertical, rectangular CS plates, or “clips”) welded to the coke drum exterior surface in spaced apart horizontal rows, and a plurality of vertically spaced insulation support rings supported by but not attached to the weldments, each support ring having a diameter greater than the external diameter of the coke drum;', 'ii) a plurality of insulation panels secured to the support rings, each insulation panel comprising insulation material and an exterior metal jacket, each insulation panel positioned between horizontally adjacent insulation panels with single-folded standing seams; and', 'iii) a plurality of tensioned insulation securing cables corresponding in number to the plurality of support rings, the cables routed through horizontally aligned eyelets in each single-folded standing seam., '(b) an insulation system installed on the coke drum exterior surface, the insulation system ...

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Номер записи: 53
16-10-2014 дата публикации

METHOD AND DEVICE FOR CHARGING COKE OVENS WITH COMPACTED COAL BY USE OF A CHARGING PLATE SEPARATOR LAYER

Номер: US20140305785A1
Автор: Badura Sven, Kim Ronald, Schucker Franz-Josef, Worberg Rainer
Принадлежит: THYSSENKRUPP INDUSTRIAL SOLUTIONS AG

Disclosed is a method and device for charging the chambers of a coke oven with compacted coal. The method includes placing a plurality of adhesion reduction particles onto a coke oven charging plate, the particles being configured to reduce at least one of adhesion forces and friction forces present between the charging plate and compacted coal to be loaded thereon, loading compacted coal onto the charging plate, moving the charging plate loaded with compacted coal to the coke oven chamber, and slidably removing the compacted coal from the charging plate such that the compacted coal is disposed in the coke oven chamber. The device comprises a metal plate configured to load compacted coal into the coke oven, a plurality of adhesion reduction particles affixed to the metal plate by an adhesive layer, and a device used to move the metal plate to a front of the firing chamber of the coke oven. 19.-. (canceled)10. A method for charging the chambers of a coke oven with compacted coal , comprising:placing a plurality of adhesion reduction particles onto a coke oven charging plate configured to charge the coke oven with compacted coal, the adhesion reduction particles being configured to form a separating layer between the charging plate and the compacted coal to be disposed thereon so as to reduce at least one of adhesion forces and friction forces present between the charging plate and compacted coal, so as to reduce the force required to slidably remove the compacted coal from the charging plate;loading compacted coal onto the charging plate, the compacted coal having the form of at least one of (1) a plurality of stacked compressed blocks of coal or (2) a compressed coal cake;moving the charging plate loaded with compacted coal to the coke oven chamber; andslidably removing the compacted coal from the charging plate such that the compacted coal is disposed in the coke oven chamber.11. The method of claim 10 , further comprising:compression molding coal directly on the ...

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Номер записи: 54
17-08-2017 дата публикации

FLUIDIZED BED COKING WITH FUEL GAS PRODUCTION

Номер: US20170233667A1
Автор: Harandi Mohsen N., Phillips Glen E., Rajagopalan Suriyanarayanan
Принадлежит:

A method for utilizing the heating value of clarified shiny oil (CSO) by in which clarified slurry oil from the settler of a fluid catalytic cracking unit is introduced as feed to the gasifier of a Flexicoking unit where it is reacted at high temperature with the air and steam to produce additional heat. In this way, the heating value of the CSO is better utilized as refinery fuel gas and plant economics are enhanced. 1. A method of realizing the heating value of a catalytically or thermally cracked bottoms stream which comprises feeding the catalytically or thermally cracked bottoms stream to a gasifier of a fluid coking unit including (i) a reactor in which a heavy oil feed is thermally cracked in a fluidized bed of coke particles to deposit coke on the particles and form cracked products and (ii) a gasifier which receives the coke particles and converts the coke and cracked products to fuel gas by reaction with steam and oxygen in an oxygen-deficient environment.2. The method of claim 1 , wherein the catalytically or thermally cracked bottoms stream comprises a clarified slurry oil (CSO) or a main fractionator bottoms from a fluid catalytic cracking unit or steam cracker tar.3. The method of claim 2 , wherein the catalytically cracked bottoms stream comprises CSO.4. A method according to in which the fluid coking unit comprises a reactor claim 1 , a heater which receives coke particles from the reactor and circulates hot coke particles to the reactor and a gasifier which receives coke particles from the heater and which circulates partly gasified coke particles to the heater.5. A method according to in which the fluid coking unit comprises a reactor and a gasifier which receives coke particles from the reactor and which circulates partly gasified coke particles directly to the reactor.6. A method according to in which the coke particles are converted to fuel gas in the gasifier at a temperature from 850 to 1000° C. and a pressure ranging from 0 to 1.000 kPag.7. A ...

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Номер записи: 55
07-09-2017 дата публикации

METHOD AND SYSTEM FOR UTILIZING SELECTIVELY DE-COUPLEABLE CONNECTIONS FOR MODULAR INSTALLATION OF A COKE DRUM

Номер: US20170253802A1
Автор: Meyer William
Принадлежит: Foster Wheeler USA Corporation

In one aspect, the present invention relates to a coke drum module, the coke drum module includes a support frame. A coke drum is disposed within the support frame. A strut is removably connected to the support frame and the coke drum. The strut becomes unloaded responsive to the coke drum contacting a support pad. The coke drum module further includes a compression member removably connected to the support frame and the coke drum. The compression member is oriented generally perpendicularly to the strut. A rigid connection is present between the coke drum and the support frame during transportation of the coke drum module. Upon removal of the strut and the compression member, the rigid connection is not present. 120-. (canceled)21. A coke drum module comprising:a support frame;a coke drum disposed within the support frame;a selectively de-coupleable connection that is selectively transitioned from a coupled state to a de-coupled state;wherein, in the coupled state, the selectively de-coupleable connection supports a weight of the coke drum during transport; andwherein, in the de-coupled state, thermal expansion of the coke drum without damage to the support frame is facilitated.22. The coke drum module of claim 21 , wherein the selectively de-coupleable connection comprises a strut oriented generally parallel to a length of the coke drum.23. The coke drum module of claim 21 , wherein the selectively de-coupleable connection is subjected to tension stress when the coke drum is oriented in a vertical direction.24. The coke drum module of claim 21 , wherein the selectively de-coupleable connection comprises a compression member.25. The coke drum module of claim 24 , wherein the compression member supports a weight of the coke drum when the coke drum is oriented in a horizontal direction.26. The coke drum module of claim 25 , wherein the compression member facilitates transport of the coke drum module.27. The coke drum module of claim 21 , wherein the selectively de- ...

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Номер записи: 56
07-09-2017 дата публикации

COKE OVEN CHARGING SYSTEM

Номер: US20170253804A1
Автор: Ball Mark Anthony, Choi Chun Wai, Mounts Dexter Junior, Quanci John Francis, Sparling Danny E.
Принадлежит:

The present technology is generally directed to coal charging systems used with coke ovens. In some embodiments, a coal charging system includes a charging head having opposing wings that extend outwardly from the charging head, leaving an open pathway through which coal may be directed toward side edges of the coal bed. In other embodiments, an extrusion plate is positioned on a rearward face of the charging head and oriented to engage and compress coal as the coal is charged along a length of the coking oven. In other embodiments, charging plates extend outwardly from inward faces of opposing wings. 1. (canceled)2. (canceled)3. (canceled)4. (canceled)5. (canceled)6. (canceled)7. (canceled)8. (canceled)9. (canceled)10. (canceled)11. (canceled)12. (canceled)13. (canceled)14. (canceled)15. (canceled)16. (canceled)17. (canceled)18. (canceled)19. (canceled)20. (canceled)21. (canceled)22. (canceled)23. (canceled)24. (canceled)25. (canceled)26. (canceled)27. (canceled)28. A coal charging system , the system comprising:an elongated charging frame having a distal end portion, proximal end portion, and opposite sides;a charging head operatively coupled with the distal end portion of the elongated charging frame; the charging head including a planar body residing within a charging head plane and having an upper edge portion, lower edge portion, opposite side portions, a front face, and a rearward face;an extrusion plate operatively coupled with the rearward face of the charging head; the extrusion plate having a coal engagement face that is oriented to face rearwardly and downwardly with respect to the charging head; anda charging conveyor operatively coupled with the elongated charging frame and having a distal end positioned adjacent and in open fluid communication with the coal engagement face of the extrusion plate so that coal is deposited immediately behind the coal engagement face of the extrusion plate.29. The coal charging system of wherein the extrusion plate ...

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Номер записи: 57
30-09-2021 дата публикации

CONTROLLING COKE MORPHOLOGY WITH SULFUR

Номер: US20210301211A1
Автор: Edmond Kazem V., Seider Sebastin K., Smith Stuart E.
Принадлежит:

Systems and methods are provided for controlling the morphology of coke produced during delayed coking. The morphology control is achieved in part by introducing elemental sulfur into the coker feedstock prior to coking. The elemental sulfur can be introduced into the feed under conditions so that the sulfur is well-dispersed within the feed for a sufficient period of time. This can allow for relatively even reaction of sulfur with components throughout the feed, resulting in a relatively small, uniform domain size distribution for the coke produced during delayed coking. This coke can correspond to shot coke. By producing coke with a small and relatively uniform domain size distribution, the risk of uneven heating within the coke can be reduced or minimized. 1. A method for controlling coke morphology during delayed coking , comprising:providing a coker feedstock that forms transition coke under standard delayed coking conditions;mixing the coker feedstock with 0.5 wt % to 5.0 wt % of elemental sulfur to form a mixed coker feedstock;maintaining the mixed coker feedstock at a temperature of 160° C. to 260° C. for 2.0 hours to 5 days to form a treated coker feedstock; andexposing the treated coker feedstock to second delayed coking conditions to form a coker effluent and treated coke comprising shot coke.2. The method of claim 1 , wherein the treated coke further comprises a lognormal domain size distribution having a value of a shape parameter σ of 0.30 or less and a value of a location parameter μ of 1.85 or less.3. The method of claim 1 , wherein the provided coker feedstock forms transition coke under standard delayed coking conditions comprising a lognormal domain size distribution having a value of a location parameter μ between 1.85 and 2.10.4. The method of claim 1 , wherein the standard delayed coking conditions comprise a temperature of 475° C. and 150 kPa-g.5. The method of claim 1 , wherein the second delayed coking conditions comprise a temperature of ...

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Номер записи: 58
21-10-2021 дата публикации

GAS INJECTOR WITH BAFFLE

Номер: US20210322934A1
Автор: GEORGE Rene, HAWRYLCHAK LARA, MOFFATT STEPHEN, Olsen Christopher S., Pandey Vishwas Kumar, PRADHAN Kailash, Shah Kartik, SHONO Eric Kihara, Swenberg Johanes F., TALLAVARJULA Sairaju
Принадлежит:

Gas injectors for providing uniform flow of fluid are provided herein. The gas injector includes a plenum body. The plenum body includes a recess, a protrusion adjacent to the recess and extending laterally away from the plenum body, and a plurality of nozzles extending laterally from an exterior surface of the plenum body. The plenum body has a plurality of holes in an exterior wall of the plenum body. Each nozzle is in fluid communication with an interior volume of the plenum body. By directing the flow of fluid, the gas injector provides for a uniform deposition. 1. A gas injector comprising: a top surface and a bottom surface opposite the top surface;', 'a recess formed into the top surface; and', at least one hole formed within a divider; and', 'a baffle adjacent the at least one hole, wherein the at least one hole provides fluid communication between an interior volume of the plenum body and the baffle, and wherein the interior volume extends from the recess, through the plenum body and the lower surface, and into the protrusion; and', 'an opening formed through a side wall of the protrusion and in fluid communication with the interior volume., 'a protrusion extending laterally away from the bottom surface of the plenum body, wherein the protrusion comprises], 'a plenum body, wherein the plenum body comprises2. The gas injector of claim 1 , wherein the baffle comprises a first extension and a second extension orthogonal the first extension.3. The gas injector of claim 2 , wherein the first extension connects to a bottom surface of the protrusion.4. The gas injector of claim 3 , wherein the second extension is spaced from the protrusion by a distance of about 0.04 inches to about 0.05 inches.5. The gas injector of claim 1 , wherein the divider has a plurality of holes that provide fluid communication between the first volume and the second volume.6. The gas injector of claim 5 , wherein the plurality of holes is disposed on a bottom surface of the protrusion.7. ...

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Номер записи: 59
21-10-2021 дата публикации

DEVICE FOR DISPENSING A FLUID, WHICH DEVICE CAN BE ARRANGED IN A REACTOR COMPRISING A FIXED CATALYTIC BED

Номер: US20210322942A1
Автор: BOUTROT Catherine, LE COZ Jean-Francois
Принадлежит: AXENS

The invention relates to a device (D) for distributing a fluid, which is able to be arranged in a fixed catalytic bed (C, C) of a reactor (R), said device comprising 232210ab. The device as claimed in claim 1 , characterized in that it comprises a plurality of distribution means () claim 1 , a plurality of manifold means (; ) claim 1 , and transfer means ();and in that:{'b': 2', '2, 'i': a', 'b, 'said manifold means (; ) are arranged one below the other,'}{'b': 10', '2', '2, 'i': a', 'b, 'said transfer means () provide the fluidic connection between the plurality of the manifold means (; ).'}3212bb. The device as claimed in claim 1 , wherein the manifold means for collecting together said fluid comprise at least one tube or an array of tubes () claim 1 , to which the pipes of the conveying means () are connected claim 1 , said tube or tubes () being closed at their ends.42b. The device as claimed in claim 1 , wherein said array of tubes () is arranged in the form of a cross claim 1 , a network claim 1 , a grid or a star.521a. The device as claimed in claim 1 , wherein the manifold means for collecting-together said fluid comprise at least one ring () claim 1 , preferably of toric or oval or polygonal shape claim 1 , to which the pipes () of the conveying means are connected.611022ab. The device as claimed in claim 1 , wherein said fluid conveying means () and/or the transfer means () extend along an axis z and each of said fluid-collecting manifold means (; ) extend in a plane (P) claim 1 , such that the axis (z) and the plane (P) form an angle (a) comprised between 60 and 120 degrees claim 1 , preferentially an angle of 90 degrees.75. The device as claimed in claim 1 , wherein said means for generating a local pressure drop comprise a restriction in the cross section for passage of the fluid of the restriction orifice () claim 1 , local narrowing or bellows type.8322ab. The device as claimed in claim 1 , wherein said fluid distribution means comprise a plurality of ...

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Номер записи: 60
29-09-2016 дата публикации

Method for producing graphite and particulates for graphite production

Номер: US20160280549A1
Автор: Kunihiko Satou, Takashi Maeda
Принадлежит: JX Nippon Oil and Energy Corp

Provided are a method for producing artificial graphite through a vertical graphitization furnace with easy circulation of inert gas, uniform heating and no damage to the furnace; and particulates used therefor. The method comprises steps of: introducing graphitizable particulates having average particle diameter of 3 to 30 mm into an inside of the furnace from upper part thereof, heating the particulates at 2200° C. to 3200° C. while making inert gas flow from lower part toward upper part thereof to graphitize the particulates, and removing the graphite through lower part thereof. The particulates have average particle diameter of 3 to 30 mm and are obtained by granulating mixture comprising 100 wt parts of graphitizable carbonaceous substance powder having average particle diameter of 10 to 20 μm, 3 to 20 wt parts of binder decomposable at lower than 1000° C., and 5 to 30 wt parts of liquid which can dissolve the binder.

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Номер записи: 61
27-09-2018 дата публикации

REACTOR

Номер: US20180272249A1
Автор: CHOI Jun Won, Im Ye Hoon, KANG Chang Hoon, KEUM Myeong Yeon, KIM Dae Hun, Kim Seong Gu, YOON Seung Hyun
Принадлежит:

The present invention relates to a reactor, and according to one aspect of the present invention, there is provided a reactor comprising a housing provided with a reaction space, a tube disposed inside the housing, an impeller provided inside the housing to allow reactants in the reaction space to flow into and out of the tube and a nozzle provided to spray a liquid from the reaction space toward the housing wall surface side. 1. A reactor comprising a housing provided with a reaction space;a tube disposed inside said housing;an impeller provided inside the housing to allow reactants in the reaction space to flow into and out of the tube; anda nozzle provided to spray a liquid from the reaction space toward the housing wall surface side.2. The reactor according to claim 1 , whereinthe nozzle is provided such that a jetting port is located at 5% or less of the distance between the housing wall surface and the tube.3. The reactor according to claim 1 , whereinthe nozzle is provided to spray the liquid toward the housing wall surface side after being extended from the housing wall surface toward the tube side.4. The reactor according to claim 3 , whereinthe nozzle is provided to have a bent part.5. The reactor according to claim 1 , whereinthe length of the nozzle is 5% or less of the distance between the housing wall surface and the tube.6. The reactor according to claim 1 , whereinthe reactor is provided such that in the reaction space, a crystallization reaction takes place, andthe nozzle sprays the liquid for eliminating crystallization heat.7. The reactor according to claim 6 , whereinthe nozzle is provided so that vapor generated by vaporization of the liquid sprayed from the nozzle during the crystallization reaction rises adjacent to the wall surface of the housing.8. The reactor according to claim 1 , whereinthe tube has a hollow opening along the height direction of the housing.9. The reactor according to claim 8 , whereinthe impeller is disposed inside the ...

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Номер записи: 62
27-08-2020 дата публикации

DEVICE AND METHOD FOR THERMAL OR THERMO-CHEMICAL TREATMENT OF MATERIAL

Номер: US20200269205A1
Автор: Esfehanian Arian, Neubauer Michael, Vervoort Peter
Принадлежит:

The invention relates to a device for the thermal or thermo-chemical treatment, more particularly calcination, of material (), more particularly battery cathode material (), comprising a housing (), in which a process space () is located. The material (), or carrying structures () loaded with the material (), can be conveyed in a conveying direction () into or through the process space () by means of a conveying system (). A process space atmosphere () prevailing in the process space () can be heated by means of a heating system (). There is a process gas system (), by means of which a process gas () can be fed to the process space (), said process gas being required for the thermal treatment of the material (). The process gas system () comprises a plurality of local injection units (), which are arranged and configured such that process gas () can be released in a targeted manner onto the material () or onto the carrying structures () loaded with material (), the process gas being released in a plurality of local process gas streams (), each having a main stream direction (). The invention also specifies a method for the thermal or thermo-chemical treatment of material (), in which process gas () is released in a targeted manner onto the material () or onto the carrying structures () loaded with material (), the process gas being released in a plurality of local process gas streams (), each having a main stream direction (). 1. An apparatus for thermal or thermochemical treatment of material , comprisinga) a housing;b) a process chamber within the housing;c) a conveying system, by means of which the material or support structures laden with the material can be conveyed in a conveying direction into or through the process chamber;d) a heating system, by means of which a process chamber atmosphere present in the process chamber can be heated up;e) a process gas system, by means of which the process chamber can be supplied with a process gas required for the thermal ...

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Номер записи: 63
27-08-2020 дата публикации

ESTERIFICATION UNIT FOR PRODUCING CRUDE METHYL METHACRYLATE, ESTERIFICATION PROCESS USING SAID UNIT AND PLANT COMPRISING SAID UNIT

Номер: US20200270195A1
Автор: Bernardin Yves, Billon Romain, Marcarian Xavier, Vallet Florent
Принадлежит:

The invention relates to an esterification unit () and esterification process for producing crude methyl methacrylate (MMA) from methacrylamide (MAM), which enable particularly to improve the yield, meaning that the organics spent acids are low; and at the same time, providing crude MMA with rather good quality, meaning that MMA concentration in crude MMA is rather high and preferably from 50 wt % to 80 wt %. According to the invention, the esterification unit comprises esterification reactors ( (or ) set up in a serial way so that there is a counter current flow between gaseous phase and liquid phase, the liquid phase flowing from first reactor () of the series to last reactor ( (or )), and the gaseous phase flowing from reactor to first reactor (). 111234511. An esterification process for producing crude methyl methacrylate (MMA) from methacrylamide (MAM) , and at least methanol and water comprising a series of linked reactors ( , . . . n , n+1 , . . . N) , wherein “n” represents the number of each reactor in the series of reactors ( , , , , etc. , and “N” represents the last reactor in the series , each reactor having an upper part and a lower part , wherein the reactors are set up in a serial way so that there is a counter current flow between a gaseous phase and a liquid phase , the liquid phase flowing from a first reactor () of the series to a last reactor (N) , and the gaseous phase flowing from the last reactor (N) to the first reactor () , said process comprising the steps of:a) introducing methacrylamide, methanol and water through lateral inlets, into a lower part of the first reactors,b) extracting a gaseous phase from the top of the reactors and introducing said gaseous phase of reactor n+1 into reactor n,c) extracting the liquid phase from the bottom of the reactors and,d) introducing said liquid phase of reactor n the reactor n+1, ande) introducing steam laterally into the last reactor.2. The esterification process for producing crude methyl ...

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Номер записи: 64
05-10-2017 дата публикации

IN SITU MONITORING OF COKE MORPHOLOGY IN A DELAYED COKER USING AC IMPEDANCE

Номер: US20170284991A1
Автор: Song Limin
Принадлежит:

Methods and systems for in situ monitoring of coke morphology in a delayed coking unit. At least one transmitting electrode and at least one receiving electrode are utilized to transmit AC current across coke being formed within the delayed coking unit. An impedance analyzer can be used to measure the impedance encountered between the transmitting electrode and the receiving electrode. This measure impedance is compared to an impedance curve comprising known impedance values for different coke morphologies to determine the morphology of coke being formed in the delayed coking unit. 1. A method for monitoring coke morphology in situ in a delayed coking unit containing coke , comprising:providing a transmitting electrode;providing a receiving electrode;transmitting an AC current at a frequency from the transmitting electrode to the receiving electrode; wherein the AC current traverses the coke within the delayed coking unit;measuring an impedance between the transmitting electrode and the receiving electrode across the coke at the frequency; andcomparing the measured impedance to an impedance curve to determine the coke morphology within the delayed coking unit.2. The method of . further comprising providing at least one additional receiving electrode.3. The method of claim 1 , further comprising at least one additional transmitting electrode.4. The method of claim 1 , wherein the transmitting electrode and receiving electrode are located within the delayed coking unit.5. The method of claim 2 , further comprising at least one additional transmitting electrode claim 2 , wherein each transmitting and receiving electrode are operated in pairs.6. The method of claim 1 , further comprising transmitting an AC current at at least one additional frequency from the transmitting electrode to the receiving electrode.7. The method of claim 1 , wherein the frequency is between 10-10 claim 1 ,000 Hz.8. The method of claim 6 , wherein the frequency is between 10-1 claim 6 ,000 Hz.9 ...

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Номер записи: 65
08-11-2018 дата публикации

Hydrogen Sulfide Production Process and Related Reactor Vessels

Номер: US20180319663A1
Автор: HASENBERG Daniel M., Mertens Ives, Pauwels Alex
Принадлежит:

The present invention discloses a hydrogen sulfide reactor vessel with an external heating system that is conductively and removably attached to an exterior portion of the reactor vessel. Also disclosed are processes for producing hydrogen sulfide utilizing the reactor vessel. 116-. (canceled)17. A HS production process comprising:controlling a reaction chamber containing liquid sulfur at a start-up temperature above the melting point of sulfur with an external heating system comprising a heated reactor conduit conductively and removably attached to an exterior surface of the reaction chamber;(ii) adding liquid sulfur to the reaction chamber to a level sufficient to immerse an internal heating system positioned within the reaction chamber;(iii) engaging the internal heating system to reach and maintain an operating temperature of the liquid sulfur of at least about 300° C.;{'sub': '2', '(iv) adding a hydrogen-containing gas into the liquid sulfur and reacting to produce HS; and'}(v) optionally, discontinuing the operation of the external heating system.18. The process of claim 17 , wherein:the start-up temperature is at least about 120° C.;the operating temperature is in a range from about 350° C. to about 600° C.; and{'sub': '2', 'the hydrogen-containing gas comprises H.'}19. The process of claim 17 , wherein the process comprises discontinuing the operation of the external heating system in step (v).20. The process of claim 17 , wherein:the process does not include a catalyst; andthe process does not employ an internal steam coil heating apparatus or a heating jacket or steam jacket on the exterior surface of the reaction chamber.21. The process of claim 17 , further comprising a step of purifying the HS by removing at least a portion of CS claim 17 , and/or at least a portion of H claim 17 , and/or at least a portion of sulfur vapor claim 17 , from the HS.22. The process of claim 21 , wherein HS is produced at a purity of at least about 95 wt. % HS.23. The ...

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Номер записи: 66
23-11-2017 дата публикации

SYSTEMS FOR PRODUCING ANODE GRADE COKE FROM HIGH SULFUR CRUDE OILS

Номер: US20170335199A1
Автор: Iqbal Rashid
Принадлежит:

Methods and systems for producing anode grade coke are disclosed, which allow anode grade coke to be produced from crude oil having a high sulfur content. A fraction of the resid is hydrotreated while another fraction of the resid is treated in a solvent deasphalting unit. A synthetic stream is provided by blending hydrotreated resid with one or more streams from the deasphalting unit. The synthetic stream is fed to an anodic coker unit. 1. A system for producing anode grade coke comprising:a vacuum distillation tower,a hydroprocessing unit;a solvent deasphalting unit; andan anode coker; whereinfeed to the anode coker comprises bottoms from the vacuum distillation tower, hydrotreated resid from the hydroprocessing unit, and a stream from the deasphalting unit.2. The system of claim 1 , wherein feed to the solvent deasphalting unit comprises bottoms from the vacuum distillation tower.3. The system of claim 1 , further comprising an atmospheric distillation tower.4. The system of claim 3 , wherein feed to the hydroprocessing unit comprises bottoms from the atmospheric distillation tower.5. The system of claim 3 , wherein feed to the solvent deasphalting unit comprises bottoms from the atmospheric distillation tower.6. The system of claim 1 , wherein the solvent deasphalting unit comprises a residuum oil supercritical extraction process.7. The system of claim 1 , wherein the stream from the deasphalting unit comprises a resins stream.8. The system of claim I claim 1 , wherein the stream from the deasphalting unit comprises a deasphalted oil stream.9. The system of claim 1 , wherein the stream from the deasphalting unit comprises two or more of a deasphalted oil stream claim 1 , a resins stream claim 1 , and an asphaltene stream.10. The system of claim 1 , wherein the anode coker is configured to produce anode grade coke.11. The system of claim 1 , wherein the anode coker is configured to produce coke comprising less than 3 wt. % sulfur.12. A method for producing anode ...

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Номер записи: 67
31-10-2019 дата публикации

NOZZLE FOR A DOWN-FLOW HYDROPROCESSING REACTOR

Номер: US20190329203A1
Автор: Breig Timothy D., Song Steven Xuqi
Принадлежит:

An improved nozzle device for a down-flow hydroprocessing reactor is disclosed. The down-flow nozzle is useful in the petroleum and chemical processing industries in catalytic reactions of hydrocarbon feedstocks in the presence of hydrogen, at an elevated temperature and pressure, to provide for the mixing and distribution of gas and liquid to reactor catalyst beds. Typical hydroprocessing applications include hydrotreating, hydrofinishing, hydrocracking and hydrodewaxing.

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Номер записи: 68
07-12-2017 дата публикации

PROCESS FOR SEPARATING COMPONENTS OF A POLYMER-MONOMER MIXTURE OBTAINED BY HIGH-PRESSURE POLYMERIZATION OF ETHYLENICALLY UNSATURATED MONOMERS

Номер: US20170348658A1
Автор: Deuerling Michael, Fibla Claudio, Finette Andre-Armand, Groos Georg, Khayrullin Danir, Littmann Dieter, Mohrbutter Juergen, Wolf Christoph, Wolfram Sven
Принадлежит: BASELL POLYOLEFINE GMBH

A process for separating polymeric and gaseous components of a polymer-monomer mixture at a pressure of from 0.12 MPa to 0.6 MPa and a temperature of from 120° C. to 300° C. in a separation vessel is provided. The separation vessel has a vertically arranged cylindrical shape with a ratio of length to diameter L/D of from 0.6 to 10 and an inlet pipe capable of introducing the polymer-monomer mixture into the separation vessel which the inlet pipe extends vertically from the top of the separation vessel into the separation vessel. Further a process for preparing ethylene homopolymers or copolymers from ethylenically unsaturated monomers in the presence of free-radical polymerization initiators at temperatures from 100° C. to 350° C. and pressures in the range of from 110 MPa to 500 MPa comprising such a process for separating a polymer-monomer mixture is provided. 1. A process for separating a polymer-monomer mixture comprising polymeric components and gaseous components into a liquid fraction and a gaseous fraction , the process comprising the steps of:(i) introducing the polymer-monomer mixture into a separation vessel;(ii) separating the polymer-monomer mixture at a pressure of from 0.12 MPa to 0.6 MPa and a temperature of from 120° C. to 300° C. into a gaseous fraction and a liquid fraction;(iii) withdrawing the gaseous fraction from the top of the separation vessel; and(iv) withdrawing the liquid fraction from the bottom of the separation vessel,wherein the polymeric components of the mixture are obtained by high-pressure polymerization of ethylenically unsaturated monomers in the presence of at least one free-radical polymerization initiator,and whereina) the separation vessel has a vertically arranged cylindrical shape with a ratio of length to diameter L/D of from 0.6 to 10;b) the separation vessel is equipped with an inlet pipe capable of introducing the polymer-monomer mixture into the separation vessel;c) the inlet pipe extends vertically from the top of ...

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Номер записи: 69
21-12-2017 дата публикации

Retractable Center Feed Injection Device

Номер: US20170362510A1
Автор: Krause Kenneth, Lah Ruben F., Larsen Gary
Принадлежит:

A retractable center feed injection device can be employed to feed residual oil into a coke drum as part of a delayed coking process. The retractable center feed injection device can include a housing within which the injection nozzle slides between an extended and a retracted position. A feed inlet is positioned on an opposite side of the coke drum from the retractable center feed injection device. When in the extended position, the injection nozzle can couple with the feed inlet and thereby form an extension of the feed inlet into the center of the coke drum. In this way, the residual oil never flows through the housing. 1. A retractable center feed injection device for use on a coke drum comprising:a housing configured to couple to a sidewall of a coke drum in alignment with a first opening in the sidewall;an injection nozzle contained within the housing, the injection nozzle having a first end and a second end, the injection nozzle being configured to slide between a retracted position and an extended position in which the first end extends into the coke drum; andan actuator that is coupled to the second end of the injection nozzle and configured to slide the injection nozzle between the retracted position and the extended position;wherein the injection nozzle includes a chamber positioned towards the first end and having one or more outlet openings that are oriented into the drum and an inlet opening that extends out through the first end such that residual oil can be flowed into the chamber via the inlet opening and out of the chamber via the one or more outlet openings.2. The retractable center feed injection device of claim 1 , further comprising:a feed inlet configured to couple to the sidewall of the coke drum in alignment with a second opening in the sidewall, the second opening being opposite the first opening, the first end of the injection nozzle coupling with the feed inlet when the injection nozzle is in the extended position.3. The retractable ...

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Номер записи: 70
21-11-2019 дата публикации

METHOD AND SYSTEM FOR OPTIMIZING COKE PLANT OPERATION AND OUTPUT

Номер: US20190352568A1
Автор: Brombolich Jeffrey Scott, Choi Chun Wai, Glass Edward A., Kesavan Parthasarathy, Mrozowicz Richard Alan, Quanci John Francis, Russell Katharine E., Vichilvongsa Khambath
Принадлежит:

The present technology is generally directed to methods of increasing coal processing rates for coke ovens. In various embodiments, the present technology is applied to methods of coking relatively small coal charges over relatively short time periods, resulting in an increase in coal processing rate. In some embodiments, a coal charging system includes a charging head having opposing wings that extend outwardly and forwardly from the charging head, leaving an open pathway through which coal may be directed toward side edges of the coal bed. In other embodiments, an extrusion plate is positioned on a rearward face of the charging head and oriented to engage and compress coal as the coal is charged along a length of the coking oven. In other embodiments, a false door system includes a false door that is vertically oriented to maximize an amount of coal being charged into the oven. 1. A method of increasing a coal processing rate of a coke oven , the method comprising:positioning a coal charging system, having an elongated charging frame and a charging head operatively coupled with a distal end portion of the elongated charging frame, at least partially within a coke oven having a maximum designed coal charge capacity, defined as a maximum volume of coal that can be charged into the coke oven according to a width and height of the coke oven multiplied by a maximum bed height, defined by a height of downcomer openings, formed in opposing side walls of the coke oven, above a coke oven floor, and a maximum coking time associated with the maximum designed coal charge, wherein the maximum designed coking time is defined as the amount of time required to fully coke the maximum designed coal charge;charging coal into the coke oven with the coal charging system in a manner that defines a first operational coal charge that is less than the maximum designed coal charge capacity;coking the first operational coal charge in the coke oven until it is converted into a first coke bed ...

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Номер записи: 71
05-12-2019 дата публикации

SYSTEM FOR PRODUCING AN AMERICAN PETROLEUM INSTITUTE STANDARDS GROUP III BASE STOCK FROM VACUUM GAS OIL

Номер: US20190367821A1
Автор: Cowart Benjamin, Lappin Frank, Peel David, Smith James Craig
Принадлежит:

A system for producing American Petroleum Institute Standards Group III Base Stock from vacuum gas oil, by injecting hydrogen, heating, partially saturating the vacuum gas oil through a plurality of hydrogen reactors connected in series with a liquid hourly space velocity (LHSV)of from 0.5 to 2.5, forming a saturated heated base oil, and coproduct. The system fractionates the saturated heated base oil to while simultaneously refluxing a cooled fuel oil fraction forming an American Petroleum Institute Standards Group III Base Stock with less than 0.03% sulfur, with greater than 90% saturates and a viscosity index greater than 120 as defined by ASTM D-2270, a viscosity from 2 to 10 centistokes as defined by ASTM D-445 a boiling range from 600 degrees F. to 1050 degrees F., and a cold crank viscosity (CCS) between 1200 and 5000 centipoise at −25 degrees C. and as defined by ASTM D-5293. 1. A system for producing an American Petroleum Institute Standards Group III Base Stock from vacuum gas oil , comprising:a. a conduit receiving a vacuum gas oil with a boiling point range from 450 degrees Fahrenheit to 1050 degrees Fahrenheit as defined by ASTM D-86;b. a first heater fluidly connected to the conduit increasing temperature of the vacuum gas oil to a temperature from 450 degrees Fahrenheit to 600 degrees Fahrenheit, forming a heated vacuum gas oil;c. a pump installed prior to the first heater, a fresh hydrogen injector and a recycle hydrogen injector simultaneously increasing pressure on the heated vacuum gas oil from 50 psig to a pressure from 1000 psig and 1500 psig by injection of hydrogen, wherein the fresh hydrogen injector comprises a nozzle that engages a flow control valve further in communication with a flow meter and a high-pressure pump and a hydrogen vaporizer for receiving liquid hydrogen from a liquid hydrogen reservoir;{'sup': '−1', 'd. a plurality of hydrogen reactors connected in series, each to a heater, each hydrogen reactor having a liquid hourly ...

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Номер записи: 72
12-12-2019 дата публикации

APPARATUS FOR PRODUCING CARBON NANOTUBE AGGREGATE

Номер: US20190374918A1
Автор: Jeong Young Jin, SONG Hyeon Jun
Принадлежит:

A carbon nanotube assembly manufacturing apparatus includes a synthesis furnace having a carbon nanotube synthesis space inside, and a gas supply unit that is disposed at a lower portion of the synthesis furnace and ejects an inert gas through a plurality of nozzles to converge carbon nanotubes discharged from the synthesis furnace. The plurality of nozzles are arranged along an arc of the gas supply unit so as to surround the carbon nanotubes discharged from the synthesis furnace and are individually adjustable. 1. A carbon nanotube assembly manufacturing apparatus comprising:a synthesis furnace having a carbon nanotube synthesis space inside; anda gas supply unit that is disposed at a lower portion of the synthesis furnace and ejects an inert gas through a plurality of nozzles to converge carbon nanotubes discharged from the synthesis furnace,wherein the plurality of nozzles are arranged along an arc of the gas supply unit so as to surround the carbon nanotubes discharged from the synthesis furnace and are individually adjustable.2. The carbon nanotube assembly manufacturing apparatus according to claim 1 , wherein the gas supply unit is spaced apart from a center of the synthesis furnace by a predetermined distance claim 1 , is located so as to have a concentric relationship with the center claim 1 , and is a tubular member formed in a circular shape.3. The carbon nanotube assembly manufacturing apparatus according to claim 1 , wherein the nozzle has one end fixed to the gas supply unit and the other end extended toward a center of the gas supply unit.4. The carbon nanotube assembly manufacturing apparatus according to claim 1 , wherein the nozzle is adjustable to have an acute angle toward a center of the gas supply unit in any one direction of an upper side claim 1 , a lower side claim 1 , a left side claim 1 , and a right side.5. The carbon nanotube assembly manufacturing apparatus according to claim 1 , wherein the nozzle is disposed to be inclined in a ...

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Номер записи: 73
12-12-2019 дата публикации

Method of Delayed Coking of Petroleum Residues

Номер: US20190375989A1
Автор: Yurchenko Nikolay
Принадлежит:

The delayed coking method includes directing a heated secondary feedstock, which contains heated primary feedstock and recirculate, from a reaction furnace to a coking chamber. Vapor-liquid coking products formed in the coking chamber are then directed to a fractionation column, which fractionates hydrocarbon gas, gasoline, light and heavy gas oils, and bottom residues. Heavy gas oil from the fractionation column is directed to a thermal cracking furnace, the products of which are cooled by cooled light gas oil and directed to an evaporator for separation. In the evaporator, gases and light boiling products are removed by evaporation and returned to the fractionation column, and the remaining distillate cracking residue is separated and used as a component of the recirculate, along with bottom residues from the fractionation column. The resulting process produces high quality and high yield needle and anode cokes. 1. A method for delayed coking of petroleum residues , comprising:(a) mixing a primary feedstock and a recirculate in a vessel to form a secondary feedstock;(b) heating the secondary feedstock in a furnace;(c) directing the heated secondary feedstock to a coking chamber to form coke and vapor-liquid coking products;(d) fractionating the vapor-liquid coking products in a fractionation column to produce gas, gasoline, light and heavy gas oils, and bottom residue;(e) thermally cracking the fraction of heavy gas oil to produce gas, gasoline, light gas oil, and distillate cracking residue;(f) evaporating the gas, gasoline, and light gas oil from the distillate cracking residue; and(g) directing the separated distillate cracking residue to the vessel as a component of the recirculate.2. The method of claim 1 , further comprising directing the fraction of bottom residue from the fractionation column to the vessel as a component of the recirculate.3. The method of claim 1 , further comprising cooling a portion of the fraction of light gas oil from the ...

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Номер записи: 74
19-12-2019 дата публикации

ELIMINATION OF POLYMER FOULING IN FLUIDIZED BED GAS-PHASE FINES RECOVERY EDUCTORS

Номер: US20190382512A1
Автор: Hendrickson Gregory G., Lowell Jeffrey S., Price Ralph J.
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

An eductor, a process and apparatus for gas phase polymerization of olefins in a polymerization reactor are disclosed. The process and apparatus employ an eductor which has an inlet which makes a bend of less than about 90° toward the outlet after entering the mixing chamber of the eductor. 128.-. (canceled)29. An eductor comprising: a first inlet and a first outlet spaced apart from the first inlet along a central axis, and', 'a sidewall circumscribing the central axis and defining a mixing chamber; and, 'a first tubular body having a hollow interior and comprising'}a second tubular body having a hollow interior and comprising a second inlet and a spaced apart second outlet, wherein the second tubular body extends into the mixing chamber through the sidewall of the first tubular body between the first inlet and the first outlet, andwherein the second tubular body comprises a bend of less than 90° toward the first outlet after extending into the mixing chamber.30. The eductor of claim 29 , wherein the second tubular body makes a first bend of about 45° from perpendicular toward the first outlet before entering the mixing chamber and a second bend of about 45° toward the first outlet after entering the mixing chamber.31. The eductor of claim 29 , wherein the second tubular body is substantially parallel to the central axis at the second outlet.32. The eductor of claim 29 , wherein the first inlet is a solid fines inlet and the second inlet is a motive gas inlet.33. The eductor of claim 32 , wherein the second outlet further comprises a nozzle in the mixing chamber.34. The eductor of claim 29 , wherein the first inlet is a motive gas inlet and the second inlet is a solid fines inlet.35. The eductor of claim 29 , wherein the first tubular body and the second tubular body below the second bend after entering the mixing chamber are coaxial.36. The eductor of claim 29 , wherein the first tubular body is at least partially cylindrical in shape.37. The eductor of claim 29 , ...

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Номер записи: 75
17-12-2020 дата публикации

DELAYED COKING FURNACE FOR HEATING COKER FEEDSTOCK

Номер: US20200392414A1
Автор: Bhattacharyya Debasis, Das Satyen Kumar, KOTTAKUNA Arjun Kumar, MAZUMDAR Sanjiv Kumar, PRADEEP Ponoly Ramachandran, Prasad Terapalli Hari Venkata Devi, RAMAKUMAR Sankara Sri Venkata, Sau Madhusudan
Принадлежит:

A delayed coking furnace () for heating coker feedstock () is disclosed. The furnace () includes a first heating zone () adapted to provide heat to the coker feedstock () through a convective heat transfer and then a second heating zone () positioned below the first heating zone () and adapted to heat the coker feedstock () through radiative heat transfer, wherein the second heating zone () include a lower portion and an upper portion. Further, said furnace () includes a plurality of burners () located at the lower portion of the second heating zone () and at least one baffle () disposed in the upper portion of the second heating zone (). Further, the present disclosure provides that the at least one baffle () is adapted to increase a convective heat transfer coefficient associated with a flue gas flowing from the second heating zone () to the first heating zone (). 1. A delayed coking furnace for heating coker feedstock , the delayed coking furnace comprising:a first heating zone adapted to provide heat to the coker feedstock through convective heat transfer;a second heating zone positioned below the first heating zone and adapted to heat the coker feedstock through radiative heat transfer, wherein the second heating zone includes a lower portion and an upper portion;a plurality of burners located at the lower portion of the second heating zone;at least one baffle disposed in the upper portion of the second heating zone, wherein the at least one baffle is adapted to increase a convective heat transfer coefficient associated with a flue gas flowing from the second heating zone to the first heating zone.2. The furnace as claimed in claim 1 , wherein the coker feedstock is heated in a range of 380-420° C. by the flue gas flowing from the second heating zone.3. The furnace as claimed in claim 1 , wherein the furnace is configured to handle the coker feedstock upto 35 wt % Conradson Carbon Residue (CCR).4. The furnace as claimed in claim 1 , further comprising a ...

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Номер записи: 76
25-03-2010 дата публикации

Vorrichtung zum Einspritzen von fluiden Medien in den Prozeßraum eines Wirbelschichtbehälters

Номер: DE102008037998A1
Автор: Thomas Böckmann
Принадлежит: HEINEN GmbH

Bei einer Vorrichtung zum Einspritzen von fluiden Medien in den Prozeßraum eines Wirbelschichtbehälters mit einem wenigstens eine seitlich ausgerichtete Einspritzdüse aufweisenden Düsenstock sowie wenigstens einem an einer Behälteröffnung des Wirbelschichtbehälters festsetzbaren Durchlaßteil zur formschlüssigen Aufnahme des Düsenstockes sind das Durchlaßteil und der Düsenstock als Kolbenführung mit in Durchlaßrichtung verlaufenden Gleitflächen ausgebildet. Dabei weist der Düsenstock wenigstens eine die Einspritzdüse vollständig aufnehmende Vertiefung, und das Durchlaßteil wenigstens ein in seine Durchlaßöffnung integriertes Absperrorgan auf.

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Номер записи: 77
06-05-2021 дата публикации

Reactor for polymerization process

Номер: WO2021086678A1
Автор: Hari Nair, Kevin B. DALY, Vetkav R. Eswaran
Принадлежит: ExxonMobil Chemical Patents Inc.

In one embodiment, a reactor includes a reactor body and a reactor head. The reactor head has a reactor head body and one or more inlets disposed tangentially to the reactor head body. In one embodiment, a polymerization process for forming polymer includes introducing in a first direction a stream including a monomer. The stream and a catalyst system are flowed in a second direction through at least one internal heat exchanger. The second direction is substantially orthogonal to the first direction. The reaction zone includes at least one internal heat exchanger. At least a portion of the monomer of the stream is polymerized in the reaction zone to produce a polymer product. The polymer product is recovered from the reaction zone.

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Номер записи: 78
12-06-1997 дата публикации

Method of charging coke oven with coal

Номер: DE19545736A1
Автор: Dieter Dr Stalherm, Hans-Guenter Piduch, Oliver Kolassa, Rainer Dr Worberg
Принадлежит: Thyssen Still Otto Anlagentechnik GmbH

A bottom-heated coking oven is filled with coal by a method in which the coal outside the oven is dumped on to a base plate at uniform height and then compacted, the plate and compacted coal cake being pushed into the oven chamber. The plate is then removed. The coal cake is 500-1000 (600-800) mm high. Also claimed is an operating machine, which can be moved along a row of adjacent coking ovens, having a base plate (3) of the dimensions of the oven base which forms a shallow and large-area coal filling and compaction chamber with side walls (9, 10) and front and rear side walls. When the coal is charged into the oven chamber, the rear end wall and the base can be moved in the longitudinal direction jointly with the base plate.

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Номер записи: 79
01-06-2006 дата публикации

Process and device for producing horizontally tamped coal cakes

Номер: WO2006056286A1
Автор: Franz-Josef Schücker
Принадлежит: UHDE GMBH

A process and device are disclosed for producing horizontally tamped coal cakes for coking in the oven chamber of a coking oven, the coal cakes being formed in a compression mould by stationary compression tools which work in the horizontal direction and with a stroke having a strictly limited length. The compression mould has a sliding stop wall which is moved away from the compression tools as the coal cake grows, under the effect of a suitable antagonistic braking force.

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Номер записи: 80
18-12-1980 дата публикации

Coking coal compacting - by projection into mould through blades of centrifugal impellers, reduces machine stresses

Номер: DE2922861A1
Автор: Gerd Dipl Ing Veit
Принадлежит: SAARBERG INTERPLAN GmbH

A fine-grained coal blend which is to be used for charging coke ovens is compressed by transferring the coal blend from a continuous conveyor to one or more impellers, each with one or more blades. The impellers revolve opposite to the direction of free fall of the coal particles so that they are compacted into clumps. The centrifugal force accelerates the clumps and projects them into a compression mould, thus effecting a further compression by impact. Several impellers can be arranged on the same drive shaft, or several shafts, each with one or more impellers, can be arranged in parallel one after another. This method produces much less noise than the conventional stamping system. It results in less high stresses for the machine and mould use for the compaction; large quantities of a coal blend can be compressed in a very short time.

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Номер записи: 81
11-04-2002 дата публикации

Method and apparatus for coal coking

Номер: WO2002029345A1
Автор: Michael P. Barkdoll
Принадлежит: Sun Coke Company

The invention provides a coke oven charging machine (10) including a mobile frame (64) and a coke oven feed device (20) on the mobile frame. The coke oven feed device includes a movable, elongate charging plate (28) having a first end and a second end, retractable side-walls (48) adjacent the charging plate, first and second end walls (44 & 46) adjacent the first and second ends of the charging plate and a shuttle section adjacent the first end of the charging for spanning an area between the first end of the charging plate and an entrance to the oven. The shuttle section has opposed shuttle side walls (52) and a shuttle end wall (50). A charging plate moving device (60) is provided for moving the charging plate into and out of the oven. The charging machine apparatus provides a means for quickly charging coking ovens with a compacted coal charge so that lower quality coals may be used to make metallurgical coke.

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Номер записи: 82
20-11-2015 дата публикации

Method of slow coking

Номер: RU2568713C2
Автор: Кеннет А. КАТАЛА
Принадлежит: Ламмус Текнолоджи Инк.

FIELD: oil and gas industry. SUBSTANCE: inventions can be used in oil refining. Slow coking furnace (10) for heating of the input material to the slow coking temperature includes heater with zone of radiation heating (14), in which the heating coil (26) with multiple parallel pipes is located. In bottom part of the radiation heating zone (14) a section of the hearth burners is located, and in top part - section of wall burners. The section of the hearth burners includes multiple hearth burners (46) located near the hearth (42), for burning in the radiation heating zone (14). Multiple hearth burners (46) make and direct flame plumes upwards, at that each flame plume is in the plane mainly parallel to the plane in which the heating coil (26) containing multiple parallel pipes is suspended. Section of wall burners includes multiple wall burners (56) located near the opposite side walls (34, 36). EFFECT: inventions reduce time of the input material presence in the radiation heating zone, increase power and average length of stroke of the slow coking furnace, reduce pressure difference in the coil, and prevent or reduce early cracking inside the coil. 16 cl, 3 dwg, 2 tbl, 1 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 568 713 C2 (51) МПК C10B 55/00 (2006.01) C10G 9/20 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2012148245/05, 08.04.2011 (24) Дата начала отсчета срока действия патента: 08.04.2011 (72) Автор(ы): КАТАЛА Кеннет А. (US) (73) Патентообладатель(и): ЛАММУС ТЕКНОЛОДЖИ ИНК. (US) Приоритет(ы): (30) Конвенционный приоритет: R U 15.04.2010 US 61/324,625 (43) Дата публикации заявки: 20.05.2014 Бюл. № 14 (45) Опубликовано: 20.11.2015 Бюл. № 32 2 5 6 8 7 1 3 (56) Список документов, цитированных в отчете о поиске: US 6237545 B1, 29.05.2001. US 2008286706 A1, 20.11.2008. US 4698313 A, 06.10.1987. SU 986476 A1, 07.01.1983. RU 64413 U1, 27.06.2007. (85) Дата начала рассмотрения заявки PCT на национальной ...

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Номер записи: 83
28-03-2017 дата публикации

An assembly for reducing slurry pressure in a slurry processing system

Номер: CA2773896C
Автор: Leonard James Humphreys
Принадлежит: Ignite Resources Pty Ltd, Licella Fibre Fuels Pty Ltd, Licella Pty Ltd

An assembly (10) for reducing pressure of slurry exiting an outlet pipe (15) of a supercritical reactor (116), the assembly (10) including a sealed collection vessel (12) and an orifice assembly (14) forming an inlet of the collection vessel (12), wherein the orifice assembly (14) comprises a plurality of orifices (17 to 20) for parallel connection with the reactor outlet pipe (15) such that flow from the outlet pipe (15) can be directed to any one of the orifices (17 to 20).

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Номер записи: 84
24-06-2022 дата публикации

GAS/LIQUID OLIGOMERIZATION REACTOR COMPRISING A DOUBLE GAS/LIQUID DISTRIBUTOR

Номер: FR3117890A1
Автор: Alexandre VONNER, Ludovic Raynal, Pedro MAXIMIANO-RAIMUNDO
Принадлежит: IFP Energies Nouvelles IFPEN

La présente invention concerne un réacteur gaz/liquide d’oligomérisation d’éthylène gazeux comprenant un dispositif d’injection d’éthylène gazeux et un dispositif d’injection de liquide, lesdits dispositifs d’injection étant avantageusement agencés de manière à ce que l’injection du liquide puisse entrainer une diminution de la taille des bulles d’éthylène, par cisaillement, lors de l’injection de l’éthylène gazeux. Le réacteur gaz/liquide selon la présente invention peut être utilisé pour toute charge oléfinique gazeuse injectée dans une phase liquide. The present invention relates to a gas/liquid reactor for the oligomerization of gaseous ethylene comprising a device for injecting gaseous ethylene and a device for injecting liquid, said injection devices being advantageously arranged so that the injection of the liquid could lead to a reduction in the size of the ethylene bubbles, by shearing, during the injection of the gaseous ethylene. The gas/liquid reactor according to the present invention can be used for any gaseous olefin feedstock injected into a liquid phase.

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Номер записи: 85
24-06-2022 дата публикации

GAS/LIQUID OLIGOMERIZATION REACTOR COMPRISING A CENTRAL PIPE

Номер: FR3117891A1
Автор: Alexandre VONNER, Ludovic Raynal, Pedro MAXIMIANO-RAIMUNDO
Принадлежит: IFP Energies Nouvelles IFPEN

La présente invention concerne un réacteur gaz/liquide d’oligomérisation d’éthylène gazeux comprenant une conduite centrale délimitant à l’intérieur de l’enceinte du réacteur une zone centrale permettant un écoulement descendant et une zone externe permettant un écoulement ascendante, permettant ainsi d’augmenter le temps de parcours des bulles de gaz injecté dans la phase liquide, sans en augmenter le volume de la phase liquide et donc le volume du réacteur. The present invention relates to a gas/liquid reactor for the oligomerization of gaseous ethylene comprising a central pipe delimiting inside the enclosure of the reactor a central zone allowing a downward flow and an outer zone allowing an upward flow, thus allowing increase the travel time of the gas bubbles injected into the liquid phase, without increasing the volume of the liquid phase and therefore the volume of the reactor.

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Номер записи: 86
06-11-2013 дата публикации

Improved reactor feed nozzles

Номер: EP2658640A1
Автор: Michael A. Silverman, Stephen K. Pavel, Steven A. KALOTA
Принадлежит: Ivanhoe Energy Inc

Improved reactor feed nozzles are disclosed. According to one embodiment, a feed nozzle comprises an inner tubing encased within an outer heat shield tubing, a first circular hole fabricated in the inner tubing, the first circular hole having a first diameter and serving as a discharge hole, a second circular hole fabricated in the outer heat shield tubing, the second circular hole having a second diameter, wherein the second diameter is larger than the first diameter; and a welded tip for extending a flow path at a declining angle, the welded tip having a section extending at a predetermined angle from the inner tubing to the discharge hole.

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Номер записи: 87
21-04-2021 дата публикации

Device for mixing process fluid with initiator in a ldpe reactor

Номер: EP3808438A1
Автор: Christof Wurnitsch, Werner BILINA
Принадлежит: Borealis AG

The present invention relates to an initiator injection nozzle 1 for mixing an initiator with a process fluid. The initiator injection nozzle 1 comprises a body 10 comprising (i) a process fluid inlet port 11 to receive the process fluid and an outlet port 17, (ii) a process fluid flow passage 13 through which the process fluid traverses along a process fluid central flow axis 15 between the process fluid inlet port 11 and the outlet port 17, wherein the process fluid flow passage 13 is at least partially defined by a constricting portion 12, a throat 14, and an expanding portion 16, (iii) an initiator inlet 30 to receive the initiator and an initiator outlet 32, and (iv) an initiator fluid flow passage 34 through which the initiator traverses along an initiator central flow axis 35 between the initiator inlet 30 and the initiator outlet 32. The initiator injection nozzle 1 is characterised by a plurality of elongated vanes 20 provided within the constricting portion 12 and extending along the process fluid central flow axis 15, and in that each of the vanes 20 has a leading end 26, a trailing end 22 and a curved vane surface 21.

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Номер записи: 88
21-04-2021 дата публикации

Initiator injection nozzle

Номер: EP3808439A1
Автор: Christof Wurnitsch, Werner BILINA
Принадлежит: Borealis AG

The present inventon relates to an initiator injection nozzle 1 for mixing an initiator with a process fluid. The initiator injection nozzle 1 comprises a body 10 comprising (i) a process fluid inlet port 11 to receive the process fluid and an outlet port 17, (ii) a process fluid flow passage 13 through which the process fluid traverses along a process fluid central flow axis 15 between the process fluid inlet port 11 and the outlet port 17, (iii) an initiator inlet 30 to receive the initiator and an initiator outlet 32, and (iv) an initiator fluid flow passage 34 through which the initiator traverses along an initiator central flow axis 35 between the initiator inlet 30 and the initiator outlet 32. The initiator injection nozzle 1 is characterised in that at least one elongated vane 20 is provided within the process fluid flow passage 13 and extends along the process fluid central flow axis 15, and in that the initiator outlet 32 is disposed on a surface 24 of the vane 20.

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Номер записи: 89
08-04-2009 дата публикации

Mixing apparatus

Номер: EP2045002A1
Автор: designation of the inventor has not yet been filed The
Принадлежит: Ineos Europe Ltd

The present invention relates to an apparatus for mixing of a first gas and a second gas, which mixing apparatus comprises: i) a linear first tube (1) for supply of the first gas, said first tube comprising an inlet (2) for the first gas at an upstream end and tapering to form a nozzle (3) at a downstream end, said nozzle having an opening of internal area of less than 10mm 2 at the outlet for the first gas and providing a pressure drop in the supply of the first gas through said first tube, and ii) a linear second tube (4) for supply of the second gas, said second tube comprising an inlet (5) for the second gas at an upstream end, a first portion (6) which forms an annulus around the outer surface of the first tube upstream of the nozzle, which annulus has a length of 5 to 50 mm and a cross-section area of 2 to 10 times the area of the opening of the nozzle and which acts to provide a pressure drop in the supply of the second gas through said second tube, and a second portion (7) which forms a sheath around the nozzle (3) of the first tube (1) and which forms an area of expanded cross-section (8) compared to the annulus, and wherein: a) the nozzle and annulus are arranged such that the pressure drops caused in the supply of the first and second gases are in a ratio of 2:1 to 1:2, b) the angle of the external taper of the nozzle is less than 12° compared to the longitudinal axis of the first tube, and c) any change in diameter of second tube in the second portion is less than 12° compared to the longitudinal axis of the second tube.

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Номер записи: 90
01-06-1982 дата публикации

Processing of heavy high-sulfur crude oil

Номер: US4332671A
Автор: Lyndon D. Boyer
Принадлежит: Conoco Inc

Heavy high-sulfur crude oil is subjected to distillation to produce gas and liquid hydrocarbon products and a residuum. The gas and liquid products are desulfurized. Part of the residuum is coked in a delayed coker, and sulfur in the coke is removed by high temperature calcination. The remainder of the residuum is air-blown to produce an asphalt product, and sulfur recovered from the other products is added to the asphalt to produce a sulfur-enriched asphalt product.

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Номер записи: 91
10-12-2003 дата публикации

在炉膛中焦化的炼焦煤饼的制作方法和装置

Номер: CN1130442C
Автор: F·凯泽, P·格罗斯
Принадлежит: SAARTECH GESELLSCHAFT fur INDUSTRIE und BERGBAUTECHNOLOGIE MBH

本发明的目的是提出一种方法和相应的捣实装置来实现用已知的经济的捣实技术竖立生产的炼焦煤饼按要求的位置即平放在炉膛中，这个目的是这样实现的，炼焦煤饼(1)以较低的煤饼高度和较大的煤饼底面按熟知的方式竖立放在一捣实模中进行捣实，然后煤饼(1)留在该捣实模中，并通过一个装在捣实模上的功能完好的翻转装置和支持装置放到这样一个位置，在该位置内尚未脱模的炼焦煤饼(1)送入炉膛中，在炉膛中脱模并放到炉底上。本发明的捣实装置特别适用于上述目的，其特征为，在捣实机的捣实模上连接一个翻转装置和支持装置(3)，在该装置上这样布置一块装料底板(2)，使它同时作为捣实模和装料底板的一部分。

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Номер записи: 92
20-04-2012 дата публикации

Method for slow coking

Номер: RU2448145C1
Автор: Виктор Павлович Запорин, Геннадий Георгиевич Валявин, Игорь Викторович Бидило, Константин Геннадьевич Валявин
Принадлежит: Общество С Ограниченной Ответственностью "Проминтех"

FIELD: chemistry. SUBSTANCE: starting material is heated in a heat exchanger 1 to 230-270°C and then to 350-430°C in a furnace 2. The hot material is fed into the bottom part of an evaporator 3 and mixed with a recirculator - heavy coker gasoil to form secondary material which is heated to reaction temperature 460-510°C in a heating-reaction furnace 5, followed by coking in one of the alternately working coking chambers 6. The formed distilled products from chambers 6 are fed for fractionation into the bottom part of a fractionation column 4 to obtain gas, gasoline, light gasoil, heavy gasoil and still residue which is fed for mixing with hot secondary material before being fed into the coking chamber 6. The quality and amount of the still residue and heavy coker gasoil is regulated by varying the temperature at the first tray in the bottom part of the fractionation column 4 by feeding heavy coker gasoil as circulating reflux. EFFECT: longer time between repairs on the equipment and output of distilled products for producing engine fuel. 1 dwg, 3 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 448 145 (13) C1 (51) МПК C10B 55/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2010149133/05, 02.12.2010 (24) Дата начала отсчета срока действия патента: 02.12.2010 (45) Опубликовано: 20.04.2012 Бюл. № 11 (73) Патентообладатель(и): Общество с ограниченной ответственностью "Проминтех" (RU) Адрес для переписки: 129085, Москва, пр-кт Мира, 101, стр.1, ООО "Патентно-правовая компания "ВЕЛЛ", пат.пов. Н.Н. Андреевой получением газа, бензина, легкого газойля, тяжелого газойля и кубового остатка, который подают на смешивание с нагретым вторичным сырьем перед подачей в камеры 6 коксования. Качество и количество кубового остатка и тяжелого газойля коксования регулируют изменением температуры на первой тарелке в нижней части ректификационной колонны 4 путем подачи на нее в качестве циркуляционного орошения тяжелого газойля ...

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Номер записи: 93
24-04-2019 дата публикации

Method of producing oil needle coke

Номер: RU2686152C1
Автор: Александр Сергеевич Кондратьев, Владимир Александрович Будник, Марат Ринатович Смаков
Принадлежит: Общество с ограниченной ответственностью "ХАММЕЛЬ"

FIELD: oil, gas and coke-chemical industries.SUBSTANCE: invention relates to oil refining, in particular, to a method of producing high-quality oil needle coke for electrode industry. Method involves preparation of feedstock by mixing heavy pyrolysis resin and heavy gasoil of catalytic cracking in ratio of (1:10)–(10:1) and carrying out shallow visbreaking with high flavouring of feedstock at pressure 0.4-1.0 MPa and temperature 460–490 °C for 15–25 minutes, production of secondary raw material by mixing of obtained initial raw materials and gas oil of coking, which content in secondary raw materials is 10–30 %, heating of secondary raw material in furnace of delayed coking to temperature of 500–520 °C at pressure of 3.0–4.5 MPa, supply of secondary raw materials to coking chamber, coking by means of three reactors operating in parallel circuit with alternate loading of raw material, and obtaining of needle coke and coking distillate, which is supplied to lower part of rectification column for fractionation. At that, the gasoline fraction vapours and gaseous cracking products of the starting material obtained in the rectification column are condensed and collected in a collecting container, from where part of gasoline fraction is fed for irrigation of upper tray of rectification column, another part is supplied into feed stream as turbulence promoter of visbreaking furnace, and gases from collection vessel are cleaned from sulphur compounds with solution of alkali and diverted to fuel network.EFFECT: invention increases output of needle coke with high operating properties, as well as production of additional products in form of gasoline and fuel gas.1 cl, 1 dwg, 1 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 686 152 C1 (51) МПК C10B 55/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10B 55/00 (2019.02) (21) (22) Заявка: 2018146608, 24.12.2018 (24) Дата начала отсчета срока действия патента: 24.12.2018 ( ...

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Номер записи: 94
27-12-2008 дата публикации

Устройство и способ для горизонтального изготовления трамбованных угольных брикетов

Номер: RU2007123583A
Автор: Франц-Йозеф ШЮККЕР, Франц-Йозеф ШЮККЕР (DE)
Принадлежит: Уде Гмбх, Уде Гмбх (De)

1. Гидравлическое прессовальное устройство для изготовления уплотненного угольного брикета из сыпучего угольного материала для использования в коксовой печи, состоящее, по меньшей мере, из одного гидравлического пуансона, одной пресс-формы, одного вложенного на днище пресс-формы и извлекаемого поддона для брикета, одного расположенного над пресс-формой качающегося желоба, отличающееся тем, что пресс-форма образована из салазок или тележки, которая имеет стенки, днище и упорную стенку, над которой поперек к направлению ее движения расположен качающийся желоб, гидравлические цилиндры, которые закреплены стационарно и выполнены с возможностью перемещения головной части цилиндров в горизонтальном направлении и спрессовывания при прямолинейном движении поступающего из качающегося желоба угольного материала посредством головной части цилиндров поперек к загрузочному желобу и под ним насквозь к упорной стенке и насквозь под плоским кожухом брикета, причем предусмотрено торможение тележки с усилием, противоположным направлению прямолинейного движения гидравлических цилиндров, и кожух брикета, который примыкает непосредственно к загрузочному желобу, а также головная часть цилиндров и качающийся желоб ориентированы параллельно.2. Устройство по п.1, отличающееся тем, что головная часть цилиндров образована из вертикальной нажимной плиты и горизонтальной запорной плиты, причем выпуск качающегося желоба в положении покоя головной части цилиндров, которое представляет собой первое конечное положение, открыт полностью, а при прямолинейном движении головной части цилиндров запорная плита прогрессивно суж ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (11) 2007 123 583 (13) A (51) ÌÏÊ C10B 45/02 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÇÀßÂÊÀ ÍÀ ÈÇÎÁÐÅÒÅÍÈÅ (21), (22) Çà âêà: 2007123583/15, 27.10.2005 (71) Çà âèòåëü(è): ÓÄÅ ÃÌÁÕ (DE) (30) Êîíâåíöèîííûé ïðèîðèòåò: 23.11.2004 DE 102004056564.3 (72) Àâòîð(û): ØÞÊÊÅÐ Ôðàíö-Éîçåô (DE) (43) Äàòà ...

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Номер записи: 95
20-05-2014 дата публикации

Способ замедленного коксования

Номер: RU2012148245A
Автор: Кеннет А. КАТАЛА
Принадлежит: Ламмус Текнолоджи Инк.

1. Печь замедленного коксования для нагревания исходного материала до температуры замедленного коксования, содержащая:нагреватель, содержащий зону радиационного нагревания, имеющую нижнюю часть, включающую в себя секцию подовых горелок, и верхнюю часть, включающую в себя секцию стенных горелок, причем секция подовых горелок содержит множество подовых горелок, расположенных вблизи пода, для горения в зоне радиационного нагревания; и причем секция стенных горелок содержит множество стенных горелок, расположенных вблизи противоположных стенок; исодержащий множество параллельных труб нагревательный змеевик, расположенный в зоне радиационного нагревания.2. Печь замедленного коксования для нагревания исходного материала до температуры замедленного коксования, содержащая:нагревательную емкость, имеющую верхнюю и нижнюю секции радиационного нагревания, содержащий множество параллельных труб вертикальный нагревательный змеевик, расположенный между и на расстоянии от противоположных боковых стенок нагревательной емкости, через которую передается исходный материал, и множество горелок, расположенных в нижней радиационной секции нагревательной емкости, на каждой стороне содержащего множество параллельных труб нагревательного змеевика, таким образом, чтобы иметь возможность производить и направлять шлейфы пламени вверх на противоположные стороны содержащего множество параллельных труб нагревательного змеевика, причем каждый отдельный шлейф пламени находится в плоскости, в основном параллельной плоскости, в которой подвешен содержащий множество параллельных труб нагревательный змеевик.3. Печь за РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2012 148 245 A (51) МПК C10B 55/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2012148245/05, 08.04.2011 (71) Заявитель(и): ЛАММУС ТЕКНОЛОДЖИ ИНК. (US) Приоритет(ы): (30) Конвенционный приоритет: (72) Автор(ы): КАТАЛА Кеннет А. (US) 15.04.2010 US 61/324,625 (85) Дата начала рассмотрения ...

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Номер записи: 96
11-05-2017 дата публикации

Method for obtaining oil needle coke

Номер: RU2618820C1
Автор: Аллаберды Ильясович Ылясов, Виктор Павлович Запорин, Геннадий Георгиевич Валявин, Николай Фёдорович Юрченко, Савия Низамовна Каримова, Сергей Витальевич СУХОВ
Принадлежит: Вестпорт Трейдинг Юроп Лимитед, Втл (Фзе), Общество с ограниченной ответственностью "Информ-технология" (ООО "Информ-технология")

FIELD: oil and gas industry. SUBSTANCE: method comprises mixing heavy gas oil catalytic cracking with a recirculate in an intermediate tank to form secondary raw material, heating the raw material, feeding it to the coking chamber at the coking temperature, and coking with producing coke and a coker distillate which is fed into the lower part of the rectification column for fractionation. Wherein extract of furfural cleaning of oil production in an amount of 20-30% of the mixture is pre-mixed with the heavy gas oil of catalytic cracking; light or heavy coker gas oil is used as recirculate, with the recirculation ratio of 1.5-2.0. After stopping the secondary raw material supply in the coking chamber, a coolant in an amount of 10-20 t/h is supplied to the coking chamber at the temperature of 500-530°C for 6-8 hours, which can be represented by light or heavy coker gas oil. EFFECT: expansion of raw material resources for obtaining needle coke with the high evaluation of microstructure and high mechanical strength. 3 cl, 2 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 618 820 C1 (51) МПК C10B 55/00 (2006.01) C10B 57/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ФОРМУЛА (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ 2016107539, 01.03.2016 (24) Дата начала отсчета срока действия патента: 01.03.2016 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 01.03.2016 (45) Опубликовано: 11.05.2017 Бюл. № 14 Адрес для переписки: 450044, Уфа-44, а/я 222, ООО"Информтехнология" (56) Список документов, цитированных в отчете о поиске: RU 2314333 C1, 10.01.2008. RU 2 6 1 8 8 2 0 R U (54) СПОСОБ ПОЛУЧЕНИЯ НЕФТЯНОГО ИГОЛЬЧАТОГО КОКСА (57) Формула изобретения 1. Способ получения нефтяного игольчатого кокса замедленным коксованием, включающий смешивание в промежуточной емкости в качестве исходного сырья тяжелого газойля каталитического крекинга с рециркулятом с образованием вторичного сырья, нагрев вторичного сырья, подачу его в камеру коксования ...

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Номер записи: 97
23-04-2020 дата публикации

Method of producing petroleum coke (embodiments)

Номер: RU2719849C1
Автор: Анатолий Аркадьевич Тихонов, Ильдар Рашидович Хайрудинов, Талгат Хатмуллович Султанов
Принадлежит: Акционерное общество "Институт нефтехимпереработки" (АО "ИНХП")

FIELD: oil, gas and coke-chemical industries.SUBSTANCE: invention relates to oil refining industry, particularly, to methods of producing petroleum coke by delayed coking oil stock with different content of volatile substances. Method involves heating of the coking raw material, its supply to the additional column with formation of secondary raw material with its further heating to 475 °C, supply to the coke chamber and fractionation of gas-vapour coking products in the rectification column. At that, according to the first embodiment of coke production with increased content of volatile substances, heat carrier - mixture of heavy and bottom-gas coke gasoil is heated in furnace to temperature of 510 °C, Then, it is supplied into reaction chamber and then through reduction valve with pressure of 0.1 MPa higher than in coke chamber, and temperature not lower than that of coking feed is supplied to bottom of coke chamber. According to the second embodiment, to produce coke with low content of volatile substances, a heat carrier with temperature of 510 °C is introduced into a hot feed stream with temperature of 505 °C, and then is fed into a coke chamber.EFFECT: technical result is higher output of components of motor fuel and higher efficiency of coking plant.6 cl, 1 tbl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 719 849 C1 (51) МПК C10B 55/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10B 55/00 (2020.02) (21)(22) Заявка: 2019114639, 13.05.2019 (24) Дата начала отсчета срока действия патента: Дата регистрации: (73) Патентообладатель(и): Акционерное общество "Институт нефтехимпереработки" (АО "ИНХП") (RU) 23.04.2020 (45) Опубликовано: 23.04.2020 Бюл. № 12 2 7 1 9 8 4 9 R U (54) Способ получения нефтяного кокса (варианты) (57) Реферат: Изобретения относятся к нефтеперерабатывающей промышленности, в частности к вариантам способа получения нефтяного кокса замедленным коксованием нефтяного сырья с ...

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Номер записи: 98
25-03-2020 дата публикации

Method of producing oil needle coke

Номер: RU2717815C1
Автор: Андрей Владимирович Альт, Виктор Павлович Запорин, Дмитрий Валерьевич Храпов, Константин Владимирович Федотов, Сергей Витальевич СУХОВ
Принадлежит: Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть-ОНПЗ"

FIELD: oil refining. SUBSTANCE: invention relates to oil refining, in particular to delayed coking process for production of petroleum coke used in production of large-size graphitized electrodes and is aimed at increasing coke yield and improving structural organization due to weighting of the coking raw material based on the boiling point temperature. Method comprises heating decantoil (heavy gasoil of catalytic cracking) as feedstock and mixing it in a column for forming secondary raw material with recycle to form secondary raw material, heating secondary raw material to coking temperature and coking in coking chambers to obtain needle coke and coking distillate, which is fed into the fractional column bottom part to fractionation with obtain hydrocarbon gas, gasoline, light and heavy caking gasoils and still gasoil, steaming coke with water vapor and cooling with water, supply of steaming and cooling products to absorber equipped with mass exchange devices. Secondary raw material formation column is equipped with mass exchange devices; at that, water vapor is supplied to lower part of secondary raw material formation column, low-boiling hydrocarbons from upper part of secondary raw material production column are directed to absorber. EFFECT: invention provides weighting of coking raw materials by boiling point temperature and, as a result, increase of its output and improvement of structural organization. 4 cl, 2 tbl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 717 815 C1 (51) МПК C10B 55/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10B 55/00 (2020.02) (21)(22) Заявка: 2019129191, 16.09.2019 (24) Дата начала отсчета срока действия патента: Дата регистрации: 25.03.2020 (45) Опубликовано: 25.03.2020 Бюл. № 9 2 7 1 7 8 1 5 R U (56) Список документов, цитированных в отчете о поиске: RU 2515323 C2, 10.05.2014. SU 1810374 A1, 23.04.1993. RU 2660008 C1, 04.07.2018. RU 2314333 C1, 10.01.2008. SU ...

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Номер записи: 99
25-06-2020 дата публикации

Radial tubular reactor

Номер: WO2020126310A1
Автор: Laurent Bournay, Pierre-Antoine Bouillon, Romain Rousset, Thomas PLENNEVAUX
Принадлежит: IFP ENERGIES NOUVELLES

The present invention relates to a tubular reactor (1) provided at one of its ends with an at least partially solid charge inlet (2) and at its opposite end with a charge outlet (3), characterized in that said reactor houses a fluid distributor (5), the external wall of which delimits a tubular or annular space (51) which is coaxial with respect to the longitudinal axis (X) of the reactor (1), - said tubular or annular space comprises a fluid inlet (6) at one of its ends, - said tubular or annular space comprises a plurality of lateral fluid outlets (7), said outlets having orifices passing through the outer wall of the distributor to emerge inside the reactor, - said fluid distributor (5) is surrounded in the reactor (1) over at least part of the length of said distributor by a filter (8) which confines the load in the space between the distributor and said filter.

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Номер записи: 100