СИСТЕМА ОДОРИЗАЦИИ ГОРЮЧЕЙ СМЕСИ

Система одоризации горючей смеси, включающая емкость-хранилище одоранта, замерную емкость с указателем уровня одоранта и линией подачи одоранта, предохранительный клапан, выход которого соединен с факелом, технологические трубопроводы и запорные краны, отличающаяся тем, что она содержит емкость для хранения горючей смеси с линией приема и насос, линия всасывания которого соединена с выходом емкости для хранения горючей смеси, а линия нагнетания соединена с линией приема горючей смеси и сообщена с линией подачи одоранта. (19) RU (11) 28 493 (13) U1 (51) МПК C10J 1/28 (2000.01) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К СВИДЕТЕЛЬСТВУ (21), (22) Заявка: 2002129472/20 , 04.11.2002 (24) Дата начала отсчета срока действия патента: 04.11.2002 (46) Опубликовано: 27.03.2003 (72) Автор(ы): Сироткин Н.С., Молчанов С.А., Шушпанов А.Т., Кушмухаметов Р.Ф. 2 8 4 9 3 R U (57) Формула полезной модели Система одоризации горючей смеси, включающая емкость-хранилище одоранта, замерную емкость с указателем уровня одоранта и линией подачи одоранта, предохранительный клапан, выход которого соединен с факелом, технологические трубопроводы и запорные краны, отличающаяся тем, что она содержит емкость для хранения горючей смеси с линией приема и насос, линия всасывания которого соединена с выходом емкости для хранения горючей смеси, а линия нагнетания соединена с линией приема горючей смеси и сообщена с линией подачи одоранта. Ñòðàíèöà: 1 U 1 U 1 (54) СИСТЕМА ОДОРИЗАЦИИ ГОРЮЧЕЙ СМЕСИ 2 8 4 9 3 (73) Патентообладатель(и): Общество с ограниченной ответственностью "Оренбурггазпром" R U Адрес для переписки: 460000, г.Оренбург, ул.Пушкинская, 20, ООО "ВолгоУралНИПИгаз", зав. патентным отделом Б.А.Дронову (71) Заявитель(и): Общество с ограниченной ответственностью "Оренбурггазпром" U 1 U 1 2 8 4 9 3 2 8 4 9 3 R U R U Ñòðàíèöà: 2 RU 28 493 U1 RU 28 493 U1 RU 28 493 U1 RU 28 493 U1 RU 28 493 U1

Установка для одоризации газа

Установка для одоризации газа, содержащая барботажную камеру, источник одоранта и трубопроводы, соединяющие их с газопроводом, отличающаяся тем, что в ее состав дополнительно включен смеситель, выполненный в виде трубки Вентури, расположенной в основном газовом потоке после входа части газового потока в барботажную камеру таким образом, что объем газового потока вдоль стакана завихрения трубки Вентури соединен с выходом из барботажной камеры. (19) RU (11) 36 377 (13) U1 (51) МПК C10J 1/28 (2000.01) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К СВИДЕТЕЛЬСТВУ (21), (22) Заявка: 2002110330/20 , 18.04.2002 (24) Дата начала отсчета срока действия патента: 18.04.2002 (46) Опубликовано: 10.03.2004 (72) Автор(ы): Рождественский Валентин Андреевич (UA) (73) Патентообладатель(и): Рождественский Валентин Андреевич (UA) R U Адрес для переписки: 61108, Украина, г. Харьков, ул. Павлика Морозова, 2, кв.12, А.С. Серюгиной 3 6 3 7 7 R U Ñòðàíèöà: 1 U 1 (57) Формула полезной модели Установка для одоризации газа, содержащая барботажную камеру, источник одоранта и трубопроводы, соединяющие их с газопроводом, отличающаяся тем, что в ее состав дополнительно включен смеситель, выполненный в виде трубки Вентури, расположенной в основном газовом потоке после входа части газового потока в барботажную камеру таким образом, что объем газового потока вдоль стакана завихрения трубки Вентури соединен с выходом из барботажной камеры. 3 6 3 7 7 U 1 (54) Установка для одоризации газа U 1 U 1 3 6 3 7 7 3 6 3 7 7 R U R U Ñòðàíèöà: 2 RU 36 377 U1 RU 36 377 U1 RU 36 377 U1 RU 36 377 U1 RU 36 377 U1 RU 36 377 U1 RU 36 377 U1

Method for the production of low voc fragranced hydrogel spheres having improved optical clarity

A method for producing low-VOC fragranced hydrogel spheres of improved optical clarity and fragrance delivery is described and comprises the steps of combining a stable oil-in-water fragrance microemulsion absent co-solvents with a coarse dry granular, super-absorbent, hydrogel-forming copolymer. The resulting discrete hydrogel spheres have transparent optical beauty and liberate fragrance into an environment leaving behind only a small amount of emulsifier once evaporated. The air freshener produced by the disclosed method provides decoration in a home when the spheres are placed in a decorative jar.

INSULATOR UNIT

An insulator unit for a multipurpose flow module, such as a plate reactor, comprising a plurality of thermally insulating layers arranged in a sandwich structure with a plurality of plates, to provide thermal insulation across the sandwich structure. 115-. (canceled)16. An insulator unit for a multipurpose flow module , comprising a plurality of thermally insulating layers arranged in a sandwich structure with a plurality of plates , to provide thermal insulation across the sandwich structure.17. An insulator unit according to claim 16 , wherein the sandwich structure comprises at least one elastic member.18. An insulator unit according to claim 17 , wherein said at least one elastic member is at least one insulating layer.19. An insulator unit according to claim 16 , wherein each insulating layer is in the form of a continuous sheet of an insulating material.20. An insulator unit according to claim 16 , wherein at least one of the plates is patterned so that to retain an adjacent insulating layer in the sandwich structure upon compression.21. An insulator unit according to claim 20 , wherein the patterned plate is provided with a plurality of openings extending through the same plate claim 20 , which openings are distributed over the plate.22. An insulator unit according to claim 21 , wherein the area of the openings make up at least 5 percent and preferably less than 20 percent of the surface area of the patterned plate.23. An insulator unit according to claim 16 , wherein at least one of the insulating layers comprises expanded PTFE or a material selected from one or more of the materials in the group consisting of expanded PTFE claim 16 , PEEK and PPS.24. An insulator unit according to claim 16 , wherein at least one of the plates is a metal plate claim 16 , preferably a stainless steel plate.25. An insulator unit according to claim 16 , wherein the insulator unit further comprises fastening means keeping the sandwich structure together.26. An insulator unit ...

TIRE PROCESSING METHOD AND TIRE PROCESSING DEVICE

In a tire constituted with a thermoplastic material and a material different from the thermoplastic material, the thermoplastic material and the material different from the thermoplastic material are easily and efficiently separated. While a tire formed of a thermoplastic material is being turned, heated air is ejected from a nozzle of a heating apparatus , and the surface of a crown portion is melted. An end portion of a cord embedded in a helical arrangement, which is formed of a material different from the thermoplastic material, is extracted from the melted region, and is sequentially wound onto a reel 1. A tire processing method comprising:a first step of, at a tire that is constituted with a thermoplastic material and a material other than the thermoplastic material, heating a portion of the thermoplastic material and either melting or softening the portion; anda second step of, at a melted or softened portion of the thermoplastic material, separating the melted or softened thermoplastic material and the material other than the thermoplastic material.2. A tire processing method comprising:a first step of, at a tire that is constituted with a plurality of thermoplastic materials having different melting points and with a material other than the thermoplastic materials, heating some of the plurality of thermoplastic materials; anda second step of separating a portion of a thermoplastic material that is either melted or softened and a thermoplastic material that is neither melted nor softened.3. The tire processing method according to claim 1 , whereina tire carcass portion of the tire extends from one bead portion to another bead portion, the tire carcass portion being formed of the thermoplastic material, and a reinforcement layer is provided at an outer periphery portion of the tire carcass portion, the reinforcement layer including a cord formed of the material other than the thermoplastic material,the first step includes heating and either melting or ...

Fragrance Dispenser for use with portable electronic device

A cover for holding and protecting a scent insert for use with a portable electronic device or other electronic device such as an IPOD, IPAD, MP3 player, laptop, for example, including a pocket for holding a removable scented insert. The pocket is an integral part of the cover or a removable pocket which is held on to the outside of the cover with an adhesive, for example. The aromatic insert is a scent impregnated porous plastic insert or plastic insert having a permeable layer sealed with nonpermeable peelable layers of plastic or paper film wherein a top layer is removed as desired, thus releasing the desired aroma. The exterior surface of the pocket is porous or includes apertures or slits for transferring the scent outside of the pocket insert holder. 1. A fragrance dispenser for portable electronic devices , comprising:a portable electronic device cover having a pocket formed therein, said pocket being configured to removably hold a scented insert, said scented insert being capable of absorbing a selected scented liquid and then releasing vapors of said scented liquid to the surrounding air; andsaid insert being held within said pocket by a door, said door being configured to rotate on a hinge, said hinge being integral with said door and said portable electronic device cover.2. The fragrance dispenser for portable electronic devices of wherein a marginal edge of said door includes a tab for providing a friction fit against a marginal edge of said pocket when said door closed.3. The fragrance dispenser for portable electronic devices of wherein said door has apertures formed therein for the purpose of increased evaporation of said scented liquid from said scented insert.4. A fragrance dispenser for a portable electronic device comprising;a front wall, a back wall and at least two side walls, said front wall and said back wall being held parallel to one another in a spaced apart relationship by said at least two side walls, thus forming a gap between said front ...

METHOD AND DEVICE FOR REFORMING PRODUCED GAS

Provided is a method of reforming a produced gas to reform tar contained in the produced gas from a gasification furnace. Quick lime comes in contact with a produced gas () from a gasification furnace () in a reformer () such that the quick lime absorbs carbon dioxide in the produced gas to generate calcium carbonate, and reforming reaction of the tar is performed with calcium as a catalyst using heat of reaction emitted during that time. In addition, as the calcium carbonate of the reformer () is supplied and burnt in a reforming agent regenerator (), the quick lime is regenerated and supplied into the reformer () again. According to the above configuration, it is possible to provide a method and device for reforming a produced gas that are capable of simplifying equipment and operation thereof. 1. A method of reforming a produced gas configured to reform tar contained in the produced gas from a gasification furnace , the method comprising:generating calcium carbonate in a reformer by bringing the produced gas from the gasification furnace in contact with quick lime so that the quick lime absorbs carbon dioxide in the produced gas, performing a reforming reaction of the tar with calcium as a catalyst using reaction heat generated when the calcium carbonate is generated, supplying the calcium carbonate in the reformer, auxiliary fuel, and air into a reforming agent regenerator to form a fluidized bed, returning the calcium carbonate to the quick lime by burning the calcium carbonate using heat by combustion of the auxiliary fuel, and supplying the quick lime into the reformer.2. The method of reforming the produced gas according to claim 1 , wherein claim 1 , in the reformer claim 1 , the reforming reaction of the tar is performed using claim 1 , in addition to the heat generated when the calcium carbonate is generated from the quick lime claim 1 , heat generated when the carbon dioxide is generated through reaction between carbon monoxide and moisture in the ...

POWER GENERATION SYSTEM AND METHOD OF OPERATING THE SAME

A power generation system includes: an air intake passage; a fuel cell system that includes a fuel cell; a case configured to house the fuel cell, a ventilator (air supply unit), and an air intake temperature detector configured to detect a temperature of the intake air supplied to the case; a combustion device that includes a combustor; an exhaust gas passage configured to discharge a flue gas generated in the combustion device to the outside; and a controller. The air intake passage and the exhaust gas passage are configured to allow heat exchange to occur between media flowing through the passages. The controller causes the combustion device to operate when the fuel cell system is activated and the temperature detected by the air intake temperature detector is equal to or lower than a first predetermined temperature. 1. A power generation system comprising:an air intake passage;a fuel cell system including a fuel cell configured to generate electric power using a fuel gas and an oxidizing gas, a case configured to house the fuel cell, an air supply unit configured to supply external air to the case through the air intake passage, and an air intake temperature detector configured to detect a temperature of the intake air supplied to the case;a combustion device including a combustor configured to combust a fuel to generate an amount of heat;an exhaust gas passage configured to discharge a flue gas generated in the combustion device to the outside; anda controller, wherein:the air intake passage and the exhaust gas passage are configured to allow heat exchange to occur between media flowing through the passages, andthe controller causes the combustion device to operate when the fuel cell system is activated and the temperature detected by the air intake temperature detector is equal to or lower than a first predetermined temperature.2. The power generation system according to claim 1 , wherein:the air intake temperature detector is provided in the air intake ...

POWER GENERATION SYSTEM AND METHOD OF OPERATING THE SAME

A power generation system according to the present invention includes: a fuel cell unit including a fuel cell, a hydrogen generator having a first combustor, and a case; a controller; a combustion unit including a second combustor; and a discharge passage formed to cause the case and the combustion unit to communicate with each other. In a case where the controller causes one of the first combustor and the second combustor to perform the ignition operation, the controller maintains an operating state of the other combustor during the period of the ignition operation of the one combustor. 115-. (canceled)16. A power generation system comprising: a fuel cell configured to generate electric power using a fuel gas and an oxidizing gas,', 'a hydrogen generator including a first combustor and configured to generate the fuel gas supplied to the fuel cell, and', 'a case configured to house at least the fuel cell and the hydrogen generator;, 'a fuel cell unit including'}a controller;a combustion unit arranged outside the case and including a second combustor configured to combust a combustible gas; anda discharge passage which is formed to cause the fuel cell unit and the combustion unit to communicate with each other and through which an exhaust gas discharged from the first combustor of the fuel cell unit and an exhaust gas discharged from the combustion unit are discharged to an atmosphere, wherein:the fuel cell unit includes a ventilator configured to operate at least in a case where the fuel cell performs an electric power generating operation and to ventilate an inside of the fuel cell unit by discharging a gas in the fuel cell unit to the discharge passage;the discharge passage is configured such that at least a gas in the case is discharged to the atmosphere; andin a case where the controller causes the second combustor to perform an ignition operation, the controller maintains an operating state of the first combustor and an operating state of the ventilator during ...

Vapor capture and release systems

Systems for selectively capturing and/or releasing particular vapors or odors are described. The systems utilize polymeric substrates such as in the shape of disks that can be infused with one or more target vapors or odors. The systems also utilize enclosures having one or more defined orifices. After placement of infused polymeric substrates within the interior of an enclosure, target agents evaporate or otherwise vapor transfer from the interior of the enclosure through the defined orifice(s) in a controlled and quantifiable manner.

SOLID OXIDE FUEL CELL DEVICE

To provide a fuel cell device capable of extending the years of service life of a reformer by suppressing thermal runaways. The present invention is a solid oxide fuel cell device, including a fuel cell module having multiple fuel cell units; a reformer disposed above the fuel cell units, for producing hydrogen by a partial oxidation reforming reaction and a steam reforming reaction; a vaporizing chamber disposed adjacent to the reformer; a combustion chamber for heating the vaporization chamber; a water supply device; a supply device for oxidant gas for electrical generation; and a controller for raising the fuel cell unit to a temperature at which electrical generation is possible; wherein fuel electrodes in each individual fuel cell unit are constituted to act as catalysts for a shift reaction, and the controller executes only the ATR step and SR step in the reformer. 1. A solid oxide fuel cell device , in which fuel is supplied to fuel cell units and the remaining fuel flow out from one end of the fuel cell units is combusted to heat a reformer , the solid oxide fuel cell device comprising:a fuel cell module including plurality of fuel cell units in which fuel electrode is formed in internal passages for passing fuel;a reformer disposed above the plurality of fuel cell units within the fuel cell module, for producing hydrogen by a partial oxidation reforming reaction resulting from the chemical reaction of fuel and reforming oxidant gas and a steam reforming reaction resulting from the chemical reaction of fuel and reforming steam;a vaporization chamber disposed above the plurality of fuel cell units and adjacent to the reformer, for vaporizing supplied water;a combustion chamber disposed inside the fuel cell module, that combusts fuel passed through the internal passage at the top end of each of the fuel cell units to heat the reformer and vaporization chamber above;a fuel supply device that, by supplying fuel to the reformer, feeds fuel reformed in the ...

FUEL CELL MODULE

A fuel cell module includes an oxygen-containing gas regulator valve for distributing and supplying the oxygen-containing gas to the heat exchanger and to the start-up combustor, a raw fuel regulator valve for distributing and supplying the raw fuel to the reformer and to the start-up combustor, and a control device. The control device includes an oxygen-containing gas distribution controller for controlling the oxygen-containing gas regulator valve and a raw fuel distribution controller for controlling the raw fuel regulator valve, each control thereof being performed at least based on any of the temperature of the fuel cell stack, the temperature of the reformer, and the temperature of the evaporator. 1. A fuel cell module comprising:a fuel cell stack formed by stacking a plurality of fuel cells for generating electricity by electrochemical reactions of a fuel gas and an oxygen-containing gas;a reformer for reforming a mixed gas of a raw fuel chiefly containing hydrocarbon and water vapor to produce the fuel gas supplied to the fuel cell stack;an evaporator for evaporating water, and supplying water vapor to the reformer;a heat exchanger for raising the temperature of the oxygen-containing gas by heat exchange with a combustion gas, and supplying the oxygen-containing gas to the fuel cell stack;an exhaust gas combustor for combusting the fuel gas discharged from the fuel cell stack as a fuel exhaust gas and the oxygen-containing gas discharged from the fuel cell stack as an oxygen-containing exhaust gas to produce the combustion gas;a start-up combustor for corn busting the raw fuel and the oxygen-containing containing gas to produce the combustion gas;an oxygen-containing gas regulator valve for distributing and supplying the oxygen-containing gas to the heat exchanger and to the start-up combustor;a raw fuel regulator valve for distributing and supplying the raw fuel to the reformer and to the start-up combustor; anda control device,wherein the control device ...

SYNCHRONOUS CONTROL OF LAMP BRIGHTNESS AND SAMPLE DIFFUSION

In response to user interaction, a signal is generated from a control element of a sample diffuser assembly. The sample diffuser assembly comprises a sample container, wherein the sample container is configured to receive a sample to be diffused; a motor operative to assist in diffusing the sample at a selectable transformation rate; a light source, wherein the light source comprises an AC lamp; and control circuitry operatively coupled to the motor and the light source. A set of signals is generated, via the control circuitry in response to the signal generated by the control element, wherein the set of signals simultaneously control the light intensity of the AC lamp based on the transformation rate produced by the motor to diffuse the sample in the sample container. 1. A sample diffuser apparatus , comprising:a sample container, wherein the sample container is configured to receive a sample to be diffused;a motor operative to assist in diffusing the sample at a selectable transformation rate;a light source, wherein the light source comprises an alternating current (AC) lamp; and a switch assembly comprising a potentiometer, wherein the potentiometer provides a voltage responsive to user interaction;', 'control circuitry operatively coupled to the switch assembly, the control circuitry configured to enable synchronous control of the transformation rate of the sample in the sample container and an intensity of light emitted by the AC lamp based on the voltage provided by the potentiometer, wherein the control circuitry comprises:', 'lamp driver circuitry operatively coupled to the AC lamp;', 'motor driver circuitry operatively coupled to the motor; and', 'a microcontroller operatively coupled to the lamp driver circuitry and the motor driver circuitry, the microcontroller programmed to generate a first signal output to the motor driver circuitry and a second signal output to the lamp driver circuitry, wherein the second signal relates to the first signal to ...

Gasification of bio-oil and alkali containing energy rich aqueous solutions from pulp mills

Process for gasification of an alkali containing energy rich aqueous solution ( 120 ) from a pulp mill in an entrained flow gasification reactor ( 2 ), the process comprising the steps of d) Supplying said alkali containing energy rich aqueous solution ( 120 ) to said gasification reactor ( 2 ), e) Gasifying said alkali containing energy rich aqueous solution ( 120 ) in the reactor ( 2 ) by using an oxidizing medium at sub-stoichiometric conditions and at a temperature below 1400 C in an outlet of said reactor ( 2 ); and, f) Producing a phase of a liquid material and a phase of a gaseous material in said reactor ( 2 ). wherein in step (a) supplying a bio-oil ( 110 ) to said gasification reactor ( 2 ), in step (b) simultaneously gasifying said alkali containing energy rich aqueous solution ( 120 ) and said bio-oil ( 110 ) in the reactor ( 2 ).

METHOD FOR DELIVERING A VOLATILE MATERIAL

A method of delivering a volatile material to the atmosphere in a continuous manner is disclosed. The method includes providing a delivery engine having a reservoir that includes a volatile material mixture. The volatile material mixture includes about 40% to about 100%, by total weight, of the volatile materials each having a vapor pressure at 25° C. of less than about 0.1 torr. The delivery system also includes a microporous membrane enclosing the reservoir, wherein the microporous membrane comprises an average pore size of about 0.01 to about 0.03 microns. 1. A method of delivering a volatile material comprising the step of providing a delivery engine comprising:a. a reservoir comprising a volatile material mixture, said volatile material mixture comprising about 40% to about 100%, by total weight, of volatile materials each having a vapor pressure at 25° C. of less than about 0.1 torr; and{'sup': 2', '2, 'b. a microporous membrane enclosing said reservoir, said microporous membrane comprising an evaporative surface area of about 2 cmto about 35 cmand an average pore size of about 0.01 to about 0.03 microns.'}2. The method of claim 1 , wherein said volatile material mixture comprises about 50% claim 1 , by total weight claim 1 , of volatile materials each having a vapor pressure at 25° C. of less than about 0.1 torr.3. The method of claim 1 , wherein said volatile material mixture comprises:a. 0% to about 15%, by total weight, of volatile materials each having a VP at 25° C. of about 0.004 torr to about 0.035 torr;b. about 0% to about 25%, by total weight, of volatile materials each having a VP at 25° C. of about 0.1 torr to about 0.325 torr; andc. about 65% to about 100%, by total weight, of volatile materials each having a VP at 25° C. of about 0.035 torr to about 0.1 torr.4. The method of claim 1 , wherein said volatile material mixture comprises a viscosity of about 1.0 cP to less than about 15 cP.5. The method of claim 1 , wherein said volatile material ...

Single-Screw Extrusion Desulfurization And Post-Processing System, And Method For Preparing Reclaimed Rubber

A single-screw extrusion desulfurization and post-processing system and a method for preparing reclaimed rubber. The single-screw extrusion desulfurization and post-processing system comprises: a single-screw desulfurization device, a single-screw post-processing device and a closed connection device for connecting the single-screw desulfurization device and the single-screw post-processing device, the single-screw post-processing device includes a post-processing feeding unit and a post-processing unit which are connected with each other, and a post-processing screw running through the post-processing feeding unit and the post-processing unit. 1. A single-screw extrusion desulfurization and post-processing system , whereinthe system comprises: a single-screw desulfurization device;the single-screw desulfurization device includes a desulfurizing feeding unit and a desulfurizing unit which are connected with each other, and a desulfurizing screw running through the desulfurizing feeding unit and the desulfurizing unit; anda heating structure is respectively disposed in the desulfurizing feeding unit, the desulfurizing unit and the desulfurizing screw; and whereinthe system further comprises: a single-screw post-processing device and a closed connection device for connecting the single-screw desulfurization device and the single-screw post-processing device;the single-screw post-processing device includes a post-processing feeding unit and a post-processing unit which are connected with each other, and a post-processing screw running through the post-processing feeding unit and the post-processing unit.2. The single-screw extrusion desulfurization and post-processing system according to claim 1 , whereinthe desulfurizing unit includes a desulfurizing feeding cylinder and at least one stage of desulfurizing cylinder; the desulfurizing feeding cylinder is connected with the at least one stage of desulfurizing cylinder; and the desulfurizing screw runs through the ...

System, Method, and Apparatus for Gasification of a Solid or Liquid

A system for gasification of a material includes a plasma generator interfaced to a reaction chamber. A feedstock such as pulverized coal is fed into a plasma jet created by the plasma generator and is gasified by the high temperatures of the plasma jet. The gas produced is then collected, filtered, and utilized, for example, in generating of electricity. Likewise, extra heat produced by the system is also used to generate electricity or other heating purposes

REACTOR

In a reactor, a first reference position is presumed to be defined by a straight line in contact with a first open end of the introduction port on the side bent toward the second flow channel and extending in the direction intersecting with the second flow channels, and a second reference position is presumed to be defined by a straight line in contact with a second open end of the introduction port on the opposite side of the first open end and extending in the direction intersecting with the second flow channel. At least part of the catalyst body is provided at least either in a region defined between the first reference position and the second reference position, or in a region defined between the second reference position and an inlet position of the first flow channels. 1. A reactor comprising:a first flow channel through which a reaction fluid flows;a second flow channel through which a heat medium flows, the second flow channel being stacked parallel to the first flow channel;an introduction port open in a direction intersecting with the second flow channel to introduce the heat medium; anda catalyst body provided in the first flow channel to promote an exothermic reaction of the reaction fluid,wherein, when a first reference position is presumed to be defined by a straight line in contact with a first open end of the introduction port on a side bent toward the second flow channel and extending in the direction intersecting with the second flow channel, and a second reference position is presumed to be defined by a straight line in contact with a second open end of the introduction port on an opposite side of the first open end and extending in the direction intersecting with the second flow channel,at least part of the catalyst body is provided at least either in a region defined between the first reference position and the second reference position, or in a region defined between the second reference position and an inlet position of the first flow channel. ...

HEATER

A heater includes a fuel cell stack assembly disposed within a heater housing and includes a plurality of fuel cells which convert chemical energy from a fuel into heat and electricity through a chemical reaction with an oxidizing agent. A combustor disposed within the heater housing receives an anode exhaust and a cathode exhaust from the fuel cell stack assembly and combusts a mixture of the anode exhaust and the cathode exhaust to produce a heated combustor exhaust. The combustor includes a combustor exhaust outlet for discharging the heated combustor exhaust into the heater housing. A baffle disposed around the fuel cell stack assembly and the combustor defines a heat transfer channel radially between the heater housing and the baffle. A flow director in fluid communication with the combustor exhaust outlet and the heat transfer channel communicates the heated combustor exhaust to the heat transfer channel. 1. A heater comprising:a heater housing extending along a heater axis;a fuel cell stack assembly disposed within said heater housing and having a plurality of fuel cells which convert chemical energy from a fuel into heat and electricity through a chemical reaction with an oxidizing agent, said fuel cell stack assembly having 1) a fuel inlet for introducing said fuel to a plurality of anodes of said plurality of fuel cells, 2) an oxidizing agent inlet for introducing said oxidizing agent to a plurality of cathodes of said plurality of fuel cells, 3) an anode exhaust outlet for discharging an anode exhaust from said plurality of fuel cells, and 4) a cathode exhaust outlet for discharging a cathode exhaust from said plurality of fuel cells;a combustor disposed within said heater housing in fluid communication with said anode exhaust outlet and said cathode exhaust outlet, said combustor being arranged to combust a mixture of said anode exhaust and said cathode exhaust to produce a heated combustor exhaust, said combustor including a combustor exhaust outlet for ...

DISASSEMBLABLE STACKED FLOW REACTOR

A plate-type flow reactor device with a first plate () having first and second opposing surfaces () and one or more through-holes (); a second plate sealed against the first surface () by at least two first O-rings (); a third plate () sealed against the second surface () by at least one second O-ring (); two or more first elongated channels () defined between the first surface () and the second plate and one or more second elongated channels () defined between the second surface () and the third plate, wherein each first channel communicates with the at least one second channel () via one or more of the through-holes () through the first plate (), and said one first channel () communicates with another first channel () of the two or more first channels () only via said at least one second channel (), and each first channel () is individually surrounded by at least one of the first O-rings () and the at least one second is individually surrounded by the at least one second O-ring (). 1. A plate-type flow reactor device comprising:at least a first plate having first and second opposing surfaces and one or more through-holes extending from the first to the second surface;at least a second plate having a second plate surface sealed against the first surface of the first plate by at least two first O-rings positioned between the first surface of the first plate and the second plate surface;at least a third plate having a third plate surface sealed against the second surface of the first plate by at least one second O-ring positioned between the second surface of the first plate and the third plate surface;two or more first elongated channels defined between the first surface of the first plate and the second plate surface by contours on or in the first surface and/or the second plate surface, and one or more second elongated channels defined between the second surface of the first plate and the third plate surface by contours on or in the second surface and/or the third ...

Method for forming synthesis gas using a plasma-catalyzed fuel reformer

A method of forming a synthesis gas utilizing a reformer is disclosed. The method utilizes a reformer that includes a plasma zone to receive a pre-heated mixture of reactants and ionize the reactants by applying an electrical potential thereto. A first thermally conductive surface surrounds the plasma zone and is configured to transfer heat from an external heat source into the plasma zone. The reformer further includes a reaction zone to chemically transform the ionized reactants into synthesis gas comprising hydrogen and carbon monoxide. A second thermally conductive surface surrounds the reaction zone and is configured to transfer heat from the external heat source into the reaction zone. The first thermally conductive surface and second thermally conductive surface are both directly exposed to the external heat source. A corresponding apparatus and system are also disclosed herein.

PROCESS FOR THE PREPARATION OF POLYMERS FROM WASTE PLASTIC FEEDSTOCKS

The present invention relates to a process for the production of polymers from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising a monomer; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an polymer. The process of the present invention allows for optimisation of the quantity of waste plastic material that finds its way back into a polymer that is produced as outcome of the process. 1. Process for the production of polymers from waste plastics feedstocks comprising the steps in an order of:(a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock;(b) providing a hydrocarbon stream B;(c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s);(d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D;(e) supplying the cracked hydrocarbon stream D to a separation unit;(f) performing a separation operation in the separation unit to obtain a product stream E comprising a monomer;(g) supplying the product stream E to a polymerisation reactor; and(h) performing a polymerisation reaction in the polymerisation reactor to obtain an polymer.2. Process according to claim 1 , wherein the ...

Method and apparatus to dispense fragrance into the air in a bowling structure

A method to condition the air in a bowling alley utilizes an oil mixture which is dispensed by conditioning apparatus which down and up a synthetic bowling lane. The oil mixture comprises original lane oil and a fragrance composition which admixed to the oil mixture to produce a fragrant lane oil which has at 1700 cma % T which is generally equivalent to the % T of the original lane oil. 1(a) providing an enclosed building structure; (i) including a first end with a base line,', '(ii) including a second end located under a pin setter, and', '(iii) extending from said first end to said second end;, '(b) providing a plurality of synthetic bowling lanes inside said structure, each of said lanes'} (i) a reservoir to store a selected quantity of lane oil for dispensation on bowling lanes, and', '(ii) a oil dispensation mechanism to dispense oil at varying rates at different locations along a bowling lane while moving both', 'toward said pin setter, and', 'away from said pin setter;, '(c) providing a conditioning apparatus to apply lane oil separately to only a selected portion of each of said bowling lanes, said conditioning apparatus including'}(d) shipping lane conditioning oil in at least one container from a remote location to said building structure, said lane conditioning oil comprising over 50% by weight mineral oil and having a medium to high viscosity in the range of 28.0 to 40.0 cSt at 40 degrees C. and having a surface tension in the range of 25 to 30 dynes/cm;(e) shipping a first fragrance composition in at least one container from a remote location to said building structure, said first fragrance composition having a scent and comprising a fragrance oil and carrier, said fragrance composition miscible in said lane conditioning oil in a proportion of fragrance composition to lane oil in the range of 1:80 to 1:10;(f) shipping a second fragrance composition in at least one container from a remote location to said building structure, said second fragrance ...

DUST SEPARATING AND CARRIER RETURNING DEVICE

Disclosed is a dust separating and carrier returning device, which comprises: an outer raw material transfer passage () and an inner carrier returning passage (), and a sieve cage () with one end thereof connected with the raw material transfer passage () and the other end sealed; a spiral conveyer belt is provided between the sieve cage () and the carrier returning passage (), with the two sides thereof connected to the inner wall of the sieve cage () and the outer wall of the carrier returning passage (); and the end of the spiral conveyer belt is connected to the rear port of the carrier returning passage () via a guide plate (). The above device achieves the dedusting of the carrier during the transmission process and the returning of the dedusted carrier to another working circle, thereby improving work efficiency and reducing the number of manufacturing process steps which in turn reduces the process cost. 1. A dust separating and carrier returning device comprising: an outer material transfer passage and an inner carrier returning passage , and a sieve cage with one end thereof connected with the material transfer passage and the other end sealed; a spiral conveyer belt is provided between the sieve cage and the carrier returning passage , with the two sides thereof connected to the inner wall of the sieve cage and the outer mall of the carrier returning passage; and the end of the spiral conveyer belt is connected to the rear port of the carrier returning passage via guide plates.2. The dust separating and carrier returning device of claim 1 , wherein the stated guide plates comprise the import plates and the export plates claim 1 , the import plates are connected with the spiral conveyor claim 1 , the export plates correspond to the position of the carrier returning passage claim 1 , and the import plates and the export plates are connected to each other claim 1 , wherein the import plates are high in the front-end and low in the back-end claim 1 , while ...

FUEL CELL MODULE

Provided is a solid oxide fuel cell module that is small in size and is capable of stably generating power. A plurality of power generation units and are located such that a first fuel cell and an oxidant gas preheater connected to a second fuel cell adjacent to the first fuel cell are adjacent to each other. A solid oxide fuel cell module includes a partition member. The partition member partitions a combustion chamber into a region including the first fuel cell and a region including the second fuel cell as well as into the region including the first fuel cell and a region including the oxidant gas preheater connected to the second fuel cell. 1. A fuel cell module comprising:a combustion chamber; anda plurality of power generation units;each power generation unit comprising:a fuel cell located in the combustion chamber;a fuel gas channel connected to the fuel cell;an oxidant gas channel connected to the fuel cell; andan oxidant gas preheater disposed in a portion of the oxidant gas channel in the combustion chamber; whereinthe plurality of power generation units are disposed such that a first one of the fuel cells and an oxidant gas preheater connected to a second one of the fuel cells adjacent to the first one of the fuel cells are adjacent to each other, andthe fuel cell module further comprising a partition disposed to partition the combustion chamber into a region comprising the first one of the fuel cells and a region comprising the second one of the fuel cells, and into the region comprising the first one of the fuel cells and a region comprising the oxidant gas preheater connected to the second one of the fuel cells.2. The fuel cell module according to claim 1 , whereinthe plurality of power generation units comprise first and second power generation units,the fuel cell of the first power generation unit is disposed on one side in a first direction with respect to the fuel cell of the second power generation unit,the fuel cell of the first power generation ...

APPARATUS AND METHOD FOR THERMALLY DEMANUFACTURING TIRES AND OTHER WASTE PRODUCTS

An apparatus and process for thermally de-manufacturing tires and other materials. The apparatus is a retort chamber with various zones in which tires are combusted to provide energy for the thermal depolymerization reaction, depolymerization takes place, and products leave the retort chamber. In one embodiment, the process reacts water with iron present in steel-belted tires to produce hydrogen, which helps to break sulfur-sulfur bonds in vulcanized materials. The water also helps control the temperature of the reaction, which allows for control over the types and relative amounts of the various depolymerization products. 1. A retort chamber comprising:a) a top,b) a bottom,c) a heater at or near the bottom of the retort chamber capable of heating the bottom to a temperature between about 900 and 1300° C.,d) two or more inlet ports located at or near the bottom of the retort chamber,e) one or more outlet ports located at or near the top of the retort chamber,f) temperature monitors at or near the top and bottom of the retort chamber,g) a temperature monitor located at a position between about 30 and about 70% of the distance between the top and the bottom of the retort chamber, andh) a vacuum line or aspirator located between about 40 and about 60% of the distance between the top and the bottom of the retort chamber, wherein the retort chamber has a cylindrical shape.2. The retort chamber of claim 1 , wherein the heater is a burner placed on a carriage claim 1 , which carriage is adapted to allow the burner to move along the bottom of the retort chamber.3. The retort chamber of claim 1 , wherein the bottom of the retort chamber comprises a plurality of registers claim 1 , which registers are spaced so as to provide substantially equal pressure along the entire bottom of the retort claim 1 , wherein substantially equal means that the pressure along the bottom of the retort chamber does not vary by more than 20%.4. The retort chamber of claim 1 , wherein one or more ...

METHOD FOR DELIVERING A VOLATILE MATERIAL

A method of delivering a volatile material to the atmosphere in a continuous manner is disclosed. The method includes providing a delivery engine having a reservoir that includes a volatile material mixture. The volatile material mixture includes about 40% to about 100%, by total weight, of the volatile materials each having a vapor pressure at 25° C. of less than about 0.1 torr. The delivery system also includes a microporous membrane enclosing the reservoir, wherein the microporous membrane comprises an average pore size of about 0.01 to about 0.03 microns. 1. A method of delivering a volatile material comprising the step of providing a delivery engine comprising:a. a reservoir comprising a volatile material mixture, said volatile material mixture comprising about 40% to about 100%, by total weight, of volatile materials each having a vapor pressure at 25° C. of less than about 0.1 torr;{'sup': 2', '2, 'b. a microporous membrane enclosing said reservoir, said microporous membrane comprising an evaporative surface area of about 2 cmto about 35 cmand an average pore size of about 0.01 to about 0.03 microns.'}2. The method of claim 1 , wherein said volatile material mixture comprises about 60% to about 90% claim 1 , by total weight claim 1 , of volatile materials each having a vapor pressure at 25° C. of about 0.01 to about 0.3 torr.3. The method of claim 1 , wherein said volatile material mixture comprises:a. 0% to about 15%, by total weight, of volatile materials each having a vapor pressure at 25° C. of about 0.004 torr to about 0.035 torr;b. about 0% to about 25%, by total weight, of volatile materials each having a vapor pressure at 25° C. of about 0.1 torr to about 0.325 torr; andc. about 65% to about 100%, by total weight, of volatile materials each having a vapor pressure at 25° C. of about 0.035 torr to about 0.1 torr.4. The method of claim 1 , wherein said volatile material mixture comprises a viscosity of about 1.0 cP to less than about 15 cP.5. The method ...

METHOD OF OPERATING A HEATER

A method is provided for operating a heater including a heater housing extending along a heater axis; a plurality of fuel cell stack assemblies disposed within the heater housing along the heater axis and having a plurality of fuel cells which convert chemical energy from a fuel cell fuel into heat and electricity through a chemical reaction with a fuel cell oxidizing agent; and a plurality of combustors disposed within the heater housing along the heater axis. The method includes supplying a combustor fuel to the plurality of combustors, combusting the combustor fuel to produce a heated combustor exhaust when the fuel cell stack assemblies are substantially electrochemically inactive, and using the heated combustor exhaust to elevate the temperature of the fuel cell stack assemblies to be electrochemically active. 1. A method for operating a heater comprising a heater housing extending along a heater axis; a plurality of fuel cell stack assemblies disposed within said heater housing along said heater axis and having a plurality of fuel cells which convert chemical energy from a fuel cell fuel into heat and electricity through a chemical reaction with a fuel cell oxidizing agent; and a plurality of combustors disposed within said heater housing along said heater axis , said method comprising:supplying a combustor fuel to said plurality of combustors;combusting said combustor fuel to produce a heated combustor exhaust when said plurality of fuel cell stack assemblies are at an inactive temperature where said plurality of fuel cell stack assemblies are substantially electrochemically inactive; andusing said heated combustor exhaust to elevate the temperature of said plurality of fuel cell stack assemblies from said inactive temperature to an active temperature where said plurality of fuel cell stack assemblies are electrochemically active.2. A method as in wherein said step of using said heated combustor exhaust to elevate the temperature of said plurality of fuel ...

HEATER WITH A FUEL CELL STACK ASSEMBLY AND A COMBUSTOR AND METHOD OF OPERATING

A heater includes a heater housing extending along a heater axis. A fuel cell stack assembly is disposed within the heater housing and includes a plurality of fuel cells which convert chemical energy from a fuel cell fuel into heat and electricity through a chemical reaction with a fuel cell oxidizing agent. A combustor disposed within the heater housing includes a combustor fuel inlet for introducing the combustor fuel into the combustor, a combustor oxidizing agent inlet for introducing a combustor oxidizing agent into the combustor, and combustor exhaust outlet for discharging a heated combustor exhaust from the combustor. An anode exhaust conduit is connected to the anode exhaust outlet and extends out of the heater housing for selectively communicating a first quantity of the anode exhaust out of the heater housing. The heater housing is heated by the fuel cell stack assembly and the heated combustor exhaust. 1. A heater comprising:a heater housing extending along a heater axis;a fuel cell stack assembly disposed within said heater housing and having a plurality of fuel cells which convert chemical energy from a fuel cell fuel into heat and electricity through a chemical reaction with a fuel cell oxidizing agent, said fuel cell stack assembly having 1) a fuel cell stack fuel inlet for introducing said fuel cell fuel to a plurality of anodes of said plurality of fuel cells, 2) a fuel cell stack oxidizing agent inlet for introducing said fuel cell oxidizing agent to a plurality of cathodes of said plurality of fuel cells, 3) an anode exhaust outlet for discharging an anode exhaust comprising unspent fuel from said plurality of fuel cells, and 4) a cathode exhaust outlet for discharging a cathode exhaust comprising unspent fuel cell oxidizing agent from said plurality of fuel cells;a combustor disposed within said heater housing for combusting a mixture of a combustor fuel and a combustor oxidizing agent to form a heated combustor exhaust, said combustor having 1) ...

FRAGRANCE DELIVERY DEVICE, SYSTEM, AND METHOD

A fragrance delivery device, system and method is provided, comprising a housing including a rupture device and an absorbent member receivable in the housing. The system further includes a cartridge insertable within the housing and containing a fragrance medium therein. The rupture device of the housing is engageable with the cartridge to release the fragrance medium from the cartridge into the housing. The absorbent member absorbs the fragrance medium and permeates a fragrance from the fragrance medium to an external environment. 1. A fragrance delivery system , comprising:a housing including a rupture device;an absorbent member receivable in the housing; anda cartridge insertable within the housing and containing a fragrance medium therein, wherein the rupture device of the housing is engageable with the cartridge to release the fragrance medium from the cartridge into the housing, and wherein the absorbent member absorbs the fragrance medium and permeates a fragrance from the fragrance medium to an external environment.2. The fragrance delivery system of claim 1 , wherein the housing includes a base member comprising the rupture device and a top member.3. The fragrance delivery system of claim 2 , wherein the top member includes a top surface and at least one sidewall depending therefrom.4. The fragrance delivery system of claim 2 , wherein the top member defines at least one aperture that receives the cartridge therein.5. The fragrance delivery system of claim 2 , wherein the top member further defines a second aperture therein and the fragrance delivery device further comprises a second cartridge containing a fragrance medium therein and receivable within the second aperture of the top member.6. The fragrance delivery device according to claim 5 , wherein the top member is rotatable with respect to the base member and the second cartridge is engageable with the rupture device of the base member to release the fragrance medium from the second cartridge.7. The ...

REACTOR

Provided is a reactor in which a catalyst to accelerate reaction of a reactant is allowed to act on a reaction fluid having the reactant. The reactor has a partition that defines, in a parallel form, a plurality of reaction flow passages through which the reaction fluid flows, and a plurality of catalyst structures, each having a catalyst and being respectively provided in each of the plurality of reaction flow passages. The partition has a communicating portion allowing the plurality of reaction flow passages to communicate mutually. 1. A reactor in which a catalyst to accelerate reaction of a reactant is allowed to act on a reaction fluid having a reactant , the reactor comprising:a partition that defines, in a parallel form, a plurality of reaction flow passages through which the reaction fluid flows; anda plurality of catalyst structures, each having the catalyst and being respectively provided in each of the plurality of reaction flow passages;wherein the partition has a communicating portion allowing the plurality of reaction flow passages to communicate with each other.2. The reactor according to claim 1 , wherein the communicating portion of the partition is arranged so that claim 1 , in a range from an inlet to an outlet of the reaction flow passage claim 1 , the plurality of reaction flow passages communicate on the inlet side.3. The reactor according to claim 1 , wherein the partition includes one or a plurality of partition walls extending along a flow direction of the reaction fluid claim 1 , the partition wall is configured to include at least two partial partition walls arranged apart from each other so as to have a gap therebetween claim 1 , and the communicating portion of the partition has the gap of the partition wall.4. The reactor according to claim 1 , wherein the partition includes one or a plurality of partition walls extending along a flow direction of the reaction fluid claim 1 , and the communicating portion of the partition has a cutout ...

THERMAL DECOMPOSITION TREATMENT APPARATUS AND THERMAL DECOMPOSITION TREATMENT METHOD

There is provided with a thermal decomposition treatment apparatus capable of ensuring a sufficient residence time of a resin. The thermal decomposition treatment apparatus for thermally decomposing a resin, comprises: a barrel into which the resin is introduced; and a moving unit configured to move the resin from an introduction port side for the resin to a discharge port side for a thermally decomposed product of the resin in the barrel, wherein the thermal decomposition treatment apparatus includes an enlarged portion having an enlarged cross-sectional area on the discharge port side of the barrel. 1. A thermal decomposition treatment apparatus for thermally decomposing a resin , comprising:a barrel into which the resin is introduced; anda moving unit configured to move the resin from an introduction port side for the resin to a discharge port side for a thermally decomposed product of the resin in the barrel, whereinthe thermal decomposition treatment apparatus includes an enlarged portion having an enlarged cross-sectional area on the discharge port side of the barrel.2. The thermal decomposition treatment apparatus according to claim 1 , wherein the moving unit includes a first moving unit on the introduction port side and a second moving unit on the discharge port side.3. The thermal decomposition treatment apparatus according to claim 2 , wherein an outer diameter of the second moving unit is larger than an outer diameter of the first moving unit.4. The thermal decomposition treatment apparatus according to claim 2 , wherein an axis of the second moving unit is shifted from an axis of the first moving unit.5. The thermal decomposition treatment apparatus according to claim 2 , wherein the second moving unit is interlocked and connected to the first moving unit via a power transmission unit.6. The thermal decomposition treatment apparatus according to claim 5 , wherein the power transmission unit includes a gear claim 5 , and the gear has a through hole.7. ...

Premixing Apparatus

A premixing apparatus has a butterfly valve provided in an air supply passage, a zero governor and a variable throttle valve interposed in a gas supply passage. A control is performed to switch a combustion capacity between at least two stages of a large-capacity stage and a small-capacity stage through change in opening degrees of the butterfly valve and the variable throttle valve. At the small-capacity time, in case the opening degree of the variable throttle valve, when regulated so that the λ becomes a predetermined value, has been changed more to the small-opening-degree side than the predetermined small-capacity opening degree, in a state in which the opening degree of the variable throttle valve has been returned to the predetermined small-capacity opening degree, the opening degree of the butterfly valve is regulated such that the λ becomes the predetermined value, and the small-capacity opening degree of the butterfly valve is renewed to the predetermined value when the λ becomes the predetermined value. 1. A premixing apparatus for mixing air with a fuel gas to supply a burner with an air-fuel mixture through a fan , including:a zero governor for regulating a secondary gas pressure to an atmospheric pressure, the zero governor being interposed in a gas supply passage whose downstream end is connected to a gas suction part disposed in an air supply passage on an upstream side of the fan; a variable throttle valve interposed in a portion, on a downstream side of the zero governor, of the gas supply passage; a butterfly valve interposed in a portion, on an upstream side of the gas suction part, of the air supply passage; an excess air ratio detecting device for detecting an excess air ratio of the air-fuel mixture; and a control device,the control device being constructed to control: switching of a combustion capacity between at least two stages of a large-capacity stage and a small-capacity stage through changes in opening degree of the butterfly valve and ...

NON-CHEMICAL, MECHANICAL PROCEDURE FOR THE DEVULCANIZATION OF SCRAP RUBBER AND/OR ELASTOMERS AND APPARATUS THEREFOR

A non-chemical, mechanical procedure for the devulcanization of scrap rubber and/or elastomers and apparatus therefor. The abstract of the disclosure is submitted herewith as required by 37 C.F.R. §1.72(b). As stated in 37 C.F.R. §1.72(b): A brief abstract of the technical disclosure in the specification must commence on a separate sheet, preferably following the claims, under the heading “Abstract of the Disclosure.” The purpose of the abstract is to enable the Patent and Trademark Office and the public generally to determine quickly from a cursory inspection the nature and gist of the technical disclosure. The abstract shall not be used for interpreting the scope of the claims. Therefore, any statements made relating to the abstract are not intended to limit the claims in any manner and should not be interpreted as limiting the claims in any manner. 1. Procedure for devulcanization of rubber and/or elastomers the molecular chains of which are destructible by mechanical and thermal stress , wherein the mechanical and thermal stress is generated in a planetary roller extruder whereat the planetary roller extruder comprising a housing , planetary spindles and a central spindle; and the central spindle is intermeshing with the planetary spindles and the planetary spindles with an internal toothing of the housing or the internal toothing of an intended liner in the housing so that a revolution of the central spindle causes a rotation of the planetary spindles around the central spindle in the housing , at which the planetary spindles of one section slide with the facing surface at a stop ring of this section , whereat in the planetary roller extruder is at least one dispersion ring intended which reduces the flow cross-section for the rubber and/or the elastomers more than a stop ring creating said mechanical and/or thermal stress.2. Procedure as per claim 1 , wherein rubber and/or elastomers comprise rubber and/or elastomers the molecular chains of which are ...

FUEL CELL APPARATUS

A fuel cell apparatus may include a fuel cell module; a heat exchanger; a circulation line connected to the heat exchanger; a heat dissipator located in the circulation line; and an exterior case which houses the fuel cell module, the heat exchanger, the heat dissipator, and at least part of the circulation line. The heat dissipator may be provided with two openings, and includes at least a duct which defines an air flow channel between the two openings; a fan located on first opening side of the two openings in the air flow channel; and a radiator located on the second opening side of the two openings in the air flow channel. The exterior case may be provided with two ventilation holes to which the two openings are connected directly or via an air passageway, respectively, and the duct includes a plurality of separable parts. 1. A fuel cell apparatus , comprising:a fuel cell module;a heat exchanger which carries out heat exchange between exhaust gas from the fuel cell module and a medium;a circulation line connected to the heat exchanger, the circulation line allowing the medium to circulate through the heat exchanger;a heat dissipator located in the circulation line, the heat dissipator cooling the medium flowing through the heat exchanger, the heat dissipator provided with two openings, a duct which defines an air flow channel between the two openings, the duct comprising a plurality of separable parts;', 'a fan located closer to a first opening of the two openings than a second opening of the two openings in the air flow channel, the fan producing flowing air; and', 'a radiator located closer to the second opening than the first opening in the air flow channel, the radiator carrying out heat exchange between the medium and air flowing through an interior of the air flow channel; and, 'the heat dissipator comprisingan exterior case which houses the fuel cell module, the heat exchanger, the heat dissipator, and at least part of the circulation line, the exterior ...

Methods for Improving Respiratory System Health and Increasing the Concentration of Hypothiocyanate Ion in Vertbrate Lungs

The present disclosure relates to methods and devices to improve respiratory system health, increase resistance to infection, and increase the hypothiocyanate ion in mammalian lungs. The methods generally comprise: generating a Hydrogen Peroxide Gas that is non-hydrated and free of ozone, and directing the gas comprising primarily Hydrogen Peroxide Gas into an environment and exposing a subject to the environment such that the Hydrogen Peroxide Gas acts to the increase of the hypothiocyanate ion in mammalian lungs. 1. An enclosed space for human or veterinary use , said enclosed space comprising purified hydrogen peroxide gas (PHPG) at a concentration of at least 0.01 parts per million wherein said PHPG is non-hydrated and free of ozone.2. The enclosed space of claim 1 , wherein said space is a dwelling.3. The enclosed space of claim 1 , wherein said purified hydrogen peroxide gas (PHPG) is introduced from an indoor air recirculation stream.4. (canceled)5. (canceled)6. (canceled)7. (canceled)8. (canceled)9. A method for treating a respiratory illness in a subject comprising:providing an environment comprising a purified hydrogen peroxide gas (PHPG) that is substantially free of hydration and ozone at a final concentration of at least 0.01 parts per million (ppm); andexposing said subject to said environment for at least one period of time, wherein said treating comprises reducing the severity of a respiratory infection, reducing the duration of a respiratory infection, reducing the severity of an allergy, preventing transmission of a respiratory infection, reducing transmission of a respiratory infection in a population, improving lung function, or any combination thereof.10. The method of claim 9 , wherein said improving lung function comprises increasing static lung volume claim 9 , increasing total lung capacity claim 9 , increasing the partial pressure of oxygen in arterial blood gases claim 9 , decreasing residual volume claim 9 , or any combination thereof.11. ...

METHOD AND SYSTEM FOR THE PRODUCTION OF METHANOL

A process for preparing methanol by a methanol synthesis reaction of carbon dioxide with hydrogen may involve a distillation step and a condensation step following the synthesis of a crude methanol. A volatile component and water may be separated off from a methanol-containing product stream, and a gas stream containing a volatile component that has been separated off may be discharged at least partially as offgas. At least part of the gas stream that has been separated off may be recirculated into the methanol synthesis reaction. A plant for preparing methanol can store or utilize electric power generated from renewable energy sources and provide facilities for discharging the offgas stream, which can be purified by catalytic after-combustion. Alternatively, the plant can be configured without discharge of an offgas substream, or the offgas streams are so small that they can be released without treatment into the environment at a suitable position. 135.-. (canceled)36. A process for preparing methanol by reaction of carbon dioxide with hydrogen , the process comprising:feeding a product stream obtained in a methanol synthesis reaction to at least one of a high-pressure separator or a low-pressure separator where a gas stream is separated off from a methanol-containing product stream;feeding the methanol-containing product stream, after the gas stream is separated off, to a distillation step where water is separated off from the methanol-containing product stream; andrecirculating volatile components that have been separated off in the distillation step at least partly into a mixing and compression section located upstream of the methanol synthesis reaction.37. The process of comprising at least one ofat least partially discharging a gas stream that contains at least one of the volatile components as offgas, orrecirculating at least part of the gas stream that contains the at least one of the volatile components to the methanol synthesis reaction.38. The process of ...

DISINFECTANT SYSTEM

A disinfectant system including a pouch enclosing a first reagent, the first reagent releasing a disinfecting vapor when exposed to moisture. A moisture transfer element is included engageable with the pouch. 1. A disinfectant system , comprising:a moisture activated first reagent releasing a disinfecting vapor when exposed to moisture;a container, the moisture activated first reagent being retainable within the container; anda hatch substantially enclosing the moisture activated first reagent within the container when movably coupled with the container, the hatch containing at least one aperture configured to controllably release the disinfecting vapor when the moisture activated first reagent is exposed to moisture.2. The disinfectant system of claim 1 , further comprising a pouch claim 1 , and wherein the pouch encloses the moisture activated first reagent.3. The disinfectant system of claim 2 , further comprising a moisture transfer element claim 2 , and wherein the moisture transfer element is releasably engageable with the pouch and the pouch is removeably insertable within a portion of the moisture transfer element.4. The disinfectant system of claim 3 , wherein the moisture transfer element defines a slit claim 3 , and wherein the pouch is removeably insertable within the slit.5. The disinfectant system of claim 3 , wherein the moisture transfer element is a sponge.6. The disinfectant system of claim 5 , wherein the sponge is removeably insertable into the container.7. The disinfectant system of claim 2 , wherein the pouch includes a moisture activated second reagent different than the moisture activated first reagent.8. The disinfectant system of claim 1 , wherein the at least one aperture includes a plurality of apertures.9. The disinfectant system of claim 1 , wherein the container is configured to retain a volume of liquid.10. The disinfectant system of claim 1 , wherein the hatch is pivotally coupled to the container.11. A disinfectant system claim 1 , ...

SYSTEMS AND METHODS FOR EXTRACTING AND PROCESSING GASES FROM SUBMERGED SOURCES

Systems and methods for extracting and processing gases from submerged sources are disclosed. A system for removing and processing a gas from a submerged area in accordance with a particular embodiment includes a membrane or other open-bottom structure having a port and being disposed over at least a portion of the submerged area so as to at least partially enclose a volume of the gas. The system can further include a chemical reactor coupled to the open-bottom structure to receive the gas, and positioned to conduct a non-combustion reaction to dissociate a constituent from a donor substance of the gas. 127-. (canceled)28. A system for removing and processing a gas from a submerged area , comprising:a membrane disposed over at least a portion of the submerged area and at least partially enclosing a gas volume, the membrane having an extraction port;an extraction conduit having first and second portions, the first portion being in fluid communication with the gas volume via the extraction port; anda chemical reactor coupled to the second portion of the extraction conduit to receive gas from the gas volume, the chemical reactor having a reaction zone positioned to conduct a non-combustion reaction to dissociate a donor substance of the gas.29. The system of wherein the membrane has a peripheral edge and a highest point located inwardly from the peripheral edge claim 28 , and wherein the extraction port is positioned at the highest point of the membrane.30. The system of wherein the membrane includes a gas release port positioned to release a portion of the gas volume from the membrane.31. The system of wherein a portion of the membrane is deformable to define claim 28 , at least in part claim 28 , a reservoir enclosing the gas volume.32. The system of claim 28 , further comprising a floating support structure carrying the chemical reactor.33. The system of claim 28 , further comprising a turbine coupled between the extraction conduit and the chemical reactor to ...

Heater with a Fuel Cell Stack Assembly and a Combustor and Method of Operating

A heater includes a heater housing; a fuel cell stack assembly within the heater housing and having a plurality of fuel cells; a combustor within the heater housing for combusting a mixture of fuel and air to form a heated combustor exhaust that is discharged into the heater housing; a combustor fuel supply conduit for supplying the fuel to the combustor; an anode exhaust conduit for communicating anode exhaust from the fuel cell stack assembly out of the heater housing; and a combustor bypass conduit in fluid communication with the combustor fuel supply conduit and the anode exhaust conduit for allowing a portion of the fuel to bypass the combustor. 1. A heater comprising:a heater housing extending along a heater axis;a fuel cell stack assembly disposed within said heater housing and having a plurality of fuel cells which convert chemical energy from a fuel into heat and electricity through a chemical reaction with an oxidizing agent, said fuel cell stack assembly having 1) a fuel cell stack fuel inlet for introducing said fuel to a plurality of anodes of said plurality of fuel cells, 2) a fuel cell stack oxidizing agent inlet for introducing said oxidizing agent to a plurality of cathodes of said plurality of fuel cells, 3) an anode exhaust outlet for discharging an anode exhaust comprising unspent fuel from said plurality of fuel cells, and 4) a cathode exhaust outlet for discharging a cathode exhaust comprising unspent fuel cell oxidizing agent from said plurality of fuel cells;a combustor disposed within said heater housing for combusting a mixture of said fuel and said oxidizing agent to form a heated combustor exhaust, said combustor having 1) a combustor fuel inlet for introducing said fuel into said combustor, 2) a combustor oxidizing agent inlet for introducing said oxidizing agent into said combustor, and 3) a combustor exhaust outlet for discharging said heated combustor exhaust from said combustor into said heater housing;a combustor fuel supply conduit ...

APPARATUS, SYSTEM, AND METHOD FOR CONVERTING VARIED SOURCE INDUSTRY WASTE INTO ENERGY

An apparatus, system, and method for processing hydrocarbon-containing wastes are described. The system and method include the use of a gasification apparatus comprising a rotary kiln reactor and a gas distributor. The rotary kiln reactor and gas distributor are configured to generate multiple reaction environments within the gasification apparatus. Each of the reaction environments has unique temperature reaction conditions to suit various physical and chemical properties associated with processing of the varied-source hydrocarbon-containing wastes. 1. An system for gasification of varied-source hydrocarbon-containing wastes , comprisinga rotary kiln configured to thermochemically transform varied-source hydrocarbon-containing wastes into combustible fuel gases, the varied-source hydrocarbon-containing wastes having varied physical and chemical properties, wherein a length and a diameter of the rotary kiln provides requisite residence time for gasification of the varied-source hydrocarbon-containing wastes and the reactor has at least two reaction zones;a feeder in communication with the rotary kiln reactor;a gas distributor substantially included within the rotary kiln, the gas distributor configured to introduce reaction gases into the rotary kiln reactor along a length of the rotary kiln;a first cyclone in communication with the kiln, the first cyclone configured to separate carbonaceous ash from non-ash carbonaceous materials;a quencher or wet heat exchanger in communication with the first cyclone, wherein a second cyclone in communication with the quencher;a burner in communication with the quencher, the burner configured to combust the non-ash carbonaceous materials.2. (canceled)3. (canceled)4. The system of claim 1 , wherein the gas distributor is configured to introduce different quantities of reaction gases along a length of the rotary kiln reactor to create reaction zones claim 1 , the reaction zones created according to chemical properties of the varied- ...

REVERSIBLE SELF-REPAIRING EPOXY RESIN AND PREPARATION AND RECOVERY REMOULDING METHOD THEREFOR

This invention provides a self-healable epoxy resin and its preparation, recycling and remolding method. With the catalyst of potassium iodide, an ester solution of 2-mercaptoacetic acid was oxidated by 30% HOto form 2,2′-dithiodiacetic acid; then 2,2′-dithiodiacetic acid was dehydrated and cyclizated by anhydride to form 1,4,5-oxadithiepane-2,7-dione; 1,4,5-oxadithiepane-2,7-dione and methylhexahydrophthalic anhydride were mixed by mass ratio and cured with epoxides to get the self-healable epoxy resin. Through controlling dynamic and permanent three-dimensional crosslinked network, the self-healable epoxy resins provided in this invention exhibit high thermal resistance and improved mechanical properties as well as excellent self-healing ability, recyclability and remoldability. This invention provides a preparation method with the merits of low cost, simple production processes, broad application prospects and strong utility. 1. A method for preparing a self-healable epoxy resin , comprising:{'sub': 2', '2, 'b': '2', '(1) by mass, at 20 to 30° C., 120 parts of 2-mercaptoacetic acid, 500 to 700 parts of ester solvent and 0.6 to 1.2 parts of potassium iodide were mixed homogeneously to obtain a solution; 80 to 90 parts of 30 wt % HOwere added dropwise to the solution and continued to react for to 4 h to get 2,2′-dithiodiacetic acid;'}(2) by mass, at 20 to 30° C., 100 parts of 2,2′-dithiodiacetic acid and 120 to 150 parts of anhydride were mixed homogeneously and continued to react for 2 to 4 h to get 1,4,5-oxadithiepane-2,7-dione;(3) by mass, at 50 to 70° C., 100 parts of epoxy resin, 42 to 84 parts of 1,4,5-oxadithiepane-2,7-dione and 0 to 43 parts of methylhexahydrophthalic anhydride were mixed homogeneously, after curing, the self-healable epoxy resin was obtained.2. A method for preparing 1 ,4 ,5-oxadithiepane-2 ,7-dione , comprising:{'sub': 2', '2, '(1) by mass, at 20 to 30° C., 120 parts of 2-mercaptoacetic acid, 500 to 700 parts of ester solvent and 0.6 to 1 ...

PROPANE VAPORIZER FOR FUEL POWERED DEVICES

The present invention is a device that supplies the latent heat for vaporization of L.P. gases. The device for a supply of fuel vapor to a fuel powered device, comprising of a supply tank; a liquid bath having a temperature control system; a LPG flow line immersed inside the liquid bath; a heating system to heat the LPG; and a vaporizer control system comprising a temperature sensor to measure the temperature of the liquid bath, the temperature sensor is connected to a solenoid valve in the vapor supply line, and wherein said temperature sensor shutting off the solenoid valve when the bath temperature drops below a predetermined temperature.

Recycle Feedstocks for On-Demand Article Manufacturing

A method of recycling a polymer structure includes converting a first polymer structure into feedstock. The first polymer structure comprises particles that are bonded to one another by chemical click bonds to form a first shape. The first polymer structure is converted into feedstock particles by breaking the click bonds. The feedstock particles are formed into a second shape, and the feedstock particles are chemically click-bonded together to form a second polymer structure having a second shape. Breaking the click bonds may include heating the particles. The structures may be formed by causing first particles having dienes to chemically bond to dienophiles of second particles. 1. A method of recycling a polymer structure , the method comprising:converting a first polymer structure comprising particles that are bonded to one another by chemical click bonds to form a first shape into feedstock particles by breaking the click bonds;forming the feedstock particles into a second shape;chemically click bonding the feedstock particles together to form a second polymer structure having a second shape.2. The method of claim 1 , wherein:breaking the click bonds includes heating the particles.3. The method of claim 1 , including:forming the first structure by causing first particles having dienes to chemically bond to dienophiles of second particles.4. The method of claim 3 , including:forming epoxy particles having surfaces;chemically bonding first polymers comprising dienes to the surfaces of the epoxy particles to form the first particles;chemically bonding second polymers comprising dienophiles to the surfaces of epoxy particles to form the second particles.5. The method of claim 4 , wherein:the first and second polymers are formed from monomeric species compatible with chemically interacting with amine species on the epoxy particle surface such that the polymer is chemically bound.6. The method of claim 5 , wherein:the polymers are synthesized in solution with the ...

REACTOR

A reactor includes a reaction-side flow passage through which a reaction fluid being a fluid constituting a reaction object flows; a temperature controller (heat-medium side flow passage) configured to heat or cool the reaction fluid from outside the reaction-side flow passage; and a catalyst configured to promote a reaction of the reaction fluid, the catalyst provided in the reaction-side flow passage so that a contact area with the reaction fluid is larger on a downstream side than on an upstream side in the reaction-side flow passage. 1. A reactor comprising:a reaction-side flow passage through which a reaction fluid as a reaction object flows;a temperature controller configured to heat or cool the reaction fluid from outside the reaction-side flow passage; anda catalyst configured to promote a reaction of the reaction fluid, the catalyst provided in the reaction-side flow passage so that a contact area with the reaction fluid is larger on a downstream side than on an upstream side in the reaction-side flow passage.2. The reactor according to claim 1 , whereinthe temperature controller includes a heat-medium side flow passage through which a heat medium flows as a fluid performing heat exchange with the reaction fluid flowing through the reaction-side flow passage, the heat-medium side flow passage being provided in parallel with the reaction-side flow passage with a heat-transfer partition in between.3. The reactor according to claim 2 , whereina gas flows as the heat medium in the heat-medium side flow passage.4. The reactor according to claim 2 , whereinthe reaction-side flow passage and the heat-medium side flow passage are alternately stacked.5. The reactor according to claim 3 , whereinthe reaction-side flow passage and the heat-medium side flow passage are alternately stacked.6. The reactor according to claim 1 , wherein:the catalyst has a plate shape; andthe catalyst is divided into a plurality of parts and arranged in a flowing direction of the reaction ...

Plasma-arc-through Apparatus and Process for Submerged Electric Arcs with Venting

An application for a recycler includes a pressure and temperature resistant metal vessel that is filled with a liquid. Within the vessel is at least one submerged electric arc between a pair of electrodes (e.g. carbon based electrodes) powered by either a DC or AC current. The electric arc produces a combustible gas as the liquid is pumped through a bore in one or both of the electrodes, delivering the liquid directly to the location of the arc, thereby reducing or eliminating any ignition of the gas by the arc. Should ignition occur, at least one vent in the electrode(s) or electrode holder(s) vents pressure from within the bore to the vessel area outside of the electrode(s). 1. An apparatus for producing usable energy comprising:a pressure and temperature resistant vessel at least partially filled with a liquid;two electrodes held within the vessel and submerged within the liquid, a bore passing through a first electrode of the two of electrodes;means for delivering an electric current to each of the two electrodes, forming an arc between the two electrodes; the liquid flows through the bore and exits the bore at the arc; andat least one vent;wherein a combustible gas is produced by the arc and the combustible gas percolates to the surface of the liquid for collection.2. The apparatus according to claim 1 , wherein at least one of the two electrodes is a carbon-based electrode.3. The apparatus according to claim 1 , wherein the electric current is a direct electric current;4. The apparatus according to claim 3 , wherein the direct electric current pulses at a frequency that is a sub-multiple of a resonating frequency of the liquid.5. The apparatus according to claim 1 , wherein the electric current is an alternating electric current.6. The apparatus according to claim 5 , wherein the alternating electric current has a variable voltage and a variable frequency.7. The apparatus according to claim 5 , wherein a frequency the alternating electric current is a sub- ...

SLAG DISCHARGE APPARATUS AND SLAG DISCHARGE METHOD

A slag crusher () is provided in a combustor of a gasifier () for gasifying a carbonaceous feedstock, and discharges falling slag generated in the combustor from the gasifier (). The slag crusher () is provided with: a screen () provided so as to intersect with the direction in which the slag falls, the screen () having a plurality of openings () and passing slag having a diameter smaller than that of the openings (); a spreader () for moving over the top surface of the screen () and crushing slag deposited on the top surface of the screen (); and a nozzle () for spraying high-pressure water onto the slag deposited on the screen (). The slag deposited on the top surface of the screen () thereby more easily passes from the openings () in the screen (). 1. A slag discharge apparatus which is provided on a combustor of a gasifier gasifying a carbonaceous feedstock and discharges slag produced in and falling from the combustor out of the gasifier , comprising:a screen which is provided transversely with respect to the fall direction of the slag and has a plurality of openings to allow slag which is smaller than diameters of the openings to pass through the screen;crushing means for moving along a top face of the screen to crush the slag accumulated on the top face of the screen; andwater flow generating means for allowing liquid to flow onto the slag accumulated on the screen to generate a water flow,wherein a plurality of crushing means adjacent to each other are provided on the top surface of the screen, the screen is partitioned between the adjacent crushing means by partition means so as to be divided, and the water flow generating means is provided for each divided region.2. The slag discharge apparatus according to claim 1 ,wherein the water flow generating means is provided on a side wall of the screen which is erected in parallel with respect to an operating direction of the crushing means.3. The slag discharge apparatus according to claim 1 ,wherein the water ...

STARTER FOR THE DEVULCANISATION OF SCRAP RUBBER

A starter for the devulcanisation of scrap rubber. The abstract of the disclosure is submitted herewith as required by 37 C.F.R. §1.72(b). As stated in 37 C.F.R. §1.72(b): A brief abstract of the technical disclosure in the specification must commence on a separate sheet, preferably following the claims, under the heading “Abstract of the Disclosure.” The purpose of the abstract is to enable the Patent and Trademark Office and the public generally to determine quickly from a cursory inspection the nature and gist of the technical disclosure. The abstract shall not be used for interpreting the scope of the claims. Therefore, any statements made relating to the abstract are not intended to limit the claims in any manner and should not be interpreted as limiting the claims in any manner. 120-. (canceled)21. A method of devulcanizing crosslinked rubber and crosslinked elastomers using a planetary roller extruder , which planetary roller extruder comprises: a central spindle , at least one group of planetary spindles , a housing , and a feed part , said method comprising the steps of:feeding vulcanized rubber and/or elastomers through said feed part and into said housing;operating said planetary roller extruder by rotating said central spindle about its rotational axis, and thereby both rotating said at least one group of planetary spindles about each of their rotational axes and revolving said at least one group of planetary spindles about said central spindle;generating mechanical and thermal stress on said vulcanized rubber and/or elastomers by kneading and/or crushing of said vulcanized rubber and/or elastomers by said central spindle and said at least one group of planetary spindles;breaking or destroying the molecular chains or bonds of said vulcanized rubber and/or elastomers by said mechanical and thermal stress; (A) adding particles of said vulcanized rubber and/or elastomers eccentrically to the center of the planetary roller extruder module between the ...

FUEL CELL SYSTEM AND METHOD FOR WARMING UP FUEL CELL SYSTEM

A fuel cell system includes a fuel cell configured to be supplied with fuel and air to generate electricity, a reformer configured to reform the fuel to be supplied to the fuel cell, a heat source device configured to heat an off-gas discharged from the fuel cell to produce a heating gas and configured to heat the reformer, a fuel cell heating device configured to heat the air to be supplied to the fuel cell using the heating gas, a fuel cell temperature acquisition unit configured to acquire a temperature of the fuel cell, and a reformer temperature acquisition unit configured to acquire a temperature of the reformer. The fuel cell system includes a controller configured to, in a warm-up operation to perform a warm-up of the reformer and a warm-up of the fuel cell, control at least one of the heat source device and the fuel cell heating device based on the temperature of the reformer and the temperature of the fuel cell to adjust at least one of a heating amount of the off-gas and a heating amount of the air by the heating gas. 19.-. (canceled)10. A fuel cell system comprising:a fuel cell configured to be supplied with fuel and air to generate electricity;a reformer configured to reform the fuel to be supplied to the fuel cell;a heat source device configured to heat an off-gas discharged from the fuel cell to produce a heating gas and configured to heat the reformer;a fuel cell heating device configured to heat the air to be supplied to the fuel cell using the heating gas;a fuel cell temperature acquisition unit configured to acquire a temperature of the fuel cell;a reformer temperature acquisition unit configured to acquire a temperature of the reformer; anda controller configured to, in a warm-up operation to perform a warm-up of the reformer and a warm-up of the fuel cell, control at least one of the heat source device and the fuel cell heating device based on the temperature of the reformer and the temperature of the fuel cell to adjust at least one of a ...

METHODS FOR MAKING RECYCLABLE AND DEPOLYMERIZABLE POLYMER NETWORK MATERIALS VIA THIOURETHANE DYNAMIC CHEMISTRY

Polythiourethane polymer networks that can be processed and/or recycled are provided. Also provided are methods of forming the polythiourethane polymer networks using excess thiol and/or a dual catalyst system and methods for reprocessing and recycling the polyurethane polymer networks. The polythiourethane polymer networks are based on thiourethane dynamic chemistry. 1. A polythiourethane composition comprising:a polythiourethane polymer network comprising polymer chains covalently linked by aliphatic crosslinkers via thiourethane linkages, wherein the aliphatic crosslinkers comprise free thiol groups; anda first catalyst that catalyzes reactions between thiol groups and isocyanate groups.2. The composition of claim 1 , wherein the mole ratio of free thiol groups to thiourethane linkages in the polythiourethane polymer network is no greater than 1:5.3. The composition of claim 1 , wherein the mole ratio of free thiol groups to thiourethane linkages in the polythiourethane polymer network is in the range from 1:20 to 1:5.4. The composition of claim 1 , wherein the first catalyst is a basic catalyst.5. The composition of claim 1 , further comprising a second catalyst that catalyzes reactions between thiol groups and isocyanate groups claim 1 , wherein the first catalyst is a basic catalyst having a pKa in water at 20° C. of at least 10 and the second catalyst is a basic catalyst having a pKa in water at 20° C. of 6 or lower.6. The composition of claim 5 , wherein the first catalyst is an amidine and the second catalyst is an organophosphine.7. The composition of claim 5 , wherein the first catalyst is 1 claim 5 ,8-diazabicyclo[5.4.0]undec-7-ene or 1 claim 5 ,5-diazabicyclo[4.3.0]non-5-ene and the second catalyst is triphenylphosphine.8. A method of forming a dynamic polythiourethane polymer network claim 5 , the method comprising: a polymer having at least two isocyanate groups;', 'an aliphatic multifunctional thiol crosslinker comprising at least three free thiol ...

Solid deodorizing compositions

METHOD FOR FORMING POLYESTER MATERIAL FROM RECYCLED FILM

A method for forming polyester material from recycled film including the following steps is provided: performing a film surface treatment on the recycled film to form a recycled material including polyester; fragmenting the recycled material to form a recycled chipped material, wherein the recycled chipped material has a first intrinsic viscosity; and forming the polyester material by the recycled chipped material, wherein the polyester material has a second intrinsic viscosity, and the second intrinsic viscosity is greater than the first intrinsic viscosity. 1. A method for forming a polyester material from a recycled film , comprising:performing a film surface treatment on the recycled film to form a recycled material comprising polyester;fragmenting the recycled material to form a recycled chipped material, wherein the recycled chipped material has a first intrinsic viscosity; andforming the polyester material by the recycled chipped material, wherein the polyester material has a second intrinsic viscosity, and the second intrinsic viscosity is greater than the first intrinsic viscosity.2. The method for forming the polyester material according to claim 1 , wherein the step of performing the film surface treatment on the recycled film is: physically removing a surface material of the recycled film.3. The method for forming the polyester material according to claim 1 , wherein the first intrinsic viscosity is less than or equal to 0.6 dL/g claim 1 , and/or the second intrinsic viscosity is greater than or equal to 0.63 dL/g.4. The method for forming the polyester material according to claim 1 , wherein the method of forming the polyester material through the recycled chipped material comprises:placing the recycled chipped material in an extruding apparatus, and performing a heating step on the recycled chipped material placed in the extruding apparatus, thereby forming the polyester material through the extruding apparatus.5. The method for forming the polyester ...

Mixed gas supply system

Method and apparatus for maintaining a constant ratio of gases in a mixture subject to steady state and intermittent flow conditions

The present invention reveals a gas mixing device which maintains constant gas ratios under both steady state and intermittent flow conditions, and reduces mixture errors inherent with multiple gauges by providing only one pressure gauge to read the inlet pressure at each inlet port. To accomplish its purpose, the device comprises a chamber defined by two opposing hollow core pistons, a downstream control valve, and an upstream delay valve. The control valve, assisted by one piston, opens and closes in response to the upper and lower operating pressure limits of a receiver. The delay valve, assisted by the other piston, closes after the control valve closes and opens abruptly only after a significant drop in pressure within the chamber, the result of the control valve having suddenly opened wide. A single pressure measuring assembly, rotatably mounted to the gas mixing device, communicates with each inlet port.

Mixing device for at least two gases

Catalytic reactor and process

Procedimiento de preparacion de un gas rico en oxido de carbono.

EL PROCESO PARA LA PREPARACION DE GAS RICO EN MONOXIDO DE CARBONO CONSTA DE LA REACCION DE UN GAS MEZCLADO DE HIDROGENO Y DIOXIDO DE CARBONO EN PRESENCIA DE UN CATALIZADOR CONVERSOR A GAS RICO EN MONOXIDO DE CARBONO, CUYO PROCESO ADEMAS CONSISTE EN HACER REACCIONAR PARTE DEL DIOXIDO DE CARBONO E HIDROGENO EN EL ALIMENTADOR DEL GAS EN UNA REACCION EXOTERMICA PARA DAR METANO EN UNA REACCION SIMULTANEA A LA DE PRODUCCION DE MONOXIDO DE CARBONO PRODUCIENDO REACCION Y LLEVANDO A CABO AMBAS REACCIONES BAJO CONDICIONES ADIABATICAS, DE MODO QUE LA REACCION EXOTERMICA DE PRODUCCION DE METANO EXOTERMICAMENTE SUMINISTRA EL CALOR NECESARIO PARA LA REACCION DE PRODUCCION EXOTERMICA DE MONOXIDO DE CARBONO.

Gel air fragrancing composition and method for making the same

An aqueous self-supporting gel composition is provided, which consists essentially of: a) 1 to 20% of a fragrance material (preferably a fragrant oil), b) 2 to 10% of a carrageenan constituent, c) 0 to 2% of a preservative, d) 0 to 2% of a coloring agent, and e) 0 to 0.5% surfactant, the balance being water and all percentages being by weight of the composition.

Способ получения синтетического газа

Изобретение относится к получению синтетического газа и может быть использовано в химической промышленности. Способ получения синтетического газа включает введение метана и углекислого газа в реакционную камеру. Через реакционную камеру направляют слой углеродсодержащего твердого материала как движущийся слой. В слое углеродсодержащего твердого материала метан и углекислый газ преобразовывают в водород и окись углерода. Образующийся в реакционной камере синтетический газ противотоком подводят к движущемуся слою и в нем охлаждают. В качестве углеродсодержащего твердого материала применяют углеродсодержащий гранулят, содержащий по меньшей мере 80 мас. % углерода. Изобретение позволяет обеспечить непрерывный режим получения синтетического газа, при котором не требуется регенерация катализатора, создать поток газообразного продукта, который в основном лишен примеси твердых частиц. 12 з.п. ф-лы, 1 ил. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 610 082 C2 (51) МПК C01B 3/34 (2006.01) B01J 8/08 (2006.01) C10J 1/20 (2006.01) C10J 1/26 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ФОРМУЛА (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ 2014103786, 05.07.2012 (24) Дата начала отсчета срока действия патента: 05.07.2012 Дата регистрации: Приоритет(ы): (30) Конвенционный приоритет: 05.07.2011 DE 102011106642.3 (73) Патентообладатель(и): ЛИНДЕ АКЦИЕНГЕЗЕЛЛЬШАФТ (DE), БАСФ СЕ (DE) (45) Опубликовано: 07.02.2017 Бюл. № 4 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 05.02.2014 (56) Список документов, цитированных в отчете о поиске: EP 0191522 A2, 20.08.1986. RU (86) Заявка PCT: EP 2012/002837 (05.07.2012) 2361809 C2, 20.07.2009. US 2003/0208959 A1, 13.11.2003. CH 409890 A, 31.03.1966. US 4726913 A, 23.02.1988. US 2003182861 A1, 02.10.2003. (87) Публикация заявки PCT: 2 6 1 0 0 8 2 R U Адрес для переписки: 129090, Москва, ул. Б. Спасская, 25, строение 3, ООО "Юридическая фирма Городисский и Партнеры" (54) СПОСОБ ПОЛУЧЕНИЯ ...

일산화탄소가 풍부한 가스의 제조방법

변환촉매의 존재하에서 수소와 이산화탄소의 혼합가스를 반응시켜서 일산화탄소가 풍부한 가스를 생성시키는 방법으로서, 그 반응은 또한 일산화탄소 생성반응과 함께 공급가스중 이산화탄소와 수소의 일부를 발열적으로 반응시켜 메탄과 형성시키는 반응을 포함하고 그 두가지 반응을 단열상태하에서 수행하여, 발열반응인 메탄생성 반응이 흡열반응인 일산화탄소 생성반응에 필요한 열을 공급하는 것으로 이루어진 것을 특징으로 하는 일산화탄소가 풍부한 가스의 제조방법.

Method for catalytic production of gas rich in carbon oxide

FIELD: chemical technology. SUBSTANCE: hydrogen-containing gas and gas containing carbon dioxide are mixed and heated. The process is carried out in adiabatic condition under pressure and with the help of catalyst. Thus gas containing carbon oxide and methane is obtained. EFFECT: improved efficiency of the method. 5 cl ДОС ПЧ Го РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (19) 13) ВИ” 2110 477 Сл 5 МК © 01 В 31/18 12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 93056193/25, 10.12.1993 (30) Приоритет: 10.12.1992 ОК 1489/92 (46) Дата публикации: 10.05.1998 (56) Ссылки: ЕК, заявка, 2593164, кл. С 01 В 31/18, 1987. (71) Заявитель: Хальдор Топсеэ А/С (ОК) (72) Изобретатель: Рикард Ваннби[0К], Шарлотте Штуб Нильзен[0К] (73) Патентообладатель: Хальдор Топсеэ А/С (ОК) (54) СПОСОБ КАТАЛИТИЧЕСКОГО ПОЛУЧЕНИЯ (57) Реферат: Использование: в производстве богатого окисью углерода газа. Сущность изобретения: водородсодержащий газ и содержащий двуокись углерода газ смешивают и БОГАТОГО ОКИСЬЮ УГЛЕРОДА ГАЗА нагревают при давлении на катализаторе в адиабатических условиях с получением газа, содержащего окись углерода и метан. 4 З.П. ф-лы. 2110477 С1 КО ДОС ПЧ Го КУЗЗАМ АСЕМСУ ГОК РАТЕМТ$ АМО ТКАОЕМАКК$ (19) ВИ "” 2110 477. 13) СЛ о ° © 01 В 31/18 12) АВЗТКАСТ ОЕ 1МУЕМТОМ (21), (22) АррИсаНоп: 93056193/25, 10.12.1993 (30) Рпошу: 10.12.1992 ОК 1489/92 (46) Рае ог рибИсаНоп: 10.05.1998 (71) АррИсапе: Кпа!’аог Торзеей А/$ (ОК) (72) пуетог. — ЕКага Уапп [ОК], Зпапове ЭМиь МИ'7еп[0К] (73) Ргорпеюг: Кпа!’аог Торзеей А/$ (0К) (54) МЕТНОО РОК САТАЕУТ!С РКОВИСТЮМ ОЕ САЗ ЕСН 1М САВКВОМ ОХШЕ (57) АБзГасЕ: НЕЕО: спеглсеа! 1есйптпоюду. ЗУВЗТАМСЕ: пуадгодеп-сощатта даз апа даз сощатта сагроп Чюхае аге пихеяа апа Пезея. Тпе ргосез$ 15 сатмед оШ шт адарацс -2- сопаШоп ипаег ргеззиге апа м Ше пер ог саамуз. ТПу$ 9даз сотатта сагроп ох4е ап тешпапе 15 оМатея. ЕЕЕЕСТ: ипргоуеа ейаепсу о {пе тапоа. 5 < 2110477 С1 КО ДУтОГЕсС ПЧ ГЭ Изобретение относится к производству ...

一种生产聚甲基丙烯酸甲酯的裂解回收设备

本发明涉及一种聚甲基丙烯酸甲酯的裂解回收设备，包括:研磨机(1)，用于对不合格PMMA品进行研磨形成小尺寸物料；失重补偿给料器(2)，接收所述小尺寸物料并分割称重后继续前输送；裂解挤出机(3)，用于接收所述失重补偿给料器(2)输送的小尺寸物料进行裂解回收；裂解挤出机分离罐(4)，用于收集所述裂解挤出机(3)中出现的溢出液体和蒸汽。本发明的聚甲基丙烯酸甲酯的裂解回收设备可实现连续化工业生产，能够提高物料裂解回收效率，降低环境污染。

制备合成气的方法

本发明提供了制备合成气(3)的方法，其中将甲烷和二氧化碳(2)引入反应空间(R)并使之在升高的温度下在固体(W)的存在下生成氢和一氧化碳。使所述甲烷和二氧化碳通过含碳的颗粒材料(W)并在高温区(H)反应。

Method of improving a solid residue of pyrolysis of car tires

FIELD: technological processes.SUBSTANCE: invention relates to the technology of processing waste tires, in particular the solid carbon-containing residue of pyrolysis of tires. Obtained refined solid carbon-containing residue can be used as sorbents, pigment paints, dyeing powder for office equipment, high-capacity capacitors and ionizers, reinforcing material in the rubber industry, smokeless fuel. Method of refining the solid residue of pyrolysis of tires is that the solid residue of pyrolysis is calcined at the temperature of 700–850 °C in the absence of oxygen of the air until the complete cessation of gas extraction processes takes place.EFFECT: invention allows to improve the quality of the solid carbon-containing residue of pyrolysis of tires, reduce the yield of volatile substances, and also remove unpleasant toxic odor and improve the ecological situation in the regions.1 cl, 3 tbl, 3 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 679 263 C1 (51) МПК C08J 11/00 (2006.01) C08J 11/12 (2006.01) C09C 1/44 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C08J 11/00 (2018.08); C08J 11/12 (2018.08); C09C 1/482 (2018.08) (21)(22) Заявка: 2018119574, 28.05.2018 (24) Дата начала отсчета срока действия патента: Дата регистрации: 06.02.2019 (45) Опубликовано: 06.02.2019 Бюл. № 4 2 6 7 9 2 6 3 R U (56) Список документов, цитированных в отчете о поиске: RU 2557652 C1, 27.07.2015. RU 2603006 С1, 20.11.2016. RU 2391359 C1, 10.06.2010. RU 2321492 C2, 10.04.2008. RU 2128196 C1, 27.03.1999. RU 2361731 C1, 20.07.2009. JP 2011137079 A, 14.07.2011. JP 2003020361 A, 24.01.2003. (54) Способ облагораживания твердого остатка пиролиза автошин (57) Реферат: Изобретение относится к технологии автошин заключается в том, что твердый остаток переработки отработанных автошин, в частности пиролиза прокаливают при температуре 700твердого углеродсодержащего остатка пиролиза 850°С в отсутствие кислорода воздуха до полного автошин. ...

The preparation process of synthetic gas from carbondioxide

Synthetic gas is prepared by continuously reacting carbon dioxide with low grade hydrocarbon or natural gas containing methane and oxygen or steam in a mole ratio of 2:1-5:1 in the presence of a catalyst that comprises nickel, alkali and alkali earth metals supported on silicone such as zeolite, silica, silicate or silica-alumina at 600-1,000deg.C and 0.5-20 atms and a space velocity of 1,000-500,000. The ratio of carbon monoxide to hydrogen in the synthetic gas is 1:2-2:1.

Catalytic Reactor

Dual fluidized bed gasifier

이중 유동층 가스화기가 제공된다. 상기 이중 유동층 가스화기는 하부에서 공기를 공급받아 연소반응을 수행하는 연소부, 상기 연소부의 연소반응 생성물을 분리하고 유동화 매체를 회수하는 사이클론 및 연료, 산화제 및 상기 연소부로부터 유동화 매체에 의해 열을 공급받아 가스화 반응을 수행하는 가스화부를 포함하는 이중 유동층 가스화기에 있어서, 상기 가스화부의 내부에 상,하부가 개방된 도관을 더 포함한다. 상기 이중 유동층 가스화기는 산화제 및 유동화 매체 간 접촉효율을 향상시켜 가스화 효율이 우수하고, 이중 유동층 가스화기의 가스화 연료로써 다양한 연료를 사용할 수 있는 효과가 있다. A dual fluidized bed gasifier is provided. The dual fluidized bed gasifier includes a combustion unit for supplying air from a lower portion to perform a combustion reaction, a cyclone for separating the combustion reaction products of the combustion unit and recovering the fluidization medium, and a fuel, an oxidant, And a gasification section for performing a gasification reaction, wherein the gasification section further includes a conduit in which an upper portion and a lower portion are opened. The dual fluidized bed gasifier improves the contact efficiency between the oxidizing agent and the fluidizing medium, and thus has an excellent gasification efficiency. Thus, it is possible to use various fuels as the gasification fuel of the fluidized bed gasifier.

Heating separator for the separation of metal and resin

본 발명은 금속 및 합성수지 적층 분리대상물의 가열분리장치에 관한 것으로, 구체적으로는 금속적층필름처럼 금속부재와 합성수지 박막이 중첩된 대상물을 가열하여 합성수지 박막을 용융 및 기화처리를 통해 제거하는 과정에서 유증기 및 그에 포함된 타르성분의 제거효율율을 최대화 시킬 수 있도록 함으로써, 대기오염을 최소화 하고 타르성분에 의한 배관 막힘 등의 문제점을 해결할 수 있는 기술이다. 그리고 필터설비를 별도 구비하지 않더라도 간소한 구조를 통해 유증기 및 타르성분의 제거가 가능하도록 함으로써, 설비의 과도한 증가 및 그에 따른 경제적부담 등을 줄일 수 있도록 한 기술이다. 또한 각 가열부를 선택적으로 분리하거나 결합할 수 있도록 함으로써, 상황에 맞게 요구되는 처리용량에 따라 설비의 규모를 조절할 수 있도록 한 기술에 관한 것이다. More particularly, the present invention relates to an apparatus for heating and separating metal and synthetic resin laminated separation objects, and more particularly, to a method of heating and separating metal and synthetic resin laminated materials by heating an object in which a metal member and a synthetic resin thin film are superimposed like a metal laminated film to remove the synthetic resin thin film by melting and vaporizing, And maximizing the efficiency of removal of the tar component contained therein, thereby minimizing air pollution and solving problems such as blockage of piping due to tar component. Even if the filter facility is not provided separately, it is possible to remove the vapor and tar components through a simple structure, thereby reducing the excessive increase of the equipment and the economic burden thereof. The present invention also relates to a technique for adjusting the size of a facility according to a processing capacity required for a specific situation by selectively separating or combining the respective heating units.

Method for preparing a welding fluid of constant physico-chemical characteristics with time, and a plant for its preparation

A method for preparing a welding fluid consisting of a mixture of at least two components. The method including the steps of withdrawing the mixture components from respective tanks and feeding them into a mixing zone at substantially identical pressures, monitoring the composition of the mixture formed, and if the composition is correct, feeding the mixture into a buffer tank to be stored.

Gas mixing control system

METHOD FOR PRODUCING SYNTHETIC GAS

1. Способ получения синтетического газа, по которому метан и углекислый газ вводят в реакционную камеру и в слое углеродсодержащего твердого материала преобразовывают в водород и окись углерода, отличающийся тем, что слой углеродсодержащего твердого материала направляют через реакционную камеру как движущийся слой, причем синтетический газ, который образуется в реакционной камере, противотоком подводят к движущемуся слою и там охлаждают в прямом теплообмене с углеродсодержащим твердым материалом.2. Способ по п. 1, отличающийся тем, что метан и углекислый газ преобразовывают при температурах между 800 и 1600°С, предпочтительно между 900 и 1400°С.3. Способ по п. 1 или 2, отличающийся тем, что в качестве углеродсодержащего твердого материала применяют углеродсодержащий гранулят, который содержит по меньшей мере 80 мас. % углерода и имеет зернистость от 0,1 до 100 мм.4. Способ по п. 1 или 2, отличающийся тем, что соотношение кислород/углерод в газообразных реагентах целенаправленно устанавливают таким образом, что углерод образуется в реакционной камере или отделяется от углеродсодержащего твердого материала.5. Способ по п. 1 или 2, отличающийся тем, что по меньшей мере часть тепловой энергии, которая требуется для производства синтетического газа, вырабатывается в реакционной камере и/или подается в реакционную камеру через горячий газ.6. Способ по п. 1 или 2, отличающийся тем, что углеродсодержащий твердый материал непрерывно направляют через реакционную камеру как движущийся слой.7. Способ по п. 1 или 2, отличающийся тем, что синтетический газ, который образуется в реакционной камере, охлаждают при циркуляции в углеродсодержащем � РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК C01B 3/34 (13) 2014 103 786 A (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2014103786/05, 05.07.2012 (71) Заявитель(и): ЛИНДЕ АКЦИЕНГЕЗЕЛЛЬШАФТ (DE), БАСФ СЕ (DE) Приоритет(ы): (30) Конвенционный приоритет: 05.07.2011 DE 102011106642.3 ( ...

Process for production of synthesis gas

합성 가스(3)의 제조를 위한 프로세스로서, 메탄 및 이산화탄소(2)가 반응 공간(R) 안으로 유입되고 수소 및 일산화탄소를 주기 위해 상승된 온도들에서 고체(W)의 존재 하에 반응된다. 메탄 및 이산화탄소는 탄소 함유 과립 재료(W)를 통과하고 고온 구역(H)에서 반응된다. As a process for the production of syngas 3, methane and carbon dioxide 2 are introduced into reaction space R and reacted in the presence of solid W at elevated temperatures to give hydrogen and carbon monoxide. Methane and carbon dioxide pass through the carbon-containing granular material (W) and are reacted in the hot zone (H).

Reactor for realization of the non-adiabatic reactions

FIELD: chemical industry; devices for realization of the non-adiabatic reactions. SUBSTANCE: the invention is pertaining to the field of chemical industry, in particular, to the reactor for realization of the non-adiabatic reactions. The reactor consists of the metallic ingot and contains, at least, one reactionary passage made through the ingot and designed for maintaining the catalyst for the non-adiabatic transformation of the reactants flow. The reactor contains the inlet channels for introduction of the stream of the reactants into the reactionary passage and the outlet channels for withdrawal of the reacted stream of the reactants; and also the heating-up or cooling device intended for maintaining the catalytic non-adiabatic transformation of the torrent of the reactants. The invention provides, that the mentioned inlet and outlet channels are made in the ingot and are located mainly perpendicularly to the reactionary passages and in parallel connect the reactionary passages. The technical result of the invention is the possibility to use of the reactor for the small-scale production works. EFFECT: the invention ensures the possibility to use of the reactor for the small-scale production works. 9 cl, 1 dwg ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß RU (19) (11) 2 299 093 (13) C2 (51) ÌÏÊ B01J 8/02 (2006.01) B01J 19/24 (2006.01) B01L 5/00 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2001131921/12, 27.11.2001 (72) Àâòîð(û): ÉÎÐÍ Ýðíñò (DK), ËÅÃÑÒÅÄ-ÍÈËÜÑÅÍ Ýðèê (DK) (24) Äàòà íà÷àëà îòñ÷åòà ñðîêà äåéñòâè ïàòåíòà: 27.11.2001 (73) Ïàòåíòîîáëàäàòåëü(è): ÕÀËÜÄÎÐ ÒÎÏÑÅÝ À/Ñ (DK) R U (30) Êîíâåíöèîííûé ïðèîðèòåò: 28.11.2000 DK PA200001789 (43) Äàòà ïóáëèêàöèè çà âêè: 20.07.2003 (45) Îïóáëèêîâàíî: 20.05.2007 Áþë. ¹ 14 2 2 9 9 0 9 3 (56) Ñïèñîê äîêóìåíòîâ, öèòèðîâàííûõ â îò÷åòå î ïîèñêå: WO 98/50147 A1, 12.11.1998. US 5958091 A, 28.09.1999. US 4973777 A, 27.11.1990. RU 2078611 C1, 10.05.1997. ...

Plant of complex waste-free preparation of gas

FIELD: oil and gas industry. SUBSTANCE: plant includes a plant for complex preparation of gas, units for production of synthesis gas and synthesis of methanol, preparation of water and methanation. During plant operation, flare gas supplied from complex gas preparation unit is mixed with deionized water coming from water preparation unit which is supplied with balanced amount of water and the aqueous condensate from synthesis gas production block and methanol synthesis. Deionization can be supplied directly from water preparation unit to synthesis gas production unit and methanol synthesis, where deizate and flare gas are heated, converted together into synthesis gas which is dried and converted into catalyst, from which methanol is recovered and supplied to complex gas preparation plant, and exhaust gas is fed to complex gas preparation plant after methanation of carbon oxides. EFFECT: increase yield of commercial gas, elimination of flare gas combustion, use of methanol from the outside. 2 cl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 635 147 C1 (51) МПК C10J 1/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ На основании пункта 1 статьи 1366 части четвертой Гражданского кодекса Российской Федерации патентообладатель обязуется заключить договор об отчуждении патента на условиях, соответствующих установившейся практике, с любым гражданином Российской Федерации или российским юридическим лицом, кто первым изъявил такое желание и уведомил об этом патентообладателя и федеральный орган исполнительной власти по интеллектуальной собственности. (21)(22) Заявка: 2017107608, 07.03.2017 07.03.2017 (73) Патентообладатель(и): Курочкин Андрей Владиславович (RU) Дата регистрации: 09.11.2017 Приоритет(ы): (22) Дата подачи заявки: 07.03.2017 2564255 C1, 27.09.2015. RU 123347 U1, 27.12.2012. RU 2254322 C1, 20.06.2005. RU 2503651 C1, 10.01.2014. (45) Опубликовано: 09.11.2017 Бюл. № 31 2 6 3 5 1 4 7 R U (54) УСТАНОВКА ...

Catalytic reactor and process

Coloured anhydrous gel element

一种使空气或密闭空间加香或除臭的有色无水凝胶成分，在非水性香基或除臭基以及至少一种不含金属的溶剂染料存在的条件下，所述凝胶成分由官能化液的态聚合物与交联剂交联而成，所述液态聚合物选自马来化的聚丁二烯、马来化的聚异戊二烯或乙烯和马来酸酐的共聚物，所述交联剂含有至少一种互补性官能团，所述染料能溶于所述非水性香基或除臭基，或者由溶于一种非水性溶剂的溶液提供，所述非水性溶剂可与所述非水性香基或除臭基相容。所述凝胶成分被结合在用作空气清新器或除臭器的装置中。

Cogeneration system for a fuel cell and Method thereof

본 발명은 연료전지 발전 시스템 및 그 방법에 관한 것이다. 본 발명에 따른 연료전지 발전 시스템은 전력생성에 필요한 연료가스를 공급하는 연료공급수단; 물 및 산화제 가스를 서로 다른 경로를 통해 공급하는 기액 공급수단; 상기 연료공급수단으로부터 공급되는 연료 및 기액 공급수단으로부터 공급되는 물을 개질하여 수소가스를 생성하는 개질기; 상기 기액 공급수단으로부터 공급받는 산화제 가스 및 상기 개질기로부터 공급받은 수소 가스를 전극에 노출시켜 전기에너지를 발생시키는 연료전지 스택; 및 상기 연료전지 스택으로부터 발생하는 배기가스를 회수하여 가열하고, 상기 가열된 배기가스를 이용하여 상기 개질기로 공급되는 연료를 가열하는 배기가스 회수수단;을 포함하되, 상기 배기가스 회수수단은 상기 연료전지 스택으로부터 발생하는 배기가스에 수소가스가 잔류하는지 여부를 감지한 후, 그 감지정보를 이용하여 상기 배기가스의 초기 이동경로 또는 정상상태 이동경로를 선택적으로 제공하는 것을 특징으로 한다. 연료전지, 폐열, 회수, 배기가스, 예열 The present invention relates to a fuel cell power generation system and method thereof. A fuel cell power generation system according to the present invention includes fuel supply means for supplying fuel gas required for power generation; Gas-liquid supply means for supplying water and oxidant gas through different paths; A reformer for reforming water supplied from the fuel supplied from the fuel supply means and water supplied from the gas liquid supply means to generate hydrogen gas; A fuel cell stack for generating electrical energy by exposing an oxidant gas supplied from the gas-liquid supply means and hydrogen gas supplied from the reformer to an electrode; And exhaust gas recovery means for recovering and heating the exhaust gas generated from the fuel cell stack, and heating the fuel supplied to the reformer using the heated exhaust gas. After detecting whether the hydrogen gas remains in the exhaust gas generated from the battery stack, and using the detection information to selectively provide the initial movement path or the steady state movement path of the exhaust gas. Fuel cell, waste heat, recovery, exhaust gas, preheating

Improvements in organic composns

提供了一种含水自撑式凝胶组合物,该组合物基本上由下列组分组成:a)1—20%香料(优选香味油),b)2—10%一种或多种角叉藻聚糖化合物或角叉藻聚糖共混物,c)0—2%防腐剂,d)0—2%着色剂,和e)66—97%水,所有百分数都是根据该组合物的重量来表示的。

Dust removal system and method for raw coke oven gas by virtue of rotary type fixed bed

本发明涉及一种转动式固定床荒煤气除尘系统及方法，该除尘系统包含除尘器、滤料再生炉、高温斗式提升机以及高温震动筛，除尘器的滤料出口与滤料再生炉的进料口连通，滤料再生炉的出料口与高温斗式提升机进料口连通，高温斗式提升机出料口与高温震动筛连通，高温震动筛分别通过管道与除尘器的滤料入口连通；本发明利用转盘位移固定、圆周旋转的机理实现滤料更新，再通过滤料再生炉、高温斗式提升机、高温震动筛实现滤料再生、筛分，实现滤料连续再生，从而有效解决了固定床滤料积碳再生困难的问题，大大提高除尘效率，减小热损耗，本发明的除尘方法工艺简单、运行稳定且成本低，能够实现滤料连续再生，大大提高除尘效率，适于工业化生产。

Fuel cell system with cooling channels and method for operating a fuel cell system with cooling channels

Brennstoffzellensystem mit Kühlkanäle aufweisenden Brennstoffzellen (26), die zu einem Brennstoffzellenstapel (10) zusammengesetzt sind, mit einem Kühlmittelkreislauf (16), bei dem Kühlmittel von einer Pumpe (72) in einem Hauptkreislauf (70), der die Kühlkanäle und einen Kühler (74) umfaßt, umwälzbar ist sowie mit einem Wärmespeicher (100) und einer Heizeinrichtung (104), dadurch gekennzeichnet, dass der Wärmespeicher (100) in einem ersten zum Kühler (74) parallelen Zweig (102) des Kühlmittelkreislaufs (16) angeordnet ist, dass ein von der Heizeinrichtung (104) erwärmbarer Wärmetauscher (106) in einem zweiten, parallel zum Wärmespeicher (100) angeordneten Zweig (108) angeordnet ist, dass eine zweite Pumpe (110) im ersten Zweig (102) vor dem Wärmespeicher (100) angeordnet ist, dass ein Zweiweg-Umschaltventil (112) vorhanden ist, das einen ersten Anschluss (114), der im ersten Zweig (102) vor der zweiten Pumpe (110), einen zweiten Anschluss (116), der im ersten Zweig (102) nach der zweiten Pumpe (110) und einen dritten Anschluss (118), der im zweiten Zweig (108) vor dem Wärmetauscher (106) angeordnet ist, aufweist und dass eine T-Verbindung (120) zwischen dem ersten Zweig (102), dem zweiten Zweig (108) und dem Hauptkreislauf (70) vorhanden ist. A fuel cell system having cooling channel fuel cells (26) assembled into a fuel cell stack (10) with a coolant circuit (16) having coolant from a pump (72) in a main circuit (70) containing the cooling channels and a radiator (74 ), is circulatable and with a heat accumulator (100) and a heater (104), characterized in that the heat accumulator (100) in a first to the radiator (74) parallel branch (102) of the coolant circuit (16) is arranged a heat exchanger (106) which can be heated by the heating device (104) is arranged in a second branch (108) arranged parallel to the heat accumulator (100) such that a second pump (110) is arranged in front of the heat accumulator (100) in the first branch (102) in that there is a two-way ...

Cold start pre-heater for a fuel cell system

A fuel cell system with fuel cells displaying cooling channels assembled to form a fuel cell stack, with a coolant cycle in which coolant is circulated by a pump in a main cycle which includes the cooling channels and a cooler and with a heat storage unit and a heating device is characterized by the fact that the heat storage unit is arranged in a branch on the coolant cycle parallel to the cooler, that a heat exchanger that can be heated by the heating device is arranged in a second branch parallel to the heat storage unit, that a second pump in the first branch is arranged in front of the heat storage unit, that a two-way switching valve is provided which displays a first connection arranged in a first branch in front of the second pump, a second connection arranged in the first branch in front of the second pump and a third connection which is arranged in the second branch in front of the heat exchanger, and that a T connection is provided between the first branch, the second branch and the main cycle.

An industrial burner using a water and oil as a fuel

본 고안에 따른 산업용 버너는 연소연료공급탱크와, 연소연료를 예열하기 위한 예열실과, 예열된 연소연료를 연소시키는 연소실과, 연소연료를 연소연료공급탱크로부터 예열실로 공급하기 위한 공급펌프로 구성되고, 연소연료공급탱크는 물공급탱크와 액체연료공급탱크로 이루어지고, 예열실은 물공급탱크로부터 공급되는 물을 수증기로 증발시키는 증발실과 액체연료공급탱크로부터 공급되는 연료를 기체연료로 기화시키는 기화실로 이루어지고, 공급펌프는 물공급펌프와 액체연료공급펌프로 이루어지며, 증발실 및 기화실에서 각각 생성된 수증기와 기체연료를 혼합시켜서 생성된 혼합연료를 연소실로 공급하는 혼합실을 더 포함하는 것을 특징으로 하므로, 연료의 소모량을 감소시키고 또한 유해가스의 생성량을 감소시킬 수 있다. The industrial burner according to the present invention is composed of a combustion fuel supply tank, a preheating chamber for preheating the combustion fuel, a combustion chamber for burning the preheated combustion fuel, and a supply pump for supplying the combustion fuel from the combustion fuel supply tank to the preheating chamber. The combustion fuel supply tank consists of a water supply tank and a liquid fuel supply tank, and the preheating chamber is an evaporation chamber for evaporating water supplied from the water supply tank into water vapor and a vaporization chamber for vaporizing fuel supplied from the liquid fuel supply tank with gaseous fuel. The supply pump is composed of a water supply pump and a liquid fuel supply pump, and further comprising a mixing chamber for supplying the mixed fuel generated by mixing the steam and gas fuel generated in the evaporation chamber and the vaporization chamber, respectively, to the combustion chamber. As a result, it is possible to reduce the consumption of fuel and also reduce the amount of harmful gas produced.

Cleaning device in heating section of brightness annealing furnace

광휘소둔라인 중 수직소둔로의 가열대에 사용되는 공기 필터를 주기적으로 교체 및 크리닝하여 가열대의 연소 효율을 높이기 위한 광휘소둔로 가열대의 크리닝 장치를 제공한다. 상기 크리닝 장치는 공기흡입 배관 상부에 교대로 설치되어 연소공기 배관으로 공급되는 공기를 필터링하는 제1, 2 필터와; 필터에 이물질이 흡착되면 공기흡입 배관 상부에 설치된 필터를 다른 필터로 교체 설치하는 필터 교체부와; 필터의 밑면으로부터 공기를 분사하여 필터에 흡착된 미세 이물질을 제거하는 필터 크리닝부와, 연소공기 배관에 생성된 응축수를 모아 연소공기 배관 바깥으로 배출하는 응축수 제거부를 포함한다. 따라서 본 발명은 연소에 필요한 공기를 원활하게 공급하여 버너의 연소 효율을 향상시키고, 응축수에 의한 필터의 오염을 방지한다. Provides a cleaning device for the bright annealing furnace heating table to increase the combustion efficiency of the heating table by periodically replacing and cleaning the air filter used for the heating table of the vertical annealing furnace of the bright annealing line. The cleaning device may include first and second filters alternately installed on an upper portion of the air suction pipe to filter the air supplied to the combustion air pipe; A filter replacement unit for replacing and installing a filter installed in the upper part of the air suction pipe with another filter when foreign matter is adsorbed to the filter; And a filter cleaning unit for removing fine foreign substances adsorbed to the filter by injecting air from the bottom of the filter, and a condensate removal unit for collecting condensate generated in the combustion air pipe and discharging the condensed water out of the combustion air pipe. Therefore, the present invention smoothly supplies the air required for combustion to improve the combustion efficiency of the burner, and to prevent contamination of the filter by condensate. 광휘소둔, 수직소둔로, 가열대, 버너, 에어필터, 응축수, 도시가스 Bright Annealing, Vertical Annealing Furnace, Heating Table, Burner, Air Filter, Condensate, City Gas

Process for the preparation of carbon monoxide rich gas

내용없음. None.

hinoki perfuming apparatus

The present invention relates to a novel whitening apparatus having a new structure of aromatherapy function capable of obtaining an aromatherapy effect by using phytoncide generated from a whitish wood. The aroma therapy apparatus according to the present invention is characterized in that a case 10 made of an opaque wood material is provided with a direction member 20 in which untreated wood distilled water and unbleached wood oil are absorbed, The distilled water from the untreated wood and the untreated wood oil are continuously discharged to the outside through the vent hole 12a. Therefore, a large amount of phytoncide contained in the purified wood distilled water and the white wood oil

Coal reburner flue gas cleaning method

本发明公开了一种新型的煤炭转化炉炉气净化方法，以便对煤炭转化炉炉气进行气固分离净化。该方法包括将煤炭转化炉生成的炉气传送至高温气体过滤装置的环节，高温气体过滤装置位于煤炭转化炉外部或整合在煤炭转化炉中；当高温气体过滤装置位于煤炭转化炉外部时，将高温气体过滤装置待过滤气体进口相比煤炭转化炉炉气出口的炉气温度的向下变动幅度保持在0～50℃的范围内，并且将炉气已通过高温气体过滤装置的过滤元件时相比煤炭转化炉炉气出口的炉气温度的向下变动幅度保持在0～80℃的范围内；当高温气体过滤装置整合在煤炭转化炉中时，使从煤炭转化炉生成炉气开始直至炉气已通过高温气体过滤装置的过滤元件的过程发生于煤炭转化炉内部。

Deodorizing apparatus

The present invention relates to a high-efficiency deodorizing device using deodorizing gas, comprising: first and second chemical liquid tanks (10, 20) in which first and second chemical liquids (M1, M2) that generate deodorizing gas when mixed are respectively stored; a stirrer (30) for generating deodorizing gas by mixing the first chemical liquid (M1) and the second chemical liquid (M2); a first metering pump (40) for supplying the first chemical liquid (M1) to the stirrer (30) in a fixed quantity; a second metering pump (50) for supplying the second chemical liquid (M2) to the stirrer (30) in a fixed quantity; a drain pump (70) for draining a chemical liquid mixture (M) accommodated in the stirrer (30); a retention reaction tank (80) in which a process for neutralizing and deodorizing malodorous gas is carried out, and an exhaust pipe (81) for exhausting deodorized air is formed; a malodorous gas supply duct (90) for supplying the malodorous gas introduced from the outside to the retention reaction tank (80); and a deodorizing gas supply duct (100) communicating with the malodorous gas supply duct (90) and supplying the deodorizing gas generated by the stirrer (30) to the malodorous gas supply duct (90). Accordingly, a large amount of malodorous gas can be continuously deodorized.

Liquid fuel combustion device

(57)【要約】本公報は電子出願前の出願データであるた め要約のデータは記録されません。

Lithographic apparatus

A humidifying apparatus is disclosed in which gas is provided to a first side of a membrane and liquid to a second side of the same membrane. The membrane is non-porous to the liquid but porous to vapor of the liquid and is liquidphilic to said liquid.

Subterranean gasification system and method

A system and method for gasification of a feedstock in a subterranean formation to produce syngas is described. An injection well is completed in the formation to inject an oxidant, provide an ignition source and convey the feedstock that includes water and one or more of a biomass, waste plastic, coal, bitumen and petcoke. Volatized hydrocarbons and gaseous reaction products are simultaneously withdrawn from a producer well from the subterranean formation to the surface. This syngas product is treated at the surface for power generation or conversion to transportation fuels and/or plastics. This method provides a low capital cost gasification unit which is capable of processing a variety of feedstock mixtures.

Sterilization stick

본 발명에 의한 살균 스틱은 깨지는 재질의 밀봉앰플이 용기본체의 내부에 배치됨과 아울러 용기본체의 재질이 연질의 가스투과성 재질로 이루어지며, 밀봉앰플을 깨뜨렸을 때 용기본체 내의 용액과 밀봉앰플 내의 물질이 혼합되어 용기본체 내부에서 발생되는 이산화염소가 용기본체 외부로 배출되는 것으로 이루어지는 살균 스틱에 있어서, 제1물질이 용기본체에 내장됨과 아울러 제2물질가 밀봉앰플에 내장되고, 상기 용기본체에 상기 밀봉앰플을 내장하고, 상기 용기본체의 표면을 감싸는 가스배출조정수단이 상기 용기본체의 외부 노출 면적을 조정하여 상기 밀봉앰플을 깨뜨렸을 때 용기본체 내에서 제1물질과 제2물질의 혼합에 따라 발생되는 이산화염소가 용기본체의 표면을 통하여 배출되는 양이 조정되며, 상기 제1물질은 아염소산나트륨 수용액이고, 상기 제2물질은 가루 형태의 구연산에 가루 형태의 산화아연인 촉매제를 혼합한 것으로 이루어진다. 따라서 본 발명은 중공파이프 또는 시트지인 가스배출조정수단이 용기본체의 외부 노출 표면적을 조정하기 때문에, 실내, 차량 내부 공간 등과 같은 온도와 습도, 악취량 등과 같은 환경에 따라 용기본체의 외부 노출 면적으로 조정하여 용기본체의 표면으로 발산되는 이산화염소의 외기 배출량을 조정하면서 공기를 용이하게 살균 및 소독할 수 있는 등의 효과를 발휘한다. In the sterilization stick according to the present invention, a breakable sealing ampoule is disposed inside the container body, and the container body is made of a soft gas-permeable material. When the sealing ampoule is broken, the solution in the container body and the material in the sealing ampoule In the sterilization stick, which is mixed and the chlorine dioxide generated inside the container body is discharged to the outside of the container body, the first material is built into the container body and the second material is built into the sealing ampoule, and the seal is on the container body When an ampoule is embedded and the gas discharge adjusting means surrounding the surface of the container body adjusts the external exposure area of the container body to break the sealing ampoule, it occurs according to the mixing of the first material and the second material in the container body The amount of chlorine dioxide discharged through the surface of the container body is adjusted, the first material is an aqueous sodium chlorite solution, and the second material is powdered citric acid and a powdery zinc oxide catalyst is mixed. . Therefore, in the present invention, since the gas discharge adjusting means, which is a hollow pipe or sheet, adjusts the external exposed surface area of the container body, ...

METHOD FOR PROCESSING RUBBER-CONTAINING WASTE AND INSTALLATION FOR ITS IMPLEMENTATION (OPTIONS)

ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (11) 2005 115 198 (13) A (51) ÌÏÊ C08J 11/04 C08J 11/20 B29B 17/00 (2006.01) (2006.01) (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÇÀßÂÊÀ ÍÀ ÈÇÎÁÐÅÒÅÍÈÅ (21), (22) Çà âêà: 2005115198/04, 19.05.2005 (43) Äàòà ïóáëèêàöèè çà âêè: 27.11.2006 Áþë. ¹ 33 Àäðåñ äë ïåðåïèñêè: 121248, Ìîñêâà, à/ 16, Å.Â. Âîéöåõîâñêîé (71) Çà âèòåëü(è): Ìàòâååâ Àëåêñåé Âèêòîðîâè÷ (RU), Äîáðîëþáîâà Òàòü íà Àëåêñååâíà (RU) R U (72) Àâòîð(û): Ìàòâååâ Àëåêñåé Âèêòîðîâè÷ (RU), Äîáðîëþáîâà Òàòü íà Àëåêñååâíà (RU) 2 0 0 5 1 1 5 1 9 8 R U Страница: 1 RU A (57) Ôîðìóëà èçîáðåòåíè 1. Ñïîñîá ïåðåðàáîòêè ðåçèíîñîäåðæàùèõ îòõîäîâ, âêëþ÷àþùèé ñòàäèþ èõ ïðåäâàðèòåëüíîé ïîäãîòîâêè, ñòàäèþ òåðìè÷åñêîãî ðàçëîæåíè â ïå÷è ñ ðàçäåëåíèåì ïðîäóêòîâ ðàçëîæåíè íà ïàðîãàçîâóþ ñìåñü è òâåðäûé îñòàòîê, ñòàäèþ âûäåëåíè æèäêîé ôàçû èç ïàðîãàçîâîé ñìåñè ñ îáðàçîâàíèåì óãëåâîäîðîäñîäåðæàùåãî ãàçà è ñòàäèþ âûäåëåíè óãëåðîäñîäåðæàùåãî ïðîäóêòà èç òâåðäîãî îñòàòêà, îòëè÷àþùèéñ òåì, ÷òî íà ñòàäèè ïðåäâàðèòåëüíîé ïîäãîòîâêè öåëûå è/èëè èçìåëü÷åííûå îòõîäû ïðîäóâàþò óãëåâîäîðîäñîäåðæàùèì ãàçîì ñ ïîñëåäóþùåé ïðîïèòêîé óãëåâîäîðîäíûì ðàñòâîðèòåëåì ïðè òåìïåðàòóðå íå âûøå 220°Ñ, ñòàäèþ òåðìè÷åñêîãî ðàçëîæåíè â ïå÷è âåäóò â ñðåäå óãëåâîäîðîäñîäåðæàùåãî ãàçà, íàãðåòîãî äî 400-500°Ñ, âûäåëåíèå æèäêîé ôàçû èç ïàðîãàçîâîé ñìåñè âåäóò â òðè ñòóïåíè, ïðè ýòîì íà ïåðâîé ñòóïåíè ïàðîãàçîâóþ ñìåñü îõëàæäàþò äî 300-360°Ñ ñ ïîñëåäóþùèì âûäåëåíèåì ò æåëîé óãëåâîäîðîäíîé ôðàêöèè, íà âòîðîé ñòóïåíè ïàðîãàçîâóþ ñìåñü îõëàæäàþò äî òåìïåðàòóðû íå âûøå 220°Ñ ñ ïîñëåäóþùèì âûäåëåíèåì ñðåäíåé óãëåâîäîðîäíîé ôðàêöèè è ðåöèðêóë öèåé ÷àñòè åå íà ñòàäèþ ïðåäâàðèòåëüíîé ïîäãîòîâêè îòõîäîâ äë èñïîëüçîâàíè â êà÷åñòâå óãëåâîäîðîäíîãî ðàñòâîðèòåë , à íà òðåòüåé ñòóïåíè ïàðîãàçîâóþ ñìåñü îõëàæäàþò äî òåìïåðàòóðû íèæå 30°Ñ ñ ïîñëåäóþùèì âûäåëåíèåì ëåãêîé óãëåâîäîðîäíîé ôðàêöèè, òâåðäûé îñòàòîê ïåðåä ñòàäèåé âûäåëåíè óãëåðîäñîäåðæàùåãî ïðîäóêòà ïîäâåðãàþò ïðîäóâêå âîçäóõîì è ...

Air flavoring agent production method

FIELD: air aromatization. SUBSTANCE: method of producing air fragrance includes preparation of absorbent base, preparation of deodorant filler, impregnation of adsorbent base with deodorant filler. Adsorbent base is represented by rice husks, and the absorbent base is impregnated with a deodorant filler by spraying with further stirring to uniform distribution of the deodorant filler in amount of 5–20 wt%. Preparation of the deodorant filler is carried out by mixing the perfume, surfactant, glycerine, glycol and water at temperature of 40 to 68 °C, with the following ratios of initial components, wt%: odorant 5.0–10.0; surfactant 0.05–0.1; glycerine 10.0–45.0; glycol 2.0–12.0; water – balance. EFFECT: invention provides an increase in the adsorbent base moisture-absorbing capacity, perfume odor stability enhancement in the temperature range from -30 to +65 °C. 1 cl, 2 tbl, 3 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 702 363 C1 (51) МПК A61L 9/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК A61L 9/04 (2019.05) (21)(22) Заявка: 2019117646, 06.06.2019 (24) Дата начала отсчета срока действия патента: Дата регистрации: 08.10.2019 (45) Опубликовано: 08.10.2019 Бюл. № 28 2 7 0 2 3 6 3 R U (54) Способ получения ароматизатора воздуха (57) Реферат: Изобретение относится к области ароматизации воздуха. Способ получения ароматизатора воздуха включает подготовку абсорбирующей основы, приготовление дезодорирующего наполнителя, пропитку адсорбирующей основы дезодорирующим наполнителем. При этом в качестве адсорбирующей основы используют рисовую лузгу, а пропитку адсорбирующей основы дезодорирующим наполнителем осуществляют методом распыления с последующим перемешиванием до равномерного распределения дезодорирующего наполнителя в количестве от Стр.: 1 (56) Список документов, цитированных в отчете о поиске: RU 2519160 C2, 10.06.2014. RU 68311 U1, 27.11.2007. SU 1690771 A1, 15.11.1991. RU 133731 U1, 27.10.2013. 5 до 20% ...

Method and apparatus for producing compound, and compound and use thereof

本发明涉及一种用于由生物质基原料生产化合物的方法和设备。根据本发明，将该生物质基原料(1)在气化装置(2)中气化用于形成气化气体(3)；将该气化气体(3)在包括含有铁基催化剂的至少一个催化剂层的反应器(4)中进行处理用于形成烃组合物(5)；从该烃组合物中回收至少一种包含烯烃的烃馏分(7，7a，7b，7c)；以及由该烃馏分形成化合物(9，11，17，19)。此外，本发明涉及该化合物及其用途。

Deodorizing composition containing pine needle oil

The present invention relates to a deodorizing composition comprising pine needle oil. The deodorizing composition is harmless to the human body and has no side effects.

Fuel cell power generation system

A fuel cell power generation system is provided to save an initial installation cost by reducing pipes and devices, to enhance a utilization efficiency of fuel, and to prevent emission of exhaust gas containing sulfur components. The fuel cell power generation system comprises: a desulfurizer(100) for removing sulfur from fuel gas; a reformer(110) for generating gas abundant in hydrogen from the desulfurized fuel gas; a fuel cell stack(120) that reacts hydrogen in the fuel gas reformed in the reformer(110) with oxygen and carbon dioxide in the air and generates electricity; and a steam generator(130) that generates water vapor to be supplied to the reformer(110). The fuel gas is desulfurized in the desulfurizer(100), and then introduced into a reformer catalyst layer(110a) and a reformer burner(110b) of the reformer(100). The fuel gas introduced into the reformer catalyst layer(110a) is mixed with water vapor generated in the steam generator(130). The resultant mixture is reacted in the catalyst layer(110a) of the reformer(110), followed by introducing the reacted gas into a fuel electrode(120a) of the fuel cell stack(120). Reformer burner combustion gas of the reformer(110) is introduced into an air electrode(120b) of the fuel cell stack(120). Fuel electrode exhaust gas of the fuel cell stack(120) is introduced into the reformer burner(110b) via the steam generator(130). Air electrode exhaust gas of the fuel cell stack(120) is re-introduced into the air electrode(120b) via the steam generator(130).

Membrane containing liquid active substance and its preparation

(57)【要約】本公報は電子出願前の出願データであるた め要約のデータは記録されません。

Flow-guiding insert for reactor chamber and reactor

FIELD: technological processes; mechanics. SUBSTANCE: flow-guiding insert for reactor chamber has rectangular section, inlet at one end of the chamber and outlet at the other end of the chamber. One of reactor chamber walls consists of heat-conducting material or membrane. Insert contains multiple elements arranged in rows, at that these elements together with chamber walls create the channel for fluid medium. Channel stretches from the first side of chamber to the second side of chamber and back again to the first side, and many times so back and forth. Elements are installed so that fluid medium is forced to flow between elements in a twisting manner. Suggested invention makes it possible to obtain precise hydrodynamic control over flow conditions for reagents that have to pass through reactor chamber. EFFECT: prevention of formation of fluid medium layers with different flow rates and stagnant zones, and obtainment of high mixing rates. 10 cl, 17 dwg ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (11) 2 336 942 (13) C2 (51) ÌÏÊ B01J 19/24 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2005119150/15, 07.11.2003 (72) Àâòîð(û): ØÎÏÀÐ Ôàáðèñ (FR) (24) Äàòà íà÷àëà îòñ÷åòà ñðîêà äåéñòâè ïàòåíòà: 07.11.2003 (73) Ïàòåíòîîáëàäàòåëü(è): ÀËÜÔÀ ËÀÂÀËÜ ÊÎÐÏÎÐÅÉÒ ÀÁ (SE) R U (30) Êîíâåíöèîííûé ïðèîðèòåò: 18.11.2002 SE 0203395-9 (43) Äàòà ïóáëèêàöèè çà âêè: 20.11.2005 (45) Îïóáëèêîâàíî: 27.10.2008 Áþë. ¹ 30 2 3 3 6 9 4 2 (56) Ñïèñîê äîêóìåíòîâ, öèòèðîâàííûõ â îò÷åòå î ïîèñêå: WO 9964146 A1, 16.12.1999. SU 1399633 A1, 30.05.1988. WO 0194006 A2, 13.12.2001. US 6451268 B1, 17.09.2002. EP 0408751 A1, 23.01.1991. (85) Äàòà ïåðåâîäà çà âêè PCT íà íàöèîíàëüíóþ ôàçó: 20.06.2005 2 3 3 6 9 4 2 R U (87) Ïóáëèêàöè PCT: WO 2004/045761 (03.06.2004) C 2 C 2 (86) Çà âêà PCT: SE 03/01719 (07.11.2003) Àäðåñ äë ïåðåïèñêè: 129010, Ìîñêâà, óë. Á.Ñïàññêà , 25, ñòð.3, ÎÎÎ "Þðèäè÷åñêà ôèðìà Ãîðîäèññêèé è Ïàðòíåðû", ...

Fuel processor providing improved measuring way for desulfurizer's status and fuel cell apparatus including the fuel processor and managing method thereof

탈황기의 상태를 측정하는 방식이 개선된 연료개질기와 그것을 갖춘 연료전지 장치 및 그 운영방법이 개시된다. 개시된 연료개질기에 구비된 탈황기는 유입구와 유출구 측 각각에 적어도 하나씩의 유황센서를 갖추고 있어서 두 센서 간 신호의 차이로 포화상태 여부를 판독하도록 된 것을 특징으로 한다. 이러한 연료개질기를 운영하게 되면, 단일 센서만으로 탈황기의 포화상태 여부를 판독하던 기존에 비해 그 판독의 정확도가 더욱 향상될 수 있으며, 측정 에러가 발생될 확률도 낮아져서 안정적이고 원활하게 연료 개질 작업을 보장할 수 있다. Disclosed are a fuel reformer having an improved method of measuring the state of a desulfurizer, a fuel cell device having the same, and a method of operating the same. The desulfurizer provided in the disclosed fuel reformer is equipped with at least one sulfur sensor on each of the inlet and outlet sides so as to read whether the saturation state by the difference between the signals between the two sensors. When operating such a fuel reformer, the accuracy of the reading can be further improved compared to the conventional method of reading whether the desulfurizer is saturated with a single sensor, and the probability of occurrence of a measurement error is lowered, thus ensuring a stable and smooth fuel reforming operation. can do.

Turbine generator having fuel cell

본 발명의 목적은 연료전지형 터빈 발전기에서 출력이 다양하게 변화나 연료전지의 작동 상태가 변화하는 경우에도, 원하는 출력을 얻을 수 있도록 용이하게 제어할 수 있는 연료전지형 터빈 발전기를 제공하는 것이다. 또한, 시스템을 복잡하게 하지 않고 가격경쟁력을 가지면서도 필요한 제어를 견실하게 수행할 수 있는 연료전지형 터빈 발전기를 제공하는 것을 목적으로 한다. 이를 위하여 본 발명에서는, 수소와 산소의 전기 화학적 반응에 의해 전류와 고온 고압의 가스를 발생시키는 연료전지; 상기 연료전지로 공기를 공급하는 압축기; 상기 연료전지에서 발생된 고온 고압의 가스에 의해 회전되는 터빈; 및 상기 터빈의 회전력에 의해 전류를 발생시키는 전동발전유닛을 포함하고, 상기 전동발전유닛, 터빈 및 압축기는 그 회전축이 일체로 형성되고, 상기 압축기 출구와 상기 터빈 입구를 연결하는 배관과, 상기 배관 상에 설치된 밸브를 더 포함하는 연료전지형 터빈 발전기를 제공한다. It is an object of the present invention to provide a fuel cell turbine generator which can be easily controlled to obtain a desired output even when the output varies in the fuel cell turbine generator or the operating state of the fuel cell changes. In addition, it is an object of the present invention to provide a fuel cell turbine generator capable of reliably performing the necessary control without complicating a system and having a cost competitiveness. To this end, the present invention, the fuel cell for generating a current and a high temperature and high pressure gas by the electrochemical reaction of hydrogen and oxygen; A compressor for supplying air to the fuel cell; A turbine rotated by a high temperature and high pressure gas generated in the fuel cell; And an electric power generating unit generating electric current by the rotational force of the turbine, wherein the electric power generating unit, the turbine, and the compressor are integrally formed with a rotating shaft, and a pipe connecting the compressor outlet and the turbine inlet; It provides a fuel cell turbine generator further comprising a valve installed on the.