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31-10-2018 дата публикации

Устройство для магнитно-резонансной модификации углеводородного топлива

Номер: RU0000184581U1
Автор: Борис Владимирович Скворцов, Дилара Раисовна Таипова, Дмитрий Борисович Скворцов, Сергей Анатольевич Борминский
Принадлежит: федеральное государственное автономное образовательное учреждение высшего образования "Самарский национальный исследовательский университет имени академика С.П. Королева"

Полезная модель относится к устройствам автоматического управления технологическими процессами производства нефтепродуктов и может быть использована для производства нефтепродуктов улучшенного качества, связанного с модификацией углеводородов, полученных в результате классических методов нефтепереработки.Решение поставленной задачи достигается тем, что в устройстве для магнитно-резонансной модификации углеводородов, содержащем емкость с углеводородным сырьем, расположенную внутри индуктора, подключенного к генератору переменного тока и помещенного в зазор постоянного магнита, магнитный поток которого ортогонален магнитному потоку индуктора, систему подвода и отвода нефтепродукта, в индуктор введен дополнительный соленоид, вход которого через первый ключ подключен к выходу генератора импульсов и через второй ключ к входу импульсного устройства регистрации ядерного магнитного резонанса, выход которого подключен к частотозадающему входу генератора переменного тока, а управляющие входы ключей и генератора импульсов подсоединены к выходу блока управления.Технический результат - быстрый поиск частот ядерного магнитного резонанса, возможность непрерывной автоматической подстройки частоты генератора на частоты ядерного магнитного резонанса компонентов поступающего сырья. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 184 581 U1 (51) МПК C10G 15/08 (2006.01) C10G 32/02 (2006.01) B01J 19/12 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК C10G 15/08 (2018.08); C10G 32/02 (2018.08); B01J 19/12 (2018.08) (21)(22) Заявка: 2018126331, 16.07.2018 (24) Дата начала отсчета срока действия патента: Дата регистрации: 31.10.2018 (45) Опубликовано: 31.10.2018 Бюл. № 31 1 8 4 5 8 1 R U (56) Список документов, цитированных в отчете о поиске: RU 140192 U, 10.05.2014. RU 2568273 C1, 20.11.2015. CA 0002837010 A1, 22.11.2012. (54) Устройство для магнитно-резонансной модификации углеводородного топлива (57) Реферат: Полезная модель ...

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Номер записи: 1
18-08-2021 дата публикации

Реактор нетермического крекинга

Номер: RU0000206053U1
Автор: Константин Витальевич Сластников
Принадлежит: Болтенков Евгений Владимирович, Константин Витальевич Сластников

Полезная модель относится к системам для крекинга, в частности, изменения свойств углеводородов жидких, газообразных и прочих жидкостей. Реактор нетермического крекинга, содержащий диэлектрический корпус, внутри залитый диэлектрическим компаудом, источник магнитного поля в виде обращенных одноименными полюсами друг к другу магнитов, содержит центральную токопроводящую часть проходнго конденсатора, причем центральный токопроводящий элемент выполнен в виде трубы переменного сечения, а второй токопроводящий элемент выполнен в виде металлической ленты, которая намотана на центральный токопроводящий элемент через диэлектрик, кроме того, вход и выход центрального токопроводящего элемента снабжены диэлектрическими соединительными элементами, которые соединены байпасом, при этом в противоположных концах части центрального токопроводящего элемента большего диаметра установлены магниты, обращенные друг к другу одноименными полюсами, а между магнитами размещен профилированный элемент, при этом в центре магнита со стороны части центрального токопроводящего элемента меньшего диаметра выполнено отверстие для вывода, а внутри части центрального токопроводящего элемента меньшего диаметра размещен спиральный навитый элемент из немагнитного материала, кроме того, корпус, центральный токопроводящий элемент и второй токопроводящий элемент образуют коаксиальную конструкцию, находящуюся внутри продольно ориентированного магнитного поля. В предлагаемом устройстве, углеводородное топливо подвергается обработке под влиянием избыточного давления по краю центростремительной зоны и зоны разряжения (низкого давления) в центре, находясь при этом в зоне действия магнитного и модулированного электрического полей. 1 ил. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 206 053 U1 (51) МПК C10G 15/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК C10G 15/08 (2021.05) (21)(22) Заявка: 2021102129, 29.01.2021 (24) Дата начала отсчета срока действия ...

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Номер записи: 2
28-02-2013 дата публикации

Method for the Treatment of a Liquid, in Particular a Mineral Oil

Номер: US20130048486A1
Автор: Anibal Luis Veneciano Rivera, Fedor Chernikov, Jose Miguel Delgado Castillo, Ruediger Uwe Nuerk
Принадлежит: Pristec Ag

A method is disclosed for the treatment of a liquid, in particular a mineral oil, for increasing the portion of low-boiling fractions. The treatment comprises generating pressure waves having a first frequency, subjecting the liquid to said pressure waves in a region of application and feeding the so-treated liquid to a tank. At least one pipe flowed through by the treated liquid and immediately following said region of application is excited to oscillations of a second frequency, which is the resonance frequency of the excited system.

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Номер записи: 3
27-06-2013 дата публикации

Processing of Dielectric Fluids with Mobile Charge Carriers

Номер: US20130161232A1
Автор: David A. Staack, Robert P. Geiger
Принадлежит: TEXAS A&M UNIVERSITY SYSTEM

Provided herewith is a novel method of controllably processing a dielectric fluid by creating discharges within the dielectric fluid from mobile charge carriers contained within the dielectric fluid. Generally, the dielectric fluid and the mobile charge carriers are between two electrodes which apply a voltage to the charge carriers. In one embodiment, the dielectric fluid is a hydrocarbon fluid such as a heavy crude oil or a fuel. In one embodiment the charge carrier comprises water droplets. In another embodiment, the mobile charge carriers are metallic balls. In both instances the discharges initiate from the mobile charge carriers.

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Номер записи: 4
01-08-2013 дата публикации

Processing biomass

Номер: US20130196386A1
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems are described that can use feedstock materials, such as cellulosic and/or lignocellulosic materials, to produce ethanol and/or butanol, e.g., by fermentation.

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Номер записи: 5
31-10-2013 дата публикации

ELECTROCHEMICAL PROCESS FOR CONVERSION OF BIODIESEL TO AVIATION FUELS

Номер: US20130284606A1
Автор: He Qinggang, Mukerjee Sanjeev
Принадлежит: NORTHEASTERN UNIVERSITY

Methods for the conversion of a biofuel such as biodiesel into an alkane composition such as an aviation fuel, kerosine, or liquified petroleum gas product involve a series of electrochemical reactions. The reactions include oxidation of methanol to carbon dioxide, reduction of fatty acid esters, and cleavage of fatty acid chains at C═C double bonds. The methods are carried out by systems of two or more electrochemical reactors. 1. A system for the chemical conversion of a biodiesel to an alkane composition , the system comprising:a first electrochemical reactor that reduces excess MeOH in a biodiesel source material to yield a first composition comprising methyl esters of aliphatic carboxylic acids;a second electrochemical reactor that fragments the methyl esters of aliphatic carboxylic acids of said first composition by carbon-carbon double bond cleavage to yield a second composition comprising short chain methyl esters of aliphatic carboxylic acids; anda third electrochemical reactor that hydrogenates the methyl esters of said second composition to yield a third composition comprising alkanes.2. A system for the chemical conversion of a biodiesel to an alkane composition , the system comprising:a first electrochemical reactor that fragments aliphatic chains of a biodiesel source material by carbon-carbon double bond cleavage to yield a first composition comprising short chain methyl esters of aliphatic carboxylic acids; anda second electrochemical reactor that performs a Kolbe reaction, whereby the aliphatic carboxylic acids of said first composition are decarboxylated to yield a second composition comprising alkanes.3. A system for the chemical conversion of a biodiesel to an alkane composition , the system comprising:a first electrochemical reactor that fragments aliphatic chains of a biodiesel source material by carbon-carbon double bond cleavage to yield a first composition comprising short chain methyl esters of aliphatic carboxylic acids; anda second ...

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Номер записи: 6
28-11-2013 дата публикации

Processing Hydrocarbons

Номер: US20130312955A1
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Systems and methods that include providing, e.g., obtaining or preparing, a material that includes a hydrocarbon carried by an inorganic substrate, and exposing the material to a plurality of energetic particles, such as accelerated charged particles, such as electrons or ions.

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Номер записи: 7
27-03-2014 дата публикации

PRODUCTION OF HYDROCARBONS FROM PYROLYSIS OF TYRES

Номер: US20140083835A1
Автор: Frediani Marco, Frediani Piero, Meini Stefano, Occhialini Silvio, Rosi Luca, Undri Andrea
Принадлежит: COOPERATIVA AUTOTRASPORTATORI FIORENTINI C.A.F-SOCIETA'COOPERATIVA A.R.L.

The present invention relates to the development of a process of microwave pyrolysis of end-of-life tyres for the production of high added value pyrolysis oils containing a fraction greater than 40% by weight of distiliable hydrocarbons comprised between 20 and 265° C., and sulphur content less than 1% by weight. 1. A process comprising subjecting to pyrolysis end-of-life tyres (ELT) by way of irradiation with microwaves (MW) , wherein:(a) the vapours derived from the pyrolysis reaction are conveyed in a fractionation system before being sent to a condensation system;or:{'sub': M %', 'M risc, '(b) the delivery of the MW is adjusted to such a power level as to obtain a mean percentage pyrolysis rate (V) of between 0.30 and 2.00/min and/or a mean heating rate (V) less than 20° C./min and the vapours derived from the pyrolysis reaction are directly sent to a condensation system, without being conveyed in a fractionation system before being sent to the condensation system;'}for obtaining pyrolysis oils having a sulphur content of <1% by weight and said oil having a fraction of hydrocarbons distillable at a temperature comprised between 20 and 265° C., said fraction of hydrocarbons being greater than 40% by weight.2. The process according to claim 1 , subparagraph (a) claim 1 , wherein the fractionation system is selected from:Dephlegmator with air-coolingDephlegmator with column filled with Fenske, Rashig, Pall, Lessing, and Cross-Partition ringsDephlegmator with column filled with Berl or Intalox saddlesDephlegmator with column filled with glass beads of various diameters (0.5 to 4 mm)Dephlegmator with plate columnor an analogous industrially viable system.3. The process according to claim claim 1 , wherein the delivery of the MW is adjusted to such a power level as to obtain a Vgreater than 0.4/min and/or a mean heating rate (V) greater than 5° C./min claim 1 , for obtaining pyrolysis oils having a sulphur content of <1% by weight and having a fraction of hydrocarbons ...

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Номер записи: 8
15-01-2015 дата публикации

INTEGRATED INTENSIFIED BIOREFINERY FOR GAS-TO-LIQUID CONVERSION

Номер: US20150014183A1
Автор: Akay Galip, Al-Harrasi Wail S. S., El-Naggar Ahmed M. A., Mohamed Abdulaziz H., ZHANG Kui
Принадлежит:

A support device for carrying a selectively permeable membrane is disclosed along with apparatuses and methods of removing long chain hydrocarbons from a stream of gas. The gas cleaning apparatus uses, individually or in combination, plasma, catalyst and electrodes containing catalysts to perform the cleaning of the gas. 117-. (canceled)18. An apparatus for the removal of long chain hydrocarbons from a stream of gas , the apparatus comprising:a vessel including at least one inlet and at least one outlet, allowing a stream of gas to pass therebetween;a plurality of electrodes including at least one anode and at least one cathode, contained within said vessel, such that said stream of gas passes between at least one said anode and at least one said cathode, wherein at least one said electrode comprises at least one catalyst.19. An apparatus according to wherein at least one cathode comprises at least one said catalyst.20. An apparatus according to wherein at least one anode and at least one cathode comprise at least one catalyst.21. An apparatus according to wherein said electrode including said catalyst further comprises at least one porous metal.22. An apparatus according to wherein said metal comprises nickel.23. An apparatus according to wherein said catalyst comprises a cobalt based catalyst.24. An apparatus according to wherein said catalyst is supported on silica.25. An apparatus according to further comprising at least one water supply for supplying a spray of water into said vessel.26. An apparatus according to further comprising at least one bed of solid material located at least partially between said electrodes.27. An apparatus according to wherein said bed comprises a fixed bed.28. An apparatus according to wherein said bed comprises a fluidised bed.29. An apparatus according to wherein said solid material comprises at least one tar adsorbent.30. An apparatus according to wherein said solid material comprises at least one catalyst.31. An apparatus ...

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Номер записи: 9
16-01-2020 дата публикации

MULTI-STAGE SYSTEM FOR PROCESSING HYDROCARBON FUELS

Номер: US20200016569A1
Автор: Johnson Alan A., Skoptsov George L.
Принадлежит:

A method for converting hydrocarbon materials into a product includes receiving a hydrocarbon feedstock in a first reaction chamber, receiving a process gas in the first reaction chamber, and forming a first set of discharge conditions in the presence of energy from a microwave generator, in the first reaction chamber, to convert the hydrocarbon feedstock into an intermediate product for delivery to a second reaction chamber. The method also includes delivering the intermediate product to the second reaction chamber, forming a second set of discharge conditions, and converting the intermediate product into a final product in the second reaction chamber. 1. A method for converting hydrocarbon materials into a product , comprising:receiving, in a first chamber, a hydrocarbon feedstock;receiving, in the first reaction chamber, a process gas;delivering a first type of energy into the first reaction chamber to form a first set of process conditions that activates or ionizes the process gas and converts the hydrocarbon feedstock into an intermediate product;delivering the intermediate product and the activated and/or ionized process gas to a second reaction chamber;delivering a second type of energy into the second reaction chamber to form a second set of process conditions, wherein one of the first type of energy or the second type of energy comprises microwave energy and the other of the first type of energy or the second type of energy is a type of energy other than microwave energy; andusing, in the second reaction chamber in the presence of the second type of energy, the activated and/or ionized process gas to convert the intermediate product into a final product.2. The method of claim 1 , wherein:the process gas comprises methane;the hydrocarbon feedstock comprises coal; converting the hydrocarbon feedstock into an intermediate product comprises converting the coal into a vaporized and/or aerosolized hydrocarbon; andconverting the intermediate product into the final ...

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Номер записи: 10
28-01-2021 дата публикации

METHOD OF RECYCLING WASTE PLASTIC MATERIAL

Номер: US20210024832A1
Автор: Buchert Jürgen
Принадлежит:

In a method for thermal processing of catalytically active waste plastics mixture, the mixture is subjected in a receiving tank to a cracking temperature to undergo a cracking reaction. The mixture is transferred to a mixer pump to produce a reaction mixture which is directed into an outgassing chamber of an intermediate tank to produce an outgassed fraction and a non-outgassed liquid fraction. The outgassed fraction to produce fuel is cooled down, and a first portion of the non-outgassed liquid fraction is returned and subjected again to the cracking temperature in the receiving tank. A second portion of the non-outgassed liquid fraction is conducted in a bypass to the outgassing chamber of the intermediate tank for outgassing while fresh mixture is added. Residual matter settling in the intermediate tank is periodically removed. 1. A method of recycling plastic comprising the steps of:comminuting waste plastic together with an active biocatalyst containing catalytically effective inorganic residue suitable for cracking of waste plastic to form a catalytically active waste plastic mixture and feeding it into a receiving tank;heating the catalytically active waste plastic mixture in the feeding receiving tank to a cracking temperature to undergo a cracking reaction;transferring the catalytically active waste plastic mixture to a mixer pump to produce a reaction mixture;directing the reaction mixture into an outgassing chamber of an intermediate tank to produce an outgassed fraction and a non-outgassed liquid fraction;cooling down the outgassed fraction to produce fuel;returning a first portion of the non-outgassed liquid fraction and subjecting it again to the cracking temperature in the receiving tank;conducting a second portion of the non-outgassed liquid fraction in a bypass to the outgassing chamber of the intermediate tank for outgassing while fresh waste plastic mixture is added; andperiodically removing from the intermediate tank settled residual matter.2. ...

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Номер записи: 11
12-02-2015 дата публикации

METHOD OF TREATING CRUDE OIL WITH ULTRASOUND VIBRATIONS AND MICROWAVE ENERGY

Номер: US20150041369A1
Автор: ROUT Bruce
Принадлежит:

The present invention relates to methods of treating heavy crude oil on the surface or in situ. The methods of the present invention include: (a) mixing the heavy crude oil with a solvent; (b) subjecting the mixture to ultrasonic vibrations; and (c) subjecting mixture treated with ultrasonic vibrations to microwave energy. 1. A method of treating heavy crude oil , the method including: (a) mixing the heavy crude oil with a solvent; (b) subjecting the mixture to ultrasonic vibrations; and (c) subjecting mixture treated with ultrasonic vibrations to microwave energy.2. The method of claim 1 , wherein the solvent is selected from the group of solvents comprising of: alkanes claim 1 , alcohols claim 1 , aromatic hydrocarbons claim 1 , fuel liquids claim 1 , reformates claim 1 , frac fluids and any combinations thereof.3. The method of claim 1 , wherein the aromatic hydrocarbon is benzene claim 1 , a benzene derivative or a combination thereof.4. The method of claim 1 , wherein the method is free of using polar substances.5. The method of claim 1 , wherein the method is free of using sensitizers.6. The method of claim 1 , wherein the solvent is provided as a mixture between the solvent and a suitable dilutant.7. An in situ method for the treatment of a heavy crude oil deposit claim 1 , the method including: (a) disposing a solvent into the heavy oil deposit claim 1 , such that a mixture is created between the solvent and the heavy crude oil in the deposit; (b) subjecting the mixture in the heavy crude oil deposit to ultrasonic vibrations; and (c) subjecting the oil deposit to microwave energy.8. The method of claim 7 , wherein the method further includes extracting the heavy crude oil from the oil deposit treated with ultrasonic vibrations and microwave energy.9. The method of claim 7 , wherein the solvent is selected from the group of solvents comprising of: alkanes claim 7 , alcohols claim 7 , aromatic hydrocarbons claim 7 , fuel liquids claim 7 , reformates claim 7 , ...

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Номер записи: 12
18-02-2016 дата публикации

Ultrasonic cavitation reactor for processing hydrocarbons and methods of use thereof

Номер: US20160046878A1
Автор: Roger K. Lott
Принадлежит: Individual

Systems and methods for upgrading or improving the quality of a heavy oil feedstock. The systems and methods described herein utilize cavitation energy, such as ultrasonic cavitation energy, to transmit ultrasonic or other cavitation energy (e.g., cavitation forces, shear, microjets, shockwaves, micro-convection, local hotspots, and the like) into heavy oil to drive hydroconversion under low pressure hydrogen condition (e.g., less than 500 psig) that are not conventionally believed to be suitable for treating heavy oil.

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Номер записи: 13
15-05-2014 дата публикации

Treatment process and apparatus for reducing high viscosity in petroleum products, derivatives, and hydrocarbon emulsions and the like

Номер: US20140130400A1
Автор: Lazarus Saidakovsky, Nicolai Novikov, Sergey Rakhinskiy
Принадлежит: Lazarus Saidakovsky, Nicolai Novikov, Sergey Rakhinskiy

The reduction of viscosity of petroleum products and hydrocarbon emulsions and the like is effected by applying electrodynamic shocks unto a foaming streamflow of the high viscosity emulsion to create a densely whirled streamflow by agitation with a high radial gradient of pressure. Chemical bonding breakup and destruction of long structured molecules of paraffin occur in the emulsion to result in the formations of free radicals and carbamides, and separation of a processed mixture into light and heavy fractions. The process alters the physiochemical properties of the emulsion to cause decrease of density, and the reduction of viscosity.

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Номер записи: 14
26-02-2015 дата публикации

Multi-stage system for processing hydrocarbon fuels

Номер: US20150057479A1
Автор: Alan A. Johnson, George L. Skoptsov
Принадлежит: H Quest Partners LP

A multi-stage system converts a hydrocarbon material to an intermediate product in a first stage and a final product in a final stage. The first stage includes a first reaction chamber configured to receive hydrocarbon and process gas. In the presence of energy, the first stage will convert the feedstock into an intermediate product for delivery to a second stage. The second stage includes a second reaction chamber configured to receive the intermediate product and a process gas. When the intermediate product and process gases are fed into the reaction chamber in the presence of energy, a plasma is formed in the second reaction chamber and converts the intermediate product into a liquid fuel.

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Номер записи: 15
03-03-2016 дата публикации

Treatment process and apparatus for reducing high viscosity in petroleum products, derivatives, and hydrocarbon emulsions, and the like

Номер: US20160060543A1
Автор: Novikov Nicolai, Rakhinskiy Sergey, Saidakovsky Lazarus
Принадлежит:

The reduction of viscosity of petroleum products and hydrocarbon emulsions and the like is effected by applying electrodynamic shocks unto a foaming streamflow of the high viscosity emulsion to create a densely whirled streamflow by agitation with a high radial gradient of pressure. Chemical bonding breakup and destruction of long structured molecules of paraffin occur in the emulsion to result in the formations of free radicals and carbamides, and separation of a processed mixture into light and heavy fractions. The process alters the physiochemical properties of the emulsion to cause decrease of density, and the reduction of viscosity. 1. An apparatus for treating a petroleum product including oil , highly viscous stable oil emulsions for reduction of viscosity , cleansing and separation of emulsions , comprising:an input storage tank for containing said petroleum product;a swirling hydro-cavitational module serving as a reactor chamber and being connected to said input storage via a pump for delivering the flow of said petroleum product into and through said swirling hydro-cavitational module;at least one input device having a discharge nozzle therein and connected to said swirling hydro-cavitational module with said discharge nozzle positioned tangential to said swirling hydro-cavitational module; said input device having a discharging chamber and a vortex chamber;a plurality of transducers located at two end walls of said vortex chamber, and the working surface of said transducers being perpendicular to the longitudinal central axis of said vortex chamber; said transducers being operative with sonic/ultrasonic frequency generators;two output devices with turbulizers deployed adjacent the end walls in opposite ends of said vortex chamber;one of said input device located at a nearest end of said vortex chamber being connected by pipelines to said input storage tank and an output storage tank for receiving said petroleum product input and the treated product ...

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Номер записи: 16
20-02-2020 дата публикации

System and Method to Decrease the Viscosity of the Crude Oil and the Potentiation of Dehydration

Номер: US20200056104A1
Автор: Gomez Luis
Принадлежит:

A method and system for producing crude oil having reduced viscosity in the processed crude and the empowerment of its dehydration process by passing crude oil over a core that ionizes-polarizes the crude oil with an electrostatic charge. The metal bar-core is an alloy with 40-70% copper by weight, 10-32% nickel, 15-40% zinc, 2-20% tin, and 0.05-10% silver. The core comprises a plurality of grooves, which allows crude oil to be agitated as it comes in contact with the core, activating an electrostatic charge. The electrostatic charge of the core creates a magnetic catalytic reaction that causes: (1) a molecular separation in molecular chains in the processed crude oil thereby lowering the viscosity and (2) stretches and twists caused by the molecular ionization-polarization of processed crude, causes that this release accordingly congenital or added water that is trapped in it, resulting in a potentiation of the dehydration of processed crude. 1. Crude oil processed by a system to maintain crude oil in a liquid state and potentiate its dehydration , comprising:exposing crude oil to a core that ionizes-polarizes the crude oil with an electrostatic charge and creating processed crude oil;wherein the core consists of a metal bar made of an alloy comprising, by weight, 40-70% copper, 10-32% nickel, 15-40% zinc, 2-20% tin, and 0.05-10% silver;wherein the metal bar of the core comprises a plurality of cuts having a concave shape and arranged diagonally on an entire surface of an upper and lower face of the metal bar of the core to create grooves, which allows the crude oil to be agitated as it comes in contact with the core, activating the electrostatic charge;wherein the core is within a casing having an inlet and an outlet at its ends for receiving and download crude oil which is to be treated; andwherein the crude oil coming from the casing is processed crude oil which has a lowered viscosity such that the processed crude oil remains in the liquid state at temperatures ...

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Номер записи: 17
05-06-2014 дата публикации

Production of hydrocarbons from copyrolysis of plastic and tyre material with microwave heating

Номер: US20140155661A1
Автор: Andrea UNDRI, Luca ROSI, Marco FREDIANI, Piero FREDIANI, Silvio OCCHIALINI
Принадлежит: COOPERATIVA AUTOTRASPORTATORI FIORENTINI CAF- &#39;COOPERATIVAARL Soc

The present invention relates to the development of a microwave pyrolysis process for plastic materials selected from PE, PP, PS, PET, PVC and mixtures thereof in the presence of end-of-life tyres, or the pyrolysis residues thereof, or other carbon materials for the production of high added value pyrolysis oils containing over 50% by weight hydrocarbons distillable between 20 and 250° C. and a sulphur content less than 1% by weight.

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Номер записи: 18
24-03-2016 дата публикации

FLUID HAMMERS, HYDRODYNAMIC SIRENS, STREAM REACTORS, IMPLEMENTATION OF SAME, AND METHODS FOR TREATMENT OF FLUIDS

Номер: US20160082405A1
Автор: FOMITCHEV-ZAMILOV Max I.
Принадлежит:

A fluid hammer/siren can operate in fast valve mode with no leakage flow. A stream reactor and process for chemical reaction acceleration provides a flow of liquid or gas forming jets, streams, vortices, or walls of cavities/bubbles that collide with each other or with other liquid, solid, or gaseous interfaces with energies (defined as the sum of molecular kinetic plus thermal energy) in excess of a chemical reaction activation energy. Wastewater treatment methods accelerate suspended particles to high velocity in a fluid flow and then decelerate rapidly by stopping the flow for accelerated inertial-force driven separation. 1. A fluid hammer operable in a fast valve mode , comprising:a gate arrangement operable to modulate fluid flow therethrough, the gate arrangement including a moveable member having at least one first opening or channel and a stationary member having at least one second opening or channel, wherein superpositioning of one of the first openings or channels and one of the second openings or channels defines a gate channel having a first width;an input channel configured to direct fluid flow to the gate arrangement, the input channel having a second width at an interface with the gate arrangement; andan output channel configured to received fluid flow from the gate arrangement,wherein the first width is substantially different from the second width to achieve the fast valve mode, andwherein total leakage area due to clearance between the rotating member and the stationary member is not greater than 10% of a largest cross-sectional area formed by said superpositioning of the first and second openings.3. The fluid hammer of or , wherein the rotating member is mechanically or magnetically coupled to a rotational drive member.4. The fluid hammer of any of to , wherein the rotating member includes an impeller or turbine arranged such that rotation of the rotating member be powered by fluid flow.5. The fluid hammer of claim 4 , further comprising a feed ...

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Номер записи: 19
23-03-2017 дата публикации

MULTI-STAGE SYSTEM FOR PROCESSING HYDROCARBON FUELS

Номер: US20170080399A1
Автор: Johnson Alan A., Skoptsov George L.
Принадлежит:

A method for converting hydrocarbon materials into a product includes receiving a hydrocarbon feedstock in a first reaction chamber, receiving a process gas in the first reaction chamber, and forming a first set of discharge conditions in the presence of energy from a microwave generator, in the first reaction chamber, to convert the hydrocarbon feedstock into an intermediate product for delivery to a second reaction chamber. The method also includes delivering the intermediate product to the second reaction chamber, forming a second set of discharge conditions, and converting the intermediate product into a final product in the second reaction chamber. 17-. (canceled)8. A method for converting hydrocarbon materials into a product , comprising:receiving, in a first reaction chamber, a hydrocarbon feedstock;receiving, in the first reaction chamber, a process gas;operating a first microwave generator to deliver microwave energy into the first reaction chamber;forming, in the first reaction chamber, a first set of discharge conditions in the presence of the energy delivered into the first reaction chamber;converting, in the first reaction chamber, the hydrocarbon feedstock into an intermediate product for delivery to a second reaction chamber, wherein a first processing time associated with the conversion of the hydrocarbon feedstock into the intermediate product is 0.008-600 seconds.9. The method of claim 8 , further comprisingdelivering the intermediate product to the second reaction chamber;operating a second microwave generator to deliver microwave energy into the second reaction chamber;forming, in the second reaction chamber, a second set of discharge conditions in the presence of the energy from delivered into the second reaction chamber; andconverting, in the second reaction chamber, the intermediate product into a final product, wherein a second processing time associated with the conversion of the intermediate product into the final product is 0.008-600 ...

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Номер записи: 20
02-04-2015 дата публикации

HYDROCARBON RESOURCE PROCESSING DEVICE INCLUDING RADIO FREQUENCY APPLICATOR AND RELATED METHODS

Номер: US20150090635A1
Автор: Parsche Francis Eugene
Принадлежит:

A hydrocarbon resource processing device may include a radio frequency (RF) source and an RF applicator coupled to the RF source. The RF applicator may include a base member being electrically conductive, and first and second elongate members being electrically conductive and having proximal ends coupled to the base member and extending outwardly therefrom in a generally parallel spaced apart relation. The first and second elongate members may have distal ends configured to receive the hydrocarbon resource therebetween. In another embodiment, the RF applicator may include an enclosure being electrically conductive and having a passageway therethrough to accommodate a flow of the hydrocarbon resource and a divider being electrically conductive and positioned within the enclosure. 123-. (canceled)24. An apparatus for processing a hydrocarbon resource comprising:a radio frequency (RF) source; and an electrically conductive enclosure having a passageway therethrough to accommodate a flow of the hydrocarbon resource, and', 'an electrically conductive divider positioned within said electrically conductive enclosure., 'an RF applicator coupled to said RF source and comprising'}25. The apparatus according to wherein said RF source and said RF applicator are configured to perform at least one of heating claim 24 , dehydrating claim 24 , cracking and hydrogenation of the hydrocarbon resource.26. The apparatus according to wherein said electrically conductive divider has an elongate shape with opposing ends coupled to adjacent portions of said electrically conductive enclosure and with opposing sides spaced inwardly from adjacent portions of said electrically conductive enclosure.27. The apparatus according to wherein said electrically conductive divider has a convex shape.28. The apparatus according to further comprising:an auxiliary RF radiating element within said electrically conductive enclosure; andan auxiliary RF source coupled to said auxiliary RF radiating element and ...

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Номер записи: 21
18-04-2019 дата публикации

MULTISPARK REACTOR

Номер: US20190112533A1
Автор: Novoselov Yury
Принадлежит:

A device includes a channel having an inlet and an outlet, a first electrode disposed within the channel, and a second electrode disposed within the channel so as to define a gap between the second electrode and the first electrode. The device further includes a power source connected to at least one of the electrodes. The second electrode includes a lumen from a first end of the second electrode to a second end of the second electrode. The lumen is configured to introduce a carrier gas to the gap. The inlet is configured to introduce a process stream to the channel. The process stream comprises a viscous petroleum feed material. The power source is configured to produce a spark within the gap, thereby generating a plasma configured to reduce a viscosity of the viscous petroleum feed material and to form a processed petroleum material. 1. A device comprising:a channel having an inlet and an outlet;a first electrode disposed within the channel;a second electrode disposed within the channel so as to define a gap between the second electrode and the first electrode; anda power source connected to at least one of the electrodes; the second electrode comprising a lumen from a first end of the second electrode to a second end of the second electrode, the lumen configured to introduce a carrier gas to the gap;', 'the inlet is configured to introduce a process stream to the channel, the process stream comprising a viscous petroleum feed material;', 'the power source is configured to produce a spark within the gap, thereby generating a plasma configured to reduce a viscosity of the viscous petroleum feed material and to form a processed petroleum material; and', 'the outlet is configured to convey the processed petroleum material from the channel to a collection point., 'wherein2. The device of claim 1 , wherein the viscous petroleum feed material comprises crude oil claim 1 , wherein molecules of the viscous petroleum feed material comprise hydrocarbon molecules claim 1 , ...

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Номер записи: 22
18-04-2019 дата публикации

Pulsed power supply

Номер: US20190112534A1
Автор: Yury Novoselov
Принадлежит: EVOenergy LLC, Lteoil LLC

The electrical circuit of power supply includes a series of discharge gaps, storage capacitors, and charging resistors. The work of multispark reactor based on the parallel breakdown of discharge gaps in the mode of self-breakdown. Simultaneous triggering of all gaps is achieved using self-breakdown on the rising edge of voltage, particularly when using the power frequency AC voltage.

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Номер записи: 23
25-04-2019 дата публикации

Treatment of Heavy Oils to Reduce Olefin Content

Номер: US20190119583A1
Автор: Chornet Michel, Chronopoulos Christos, Dehkissia Soumaine
Принадлежит:

A process for treating heavy oil to provide a treated heavy oil having a reduced density and viscosity, as well as an olefin content that does not exceed 1.0 wt. %. The process comprises separating the initial heavy oil into a first fraction, which in general contains lower-boiling components, and a second fraction. The second fraction comprises a heavy oil having a p-value of at least 5% greater than the p-value of the initial heavy oil prior to separating the initial heavy oil into the first fraction and the second fraction, and the second fraction has an aromaticity that is no more than 5% less than the aromaticity of the initial heavy oil prior to separating the initial heavy oil into the first fraction and the second fraction. The second fraction then is upgraded to reduce the density and viscosity of the heavy oil. After the second fraction is upgraded, it is recombined with at least a portion of the first fraction to provide a treated heavy oil having an olefin content that does not exceed 1.0 wt. %. The separation of the initial heavy oil into first and second fractions enables one to achieve improved reduction of the density and viscosity of the treated heavy oil while maintaining the olefin content at an acceptable level. 1. A process for treating a heavy oil to provide a treated heavy oil having a reduced density and viscosity , and an olefin content that does not exceed 1.0 wt. % , comprising:(a) separating an initial heavy oil into a first fraction and a second fraction, wherein said second fraction comprises a heavy oil having a p-value of at least 5% greater than the p-value of said initial heavy oil prior to separating said initial heavy oil into said first fraction and said second fraction, and said second fraction has an aromaticity that is no more than 5% less than the aromaticity of said initial heavy oil prior to separating said initial heavy oil into said first fraction and said second fraction;(b) reducing the density and viscosity of said ...

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Номер записи: 24
27-05-2021 дата публикации

Submerged methane and hydrogen mixture discharge in liquid hydrocarbons

Номер: US20210155855A1
Автор: David Staack, Kunpeng Wang
Принадлежит: TEXAS A&M UNIVERSITY SYSTEM

A process and apparatus for cracking liquid hydrocarbon materials into light hydrocarbon fractions using a carrier gas including methane and hydrogen.

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Номер записи: 25
10-05-2018 дата публикации

System and Method to Decrease the Viscosity of the Crude Oil and the Potentiation of Dehydration

Номер: US20180127663A1
Автор: Gomez Luis
Принадлежит:

A method and system for reducing viscosity in the crude oil and the empowerment of its dehydration process pass crude oil over a core that ionizes-polarizes the crude oil with an electrostatic charge. The metal bar core made of an alloy which includes, a weight of, 40-70% copper, 10-32% nickel, 15-40% zinc, 2-20% tin, and 0.05-10% silver. The metal bar core comprises a plurality of grooves, which allows crude oil to be agitated as it comes in contact with the core, activating an electrostatic charge. The electrostatic charge of the core creates a magnetic catalytic reaction that causes: (1) a molecular separation in the molecular chains within crude oil thereby lowering the viscosity and (2) stretches and twists caused by the molecular ionization-polarization of crude oil, causes that this release accordingly congenital or added water that is trapped in it, resulting in a potentiation of the dehydration of crude oil. 2. The system of claim 1 , wherein the core is disposed on a crude oil supply line. This is a divisional patent application based upon and claiming the benefit of U.S. patent application Ser. No. 14/789,538, filed Jul. 1, 2015, now pending, the contents of which is incorporated herein by reference thereto. This is a normal request for patent system and method to decrease the viscosity of the crude oil and the empowerment of their dehydration.The present invention relates to a method for treating crude oil (hereinafter may be referred to only as “crude”) in a way that (a) crude oil maintains one viscosity less than a given temperature and (b) strengthen the methods for the removal of water (dehydration). Low viscosity allows oil to be maintained in a liquid state and fluid at low temperatures and without heat, when normally it would not be so. As for the decrease of viscosity, this eliminates the need for heating oil in order to pump it and transport it steadily and even for certain crude, can eliminates the need to use chemicals flow improvers. With ...

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Номер записи: 26
11-05-2017 дата публикации

Photochemical hydrogenation of heavy fractions of hydrocarbon streams

Номер: US20170128907A1
Автор: Felipe Pereira FLEMING, Rodrigo Jose Correa
Принадлежит: Petroleo Brasileiro SA Petrobras, Universidade Federal do Rio de Janeiro UFRJ

The present invention describes a photochemical hydrogenation process for heavy fractions of hydrocarbon streams where the aromatic and polyaromatic compounds present in that fraction selectively react in the presence of an alkoxide, when subjected to electromagnetic irradiation.

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Номер записи: 27
01-06-2017 дата публикации

HYBRID FUEL AND METHOD OF MAKING THE SAME

Номер: US20170152453A1
Автор: Goerz David
Принадлежит:

A hybrid fuel and methods of making the same. A process for making a hybrid fuel includes the steps of combining a biofuel emulsion blend and a liquid fuel product to form a hybrid fuel. Optionally, the hybrid fuel can be combined with water in a water-in-oil process and include oxygenate additives and additive packages. A hybrid fuel includes blends of biofuel emulsions and liquid fuel products, including light gas diesel. Optionally, the hybrid fuel can include water, oxygenate additives, and other additive packages. 1. A process for the preparation of a hybrid fuel , the process comprising:introducing a first reactant into a reactor, wherein the first reactant comprises at least one of a natural gas, a light gas, and a biogas;exposing the first reactant to the reactor, wherein the reactor comprises at least one of a non-thermal plasma source, an ultrasonic excitation, a magnetic field, a UV light, a catalyst, and a radiation source, the reactor generating conditions sufficient to reform the first reactant to form a reaction products comprising at least one of a syngas, free radicals, a rotationally energetic reactant, at least one of vibrationally and rotationally energetic reactant, and energetic electrons;introducing a first liquid feed fuel into the reactor;intimately contacting the reaction products with the first liquid feed fuel; andproducing, from the intimate contact between the reaction products and the first liquid feed fuel in the reactor, a modified liquid fuel that is different from the first liquid feed fuel.2. The process of claim 1 , wherein the reactor comprises thorium.3. The process of claim 1 , further comprising:exposing the first reactant to the first liquid feed fuel; andactivating the first reactant via exposure to a UV source.4. The process of claim 1 , further comprising:exposing the first liquid feed fuel to the conditions sufficient to reform the first reactant to form reaction products; andexciting oil fractions therein such that the ...

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Номер записи: 28
23-06-2016 дата публикации

PROCESS FOR CRACKING OF LIQUID HYDROCARBON MATERIALS BY PULSED ELECTRICAL DISCHARGE AND DEVICE FOR ITS IMPLEMENTATION

Номер: US20160177190A1
Автор: Novoselov Yury
Принадлежит:

A carrier gas jet is injected into a liquid hydrocarbon material to form a liquid hydrocarbon-gas mixture; flowing the liquid hydrocarbon-gas material through an inter-electrode gap of a discharge chamber, the inter-electrode gap defined by a spaced pair of electrodes, the electrodes being connected to a capacitor; charging the capacitor to a breakdown voltage of the carrier gas; generating a spark discharge in the inter-electrode gap; and recovering a hydrocarbon fraction that includes lower molecular weight hydrocarbons than the liquid hydrocarbon material. 1. A process comprising:introducing a liquid hydrocarbon material into a discharge chamber;flowing the liquid hydrocarbon-gas material through an inter-electrode gap within the discharge chamber, the inter-electrode gap defined by a spaced apart positive electrode (anode) and a negative electrode (cathode), both the electrodes being connected to a capacitor;injecting in the inter-electrode gap a carrier gas into the liquid hydrocarbon material to form a liquid hydrocarbon-gas mixture;charging the capacitor to a breakdown voltage of the carrier gas;generating a spark discharge in the inter-electrode gap; andrecovering a hydrocarbon fraction comprising lower molecular weight hydrocarbons than the liquid hydrocarbon material.2. The process of claim 1 , wherein the liquid hydrocarbon material comprises petroleum products claim 1 , straight and branched chain paraffin hydrocarbons claim 1 , cyclo-paraffin hydrocarbons claim 1 , mono-olefin hydrocarbons claim 1 , diolefin hydrocarbons claim 1 , alkene hydrocarbons claim 1 , or aromatic hydrocarbons.3. The process of claim 1 , wherein the liquid hydrocarbon material comprises crude oil.4. The process of claim 3 , wherein the hydrocarbon fraction comprises diesel fuel claim 3 , light kerosene claim 3 , or and gasoline.5. The process of claim 1 , wherein the carrier gas comprises hydrogen claim 1 , methane claim 1 , or natural gas.6. The process of which is a continuous ...

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Номер записи: 29
22-06-2017 дата публикации

PROCESSING MATERIALS

Номер: US20170175007A1
Автор: Medoff Marshall
Принадлежит:

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems are described that can use feedstock materials, such as cellulosic and/or lignocellulosic materials and/or starchy materials, to produce ethanol and/or butanol, e.g., by fermentation. Hydrocarbon-containing materials are also used as feedstocks. 1. A method of processing a hydrocarbon-containing material , the method comprising: irradiating with accelerated particles a combination formed by combining the hydrocarbon-containing material with an inorganic material , to produce an irradiated combination , wherein the hydrocarbon-containing material is coal.2. The method of wherein the hydrocarbon-containing material comprises a solid claim 1 , particulate claim 1 , powder claim 1 , liquid claim 1 , gas or a combination thereof.3. The method of wherein the hydrocarbon-containing material comprises the liquid.4. The method of claim 1 , wherein the particles comprise electrons accelerated to a speed of greater than 75% the speed of light.5. The method of claim 1 , wherein the hydrocarbon-containing material is combined with the inorganic material by dry blending or co-comminuting.6. The method of claim 5 , wherein during co-comminuting claim 5 , each of the hydrocarbon-containing material and the inorganic material is cooled to a temperature below 25° C.7. The method of claim 5 , wherein during co-comminuting claim 5 , each of the hydrocarbon-containing material and the inorganic material is cooled to a temperature below 0° C.8. The method of claim 1 , wherein the inorganic material comprises a metal or a metal alloy.9. The method of claim 8 , wherein the metal or metal alloy is selected from the group consisting of ferrous metals claim 8 , base metals claim 8 , noble metals claim 8 , precious metals claim 8 , and transition metals.10. The method of claim 8 , wherein the metal or metal alloy comprises aluminum.11. The ...

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Номер записи: 30
04-06-2020 дата публикации

Mobile Transport Fuel Refinery System and Method, Fuel Refinery and Dispensing System and Method, and Fuel Composition

Номер: US20200172816A1
Автор: Koch Joshua F.
Принадлежит:

A fuel refinery system comprising a particulate filter adapted to remove particulates from fuel flowing through the fuel conduction system, a water filter adapted to remove water from fuel flowing through the fuel conduction system following its passage through the particulate filter, a magnetic field of sufficient strength to further refine the fuel flowing through the fuel conduction system following its passage through the water filter, a catalyst injector configured to inject the catalyst from a catalyst tank into the fuel flowing through the fuel conduction system following its passage through the magnetic field, a dispensing conduit configured to conduct the fuel from the fuel refinement apparatus following injection of the catalyst. 1. A fuel composition produced by the process of the following steps performed upon a fuel containing particulates and water:removing particulates from the fuel;removing water from the fuel;subjecting the fuel to a magnetic field of sufficient strength to further refine the fuel following the removal of particulates and water; andadmixing a catalyst into the fuel following its refinement by the magnetic field.2. The fuel composition of wherein a particulate content of the fuel composition produced by the process is below about 2 microns.3. The fuel composition of wherein a water content of the fuel composition produced by the process is below about 10 PPM.4. The fuel composition of wherein a microbial content of the fuel composition produced by the process is below about 1 CFV/mL.5. The fuel composition of wherein a cetane value of the fuel composition produced by the process is in the range of 45-52.6. The fuel composition of wherein a lubricity value of the fuel composition produced by the process is in the range of 2.65 CST or greater.7. The fuel composition of wherein the catalyst comprises hydrocarbons and ketones and is present in a ratio in the range of at least 1/1000.8. A fuel composition comprising a fuel hydrocarbon ...

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Номер записи: 31
06-07-2017 дата публикации

A METHOD OF CRACKING AND/OR DEMULSIFICATION OF HYDROCARBONS AND/OR FATTY ACIDS IN EMULSIONS

Номер: US20170190984A1
Автор: HALEK James Michael, KOHLIK Karel
Принадлежит:

The invention relates generally to a method for cracking and/or demulsification of hydrocarbons and/or fatty acids in emulsions, wherein these hydrocarbons and/or fatty acids in emulsions are exposed to an electromagnetic field created by a microwave emitting process, whereas this electromagnetic field is correlated with the oscillation frequency of the longer chained molecules of these hydrocarbons and/or fatty acids, by either adapting the exact correlated frequency and/or by adjusting the electromagnetic field to the properties of the targeted hydrocarbon and/or fatty acid molecules and its emulsions by adding suitable catalysts and by applying the correlated microwave output power. 1. A method of cracking and/or demulsification of hydrocarbons and/or fatty acids in emulsions characterized in that these hydrocarbons and/or fatty acids in emulsions are being exposed town electromagnetic field by emitting microwaves that are correlated with the oscillation frequency of the targeted molecules of these hydrocarbons and/or fatty acids.2. The method in accordance with claim 1 , characterized in that the emulsion of hydrocarbons and/or fatty acids consists of emulsions of the water-in-oil (W/O) claim 1 , oil in water (O/W) or water-in-oil-in-water (W/O/W) types.3. The method in accordance with or claim 1 , characterized in that the method is executed in a formation (pay zone) below surface or on surface outside of a formation.4. The method in accordance with to claim 1 , characterized in that it comprises the following consecutive steps:a) determining the oscillation frequency of the targeted molecules of the hydrocarbons and/or fatty acids in the emulsion using well-known methods, comprising the use of oscilloscopes or spectrometry or calculation, to adjust the electromagnetic field so that the microwaves correlate with the determined oscillation frequency;b) correlating and equalizing the microwave energy with the determined hydrocarbon and or/fatty acid molecule ...

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Номер записи: 32
16-10-2014 дата публикации

Processing Hydrocarbons

Номер: US20140305634A1
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Systems and methods that include providing, e.g., obtaining or preparing, a material that includes a hydrocarbon carried by an inorganic substrate, and exposing the material to a plurality of energetic particles, such as accelerated charged particles, such as electrons or ions.

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Номер записи: 33
11-07-2019 дата публикации

PROCESSING BIOMASS

Номер: US20190211501A1
Автор: Medoff Marshall
Принадлежит:

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems are described that can use feedstock materials, such as cellulosic and/or lignocellulosic materials, to produce ethanol and/or butanol, e.g., by fermentation. 1. A method comprising:converting a treated biomass feedstock, utilizing an enzyme or a microorganism, to produce a product, wherein the feedstock has been treated by:preparing an untreated biomass feedstock by reducing one or more dimensions of individual pieces of biomass;irradiating the untreated biomass feedstock; andmechanically treating the irradiated biomass feedstock to reduce one or more dimensions of individual pieces of the pretreated biomass feedstock.2. The method of claim 1 , wherein the treated biomass feedstock has an uncompressed bulk density of less than about 0.6 g/cm3 claim 1 , wherein bulk density is determined using ASTM D1895B.3. The method of claim 1 , wherein the treated biomass feedstock includes fibers having a length/diameter (L/D) ratio of at least about 5.4. The method of claim 1 , wherein mechanically treating the irradiated biomass feedstock comprises milling the feedstock.5. The method of claim 1 , wherein the untreated biomass feedstock comprises a cellulosic or lignocellulosic material.6. The method of claim 5 , wherein the biomass feedstock is selected from the group consisting of paper claim 5 , paper products claim 5 , paper waste claim 5 , wood claim 5 , particle board claim 5 , sawdust claim 5 , agricultural waste claim 5 , sewage claim 5 , silage claim 5 , grasses claim 5 , rice hulls claim 5 , bagasse claim 5 , cotton claim 5 , jute claim 5 , hemp claim 5 , flax claim 5 , bamboo claim 5 , sisal claim 5 , abaca claim 5 , straw claim 5 , corn cobs claim 5 , corn stover claim 5 , switchgrass claim 5 , alfalfa claim 5 , hay claim 5 , coconut hair claim 5 , seaweed claim 5 , algae claim 5 , and mixtures thereof.7. The method ...

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Номер записи: 34
23-10-2014 дата публикации

APPARATUSES AND METHODS FOR HYDRODYNAMIC CAVITATION TREATMENT OF LIQUIDS

Номер: US20140316180A1
Автор: FOMITCHEV-ZAMILOV Max I.
Принадлежит: Quantum Vortex, Inc.

An apparatus for breaking molecular bonds of a liquid may include a first arrangement configured to create macroscopic flow of a liquid such that a molecule of the liquid has a velocity corresponding to a bond disassociation energy of the molecule. The apparatus may also include a second arrangement configured to collide the macroscopic flow of liquid with an obstacle. The collision results in molecular collisions having an energy that exceeds the bond disassociation energy of the molecule. 1. An apparatus for breaking molecular bonds of a liquid , comprising:a first arrangement configured to create macroscopic flow of a liquid such that a molecule of said liquid has a velocity corresponding to a bond disassociation energy of said molecule; anda second arrangement configured to collide said macroscopic flow of said liquid with an obstacle, said collision resulting in molecular collisions having an energy that exceeds said bond disassociation energy of said molecule.2. The apparatus of claim 2 , wherein the apparatus is configured to increase the pressure and/or temperature of the liquid so as to lower the flow velocity required to correspond to a bond disassociation energy of said molecule3. The apparatus of claim 1 , further comprising:a source of liquid containing a hydrocarbon molecule at a desired cracking temperature, the first arrangement being configured to create macroscopic flow of said liquid such that the hydrocarbon molecule has a velocity comparable with a thermal velocity of the hydrocarbon molecule at said desired cracking temperature, said collision resulting in molecular collisions having an energy that exceeds a disassociation energy of a C—C bond of said hydrocarbon molecule.4. The apparatus of claim 3 , wherein the apparatus is configured to increase the pressure and/or temperature of the hydrocarbon liquid so as to lower the velocity of macroscopic flow of said liquid that creates molecular collisions having an energy that exceeds a ...

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Номер записи: 35
23-08-2018 дата публикации

Heavy Fossil Hydrocarbon Conversion and Upgrading Using Radio-Frequency or Microwave Energy

Номер: US20180237704A1
Автор: Bearden Mark D., Bergsman Theresa M., Roberts Benjamin Q., Smurthwaite Tricia D., Strohm James J.
Принадлежит:

Conversion of heavy fossil hydrocarbons (HFH) to a variety of value-added chemicals and/or fuels can be enhanced using microwave (MW) and/or radio-frequency (RE) energy. Variations of reactants, process parameters, and reactor design can significantly influence the relative distribution of chemicals and fuels generated as the product. In one example, a system for flash microwave conversion of HFH includes a source concentrating microwave or RF energy in a reaction zone having a pressure greater than 0.9 atm, a continuous feed having HFH and a process gas passing through the reaction zone, a HFH-to-liquids catalyst contacting the HFH in at least the reaction zone, and dielectric discharges within the reaction zone. The HFH and the catalyst have a residence time in the reaction zone of less than 30 seconds. In some instances, a plasma can form in or near the reaction zone. 1: A method for selectively preparing paraffins from heavy fossil hydrocarbons (HFH) , the method comprising:providing reactants to a reaction zone, the reactants comprising HFH, catalyst, and methane;exposing the reactants in the reaction zone to microwave or RF energy, the exposing selectively converting at least a portion of the HFH to paraffins; andrecovering at least the paraffins from the reaction zone.2: The method of claim 1 , wherein the catalyst comprises one or more of iron claim 1 , char claim 1 , and/or a promoter of dielectric discharge.3: The method of claim 1 , wherein the pressure in the reaction zone is from between 0.9 atm and 7 atm.4: The method of claim 1 , wherein the reactants are exposed within the reaction zone for residence time from between 5 milliseconds and 30 seconds.5: The method of wherein the paraffins comprise straight chained hydrocarbons.6: The method of wherein the exposing selectively converts the HFH to paraffins rather than aromatic hydrocarbons.7: A method for converting aromatic hydrocarbons of heavy fossil fuel (HFH) to alkylated aromatic hydrocarbons claim ...

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Номер записи: 36
09-09-2021 дата публикации

Sulfonated Lignin-Derived Compounds and uses Thereof

Номер: US20210276945A1
Автор: GEIGLE Peter, HARTWIG Jan, KRAWCZYK Nastaran, LARIONOV Evgeny, MOELLER Alexander
Принадлежит: CMBLU PROJEKT AG

The present invention relates to novel lignin-derived compounds and compositions comprising the same and their use as redox flow battery electrolytes. The invention further provides a method for preparing said compounds and compositions as well as a redox flow battery comprising said compounds and compositions. Additionally, an assembly for carrying out the inventive method is provided. 2. The redox flow battery according to claim 1 , wherein said redox flow battery comprises a first (optionally aqueous) electrolyte solution comprising a first (redox active) electrolyte; a first electrode in contact with said first (optionally aqueous) electrolyte solution; a second (optionally aqueous) electrolyte solution comprising a second (redox active) electrolyte; a second electrode in contact with said second (optionally aqueous) electrolyte solution; wherein one or both of the first and second (redox active) electrolytes comprise the at least one sulfonated (and optionally further derivatized) low molecular weight aromatic compound.3. The redox flow battery of claim 1 , wherein the sulfonated low molecular weight aromatic compound corresponds in structure to Formula (X) or (XI) claim 1 , and wherein Rand Rare independently selected from H and SOH; Ris selected from H claim 1 , OH claim 1 , C-Calcohol claim 1 , and SOH; and Ris selected from H claim 1 , OH and C-Calcohol.4. The redox flow battery of claim 1 , wherein the sulfonated low molecular weight aromatic compound is characterized by one of the following:{'sup': '4', 'sub': '3', 'a) Ris SOH;'}{'sup': 4', '3, 'sub': '3', 'b) Ris SOH, Ris methoxy;'}{'sup': 4', '2', '3, 'sub': '3', 'c) Ris SOH, Rand Rare methoxy;'}{'sup': 1', '4, 'sub': '3', 'd) Rand Rare SOH;'}{'sup': 1', '4', '3, 'sub': '3', 'e) Rand Rare SOH, Ris methoxy; or'}{'sup': 2', '4', '3, 'sub': '3', 'f) Rand Rare SOH, and Ris methoxy.'}5. The redox flow battery of claim 1 , wherein the sulfonated low molecular weight aromatic compound corresponds in structure ...

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Номер записи: 37
07-09-2017 дата публикации

MOBILE TRANSPORT FUEL REFINERY SYSTEM AND METHOD, FUEL REFINERY AND DISPENSING SYSTEM AND METHOD, AND FUEL COMPOSITION

Номер: US20170253812A1
Автор: Koch Joshua F.
Принадлежит:

A mobile diesel fuel refinery system comprise a particulate filter adapted to remove particulates from diesel fuel flowing through the diesel fuel conduction system, a water filter adapted to remove water from diesel fuel flowing through the diesel fuel conduction system following its passage through the particulate filter, a magnetic field of sufficient strength to further refine the diesel fuel flowing through the diesel fuel conduction system following its passage through the water filter, a catalyst injector configured to inject the catalyst from a catalyst tank into the diesel fuel flowing through the diesel fuel conduction system following its passage through the magnetic field, a dispensing conduit configured to conduct the diesel fuel from the diesel fuel refinement apparatus following injection of the catalyst. 1. A fuel refinement apparatus comprising:a particulate filter;a water filter;a magnetic field;a catalyst injector; anda dispensing conduit.2. The fuel refinement apparatus of wherein the particulate filter is of sufficient fineness to reduce a microbial contamination in a fuel.3. The fuel refinement apparatus of wherein the particulate filter comprises a pressure gauge.4. The fuel refinement apparatus of wherein the water filter is of sufficient fineness to reduce particles of about 10 microns in a fuel.5. The fuel refinement apparatus of wherein the water filter additionally comprises a pressure gauge.6. The fuel refinement apparatus of claim 1 , further comprising a catalyst claim 1 , wherein the catalyst comprises aromatic hydrocarbons and ketones.7. The fuel refinement apparatus of wherein the catalyst injector additionally comprises a flow sensor.8. The fuel refinement apparatus of comprises further comprising a fuel leak sensor.9. The fuel refinement apparatus of further comprising a system configured to monitor or control at least one: (1) a power applied claim 1 , (2) a system power claim 1 , (3) a fuel head optimal claim 1 , (4) a primary ...

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Номер записи: 38
04-12-2014 дата публикации

Heavy Fossil Hydrocarbon Conversion and Upgrading Using Radio-Frequency or Microwave Energy

Номер: US20140353207A1
Автор: Bearden Mark D., Bergsman Theresa M., Roberts Benjamin Q., Smurthwaite Tricia D., Strohm James J.
Принадлежит:

Conversion of heavy fossil hydrocarbons (HFH) to a variety of value-added chemicals and/or fuels can be enhanced using microwave (MW) and/or radio-frequency (RF) energy. Variations of reactants, process parameters, and reactor design can significantly influence the relative distribution of chemicals and fuels generated as the product. In one example, a system for flash microwave conversion of HFH includes a source concentrating microwave or RF energy in a reaction zone having a pressure greater than 0.9 atm, a continuous feed having HFH and a process gas passing through the reaction zone, a HFH-to-liquids catalyst contacting the HFH in at least the reaction zone, and dielectric discharges within the reaction zone. The HFH and the catalyst have a residence time in the reaction zone of less than 30 seconds. In some instances, a plasma can form in or near the reaction zone. 1. A method for selectively preparing paraffins from heavy fossil hydrocarbons (HFH) , the method comprising:providing reactants to a reaction zone, the reactants comprising HFH, catalyst, and methane;exposing the reactants in the reaction zone to microwave or RF energy, the exposing selectively converting at least a portion of the HFH to paraffins; andrecovering at least the paraffins from the reaction zone.2. The method of claim 1 , wherein the catalyst comprises one or more of iron claim 1 , char claim 1 , and/or a promoter of dielectric discharge.3. The method of claim 1 , wherein the pressure in the reaction zone is from between 0.9 atm and 7 atm.4. The method of claim 1 , wherein the reactants are exposed within the reaction zone for residence time from between 5 milliseconds and 30 seconds.5. The method of wherein the paraffins comprise straight chained hydrocarbons.6. The method of wherein the exposing selectively converts the HFH to paraffins rather than aromatic hydrocarbons.7. A method for converting aromatic hydrocarbons of heavy fossil fuel (HFH) to alkylated aromatic hydrocarbons claim ...

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Номер записи: 39
22-09-2016 дата публикации

HYDROCARBON RESOURCE PROCESSING DEVICE INCLUDING RADIO FREQUENCY APPLICATOR AND RELATED METHODS

Номер: US20160272897A1
Автор: Parsche Francis Eugene
Принадлежит:

A hydrocarbon resource processing device may include a radio frequency (RF) source and an RF applicator coupled to the RF source. The RF applicator may include a base member being electrically conductive, and first and second elongate members being electrically conductive and having proximal ends coupled to the base member and extending outwardly therefrom in a generally parallel spaced apart relation. The first and second elongate members may have distal ends configured to receive the hydrocarbon resource therebetween. In another embodiment, the RF applicator may include an enclosure being electrically conductive and having a passageway therethrough to accommodate a flow of the hydrocarbon resource and a divider being electrically conductive and positioned within the enclosure. 137-. (canceled)38. A method for processing a hydrocarbon resource comprising: an electrically conductive enclosure having a passageway therethrough to accommodate a flow of the hydrocarbon resource, and', 'an electrically conductive divider positioned within the enclosure; and, 'applying radio frequency (RF) power from an RF source to an RF applicator coupled to the RF source, the RF applicator comprising'}flowing the hydrocarbon resource through the passageway to process the hydrocarbon resource with the RF power.39. The method according to wherein applying RF power comprises applying RF power so that the RF source and the RF applicator cooperate to perform at least one of heating claim 38 , dehydrating claim 38 , cracking and hydrogenation of the hydrocarbon resource.40. The method according to wherein the electrically conductive divider has an elongate shape with opposing ends coupled to adjacent portions of the electrically conductive enclosure and with opposing sides spaced inwardly from adjacent portions of the electrically conductive enclosure.41. The method according to wherein the electrically conductive divider has a convex shape.42. The method according to further comprising ...

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Номер записи: 40
21-09-2017 дата публикации

MOBILE TRANSPORT FUEL REFINERY SYSTEM AND METHOD, FUEL REFINERY AND DISPENSING SYSTEM AND METHOD, AND FUEL COMPOSITION

Номер: US20170267935A1
Автор: Koch Joshua F.
Принадлежит:

A fuel refinery system comprising a particulate filter adapted to remove particulates from fuel flowing through the fuel conduction system, a water filter adapted to remove water from fuel flowing through the fuel conduction system following its passage through the particulate filter, a magnetic field of sufficient strength to further refine the fuel flowing through the fuel conduction system following its passage through the water filter, a catalyst injector configured to inject the catalyst from a catalyst tank into the fuel flowing through the fuel conduction system following its passage through the magnetic field, a dispensing conduit configured to conduct the fuel from the fuel refinement apparatus following injection of the catalyst.

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Номер записи: 41
13-10-2016 дата публикации

SUPERSONIC SHOCK WAVE REACTORS, AND ASSOCIATED SYSTEMS AND METHODS

Номер: US20160296904A1
Автор: CERFF Robert, Hansen Viggo, Knowlen Carl, MATTICK Arthur T., Stevens Carl J.
Принадлежит:

Apparatuses and associated methods for forming olefins from saturated hydrocarbon feedstock are disclosed herein. In one embodiment, a carrier gas is introduced at a supersonic velocity to a feedstock injector section. A feedstock gas is introduced tot he carrier gas stream using feedstock injectors that are offset in the streamwise direction one from another. The upstream feedstock injectors are positioned to inject feedstock gas to create plumes that improve penetration depth of the feedstock gas and reduce pressure losses at the downstream feedstock injectors. The feedstock gas can be regeneratively preheated by cooling the convergent-divergent nozzle. Water, steam and/or hydrogen gas can be injected into the apparatus for cooling the throat of the convergent-divergent nozzle. 13-. (canceled)4. A shock wave reactor , comprising:a feedstock injector section having an inlet for receiving a carrier gas at supersonic velocity;a first feedstock injector positioned to inject a feedstock gas into the feedstock injector section at a first angle with respect to a longitudinal axis of the feedstock injector section; anda second feedstock injector positioned to inject the feedstock gas into the feedstock injector section at a second angle with respect to the longitudinal axis of the feedstock injector section, wherein the second angle is greater than the first angle.5. The reactor of example 4 wherein the second feedstock injector is positioned to inject the feedstock gas within a plume zone created by the first feedstock injector.6. The reactor of example 4 , further comprising a third feedstock injector positioned to inject the feedstock gas into the feedstock injector section at a third angle with respect to the longitudinal axis of the feedstock injector section , wherein the third angle is greater than the second angle.7. The reactor of wherein the first and second feedstock injectors are generally aligned in a direction of the longitudinal axis.8. The reactor of ...

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Номер записи: 42
05-11-2015 дата публикации

Systems and methods of integrated separation and conversion of hydrotreated heavy oil

Номер: US20150315497A1
Автор: Patrick Loring Hanks, William Ernest Lewis
Принадлежит: ExxonMobil Research and Engineering Co

Systems and methods are providing for integrating a cavitation unit to the backend separation system of a hydrotreater to improve conversion,

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Номер записи: 43
26-10-2017 дата публикации

Method and apparatus for processing hydrocarbons

Номер: US20170306245A1
Автор: Erkki Lindberg
Принадлежит: EKO HARDEN TECHNOLOGIES Oy

A method and apparatus break down compounds, typically hydrocarbons, through oxidation. The compounds may still be in-situ or in a man-made location. The method for the processing of hydrocarbons within a location, provides for: a) introducing two electrodes into the location containing the hydrocarbons; b) providing connections between a voltage source and the electrodes; c) applying a voltage of a first polarity to the connections for a first period of time, under the control of a voltage controller; d) applying a voltage of a second, reversed, polarity to the connections for a second period of time, under the control of the voltage controller; e) repeating steps c) and d); steps c), d) and e) promoting the generation of free radicals thereby promoting a reduction in the length of the carbon chain and/or a reduction in the sulphur content and/or a reduction in the heavy metal content of the hydrocarbons.

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Номер записи: 44
25-10-2018 дата публикации

FUEL REFORMER FOR VEHICLE

Номер: US20180306145A1
Автор: Inami Norio
Принадлежит: TOYOTA JIDOSHA KABUSHIKI KAISHA

Provided is a fuel reformer for a vehicle. The vehicle includes an internal combustion engine, a fuel tank in which fuel of the internal combustion engine is stored, and a fuel supply device configured to supply the fuel in the fuel tank to the internal combustion engine. The fuel reformer includes an irradiator configured to emit light from an irradiation portion. The irradiation portion is disposed at a position where the fuel stored in the fuel tank is irradiated with the light without the light passing through a gas phase region in the fuel tank. 1. A fuel reformer for a vehicle including an internal combustion engine , a fuel tank in which fuel of the internal combustion engine is stored , and a fuel supply device configured to supply the fuel in the fuel tank to the internal combustion engine , the fuel reformer comprising an irradiator configured to emit light from an irradiation portion ,wherein the irradiation portion is disposed at a position where the fuel stored in the fuel tank is irradiated with the light without the light passing through a gas phase region in the fuel tank.2. The fuel reformer according to claim 1 , wherein:the irradiation portion is disposed at a position on an upper surface of a bottom wall of the fuel tank; andthe irradiation portion is configured to emit the light to at least an upper region of the fuel tank.3. The fuel reformer according to claim 1 , wherein:the irradiation portion is disposed to configure a part or an entire area of a bottom wall of the fuel tank; andthe irradiation portion is configured to emit the light to at least an upper region of the fuel tank.4. The fuel reformer according to claim 1 , wherein:the irradiation portion is disposed at a position on a lower surface of a bottom wall of the fuel tank;the irradiation portion is configured to emit the light to at least an upper region of the fuel tank; andat least a portion of the bottom wall of the fuel tank that is irradiated with the light is formed of a ...

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Номер записи: 45
01-11-2018 дата публикации

Production of Oil by Pyrolysis of Coal

Номер: US20180311657A1
Автор: Boldor Dorin, Hayes Daniel
Принадлежит: Board of Supervisors of Louisiana State University and Agricultural and Mechanical College

Catalysts useful in transforming biomass to bio-oil are disclosed, as are methods for making such catalysts, and methods of transforming biomass to bio-oil. The catalysts are especially useful for, but are not limited to, microwave- and induction-heating based pyrolysis of biomass, solid waste, and other carbon containing materials into bio-oil. The catalysts can also be used for upgrading the bio-oil to enhance fuel quality. 1. A method of producing oil from coal by pyrolysis; said method comprising the steps of:(a) cleaning the surface of one or more metallic substrate particles, wherein each metallic substrate particle has a longest dimension between about 100 μm and about 5 mm;(b) oxidizing or nitriding the surfaces of the metallic substrate particles, to covalently attach oxide or nitride groups to the surfaces of the metallic substrate particles;(c) covalently bonding one or more linker groups to the oxide, to the nitride, or to the metal surface;(d) covalently bonding one or more seed layers to the one or more linker groups, wherein the one or more seed layers comprise ruthenium, rhodium, palladium, silver, osmium, iridium, platinum, gold, copper, rhenium, mercury, aluminum oxide, nickel(11) oxide, or nickel(11) oxide;(e) covalently bonding a catalyst layer to the one or more seed layers, wherein the catalyst layer comprises a metal, a metal oxide, a doped metal, or a zeolite; wherein the resulting catalyst/support composition is adapted to directly absorb electromagnetic energy from microwave irradiation, or electromagnetic induction, or both, and thereby to be rapidly heated to a temperature between about 250° C. and about 1000° C.;(f) heating the catalyst/support composition to a temperature between about 250° C. and about 1000° C. by microwave irradiation, or by electromagnetic induction, or both, in an inert atmosphere inside a reactor;(g) contacting coal with the heated catalyst/support composition for a time sufficient to transform at least a portion ...

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Номер записи: 46
09-11-2017 дата публикации

Treatment of Heavy Oils to Reduce Olefin Content

Номер: US20170321133A1
Автор: Chornet Michel, Chronopoulos Christos, Dehkissia Soumaine
Принадлежит:

A process for treating heavy oil to provide a treated heavy oil having a reduced density and viscosity, as well as an olefin content that does not exceed 1.0 wt. %. The process comprises separating the initial heavy oil into a first fraction, which in general contains lower-boiling components, and a second fraction. The second fraction comprises a heavy oil having a p-value of at least 5% greater than the p-value of the initial heavy oil prior to separating the initial heavy oil into the first fraction and the second fraction, and the second fraction has an aromaticity that is no more than 5% less than the aromaticity of the initial heavy oil prior to separating the initial heavy oil into the first fraction and the second fraction. The second fraction then is upgraded to reduce the density and viscosity of the heavy oil. After the second fraction is upgraded, it is recombined with at least a portion of the first fraction to provide a treated heavy oil having an olefin content that does not exceed 1.0 wt. %. The separation of the initial heavy oil into first and second fractions enables one to achieve improved reduction of the density and viscosity of the treated heavy oil while maintaining the olefin content at an acceptable level. 1. A process for treating a heavy oil to provide a treated heavy oil having a reduced density and viscosity , and an olefin content that does not exceed 1.0 wt. % , comprising:(a) separating an initial heavy oil into a first fraction and a second fraction, wherein said second fraction comprises a heavy oil having a p-value of at least 5% greater than the p-value of said initial heavy oil prior to separating said initial heavy oil into said first fraction and said second fraction, and said second fraction has an aromaticity that is no more than 5% less than the aromaticity of said initial heavy oil prior to separating said initial heavy oil into said first fraction and said second fraction;(b) reducing the density and viscosity of said ...

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Номер записи: 47
15-10-2020 дата публикации

System and method for cold cracking under a condition of modified density of physical vacuum

Номер: US20200325402A1
Автор: Fedor Chernikov, Jose Miguel Delgado Castillo, Joseph M. Laura
Принадлежит: New Vacuum Technologies LLC

Method to change the molecular composition of a target medium under a condition of modified physical vacuum structure, includes introducing into an exposure chamber the target medium having a Raman spectrum with a predetermined target spectral resonance; rotating a source hydrocarbon medium in a drum adjacent to the exposure chamber, to produce a vacuum and magnetic influence; propagating the vacuum and magnetic influence to the target medium in the exposure chamber; applying a mechanical vibration to the target medium to vibrate the target medium on a molecular scale, to create colloidal molecular vibrations; transferring energy from the colloidal molecular vibrations to an electron system of atoms in molecules of the target medium until at least a portion of the molecules of the target medium cracks into shorter molecular hydrocarbon products; and withdrawing the shorter hydrocarbon molecular products from the exposure chamber.

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Номер записи: 48
29-11-2018 дата публикации

PROCESSING HYDROCARBONS

Номер: US20180340405A1
Автор: Medoff Marshall
Принадлежит:

Systems and methods that include providing, e.g., obtaining or preparing, a material that includes a hydrocarbon carried by an inorganic substrate, and exposing the material to a plurality of energetic particles, such as accelerated charged particles, such as electrons or ions. 1. A method comprising:exposing a material comprising a hydrocarbon carried by an inorganic substrate to at least 0.5 megarads of radiation.2. The method of claim 1 , wherein the inorganic substrate comprises exterior surfaces claim 1 , and wherein the hydrocarbon is carried on at least some of the exterior surfaces.3. The method of claim 1 , wherein the inorganic substrate comprises interior surfaces claim 1 , and wherein the hydrocarbon is carried on at least some of the interior surfaces.4. The method of claim 1 , wherein the material comprises oil shale.5. The method of claim 1 , wherein the material comprises oil sand.6. The method of claim 1 , wherein the inorganic substrate comprises a material having a thermal conductivity of less than 5 W mK.7. The method of claim 1 , wherein the inorganic substrate comprises at least one of an aluminosilicate material claim 1 , a silica material claim 1 , and an alumina material.8. The method of claim 7 , wherein the substrate further comprises a noble metal claim 7 , such as platinum claim 7 , iridium claim 7 , or rhodium.9. The method of claim 7 , wherein the substrate comprises a zeolite material.10. The method of claim 9 , wherein the zeolite material has a base structure selected from the group consisting of ZSM-5 claim 9 , Zeolite Y claim 9 , Zeolite Beta claim 9 , mordenite claim 9 , ferrierite claim 9 , and mixtures of any two or more of these structures.11. The method of wherein the radiation is in the form of energetic particles.12. The method of wherein exposing the hydrocarbon to radiation reduces the molecular weight by at least about 25%.13. The method of wherein the hydrocarbon initially has a molecular weight of from about 300 to ...

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Номер записи: 49
22-12-2016 дата публикации

System and Method to Decrease the Viscosity of the Crude Oil and the Potentiation of Dehydration

Номер: US20160369178A1
Автор: Gomez Luis
Принадлежит:

A method and system for reducing viscosity in the crude oil and the empowerment of its dehydration process pass crude oil over a core that ionizes-polarizes the crude oil with an electrostatic charge. The metal bar core made of an alloy which includes, a weight of, 40-70% copper, 10-32% nickel, 15-40% zinc, 2-20% tin, and 0.05-10% silver. The metal bar core comprises a plurality of grooves, which allows crude oil to be agitated as it comes in contact with the core, activating an electrostatic charge. The electrostatic charge of the core creates a magnetic catalytic reaction that causes: (1) a molecular separation in the molecular chains within crude oil thereby lowering the viscosity and (2) stretches and twists caused by the molecular ionization-polarization of crude oil, causes that this release accordingly congenital or added water that is trapped in it, resulting in a potentiation of the dehydration of crude oil. 1. A method for reducing sulfur contaminants and lowering viscosity in crude oil and the potentiation of dehydration comprising:passing crude oil over a core that ionizes-polarizes the crude oil with an electrostatic charge;wherein the core consists of a metal bar being made of an alloy comprising, by weight, 40-70% copper, 10-32% nickel, 15-40% zinc, 2-20% tin, and 0.05-10% silver;wherein in the core is within a casing having an inlet and an outlet at its ends for receiving and discharging the crude oil to be treated; andwherein the core is disposed in a crude oil supply line.2. The method of claim 1 , wherein the metal bar of the core comprises a plurality of cuts having a concave shape and arranged diagonally along an entire surface of an upper and lower face of the metal bar of the core to create grooves claim 1 , which allows the crude oil to be agitated as it comes in contact with the core claim 1 , activating the electrostatic charge.3. The method of claim 2 , wherein the electrostatic charge creates a magnetic catalytic reaction that causes a ...

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Номер записи: 50
13-12-2018 дата публикации

DEVICE FOR TREATMENT OF A LIQUID

Номер: US20180355260A1
Автор: Castillo Jose Miguel Delgado, Chernikov Fedor, Nuerk Ruediger Uwe, Rivera Anibal Luis Veneciano
Принадлежит:

A device is configured to increase the portion of low-boiling fractions of a liquid, particularly mineral oil. A device includes a pressure wave generator for generating a pressure wave having a first frequency, in which the pressure wave generator is arranged to subject the liquid to the pressure waves in a region of application, at least one pipe which is arranged through which treated liquid flows after the region of application, and means for exciting the at least one pipe through which such treated liquid flows to oscillations of a second frequency, which is the resonance frequency of the excited system. 17.-. (canceled)8. A device for the treatment of a liquid , in particular a mineral oil , for increasing the portion of low-boiling fractions comprising a pressure wave generator for generating a pressure wave having a first frequency , said pressure wave generator being arranged to subject the liquid to said pressure waves in a region of application , at least one pipe arranged immediately following said region of application , and means for exciting said pipe and treated liquid flowing through it to oscillations of a second frequency , which is the resonance frequency of the excited system.9. A device according to claim 8 , wherein said device further comprises a recirculation pipe for withdrawing a portion of the treated liquid downstream of the pressure wave generator at a site of withdrawal and for refeeding the treated liquid to the pressure wave generator at a site of refeed upstream of the pressure wave generator claim 8 , and at least one adjustable throttle valve is arranged in the recirculation pipe for adjustment of pressure.10. A device according to claim 8 , wherein the pressure wave generator is connected via flowed-through pipings with the liquid to be treated claim 8 , in particular mineral oil.11. A device according to claim 9 , wherein the pressure wave generator is connected via flowed-through pipings with the liquid to be treated claim 9 , ...

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Номер записи: 51
13-12-2018 дата публикации

METHOD FOR ADJUSTING THE OPERATING POINT OF A PRESSURE WAVE GENERATOR FOR TREATING A LIQUID

Номер: US20180355261A1
Автор: Castillo Jose Miguel Delgado, Chernikov Fedor, Nuerk Ruediger Uwe, Rivera Anibal Luis Veneciano
Принадлежит:

A method for adjusting the operating point of a pressure wave generator for treating a first liquid, in particular a mineral oil, with pressure waves of a first frequency for increasing the portion of low-boiling fractions in the liquid. The pressure wave generator is communicated with a second liquid, in particular water, via flowed-through pipe(s) (piping(s) and the frequency of application via the pressure wave generator is varied. An operating point is determined as a maximum in temperature rise of the second liquid, after passing the pressure wave generator, as a function of the frequency of application. 114-. (canceled)15. A method for adjusting the operating point of a pressure wave generator for treating a liquid , in particular a mineral oil with pressure waves of a first frequency for increasing the portion of low-boiling fractions in the liquid characterized in that the pressure wave generator is communicated with a liquid , in particular water , via flowed-through pipings and the frequency of application is varied and the operating point is determined as a maximum in temperature rise of the liquid after passing the pressure wave generator as a function of the frequency of application.16. A method for determining an operating point of a pressure wave generator for treating a first liquid consisting essentially of mineral oil with pressure waves of a first frequency for increasing the portion of low-boiling fractions , wherein the method comprises flowing a second liquid comprising water through the pressure wave generator , varying the frequency generated by the pressure wave generator , determining the operating point as a maximum in temperature rise of the second liquid from before and after passing through pressure wave generator as a function of the frequency applied to the second liquid by the pressure wave generator.17. A method according to claim 16 , wherein the maximum rise in temperature is 10° C. to 35° C.18. A method according to claim 16 , ...

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Номер записи: 52
20-12-2018 дата публикации

METHODS FOR REDUCING THE VISCOSITY OF A LIQUID

Номер: US20180361344A1
Автор: Lennykh Konstantin, Selivanov Konstantin
Принадлежит: Active Resource Technologies Ltd.

A device and method are disclosed to mix two or more liquids to reduce their viscosity, specific gravity or density. The device can also take a heavy fuel oil and following treatment, produce a lighter fuel oil. The invention also comprises a method and procedure for mixing two or more liquids as well as producing a lighter fuel oil from a heavy fuel oil. 1. A method for reducing the viscosity of an at least one liquid using a device configured for resonance excitation of said at least one liquid , the method comprising the steps of:closing a shutoff valve of the device;draining the device of air;establishing a flow through the device of the at least one liquid;recording the flow of said at least one liquid using a flow meter of the device;diluting the at least one liquid with a further liquid of relatively lower density by mixing said liquids using resonance excitation;establishing a desired ratio between said liquids using the flow meter;modulating a flow of said liquids;monitoring a viscosity of said liquids to achieve a desired blend ratio thereof; andperforming a fractioning process on said liquids.2. The method of claim 1 , further comprising the step of maintaining an even mixture of said liquids.3. The method of wherein the step of establishing a flow through the device of the at least one liquid comprises the step of establishing a flow through the device of an at least one hydrogen-bonded liquid.4. The method of claim 3 , wherein the step of establishing a flow through the device of an at least one hydrogen-bonded liquid comprises the step of establishing a flow through the device of at least one of a heavy fuel oil claim 3 , a bitumen claim 3 , and a hydrocarbon contaminated water.5. The method of claim 3 , wherein the step of establishing a flow through the device of heavy fuel oil comprises the step of establishing a flow through the device of a high paraffinic crude oil.6. The method of claim 1 , wherein the step of performing a fractioning process ...

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Номер записи: 53
28-12-2017 дата публикации

MACROSCOPIC ARTIFICIAL DIELECTRIC SUSCEPTOR FOR MAKING BIOCHEMICALS

Номер: US20170369786A1
Автор: Dalton Robert Carl
Принадлежит:

A macroscopic artificial dielectric susceptor for making biochemicals 1. A process for creating at least one biochemical species that is a biochemical product from at least one biochemical species that is a biochemical reactant originating from biomass where the biochemical reactant is part of a chemical species flow comprising passing the chemical species flow through a macroscopic artificial dielectric susceptor structure that is a gas-permeable susceptor , and subjecting the structure to at least one wavelength of applied electromagnetic energy , the structure consisting of at least two regions where first regions and second regions are solid materials , the second regions contain a solid catalytic material , the first regions and the second regions having different dielectric properties to at least one wavelength of the applied electromagnetic energy , the dielectric properties of the first regions being greater than the depth of penetration of the second regions , wherein: (a) the first regions are discontinuously interspersed at least a certain distance from each other between and among the second regions , (b) the transmission of the applied electromagnetic energy by the first regions provides a means for increase interaction between the applied electromagnetic energy and the chemical species flow (c) the transmission of the applied electromagnetic energy by the first regions provides a means for increased interaction between the applied electromagnetic energy and the second regions in the gas-permeable susceptor to interact with the catalyst of the second regions , and (d) the distance between each of the first regions and a volume fraction of the structure that the first regions make up assists the applied electromagnetic energy to penetrate the structure and to interact volumetrically with the susceptor and the chemical species flow passing through the susceptor and allows for the synthesis of at least one biochemical product species that is created by ...

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Номер записи: 54
24-12-2020 дата публикации

Microwave-Based Recovery Of Hydrocarbons And Fossil Fuels

Номер: US20200399541A1
Автор: Everleigh Carl, Forthe Julian, Pringle Frank G.
Принадлежит:

The present invention provides methods for decomposing and extracting compositions for the recovery of petroleum-based materials from composites comprising those petroleum-based materials, comprising subjecting the compositions and/or composites to microwave radiation, wherein the microwave radiation is in the range of from about 4 GHz to about 18 GHz. The present invention also provides for products produced by the methods of the present invention and for apparatuses used to perform the methods of the present invention. 1. An apparatus for extracting a petroleum-based material from a composite comprising petroleum-based material , comprising:a microwave radiation generator, wherein said generator is capable of applying microwave radiation characterized as having at least one frequency component in the range of from about 4 GHz to about 18 GHz; andat least one container to collect said extracted petroleum-based material.2. The apparatus of claim 1 , wherein the microwave radiation generator is capable of applying a microwave radiation frequency of between about 4.0 and about 12.0 GHz.3. The apparatus of claim 2 , wherein the microwave radiation generator is capable of applying a microwave radiation frequency of between about 7.9 and about 8.7 GHz.4. The apparatus of claim 1 , wherein the microwave radiation generator is capable of applying a sweeping range of microwave radiation frequencies of between about 4.0 and about 12.0 GHz.5. The apparatus of claim 4 , wherein the range of frequencies of said radiation is in the C-Band frequency range.6. The apparatus of claim 4 , wherein the range of frequencies of said radiation is in the X-Band frequency range.7. The apparatus of claim 4 , wherein the range of frequencies of said radiation is in the range of from about 5.8 GHz to about 7.0 GHz.8. The apparatus of claim 4 , wherein the frequency of said radiation is in the range of from about 7.9 GHz to about 8.7 GHz.9. The apparatus of claim 1 , further comprising at least ...

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Номер записи: 55
06-03-2003 дата публикации

Method to treat emulsified hydrocarbon mixtures

Номер: US20030042174A1
Автор: Douglas Austin
Принадлежит: Petronetics LLC

A method of liberating various existing hydrocarbon fractions from emulsified hydrocarbon mixtures without the need of additives, catalysts or heating using ultrasonic cavitation. Ultrasonic energy is provided at a rate sufficient to induce cavitation in the emulsified hydrocarbon mixture without causing cracking. The high temperatures and high pressures resulting from cavitation disrupt the emulsion thereby liberating existing lighter hydrocarbons in the diesel range or lighter for recovery via more traditional separation technologies. The resulting upgraded petroleum product exhibits lower distillation curves and decreased pollution causing components. Further, a wide variety of feedstocks can be treated according to the method of this invention.

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Номер записи: 56
20-03-2003 дата публикации

Method to liberate hydrocarbon fractions from hydrocarbon mixtures

Номер: US20030051989A1
Автор: Douglas Austin
Принадлежит: Petronetics LLC

A method of liberating various existing hydrocarbon fractions from hydrocarbon mixtures without the need of additives, catalysts or heating using ultrasonic cavitation. Ultrasonic energy is provided at a rate sufficient to induce cavitation in the hydrocarbon mixture without causing cracking. The high temperatures and high pressures resulting from cavitation reduce intermolecular forces between hydrocarbons thereby liberating existing lighter hydrocarbons in the diesel range or lighter for recovery via more traditional separation technologies. The resulting upgraded petroleum product exhibits lower distillation curves and decreased pollution causing components. Further, a wide variety of feedstocks can be treated according to the method of this invention.

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Номер записи: 57
04-12-2013 дата публикации

整合的加氢裂化和流化催化裂化系统和方法

Номер: CN103429708A
Автор: A·M·阿勒-索马利, M·M·阿勒-图巴伊提, O·R·克塞奥卢
Принадлежит: Saudi Arabian Oil Co

本发明提供一种裂化烃类原料的系统和方法，就希望的产品产率而言，其允许显著的灵活性。整合的方法包括将原料和氢引入到包含第一加氢裂化催化剂的第一加氢裂化反应区域中以产生第一区域流出物。将该第一区域流出物通到分馏区域中以至少产生低沸点馏分和高沸点馏分，以及任选地一种或多种中间馏分。将底部馏分输送到流化催化裂化反应和分离区域中，从这里回收烯烃和汽油。

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Номер записи: 58
20-11-2014 дата публикации

Oil refining waste treatment method

Номер: RU2532907C2
Автор: Джон Скейрс
Принадлежит: П-Фьюэл Лтд

FIELD: oil and gas industry. SUBSTANCE: invention is related to processing of oil refining wastes. The oil refining waste treatment method includes delivery of oil refining and plastic processing wastes and heating of the combined wastes using far-infrared radiation in order to split off volatile hydrocarbons, wherein the split off volatile hydrocarbons a collected for further usage. EFFECT: sound management of wastes, which includes uniform heating, minimisation of hot stains formation, minimisation of heat losses, reduction of coke deposits in the process of the method implementation. 8 cl, 1 tbl, 1 dwg, 3 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК C10G 15/00 B09B 3/00 C10G 32/00 C08J 11/00 C10G 1/00 (13) 2 532 907 C2 (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2011105024/04, 07.07.2009 (24) Дата начала отсчета срока действия патента: 07.07.2009 (72) Автор(ы): СКЕЙРС Джон (AU) (73) Патентообладатель(и): П-ФЬЮЭЛ ЛТД (AU) Приоритет(ы): (30) Конвенционный приоритет: (43) Дата публикации заявки: 20.08.2012 Бюл. № 23 R U 11.07.2008 AU 2008903565 (45) Опубликовано: 20.11.2014 Бюл. № 32 1923957 A, 07.03.2007. CN 1492024 A, 28.04.2004. RU 2005138138 A, 20.06.2007. US 20040235970 A1, 25.11.2004 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 11.02.2011 2 5 3 2 9 0 7 (56) Список документов, цитированных в отчете о поиске: KR 20020016566 A, 04.03.2002. CN 2 5 3 2 9 0 7 R U UA 2009/000878 (07.07.2009) C 2 C 2 (86) Заявка PCT: (87) Публикация заявки PCT: WO 2010/003180 (14.01.2010) Адрес для переписки: 129090, Москва, ул. Большая Спасская, 25, стр. 3, ООО "Юридическая фирма "Городисский и Партнеры" (54) СПОСОБ ПЕРЕРАБОТКИ ОТХОДОВ ПЕРЕРАБОТКИ НЕФТИ (57) Реферат: Изобретение относится к способу переработки углеводороды собирают для последующего отходов. Способ переработки отходов использования. Технический результат переработки нефти включает подачу ...

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Номер записи: 59
12-03-2013 дата публикации

Petroleum upgrading process

Номер: US8394260B2
Автор: Ki-Hyouk Choi
Принадлежит: Saudi Arabian Oil Co

A process for upgrading a heavy oil stream by completely mixing the heavy oil stream with a water stream prior to the introduction of an oxidant stream. A mixture of the heavy oil stream and the water stream are subjected to operating conditions, in the presence of the oxidant stream, that are at or exceed the supercritical temperature and pressure of water. The resulting product stream is a higher value oil having low sulfur, low nitrogen, and low metallic impurities as compared to the heavy oil stream.

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Номер записи: 60
10-01-2017 дата публикации

Method for processing oil wastes

Номер: RU2606385C1
Автор: Валентин Ивлиевич Фролов, Владимир Арнольдович Винокуров, Михаил Павлович Крестовников, Сергей Викторович Лесин
Принадлежит: Федеральное государственное бюджетное образовательное учреждение высшего образования &#34;Российский государственный университет нефти и газа (национальный исследовательский университет) имени И.М. Губкина&#34;

FIELD: oil and gas industry; waste processing and recycling. SUBSTANCE: present invention relates to a method of processing oil wastes containing water and mechanical impurities. Method comprises pre-activation of homogenised raw material with electromagnetic radiation with frequency 40.0–55.0 MHz, radiation power 0.2–0.6 kW for 1–8 hours, then activated material is heated in a single-flow vertical reactor in two stages, first stage is carried out at temperature of 110–120 °C with formation of steam-gas phase of first stage with its output from top of reactor, second stage is carried out at temperature of up to 375–400 °C with formation of steam-gas phase of second stage, coming from top of reactor, and solid residue with subsequent separation of steam-gas phases of first and second stages into water, liquid hydrocarbon phase and gas. Raw material is heated by means of high-frequency inductors with frequency of 8–20 kHz and power of 40–80 kW in presence of pre-heated steel balls fed into reactor cavity while ensuring their rotational motion in raw material under action of electromagnetic field, generated by inductors of low frequency 45–55 Hz and power of 6–10 kW, and inductors are arranged in series along reactor height with alternating low and high-frequency inductors, starting from low frequency inductor, located in upper part of reactor. EFFECT: proposed method enables to obtain desired products with high output, as well as increase content of hydrogen in obtained hydrocarbon gas. 1 cl, 1 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 606 385 C1 (51) МПК C10G 15/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ФОРМУЛА (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ 2015156814, 29.12.2015 (24) Дата начала отсчета срока действия патента: 29.12.2015 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 29.12.2015 (45) Опубликовано: 10.01.2017 Бюл. № 1 (56) Список документов, цитированных в отчете о поиске: RU 2246525C1, 20.02.2005. ...

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Номер записи: 61
27-04-2007 дата публикации

Method of the fractionation of the hydrocarbon raw and the installation for its realization

Номер: RU2298027C2
Автор: Николай Геннадьевич Шляхтин, хтин Николай Геннадьевич Шл
Принадлежит: Николай Геннадьевич Шляхтин

FIELD: oil processing industry; methods and devices of the fractionation of the hydrocarbon raw. SUBSTANCE: the invention is pertaining to the oil the oil products production process and may be used at the installations with the atmospheric and vacuum columns intended for fractionation distillation of the petroleum. At realization of the method act upon the hydrocarbon raw by the electromagnetic oscillations using the preliminary and main electromagnetic excitation. The preliminary action on the hydrocarbon raw is exercised in the working tanks or in the pipeline before the kilns of heating, and the main action is exercised in the rectification tower itself due to its resonant excitation. In the installation for realization of the method the source of the preliminary excitation is made in the form of the electromagnetic emitter with the preset frequency of oscillation, and the rectification tower after its resonance activation serves as the main exciter of the hydrocarbon raw under condition of provision of its operation in the self-oscillation mode. The formula for calculation of the oscillation frequency as the variable includes the temperature of the separation of the appropriate fraction. The technical result of the invention is the increased output of the light oils at reduction of the power inputs. EFFECT: the invention ensures the increased output of the light oils at reduction of the power inputs. 6 cl, 1 dwg ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß RU (19) (11) 2 298 027 (13) C2 (51) ÌÏÊ C10G 7/00 (2006.01) C10G 15/08 (2006.01) B01J 19/12 (2006.01) B01D 3/14 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2005115548/04, 24.05.2005 (72) Àâòîð(û): Øë õòèí Íèêîëàé Ãåííàäüåâè÷ (RU) (24) Äàòà íà÷àëà îòñ÷åòà ñðîêà äåéñòâè ïàòåíòà: 24.05.2005 (73) Ïàòåíòîîáëàäàòåëü(è): Øë õòèí Íèêîëàé Ãåííàäüåâè÷ (RU) (43) Äàòà ïóáëèêàöèè çà âêè: 20.11.2006 R U (45) Îïóáëèêîâàíî: 27.04.2007 Áþë. ¹ 12 ...

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Номер записи: 62
27-04-2010 дата публикации

Method and unit for preparation and fine processing of hydrocarbon stock

Номер: RU2387697C1
Автор: Владимир Андреевич Золотухин
Принадлежит: Владимир Андреевич Золотухин

FIELD: oil and gas production. SUBSTANCE: invention refers to a method of preparing and fine processing of hydrocarbon stock involving heating of stock and hydrogen, preparation of end-products; herewith liquid (oil, black oil, oil refining and petrochemistry remains) charge stock is heated up to the temperature above 20-50°C and exposed to thermal and/or thermomechanical (non-catalytic) cracking, molecular hydrogen and/or hydrogen enriched light hydrogenous mediums (natural or accompanying gas, gas and light fractions of oil refining and petrochemistry), if required are heated up separately from charge stock, supplied at greater pressure than that of the heating stage, to the stage of producing active atomic hydrogen and/or light radicals to a reactor or reactor package with a catalyst heated to the required temperature, thereafter produced active hydrogen and/or light radicals are supplied to a stock heating and cracking zone for the reaction; the reaction products are supplied to the separation stage; a portion of gas and light fractions and also unreacted hydrogen and/or light hydrogenous initial mediums after the separation stage are supplied to the start of the process and introduced into the charge stock, light end fractions of reaction after the separation stage mainly with end boiling point to 350-360°C, partially or completely supplied on the stage of producing light end commodity products (condensed gas, petrol, kerosene, diesel fuel) and/or partially returned and introduced into charge stock, heavy remains after the separation stage mainly with start boiling point 360°C and above, are partially or completely supplied for producing heavy commodity products (bitumen, coke), and, probably, partially or completely supplied for reprocessing by the given method to the start of the process together with charge stock; the stock and/or separation remain cracking and heating stages, hydrogen and/or hydrogenous medium and catalyst heating, production of active ...

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Номер записи: 63
16-03-2022 дата публикации

Non-thermal cracking reactor

Номер: RU2766847C1
Автор: Константин Витальевич Сластников
Принадлежит: Болтенков Евгений Владимирович, Константин Витальевич Сластников

FIELD: chemistry; technological processes. SUBSTANCE: invention relates to systems for cracking, in particular, changing properties of hydrocarbons of liquid, gaseous and other liquids. Invention relates to a non-thermal cracking reactor, comprising a dielectric housing filled with a dielectric compound inside, a magnetic field source in the form of magnets with like poles facing each other, comprising a central current-conducting part of a feedthrough capacitor, wherein central conductive element is composed of variable-section tube while second conductive element is composed of metal band wound on central conductive element via dielectric. Input and output of the central current-conducting element are equipped with dielectric connecting elements, which are connected by a bypass, at that, in opposite ends of the part of the central current-conducting element of larger diameter there installed are magnets facing each other with similar poles, and between the magnets there is a profiled element. In the centre of the magnet on the side of the part of the central current-conducting element of a smaller diameter there is an outlet hole, and inside the part of the central current-conducting element of a smaller diameter there is a spiral wound element made of non-magnetic material, besides, the housing, the central current-conducting element and the second current-conducting element form a coaxial structure located inside the longitudinally oriented magnetic field. EFFECT: formation of centripetal movement of working medium along the whole part of central current-conducting element of large and small diameters. 1 cl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 766 847 C1 (51) МПК C10G 15/08 (2006.01) F02M 27/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10G 15/08 (2021.08); F02M 27/04 (2021.08) (21)(22) Заявка: 2021102157, 29.01.2021 (24) Дата начала отсчета срока действия патента: (73) ...

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Номер записи: 64
07-11-2018 дата публикации

Method of determining optimum parameters for the refining of light oil products and the device for its implementation

Номер: RU2671868C1
Автор: Александр Васильевич Исаев, Владимир Петрович Попов, Вячеслав Валентинович Пащенко, Кирилл Владимирович Бакланов, Надежда Павловна Аверина, Сергей Васильевич Дунаев
Принадлежит: Вячеслав Валентинович Пащенко

FIELD: petroleum industry. SUBSTANCE: invention relates to a method for refining light petroleum products for the production of winter diesel fuel from them with the establishment of optimal parameters at their refining by adjusting the parameters of the cavitation effect and the destructive hydrogenation (hydrogenation) associated with such an indicator of the target product as its turbidity temperature and analysis of intermediate samples from each cavitation exposure apparatus and hydrogenator, determined by the results of IR spectroscopy and methods of physicochemical analysis of cooled samples of products before and after each cavitation apparatus and hydrogenation apparatus, in which the starting product is first subjected to the above analysis, then, by means of a control and safety unit, in an acoustic cavitator with a magnetostrictive radiator of ultrasonic vibrations and a hydrogenator, the initial parameters of their operation. In this case, the initial product is first subjected to a cavitation effect, intermediate sample is taken at the outlet of the cavitator, cooled to 30–50 °C, analyzed, removing its spectra and determining the physicochemical parameters, including the cloud point, the optimum performance of the cavitator is determined by comparing the results of the analysis of the samples with the expected properties of the samples characterizing their low-temperature properties, if necessary, the parameters of the cavitator are adjusted and then, if necessary, a repeated cavitation effect on the initial product is carried out, taking into account possible adjustment of the parameters of the cavitator, obtained cooled samples at the outlet of the cavitator are re-analyzed, and the cavitation effect on the initial product is terminated until the expected values of the intermediate product are achieved at the exit from the cavitator, resulting intermediate is then subjected to destructive hydrogenation at 260–300 °C in the hydrogenation reactor on ...

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Номер записи: 65
20-09-2008 дата публикации

Method of electrochemical cracking of heavy oil products

Номер: RU2333932C1
Автор: Владимир Анатольевич Щукин
Принадлежит: Владимир Анатольевич Щукин

FIELD: chemistry. SUBSTANCE: invention relates to the field of oil refining, namely, to process of electrochemical cracking of heavy raw oil. The invention concerns method of electrochemical cracking of heavy oil products under the action of electric current. The process is carried out at excessive pressure of 0.01-0.5 MPa and temperature of 380-450°C, in presence of alloys of metals Al, Cr, Ni, Fe, which are used as separate conductors placed in the region of cracking in contact with raw material, through which electric current with voltage of 0.1-10 kV and current value of 1-1·10 4 A is run. EFFECT: increase in output of light distillate fractions and obtaining only marketable products i.e. Diesel-oil fractions and non-oxidised bitumen with essential simplicity of the method and high manufacturability of the process. 1 ex, 1 tbl ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (11) 2 333 932 (13) C1 (51) ÌÏÊ C10G 15/08 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2007142521/04, 19.11.2007 (72) Àâòîð(û): Ùóêèí Âëàäèìèð Àíàòîëüåâè÷ (RU) (24) Äàòà íà÷àëà îòñ÷åòà ñðîêà äåéñòâè ïàòåíòà: 19.11.2007 (73) Ïàòåíòîîáëàäàòåëü(è): Ùóêèí Âëàäèìèð Àíàòîëüåâè÷ (RU) (45) Îïóáëèêîâàíî: 20.09.2008 Áþë. ¹ 26 R U (56) Ñïèñîê äîêóìåíòîâ, öèòèðîâàííûõ â îò÷åòå î ïîèñêå: RU 94013148 A1, 20.12.1995. RU 2122011 C1, 20.11.1998. RU 2179570 Ñ1, 20.02.2002. US 1585573 A, 18.05.1926. 2 3 3 3 9 3 2 Èçîáðåòåíèå êàñàåòñ ñïîñîáà ýëåêòðîõèìè÷åñêîãî êðåêèíãà ò æåëûõ íåôòåïðîäóêòîâ ïîä âîçäåéñòâèåì ýëåêòðè÷åñêîãî òîêà, ïðîöåññ âåäóò ïðè èçáûòî÷íîì äàâëåíèè 0,01-0,5 ÌÏà è òåìïåðàòóðå 380-450°Ñ, â ïðèñóòñòâèè ñïëàâîâ ìåòàëëîâ Al, Cr, Ni, Fe, êîòîðûå èñïîëüçóþò â âèäå îòäåëüíûõ ïðîâîäíèêîâ, óñòàíîâëåííûõ â çîíå êðåêèíãà â êîíòàêòå ñ ñûðüåì, ÷åðåç êîòîðûå ïðîïóñêàþò ýëåêòðè÷åñêèé òîê ñ íàïð æåíèåì 0,110 ê è âåëè÷èíîé òîêà 1-1⋅10 4 À. 1 òàáë. R U (57) Ðåôåðàò: Èçîáðåòåíèå îòíîñèòñ ê îáëàñòè íåôòåïåðåðàáîòêè, â ÷àñòíîñòè ê ...

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Номер записи: 66
04-10-2012 дата публикации

Hybrid fuel and method of making the same

Номер: WO2012135515A2
Автор: David J. GOERZ
Принадлежит: Fuelina, Inc.

A hybrid fuel and methods of making the same are disclosed. A process for making a hybrid fuel includes the steps of combining a biofuel emulsion blend and a liquid fuel product to form a hybrid fuel. Optionally, the hybrid fuel can be combined with water in a water-in-oil process and include oxygenate additives and additive packages. A hybrid fuel includes blends of biofuel emulsions and liquid fuel products, including light gas diesel. Optionally, the hybrid fuel can include water, oxygenate additives, and other additive packages.

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Номер записи: 67
25-09-2018 дата публикации

Synthetic gas production method

Номер: RU2668043C1
Автор: Александр Всеволодович Шумовский, Владимир Арнольдович Винокуров, Евгений Владимирович Иванов, Евгений Григорьевич Горлов, Марина Юрьевна Нисковская, Павел Александрович Гущин, Юрий Павлович Ясьян
Принадлежит: Федеральное государственное бюджетное образовательное учреждение высшего образования &#34;Кубанский государственный технологический университет&#34; (ФГБОУ ВО &#34;КубГТУ&#34;)

FIELD: technological processes.SUBSTANCE: invention relates to a method for producing synthesis gas by thermochemical processing of a combined feedstock consisting of plant material and a heavy hydrocarbon feedstock. Process is carried out by heating the heavy hydrocarbon feedstock to a temperature of 60–90 °C, and the vegetable raw material is subjected to grinding to a degree of grinding of at least 100 mcm. Thereafter, said heavy hydrocarbon feedstock and plant raw materials are mixed, followed by dispersing the resulting mixture in the presence of water and carbon black to form a slurry, which is subjected to successive acoustic treatment with a frequency of 21–25 kHz, an emission intensity of 5–10 W/cmat a temperature of 50–70 °C and processing time of 1–3 hours and electromagnetic processing with a radiation frequency of 40–60 MHz, capacity of 0.2–0.6 kW at a temperature of 50–70 °C, treatment time 1.0–8.0 hours. Gasification of the treated suspension is then carried out at a temperature of 800–1,200 °C to produce a synthesis gas that is purified with the separation of the carbon black used in the dispersing step.EFFECT: technical result consists in increasing the ratio H:CO in synthesis gas with simultaneous reduction of soot formation.1 cl, 3 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 668 043 C1 (51) МПК C10J 3/00 (2006.01) C10G 15/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10J 3/00 (2018.05); C10G 15/08 (2018.05) (21)(22) Заявка: 2017146025, 26.12.2017 (24) Дата начала отсчета срока действия патента: Дата регистрации: 25.09.2018 (45) Опубликовано: 25.09.2018 Бюл. № 27 Адрес для переписки: 350072, г.Краснодар, ул. Московская, 2, ФГБОУ ВО "КубГТУ", отдел интеллектуальной собственности, начальнику ОИС Тихомировой Н.А. 2904405 A1, 01.02.2008. RU 41307 U1, 20.10.2004. RU 2233312 C1, 27.07.2004. RU 2464295 C2, 20.10.2012. C 1 2 6 6 8 0 4 3 (56) Список документов, цитированных в отчете о поиске: ...

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Номер записи: 68
31-10-2012 дата публикации

Method of making an irradiated wood product

Номер: EP2415811A3
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

The invention relates to a method of making an irradiated wood product, the molecular weight of the carbohydrate-containing material contained in said wood product being thus increased; as well as to an irradiated wood product.

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Номер записи: 69
30-01-2019 дата публикации

Coal organic mass destruction method and process line for its implementation

Номер: RU2678591C1
Автор: Василий Иванович Мурко, Виктор Иванович Карпенок, Владимир Иванович Федяев, Вячеслав Викторович Шилин, Марина Петровна Баранова
Принадлежит: Василий Иванович Мурко, Вячеслав Викторович Шилин

FIELD: technological processes.SUBSTANCE: invention relates to the coal organic mass liquefaction technology during the coal deep processing. Coal raw materials organic compounds destruction method in the medium of organic solvent includes the simultaneous or sequential extreme physical impact on the destructible raw materials by wave hydrodynamic ultrasonic and electromagnetic fields with energy and frequencies corresponding to the destructible organic compounds resonant frequencies and / or the molecules oscillations frequency with subsequent temperature effect within the atmospheric distillation limits. Method differs in that the raw coal is preliminary subjected to wet grinding to cl. 0-1(3) mm followed by the prepared coal-water slurry demineralization by the oil granulation method with production of coal-oil granulate and coal concentrate, and water rock suspension, at that, prepared on the basis of the produced coal-oil granulate an organoleptic suspension and an organic solvent are subjected to the extreme physical impacts, wherein as the latter, the oil granulation agent is preferably used, and the resulting water rock suspension is dehydrated and the separated water is returned to the process head. Extreme physical effects include hydrodynamic cavitation, electromagnetic radiation, ultrasound, etc. Also claimed is the coal raw materials destruction processing line.EFFECT: reduction in production costs, increase in the coal raw materials organic compounds destruction process efficiency and used in the processing line equipment mechanical reliability, the liquid fractions yield is more than 90 %, at that, the mineral residue was 1½ %.2 cl, 3 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 678 591 C1 (51) МПК C10G 1/00 (2006.01) C10G 15/08 (2006.01) C10B 47/00 (2006.01) B02C 23/00 (2006.01) B01J 2/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10G 1/00 (2018.08); C10G 15/08 (2018.08); C10B 47/00 ( ...

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Номер записи: 70
28-01-2019 дата публикации

Patent RU2015131633A3

Номер: RU2015131633A3
Автор: [UNK]
Принадлежит: [UNK]

ВИ“? 2015131633” АЗ Дата публикации: 28.01.2019 Форма № 18 ИЗИМ-2011 Федеральная служба по интеллектуальной собственности Федеральное государственное бюджетное учреждение 5 «Федеральный институт промышленной собственности» (ФИПС) ОТЧЕТ О ПОИСКЕ 1. . ИДЕНТИФИКАЦИЯ ЗАЯВКИ Регистрационный номер Дата подачи 2015131633/10(048788) 29.07.2015 Приоритет установлен по дате: [ ] подачи заявки [ ] поступления дополнительных материалов от к ранее поданной заявке № [ ] приоритета 24.05.2011 по первоначальной заявке № 2011120911 из которой данная заявка выделена [ ] подачи первоначальной заявки № из которой данная заявка выделена [ ] подачи ранее поданной заявки № [ ] подачи первой(ых) заявки(ок) в государстве-участнике Парижской конвенции (31) Номер первой(ых) заявки(ок) (32) Дата подачи первой(ых) заявки(ок) (33) Код страны 1. 60/854,519 26.10.2006 05 2. 60/863,290 27.10.2006 05 3. 60/859,911 17.11.2006 05 4. 60/875,144 15.12.2006 05 5. 60/881,891 23.01.2007 05 Название изобретения (полезной модели): [Х] - как заявлено; [ ] - уточненное (см. Примечания) ПЕРЕРАБОТКА БИОМАССЫ Заявитель: КСИЛЕКО, ИНК., 05 2. ЕДИНСТВО ИЗОБРЕТЕНИЯ [Х] соблюдено [ ] не соблюдено. Пояснения: см. Примечания 3. ФОРМУЛА ИЗОБРЕТЕНИЯ: [Х] приняты во внимание все пункты (см. п см. Примечания [ ] приняты во внимание следующие пункты: [ ] принята во внимание измененная формула изобретения (см. Примечания) 4. КЛАССИФИКАЦИЯ ОБЪЕКТА ИЗОБРЕТЕНИЯ (ПОЛЕЗНОЙ МОДЕЛИ) (Указываются индексы МПК и индикатор текущей версии) С]12Р 5/00 (2006.01) С]ЗК 1/02 (2006.01) С05В 1/00 (2006.01) ВО1. 19/08 (2006.01) 5. ОБЛАСТЬ ПОИСКА 5.1 Проверенный минимум документации РСТ (указывается индексами МПК) С12Р5/00, С13К 1/02, С08В 1/00, ВО1319/08. 5.2 Другая проверенная документация в той мере, в какой она включена в поисковые подборки: 5.3 Электронные базы данных, использованные при поиске (название базы, и если, возможно, поисковые термины): Е-Габгагу, Езрасепе, РаЗеагсв, РАТЕМТСОРЕ, КОРТО, МСВ1, ЕМВГ-ЕВ1, Соозе, Соозе эсрБо][аг, ...

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Номер записи: 71
20-11-2006 дата публикации

METHOD FOR FACTIONING HYDROCARBON RAW MATERIALS AND INSTALLATION FOR ITS IMPLEMENTATION

Номер: RU2005115548A
Автор: Николай Геннадьевич Шляхтин, хтин Николай Геннадьевич Шл (RU)
Принадлежит: Николай Геннадьевич Шляхтин, хтин Николай Геннадьевич Шл (RU)

ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (11) 2005 115 548 (13) A (51) ÌÏÊ C10G 7/00 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÇÀßÂÊÀ ÍÀ ÈÇÎÁÐÅÒÅÍÈÅ (21), (22) Çà âêà: 2005115548/04, 24.05.2005 (71) Çà âèòåëü(è): Øë õòèí Íèêîëàé Ãåííàäüåâè÷ (RU) (43) Äàòà ïóáëèêàöèè çà âêè: 20.11.2006 Áþë. ¹ 32 (72) Àâòîð(û): Øë õòèí Íèêîëàé Ãåííàäüåâè÷ (RU) R U Àäðåñ äë ïåðåïèñêè: 101990, Ìîñêâà, Ïåòðîâåðèãñêèé ïåð., 4, "Àãåíòñòâî Åðìàêîâà, Ñòîë ðîâà è Ïàðòíåðû", ïàò.ïîâ. Å.À.Åðìàêîâîé (54) ÑÏÎÑÎÁ ÔÐÀÊÖÈÎÍÈÐÎÂÀÍÈß ÓÃËÅÂÎÄÎÐÎÄÍÎÃÎ ÑÛÐÜß È ÓÑÒÀÍÎÂÊÀ ÄËß ÅÃÎ A 2 0 0 5 1 1 5 5 4 8 R U Страница: 1 RU A (57) Ôîðìóëà èçîáðåòåíè 1. Ñïîñîá ôðàêöèîíèðîâàíè óãëåâîäîðîäíîãî ñûðü , âêëþ÷àþùèé êîëåáàòåëüíîå âîçäåéñòâèå íà óãëåâîäîðîäíîå ñûðüå, åãî òåðìè÷åñêèé êðåêèíã è ïîëó÷åíèå â ðåêòèôèêàöèîííîé êîëîííå èç ïàðîîáðàçíîé ôàçû êîíå÷íûõ ïðîäóêòîâ, îòëè÷àþùèéñ òåì, ÷òî êîëåáàòåëüíîå âîçäåéñòâèå íà óãëåâîäîðîäíîå ñûðüå âåäóò ïóòåì ïðåäâàðèòåëüíîãî è îñíîâíîãî âîçäåéñòâèé ýëåêòðîìàãíèòíûìè êîëåáàíè ìè, ïðè ýòîì ïðåäâàðèòåëüíîå âîçäåéñòâèå íà óãëåâîäîðîäíîå ñûðüå âåäóò â ïðîöåññå ïîäà÷è íà òåðìè÷åñêèé êðåêèíã, à îñíîâíîå - â ðåêòèôèêàöèîííîé êîëîííå, âîçäåéñòâó â íåé íà óãëåâîäîðîäíîå ñûðüå íà îäíîé èç âûáðàííîé äë îòáîðà ñîîòâåòñòâóþùåé ôðàêöèè óãëåâîäîðîäíîãî ñûðü ÷àñòîòû, ïîä÷èí þùåéñ îáùåé çàâèñèìîñòè F=(153511+562,311⋅Ò)⋅10 8, Ãö, ãäå Ò - òåìïåðàòóðà óãëåâîäîðîäíîãî ñûðü , ãðàäóñ; 562,311- óíèâåðñàëüíà ïîñòî ííà , õàðàêòåðèçóþùà âåëè÷èíó èçìåíåíè ÷àñòîòû êîëåáàíè àòîìà âîäîðîäà ïðè èçìåíåíèè òåìïåðàòóðû íà îäèí ãðàäóñ, Ãö/ãðàäóñ; 153511 - îïåðàòîð, ïîëó÷àåìûé óìíîæåíèåì óíèâåðñàëüíîé ïîñòî ííîé íà 273 ãðàäóñà, Ãö. 2. Ñïîñîá ïî ï.1, îòëè÷àþùèéñ òåì, ÷òî ïðåäâàðèòåëüíîå âîçäåéñòâèå âåäóò â òðóáîïðîâîäå, ïîäàþùåì óãëåâîäîðîäíîå ñûðüå íà òåðìè÷åñêèé êðåêèíã. 3. Ñïîñîá ïî ï.1, îòëè÷àþùèéñ òåì, ÷òî ïðåäâàðèòåëüíîå âîçäåéñòâèå âåäóò â ðàáî÷åé åìêîñòè èëè åìêîñò õ, èñïîëüçóåìûõ äë õðàíåíè è ïîäà÷è óãëåâîäîðîäíîãî ñûðü íà òåðìè÷åñêèé êðåêèíã. 4. Óñòàíîâêà äë ...

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Номер записи: 72
22-09-2011 дата публикации

High shear process for processing naphtha

Номер: WO2011084564A3
Автор: Abbas Hassan, Aziz Hassan, Gregory G. Borsinger, Krishnan Viswanathan
Принадлежит: H R D Corporation

A method and system for processing naphtha, including a high shear mechanical device. In one embodiment, the method comprises forming a dispersion of gas in a naphtha hydrocarbon liquid in a high shear device prior to introduction in a cracking reactor/furnace. In another instance the system for processing naphtha comprises a high shear device for mechanically shearing hydrocarbons.

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Номер записи: 73
02-09-2014 дата публикации

High shear process for processing naphtha

Номер: US8821713B2
Автор: Abbas Hassan, Aziz Hassan, Gregory G. Borsinger, Krishnan Viswanathan
Принадлежит: HRD Corp

A method and system for processing naphtha, including a high shear mechanical device. In one embodiment, the method comprises forming a dispersion of gas in a naphtha hydrocarbon liquid in a high shear device prior to introduction in a cracking reactor/furnace. In another instance the system for processing naphtha comprises a high shear device for mechanically shearing hydrocarbons.

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Номер записи: 74
29-12-2015 дата публикации

High shear process for processing naphtha

Номер: US9222033B2
Автор: Abbas Hassan, Aziz Hassan, Gregory G. Borsinger, Krishnan Viswanathan
Принадлежит: HRD Corp

A method and system for processing naphtha, including a high shear mechanical device. In one embodiment, the method comprises forming a dispersion of gas in a naphtha hydrocarbon liquid in a high shear device prior to introduction in a cracking reactor/furnace. In another instance the system for processing naphtha comprises a high shear device for mechanically shearing hydrocarbons.

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Номер записи: 75
27-11-2008 дата публикации

Ultrasonic conversion of oil residue into usable oils

Номер: RU2339676C2
Автор: Рудольф В. ГАННЕРМАН, Рудольф В. ГАННЕРМАН (US)
Принадлежит: Сальфко, Инк.

Изобретение относится к способу конверсии компонентов нефтяного остатка, имеющих до обработки температуры кипения примерно от 200°С (400°F) до 430°С (800°F), в продукты, имеющие температуры кипения, которые ниже, по меньшей мере, примерно на 11°С (20°F), включающему следующие стадии: (а) комбинирование нефтяного остатка с водной жидкостью с образованием эмульсии, (б) воздействие на эмульсию ультразвуком, (в) извлечение органической фазы из эмульсии после указанного воздействия, причем для образования эмульсии используют добавку, представляющую собой жидкие алифатические углеводороды C 15 -C 20 и смеси таких углеводородов или диалкиловый эфир. Применение данного способа позволяет извлечь большее количество пригодного к употреблению масла из нефтяного остатка. 6 з.п. ф-лы, 1 ил. ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (11) 2 339 676 (13) C2 (51) ÌÏÊ C10G 15/08 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2006136425/04, 18.02.2005 (72) Àâòîð(û): ÃÀÍÍÅÐÌÀÍ Ðóäîëüô Â. (US) (24) Äàòà íà÷àëà îòñ÷åòà ñðîêà äåéñòâè ïàòåíòà: 18.02.2005 (73) Ïàòåíòîîáëàäàòåëü(è): ÑÀËÜÔÊÎ, ÈÍÊ. (US) R U (30) Êîíâåíöèîííûé ïðèîðèòåò: 17.03.2004 US 10/803,802 (43) Äàòà ïóáëèêàöèè çà âêè: 27.04.2008 (45) Îïóáëèêîâàíî: 27.11.2008 Áþë. ¹ 33 2 3 3 9 6 7 6 (56) Ñïèñîê äîêóìåíòîâ, öèòèðîâàííûõ â îò÷åòå î ïîèñêå: RU 2151165 C1, 20.06.2000. ÌÎÐÎÇΠÃ.À. Ïðèìåíåíèå òîïëèâ è ìàñåë â äèçåë õ. Ì.: ÍÅÄÐÀ, 1964, ñ.51. US 5110443 À, 05.05.1992. US 3497005 À, 24.02.1970. RU 2078116 Ñ1, 27.04.1997. 2 3 3 9 6 7 6 R U (86) Çà âêà PCT: US 2005/005408 (18.02.2005) C 2 C 2 (85) Äàòà ïåðåâîäà çà âêè PCT íà íàöèîíàëüíóþ ôàçó: 17.10.2006 (87) Ïóáëèêàöè PCT: WO 2005/091859 (06.10.2005) Àäðåñ äë ïåðåïèñêè: 103735, Ìîñêâà, óë. Èëüèíêà, 5/2, ÎÎÎ "Ñîþçïàòåíò", Í.Í.Âûñîöêîé (54) ÊÎÍÂÅÐÑÈß ÍÅÔÒßÍÎÃÎ ÎÑÒÀÒÊÀ  ÏÐÈÃÎÄÍÛÅ Ê ÓÏÎÒÐÅÁËÅÍÈÞ ÌÀÑËÀ Ñ ÏÐÈÌÅÍÅÍÈÅÌ ÓËÜÒÐÀÇÂÓÊÀ (57) Ðåôåðàò: Èçîáðåòåíèå îòíîñèòñ ê ñïîñîáó êîíâåðñèè êîìïîíåíòîâ íåôò ...

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Номер записи: 76
31-10-2018 дата публикации

Device for treatment of liquid and gaseous substances containing hydrogen and carbon

Номер: RU2671451C2
Автор: Ченгиз ЭРИЙЛЬМАЗ
Принадлежит: Ченгиз ЭРИЙЛЬМАЗ

FIELD: chemistry.SUBSTANCE: invention relates to devices for treating liquid hydrocarbon fuels. Disclosed device for treating liquid and gaseous substances containing hydrogen and hydrocarbon, consisting of non-magnetic, cylindrical brass outer casing 1, having exhaust part 6 and inner part 3 having a thread, into which a cylindrical magnet assembly is inserted, consisting of thirteen rare-earth neodymium magnets, made in the form of a circular ring with a central opening and separated by non-magnetic PVC gaskets, made in the form of a thin round ring. Central opening of the cylindrical magnet assembly defines an annular magnetisation chamber through which the treated fluid passes. Casing 1 is closed by a brass threaded cap 2, having inlet part 5.EFFECT: providing an improved method and a new generation simplified device for treatment of hydrogen and hydrocarbon consisting liquid and gas substances as water to remove contaminants thereof and more particularly liquid and gaseous hydrocarbon fuels, such as gasoline, gasohol, diesel fuel, kerosene, propane, natural gas, oil like to enhance the combustion efficiency for therein.6 cl, 11 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 671 451 C2 (51) МПК F02M 27/04 (2006.01) F02B 51/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 19/08 (2018.02); C10G 32/02 (2018.02); C10L 1/02 (2018.02); C10L 1/04 (2018.02); C10L 3/101 (2018.02); F02B 51/04 (2018.02); F02M 27/045 (2018.02) (21)(22) Заявка: 2016144083, 11.04.2014 11.04.2014 (73) Патентообладатель(и): ЭРИЙЛЬМАЗ Ченгиз (TR) Дата регистрации: 31.10.2018 Приоритет(ы): (30) Конвенционный приоритет: 09.04.2014 TR 2014 - G - 127798 PT 2014/04119 (43) Дата публикации заявки: 15.05.2018 Бюл. № 2052652 C1, 20.01.1996. RU 2327895 C2, 27.06.2008. JP H11-182363 A, 06.07.1999. RU 38847 U1, 10.07.2004. WO 1997029279 A1, 14.08.1997. 14 (45) Опубликовано: 31.10.2018 Бюл. № 31 C 2 C 2 (85) Дата начала рассмотрения заявки PCT ...

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Номер записи: 77
21-08-2017 дата публикации

Method for heavy oil feedstock processing

Номер: RU2628611C1
Автор: Артем Олегович Ромашев, Надежда Валерьевна Николаева, Татьяна Николаевна Александрова
Принадлежит: федеральное государственное бюджетное образовательное учреждение высшего образования &#34;Санкт-Петербургский горный университет&#34;

FIELD: oil and gas industry. SUBSTANCE: method for cavitation extraction recovery of valuable metals from heavy oil feedstock involves mixing initial feed oil with water and kerosene. The resulting mixture is processed ultrasonically at frequency ranging from 22 to 44 kHz for 5 to 10 minutes. Then, the light fraction is sent for processing, and heavy fraction is mixed with water and chemical extractant. The resulting suspension is processed ultrasonically at frequency ranging from 22 to 44 kHz for 10 to 20 minutes. Heavy fraction is transported to cavitation treatment, where asphaltene fraction associated with the metals is released. The resulting asphaltene fraction is fed to enrichment processing for recovery of metals using traditional enrichment and metallurgical technologies. The light fraction after cavitation treatment contains metalloporphyrins and combines with light fraction after ultrasonic treatment and is sent to the pharmaceutical industry. EFFECT: increasing yield of light fractions and increasing depth of heavy oil feedstock processing by means of extracting valuable metals. 2 tbl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 628 611 C1 (51) МПК C10G 15/08 (2006.01) B01J 19/08 (2006.01) B01J 19/10 (2006.01) C10G 7/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2016138893, 03.10.2016 (24) Дата начала отсчета срока действия патента: 03.10.2016 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 03.10.2016 (45) Опубликовано: 21.08.2017 Бюл. № 24 C 1 2394067 C2, 10.07.2010. RU 2346024 C1, 28.08.2003. EA 21729 B1, 31.08.2015. (54) СПОСОБ ПЕРЕРАБОТКИ ТЯЖЕЛОГО НЕФТЯНОГО СЫРЬЯ (57) Реферат: Изобретение относится к области кавитационную обработку, где происходит нефтепереработки, в частности к извлечению выделение асфальтеновой фракции, металлов из тяжелого нефтяного сырья, и может ассоциированной с металлами. Полученная быть использовано при обогащении асфальтеновая фракция ...

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Номер записи: 78
22-09-2017 дата публикации

Method of allocating concentrate of valuable metals contained in heavy oils and products of their processing

Номер: RU2631427C1
Автор: Константин Андреевич Аверин, Мурат Яхьяевич Висалиев, Саламбек Наибович Хаджиев, Татьяна Владимировна Мокочунина, Хусаин Магамедович Кадиев, Юрий Анатольевич Лебедев
Принадлежит: федеральное государственное автономное образовательное учреждение высшего образования &#34;Московский физико-технический институт (государственный университет)&#34;

FIELD: chemistry. SUBSTANCE: presented method includes processing heavy crude oil with a low-temperature plasma generated by microwave (MW) electromagnetic radiation. The method is implemented as follows. Heavy crude oil is loaded to the heated reactor equipped with an electrode with a through-hole for supplying inert gas-argon. An inert gas is fed through the electrode, after which the power is turned on and the plasma is generated. At the tip of the electrode, a breakdown is initiated with further formation of gas bubbles, the temperature inside of which reaches 1500 K. The processing of crude oil is carried out for 2 minutes. Heavy crude oil is used as a processed sample with the density of 900 to 1100 kg/m 3 . A copper rod is used as a material for the electrode. The method allows to obtain a concentrate of valuable metals such as Ni, V, Mo, Co, Cu, Zn, and others contained in crude oil. EFFECT: production of a solid product from heavy crude oil and liquid hydrocarbons with a reduced metal content. 2 cl, 3 tbl, 3 ex, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (51) МПК C10G 15/12 C10G 15/08 C10G 32/02 C22B 23/00 C22B 34/00 C22B 59/00 (11) (13) 2 631 427 C1 (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2016149262, 15.12.2016 (24) Дата начала отсчета срока действия патента: 15.12.2016 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 15.12.2016 (45) Опубликовано: 22.09.2017 Бюл. № 27 Адрес для переписки: 141700, Московская обл., г. Долгопрудный, Институтский пер., 9, МФТИ, отдел по интеллектуальной собственности (56) Список документов, цитированных в отчете о поиске: RU 2535211 C2, 10.12.2014. RU 2 6 3 1 4 2 7 R U (54) Способ выделения концентрата ценных металлов, содержащихся в тяжелых нефтях и продуктах их переработки (57) Реферат: Изобретение относится к способу выделения пузырей, температура внутри которых достигает ценных металлов, ...

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Номер записи: 79
04-03-2010 дата публикации

Self-sustaining cracking of hydrocarbons

Номер: US20100051444A1
Автор: Raissa F. Zaikina, Yuriy A. Zaikin
Принадлежит: PetroBeam Inc

The present disclosure provides a simple and efficient method for the self-sustaining radiation cracking of hydrocarbons. The method disclosed provides for the deep destructive processing of hydrocarbon chains utilizing hydrocarbon chain decomposition utilizing self-sustaining radiation cracking of hydrocarbon chains under a wide variety of irradiation conditions and temperature ranges (from room temperature to 400° C.). Several embodiments of such method are disclosed herein, including; (i) a special case of radiation-thermal cracking referred to as high-temperature radiation cracking (HTRC); (ii) low temperature radiation cracking (LTRC); and (iii) cold radiation cracking (CRC). Such methods were not heretofore appreciated in the art. In one embodiment, a petroleum feedstock is subjected to irradiation to initiate and/or at least partially propagate a chain reaction between components of the petroleum feedstock. In one embodiment, the treatment results in hydrocarbon chain decomposition; however, other chemical reactions as described herein may also occur.

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Номер записи: 80
16-12-2014 дата публикации

Self-sustaining cracking of hydrocarbons

Номер: US8911617B2
Автор: Raissa F. Zaikina, Yuriy A. Zaikin
Принадлежит: PetroBeam Inc

The present disclosure provides a simple and efficient method for the self-sustaining radiation cracking of hydrocarbons. The method disclosed provides for the deep destructive processing of hydrocarbon chains utilizing hydrocarbon chain decomposition utilizing self-sustaining radiation cracking of hydrocarbon chains under a wide variety of irradiation conditions and temperature ranges (from room temperature to 400° C.). Several embodiments of such method are disclosed herein, including; (i) a special case of radiation-thermal cracking referred to as high-temperature radiation cracking (HTRC); (ii) low temperature radiation cracking (LTRC); and (iii) cold radiation cracking (CRC). Such methods were not heretofore appreciated in the art. In one embodiment, a petroleum feedstock is subjected to irradiation to initiate and/or at least partially propagate a chain reaction between components of the petroleum feedstock. In one embodiment, the treatment results in hydrocarbon chain decomposition; however, other chemical reactions as described herein may also occur.

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Номер записи: 81
05-06-2012 дата публикации

Self-sustaining cracking of hydrocarbons

Номер: US8192591B2
Автор: Raissa F. Zaikina, Yuriy A. Zaikin
Принадлежит: PetroBeam Inc

The present disclosure provides a simple and efficient method for the self-sustaining radiation cracking of hydrocarbons. The method disclosed provides for the deep destructive processing of hydrocarbon chains utilizing hydrocarbon chain decomposition utilizing self-sustaining radiation cracking of hydrocarbon chains under a wide variety of irradiation conditions and temperature ranges (from room temperature to 400° C.). Several embodiments of such method are disclosed herein, including; (i) a special case of radiation-thermal cracking referred to as high-temperature radiation cracking (HTRC); (ii) low temperature radiation cracking (LTRC); and (iii) cold radiation cracking (CRC). Such methods were not heretofore appreciated in the art. In one embodiment, a petroleum feedstock is subjected to irradiation to initiate and/or at least partially propagate a chain reaction between components of the petroleum feedstock. In one embodiment, the treatment results in hydrocarbon chain decomposition; however, other chemical reactions as described herein may also occur.

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Номер записи: 82
18-04-2017 дата публикации

Processing materials

Номер: US9624443B2
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems are described that can use feedstock materials, such as cellulosic and/or lignocellulosic materials and/or starchy materials, to produce ethanol and/or butanol, e.g., by fermentation. Hydrocarbon-containing materials are also used as feedstocks.

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Номер записи: 83
31-07-2018 дата публикации

Processing materials

Номер: US10035958B2
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems are described that can use feedstock materials, such as cellulosic and/or lignocellulosic materials and/or starchy materials, to produce ethanol and/or butanol, e.g., by fermentation. Hydrocarbon-containing materials are also used as feedstocks.

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Номер записи: 84
15-05-2018 дата публикации

MORE EFFECTIVE TREATMENT OF LIQUID AND GAS-CONTAINING SUBSTANCES CONTAINING HYDROGEN AND HYDROCARBONS, BASED ON THE MAXIMUM INCREASED SUFFICIENT MAGNETIC EFFECT, CREATED IMPROVEMENT OF IMPROVEMENT.

Номер: RU2016144083A
Автор: Ченгиз ЭРИЙЛЬМАЗ
Принадлежит: Ченгиз ЭРИЙЛЬМАЗ

РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2016 144 083 A (51) МПК F02M 27/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2016144083, 11.04.2014 (71) Заявитель(и): ЭРИЙЛЬМАЗ Ченгиз (TR) Приоритет(ы): (30) Конвенционный приоритет: 09.04.2014 TR 2014 - G - 127798 PT 2014/04119 (72) Автор(ы): ЭРИЙЛЬМАЗ Ченгиз (TR) (85) Дата начала рассмотрения заявки PCT на национальной фазе: 09.11.2016 R U (43) Дата публикации заявки: 15.05.2018 Бюл. № 14 (86) Заявка PCT: (87) Публикация заявки PCT: WO 2015/156745 (15.10.2015) R U (54) БОЛЕЕ ЭФФЕКТИВНАЯ ОБРАБОТКА ЖИДКИХ И ГАЗООБРАЗНЫХ ВЕЩЕСТВ, СОДЕРЖАЩИХ ВОДОРОД И УГЛЕВОДОРОДЫ, ЗА СЧЕТ МАКСИМАЛЬНО УВЕЛИЧЕННОГО ДОСТАТОЧНОГО МАГНИТНОГО ВОЗДЕЙСТВИЯ, СОЗДАВАЕМОГО УСОВЕРШЕНСТВОВАННЫМ УСТРОЙСТВОМ НОВОГО ПОКОЛЕНИЯ (57) Формула изобретения 1. Упрощенное устройство нового поколения, отличающееся, в общем, наличием немагнитного цилиндрического наполненного латунью наружного цельного корпуса, который, в общем, состоит из 3 основных частей, в котором одна из основных частей, представляющая собой немагнитный цилиндрический наполненный латунью наружный полукорпус, имеет полную наружную длину, равную 183 мм (17, 18) и наружный ∅42 мм (9, 16), и состоит из 3 секций разного размера, где обычно первая секция основной части, образующая полностью закрытую сторону немагнитного цилиндрического наполненного латунью наружного корпуса (1), имеет сопло (6) (наружный ∅12 мм и внутренний ∅8 мм и длина 30 мм), используемое как выпускное отверстие (7), через которое жидкие и газообразные вещества, состоящие из водорода и углеводородов, такие как вода, и более конкретно, жидкие и газообразные углеводородные топлива, такие как бензин, бензоспирт, дизельное топливо, керосин, пропан, природный газ, масло, выходят из упрощенного устройства нового поколения, и вторая секция основной части, которая образует внутреннее цилиндрическое открытое ложе (3), имеет (наружный ∅42 мм и внутренний ∅31 мм и длину 148 мм) ( ...

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Номер записи: 85
07-07-2020 дата публикации

Processing biomass

Номер: US10704196B2
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems are described that can use feedstock materials, such as cellulosic and/or lignocellulosic materials, to produce ethanol and/or butanol, e.g., by fermentation.

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Номер записи: 86
20-05-2005 дата публикации

Method of initiation of chain reactions of dissociation and polycondensation of hydrocarbons and a device for its realization

Номер: RU2252069C2
Автор: А.В. Чесноков, А.З. Ишмухаметов, В.М. Нистратов, В.П. Смирнов, Виктор Капитонович Петухов, И.Н. Музалевска, И.Н. Музалевская, И.Р. Хайрудинов
Принадлежит: Бердников Юрий Фаридович, Нистратов Виталий Михайлович, Смирнов Валентин Пантелеймонович

FIELD: chemical industry; natural gas industry; petroleum industry; petrochemical industry and other industries. SUBSTANCE: the invention falls into chemical industry, natural gas industry, petroleum industry, petrochemical industry and other branches pertaining to processing of hydrocarbon raw material, in particular, with production of a condensate consisting of light hydrocarbon gases and with processing of high-viscosity petroleum and petroleum residue. Substance of the invention: the method provides for a thermal treatment of the raw materials and treatment of a surface of a layer or a stream of a feed stock in a gaseous medium containing hydrogen and-or gaseous alkanes at a heightened temperature and an atmospheric pressure by ionizing radiation of relativistic electrons with energy in the range from about 0.5 up to about 10.0 MeV, preferably, from about 0.5 up to about 2.5 MeV at a width of the layer or a stream of a feed stock equal to the depth of sorption of the electronic emission, defined by the ratio λ x ρ = 0.5 E - 0.1, where λ - the depth of sorption of the electronic emission, cm; ρ - a density of the raw material, g /cm 3 ; E - energy of electrons, MeV. Electrons irradiation is conducted onto the one side of the layer or from the two counter sides of the layer in the mode of a continuous irradiation or in a pulsed - periodic mode. The invention offers devices for realization of the method. The invention allows to increase output of the low-molecular hydrocarbons and to ensure a desirable productivity of the process. EFFECT: the invention ensures an increased output of the low-molecular hydrocarbons and a desirable productivity of the process. 20 cl, 8 ex, 5 dwg, 3 tbl ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (51) ÌÏÊ 7 (11) 2 252 069 (13) C2 B 01 J 19/08, C 10 G 15/10 ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2003122425/15, 24.07.2003 (24) Äàòà íà÷àëà äåéñòâè ïàòåíòà: ...

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Номер записи: 87
19-06-2017 дата публикации

Heavy feedstock refining method

Номер: RU2622650C1
Автор: Валентин Ивлиевич Фролов, Владимир Арнольдович Винокуров, Павел Александрович Гущин, Сергей Викторович Лесин
Принадлежит: Федеральное государственное бюджетное образовательное учреждение высшего образования &#34;Российский государственный университет нефти и газа (национальный исследовательский университет) имени И.М. Губкина&#34;

FIELD: oil and gas industry. SUBSTANCE: invention relates to a method for processing heavy feedstock by mixing the said feedstock with solid iron-containing waste of metalworking with particle sizes of not more than 100 mcm and asphalt-resin-paraffin deposits, waste of the oil production process, taken in an amount of 0.03-0.1% and 3.0-5.0% of the mass of heavy oil feedstock, activation of formed mixture by electromagnetic radiation with a frequency of 40-55 MHz, a power of 0.2-0.6 kW, at a temperature of 40°-70°C, for 1-8 hours, subsequent thermal cracking of activated mixture at a temperature of 370-420°C and separation of cracking products to obtain the desired cuts. EFFECT: method allows to increase the quality of gasoline, diesel and gasoil cuts obtained, while maintaining the yield. 2 tbl, 1 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 622 650 C1 (51) МПК C10G 15/08 (2006.01) C10G 9/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ФОРМУЛА (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ 2016135653, 02.09.2016 (24) Дата начала отсчета срока действия патента: 02.09.2016 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 02.09.2016 (45) Опубликовано: 19.06.2017 Бюл. № 17 (56) Список документов, цитированных в отчете о поиске: В.А. Винокуров и др. Особенности (57) Формула изобретения Способ переработки тяжелого нефтяного сырья путем смешения указанного сырья с твердым железосодержащим отходом металлообработки с размерами частиц не более 100 мкм и асфальтосмолопарафиновыми отложениями - отходом процесса добычи нефти, взятыми в количестве соответственно 0,03-0,1% и 3,0-5,0% от массы тяжелого нефтяного сырья, активации образованной смеси электромагнитным излучением с частотой 40-55 МГц, мощностью 0,2-0,6 кВт, при температуре 40-70°C, в течение 1-8 ч, последующего термического крекинга активированной смеси при температуре 370420°C и разделения продуктов крекинга с получением целевых фракций. R U 2 6 2 2 6 5 0 (54) СПОСОБ ...

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Номер записи: 88
11-11-2022 дата публикации

High-temperature impact heating for thermochemical reactions

Номер: KR20220150981A
Автор: 둥샤 리우, 량빙 후, 용강 야오, 치 동
Принадлежит: 유니버시티 오브 매릴랜드, 칼리지 파크

하나 이상의 반응물이 제1 기간 동안 반응기에서 가열 요소와 열 접촉하도록 흐른다. 가열 사이클의 제1 부분 동안, 하나 이상의 열화학 반응이 개시되도록 가열 요소로 가열함으로써 하나 이상의 반응물에 제1 온도가 제공된다. 상기 하나 이상의 열화학 반응은 열분해, 열발산, 합성, 수소화, 탈수소화, 가수소분해, 또는 이들의 임의의 조합을 포함한다. 제1 가열 요소는 줄 가열에 의해 작동하고 기체가 통과할 수 있도록 하는 다공성 구조를 갖는다. 상기 가열 사이클의 제2 부분 동안, 하나 이상의 반응물은 예를 들어 가열 요소의 전원을 차단함으로써 제1 온도보다 낮은 제2 온도로 제공된다. 제1 기간의 지속 시간은 5초 미만인 가열 사이클의 지속 시간 이상이다.

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Номер записи: 89
06-12-2018 дата публикации

Method for the treatment of a liquid, in particular a mineral oil

Номер: KR101925925B1
Автор: 뤼디게르 우베 뉘르크, 아니발 루이스 베네치아노 리베라, 카스틸로 요세 미구엘 델가도, 페도르 체르니코브
Принадлежит: 프리스텍 아게

본원에는 액체 중의 저비점 분획의 부분을 증가시키기 위해 액체, 특히 미네랄 오일을 제 1 주파수의 압력파로 처리함에 있어서 압력파 발생기의 작동점을 조절하기 위한 방법으로서, 압력파 발생기가 관통 파이핑을 통해 액체, 특히 물과 소통되고, 적용 주파수가 변화되고, 작동점이 적용 주파수의 함수로서 압력파 발생기를 통과한 후에 액체의 최대 온도 증가치로서 결정됨을 특징으로 하는 방법이 기술된다. A method for controlling the operating point of a pressure wave generator in treating a liquid, particularly a mineral oil, with a pressure wave of a first frequency to increase a fraction of a low boiling fraction in the liquid, the method comprising: Characterized in that it is characterized in that it is in particular communicated with water, the applied frequency is changed and the operating point is determined as the maximum temperature increase of the liquid after passing through the pressure wave generator as a function of the applied frequency.

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Номер записи: 90
22-05-2019 дата публикации

Synthetic gas production method

Номер: RU2688737C1
Автор: Александр Всеволодович Шумовский, Владимир Арнольдович Винокуров, Евгений Владимирович Иванов, Евгений Григорьевич Горлов, Марина Юрьевна Нисковская, Павел Александрович Гущин, Юрий Павлович Ясьян
Принадлежит: Федеральное государственное бюджетное образовательное учреждение высшего образования &#34;Кубанский государственный технологический университет&#34; (ФГБОУ ВО &#34;КубГТУ&#34;)

FIELD: technological processes.SUBSTANCE: invention relates to production of synthesis gas by thermochemical treatment of vegetal raw materials and heavy hydrocarbon material. Method includes heating of heavy hydrocarbon material to 60–90 °C, milling vegetal raw material to particle size of not more than 200 mcm, pyrolysis of milled vegetal raw material at 500–800 °C to produce first gas stream, resin and semi-coke, mixing resin and semi-coke with heavy hydrocarbon feedstock. Method then includes dispersing said mixture in the presence of an aqueous suspension of soot and water to obtain a suspension which is successively subjected to acoustic treatment with a radiation frequency of 21–25 kHz, radiation intensity of 5–10 W/cm, treatment time 1.0–3.0 h and electromagnetic processing with radiation frequency of 40–60 MHz, power of 0.2–0.6 kW, processing time of 1.0–8.0 hours at temperature of 50–70 °C to form a treated suspension, which is fed for gasification at 800–1,400 °C to produce a second gas stream, separating the aqueous soot suspension from the second gas stream. Then, the first gas flow and the second gas flow are mixed after separating the aqueous suspension of soot and the formed mixture is purified to obtain the target synthetic gas.EFFECT: technical result is higher ratio H:CO in synthesis gas with simultaneous reduction of soot formation.1 cl, 3 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 688 737 C1 (51) МПК C10J 3/00 (2006.01) C10B 53/02 (2006.01) C10G 15/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10J 3/00 (2019.02); C10B 53/02 (2019.02); C10G 15/08 (2019.02) (21)(22) Заявка: 2018130791, 24.08.2018 (24) Дата начала отсчета срока действия патента: Дата регистрации: 22.05.2019 (45) Опубликовано: 22.05.2019 Бюл. № 15 Адрес для переписки: 350072, г. Краснодар, ул. Московская, 2, ФГБОУ ВО "КубГТУ", отдел интеллектуальной собственности, начальнику ОИС Тихомировой Н.А. 2464295 C2, 20.10. ...

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Номер записи: 91
20-09-2015 дата публикации

Composition for producing product selected from alcohols, organic acids, sugars, hydrocarbons and mixes thereof

Номер: RU2563357C2
Автор: Маршалл Медофф
Принадлежит: Ксилко, Инк.

FIELD: chemistry. SUBSTANCE: invention relates to biotechnology. Disclosed composition for preparation of a product, selected from a group consisting of alcohols, organic acids, sugars, hydrocarbons and mixes thereof. The composition contains cellulosic or lignocellulosic material and cellulolytic enzyme and/or a fermentation-triggering microorganism. According to gel-permeating chromatography results, the cellulosic or lignocellulosic material has a peak of maximum molecular weight of less than 25000 and crystallinity of less than 55%, determined by X-ray diffraction, wherein the material has a bulk density of less than 0.5 g/cm 3 , determined according to ASTM D18 95B. EFFECT: higher fermentation capacity of cellulosic or lignocellulosic material. 13 cl, 40 dwg, 9 tbl, 20 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 563 357 C2 (51) МПК C08L 1/02 (2006.01) C12P 7/08 (2006.01) C10G 1/00 (2006.01) C10G 32/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2011120911/10, 24.05.2011 (24) Дата начала отсчета срока действия патента: 26.10.2007 (72) Автор(ы): МЕДОФФ Маршалл (US) (73) Патентообладатель(и): КСИЛКО, ИНК. (US) Приоритет(ы): (30) Конвенционный приоритет: 2 5 6 3 3 5 7 R U (56) Список документов, цитированных в отчете о поиске: YE SUN et al. Hydrolysis of lignocellulosic materials for ethanol production: a review // Bioresource Technology, 83, 2002, p. 1-11. WO 0202288 A1, 10.01.2002. А.А. ЕФРЕМОВ и др. Получение левулиновой кислоты из лигноцеллюлозного сырья в присутствии катализаторов кислотного типа // Химия растительного сырья, N4, 1999, с. 6175 Адрес для переписки: 129090, Москва, ул. Б. Спасская, 25, строение 3, ООО "Юридическая фирма Городисский и Партнеры" (54) КОМПОЗИЦИЯ ДЛЯ ПОЛУЧЕНИЯ ПРОДУКТА, ВЫБРАННОГО ИЗ СПИРТОВ, ОРГАНИЧЕСКИХ КИСЛОТ, САХАРОВ, УГЛЕВОДОРОДОВ И ИХ СМЕСЕЙ (57) Реферат: Изобретение относится к области процессы. Целлюлозный или лигноцеллюлозный биотехнологии. Предложена ...

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Номер записи: 92
19-12-2017 дата публикации

Method of magnetic activation of liquid high molecular hydrocarbons and device for method implementation

Номер: RU2638921C2
Автор: Михаил Павлович Крестовников
Принадлежит: Михаил Павлович Крестовников

FIELD: electricity. SUBSTANCE: method of magnetic activation of liquid high-molecular hydrocarbons, in which a current pulse is passed through the conductors located in a liquid flow to create a magnetic field in a liquid flowing through a diamagnetic tube and a device for implementing this method, in which the magnetic field formers are outside the pipe, and metal conductors are installed inside the pipe, the insulated ends of which are led out to the outside of the pipe and are connected to pulsed power sources via the controlled switches. EFFECT: increasing the magnetic activation of hydrocarbons allows to reduce the heating temperature of hydrocarbons during processing by thermal decomposition and to reduce coking on the heating surfaces. 5 cl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 638 921 C2 (51) МПК C10G 15/08 (2006.01) C10G 15/00 (2006.01) C02F 1/46 (2006.01) C02F 1/48 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2016117910, 06.05.2016 (24) Дата начала отсчета срока действия патента: 06.05.2016 (72) Автор(ы): Крестовников Михаил Павлович (RU) (73) Патентообладатель(и): Крестовников Михаил Павлович (RU) Дата регистрации: (56) Список документов, цитированных в отчете о поиске: RU 2167824 C2, 27.05.2001. RU Приоритет(ы): (22) Дата подачи заявки: 06.05.2016 127070 U1, 20.04.2013. EA 10012 B1, 30.06.2008. US 20090188846 A1, 30.07.2009. R U 19.12.2017 (43) Дата публикации заявки: 10.11.2017 Бюл. № 31 2 6 3 8 9 2 1 R U (54) СПОСОБ МАГНИТНОЙ АКТИВАЦИИ ЖИДКИХ ВЫСОКОМОЛЕКУЛЯРНЫХ УГЛЕВОДОРОДОВ И УСТРОЙСТВО ДЛЯ РЕАЛИЗАЦИИ СПОСОБА (57) Реферат: Описаны способ магнитной активации жидких металлические проводники, изолированные концы высокомолекулярных углеводородов, в котором которых выведены наружу трубы и через для создания магнитного поля в жидкости, управляемые коммутаторы подключены к протекающей по диамагнитной трубе, импульсным источникам электроэнергии. пропускают импульсы тока по ...

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Номер записи: 93
06-03-2013 дата публикации

Purification method of extra-heavy oil and Purification apparatus of extra-heavy oil

Номер: KR101239083B1
Автор: 김광호, 나정걸, 노남선, 신대현, 전상구, 정수현
Принадлежит: 한국에너지기술연구원

본 발명은 추출탑 내부에 고전압의 전기장을 인가하여 초중질원유 내 아스팔텐을 효과적으로 제거하는 초중질원유의 정제방법 및 정제장치에 관한 것으로, 더욱 상세하게는 탄소수 3~8개의 탄화수소로 구성된 용매와 초중질원유를 혼합하고 이에 고전압의 전기장을 인가하여 초중질원유 내의 아스팔텐 분산 특성을 변화시킴으로써 초중질원유의 응집을 유도하고 이와 동시에 용매와 초중질원유의 접촉을 원활히 하여 용매 추출 효과를 극대화한 다음, 전기장 인가를 중지하여 상부의 아스팔텐 제거 오일 층과 하부의 아스팔텐 층으로 분리시킴으로써 아스팔텐이 제거된 원유를 회수하는 방법 및 장치에 관한 것이다. 즉, 본 발명은 간단한 공정 구성과 온화한 조업 조건을 특징으로 하므로 기존의 탈아스팔텐 용매 추출 공정이 안고 있던 막대한 장치비 및 에너지 다소비 문제를 해결하여 초중질원유 고도화에 소요되는 설치, 운전 비용을 감소할 수 있는 것이다.

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Номер записи: 94
16-06-2015 дата публикации

Processes and systems for obtaining aromatics from catalytic cracking hydrocarbons

Номер: KR20150066586A
Автор: 마크 록하트, 미르체아 크레토이유, 웨이후아 진, 조셉 씨. 젠트리, 쫑이 딩, 칼람부르 쉬얌쿠마르, 핀티 왕
Принадлежит: 쥐티씨 테크놀로지 유에스,엘엘씨

촉매 분해 탄화수소, 구체적으로 C 4 스트림 및 C 5 + 스트림으로부터 파라자일렌을 제조하는 방법이 개시된다. 각 공정 과정은 상대적으로 저렴한 원료로부터 높은 파라자일렌 수율을 얻기 위한 목적에 전체적으로 잘 맞춰져 있다.

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Номер записи: 95
21-12-2021 дата публикации

Method for processing liquid hydrocarbonic paraffinic raw materials

Номер: RU2762549C1
Автор: Валерий Владимирович Хомяков, Максим Александрович Промтов
Принадлежит: Акционерное общество «ПлазмаТЭК технолоджи»

FIELD: liquid hydrocarbon processing. SUBSTANCE: invention relates to the field of preparation and primary processing of liquid hydrocarbon paraffinic raw materials. The invention relates to a method for processing liquid hydrocarbon paraffinic raw materials, including heating the raw material by mixing with a coolant or transferring heat through a separating baffle, hydrodynamic pulsation action, including cavitation action, the introduction of chemical reagents that activate the process of destruction of intermolecular and intramolecular bonds, separation of raw materials into a light low-boiling vapor-gas fraction and heavy liquid high-boiling fraction, their direction for further processing separately or in a mixture. Part of the light low-boiling steam-gas fraction is sent for mixing with the feedstock in the zones of hydrodynamic pulsation and cavitation treatment, where the flow of hydrocarbon paraffinic feedstock is subjected to at least two successive stages of hydrodynamic pulsation and cavitation effects, and substances are used as chemical reagents that in contact with each other react or decompose producing heat and gases. The heating of paraffinic hydrocarbon raw materials due to the heat of the coolant, hydrodynamic pulsation, cavitation effects and the heat of reactions of chemical substances is carried out to a temperature of no more than 90°С. EFFECT: reduction of capital and operating, including energy, costs, an increase in the content of light hydrocarbons in the initial hydrocarbon feedstock, an increase in the reliability and controllability of the process of destruction of hydrocarbon compounds, simplification of the hardware design of the process of preparation of hydrocarbon paraffinic feedstock (HPF) for deep processing. 5 cl, 2 ex, 4 tbl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 762 549 C1 (51) МПК C10G 15/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10G 15/08 (2021. ...

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Номер записи: 96
04-12-2020 дата публикации

Method of producing hydrocarbon fuel from coal

Номер: RU2737888C1
Автор: Евгений Петрович Яковенко
Принадлежит: Евгений Петрович Яковенко

Изобретение раскрывает способ получения углеводородного топлива из угля, включающий его предварительное мокрое измельчение, смешение измельченного угля с органическим растворителем, воздействие на полученную смесь путем гидродинамической кавитации, характеризующийся тем, что мокрое измельчение угля осуществляют до получения водоугольной пасты с плотностью до 1,3 кг/м 3 , которую затем перекачивают в емкость для смешивания с органическим растворителем и обрабатывают с помощью кавитационного гидроударного диспергатора, осуществляя гидроизмельчение угля до 0,003-0,01 мм и гомогенизацию водоугольной пасты и органического растворителя, процесс контролируют отбором проб и при достижении плотности полученной гомогенной пасты 0,99-1,1 г/см 3 ее направляют в накопительную емкость, а затем подают в верхнюю часть наклонного реактора для электроимпульсной обработки, после которой полученный продукт через нижнюю часть реактора направляют в накопительную емкость готового продукта для отстаивания. Технический результат заключается в упрощении технологического процесса получения углеводородного топлива, повышении выхода годного продукта, сокращении расхода органического растворителя и получении углеводородного топлива, по плотности соответствующего средней и тяжелой природной нефти. 4 з.п. ф-лы, 1 пр., 1 ил. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 737 888 C1 (51) МПК C10G 1/06 (2006.01) C10G 1/00 (2006.01) C10G 1/04 (2006.01) C10G 1/02 (2006.01) C10G 15/08 (2006.01) C10L 8/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10G 1/06 (2020.08); C10G 1/00 (2020.08); C10G 1/04 (2020.08); C10G 1/02 (2020.08); C10G 15/08 (2020.08); C10L 8/00 (2020.08) (21)(22) Заявка: 2020117246, 12.05.2020 12.05.2020 (73) Патентообладатель(и): Яковенко Евгений Петрович (RU) Дата регистрации: 04.12.2020 Приоритет(ы): (22) Дата подачи заявки: 12.05.2020 (45) Опубликовано: 04.12.2020 Бюл. № 34 2 7 3 7 8 8 8 R U (54) СПОСОБ ПОЛУЧЕНИЯ ...

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Номер записи: 97
21-11-2017 дата публикации

Conversion of heavy fossil hydrocarbons and modernization using radio frequency or microwave energy

Номер: RU2636151C2
Автор: Бенджамин К. РОБЕРТС, Джеймс А. ФРАНЦ, Джеймс Дж. СТРОМ, Джеффри У. ГРИФФИН, Джон К. ЛАЙНХЭН, Дуглас Л. МАКМЕЙКИН, Дэвид М. ШИН
Принадлежит: Баттелле Мемориал Инститьют

FIELD: oil and gas industry.SUBSTANCE: invention relates to a method for continuous instantaneous conversion of heavy fossil hydrocarbons (HFH) mixture, comprising one or more of bitumen, coal of any kind, oil sands, oil shales, oil resins, asphaltenes and predasphaltenes, as well as any other kerogen-containing materials. The method comprises: flowing a continuously fed stock, containing said HFH mixture and process gas through a reaction zone having more than 0.9 atmospheres pressure; dspersing said HFH mixture and the HFH distillation catalyst in the liquid in the process gas, and contacting said HFH mixture and catalyst at least in the reaction zone; concentrating microwave or radio frequency (RF) energy in the reaction zone using a microwave source or RF energy; and the generation of dielectric discharges in the reaction zone. In this case, said HFH mixture and the catalyst have stay period in the reaction zone less than 30 seconds. Also, the invention relates to two variants of continuous conversion system for HFH mixture.EFFECT: invention allows to reduce the environmental impact of heavy fossil hydrocarbons, and also allows conversion at lower temperature and pressure.30 cl, 16 tbl, 5 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 636 151 C2 (51) МПК C10G 15/08 (2006.01) C10G 1/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2014138093, 20.11.2012 (24) Дата начала отсчета срока действия патента: 20.11.2012 Дата регистрации: Приоритет(ы): (30) Конвенционный приоритет: 21.02.2012 US 13/401,216 (45) Опубликовано: 21.11.2017 Бюл. № 33 (56) Список документов, цитированных в отчете о поиске: EP 0601798 A1, 15.06.1994. US (85) Дата начала рассмотрения заявки PCT на национальной фазе: 22.09.2014 2004074759 A1, 22.04.2004. WO 0238523 A1, 16.05.2002. US 4279722 A, 21.07.1981. US 6171479 B1, 09.01.2001. US 6184427 B1, 06.02.2001. US 2007102279 A1, 10.05.2007. RU 2342997 C2, 10.01.2009. (86) Заявка PCT ...

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Номер записи: 98
10-10-2015 дата публикации

OIL WASTE PROCESSING METHOD

Номер: RU2014112447A
Автор: Алексей Сергеевич Градов, Евгений Сергеевич Сусеков
Принадлежит: Алексей Сергеевич Градов, Евгений Сергеевич Сусеков, Общество С Ограниченной Ответственностью &#34;Научно-Производственное Объединение Инноватех&#34;

1. Способ переработки нефтяных отходов, включающий подачу отходов в реактор, обогрев реактора высокотемпературными дымовыми газами, подачу перегретого водяного пара в реактор, отделение горючего газа от жидких углеводородов и пара путем охлаждения в теплообменнике, разделение жидких углеводородов и воды, использование горючего газа и жидких углеводородов для производства высокотемпературных дымовых газов, вывод из реактора твердого остатка, отличающийся тем, что производство высокотемпературных дымовых газов осуществляют путем совместного сжигания горючих газов, жидких углеводородов и воды, при этом подачу водяного пара в реактор осуществляют в смеси с высокотемпературными дымовыми газами при массовом соотношении 1:(0,1÷0,5), в теплообменнике горючие газы, жидкие углеводороды и водяной пар охлаждают до температуры 20÷100°C путем теплообмена с теплоносителем, который далее используют для сушки исходных отходов, причем жидкие углеводороды отделяют от воды частично и устанавливают массовое соотношение жидких углеводородов и воды в смеси в пределах 1:(0,1÷4,0).2. Способ переработки нефтяных отходов по п.1, отличающийся тем, что твердый остаток выводят из реактора при температуре 400÷600°C и подают в газогенератор, в котором получают генераторный газ, сжигают данный газ, а продукты сгорания используют для обогрева реактора.3. Способ переработки нефтяных отходов по пп.1 и 2, отличающийся тем, что смесь воды и жидких углеводородов подвергают кавитационному воздействию путем наложения ультразвука с частотой в пределах 20÷200 кГц и интенсивностью колебаний 1,0÷5,0 Вт/см. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2014 112 447 (13) A (51) МПК C10G 9/00 (2006.01) C10G 99/00 (2006.01) F23G 5/027 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (71) Заявитель(и): Общество с ограниченной Приоритет(ы): ответственностью "Научно(22) Дата подачи заявки: 31.03.2014 производственное объединение Инноватех" (RU), (43) Дата публикации заявки: 10.10.2015 Бюл ...

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15-05-2018 дата публикации

Patent RU2016144083A3

Номер: RU2016144083A3
Автор: [UNK]
Принадлежит: [UNK]

РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2016 144 083 A (51) МПК F02M 27/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2016144083, 11.04.2014 (71) Заявитель(и): ЭРИЙЛЬМАЗ Ченгиз (TR) Приоритет(ы): (30) Конвенционный приоритет: 09.04.2014 TR 2014 - G - 127798 PT 2014/04119 (72) Автор(ы): ЭРИЙЛЬМАЗ Ченгиз (TR) (85) Дата начала рассмотрения заявки PCT на национальной фазе: 09.11.2016 R U (43) Дата публикации заявки: 15.05.2018 Бюл. № 14 (86) Заявка PCT: (87) Публикация заявки PCT: WO 2015/156745 (15.10.2015) R U (54) БОЛЕЕ ЭФФЕКТИВНАЯ ОБРАБОТКА ЖИДКИХ И ГАЗООБРАЗНЫХ ВЕЩЕСТВ, СОДЕРЖАЩИХ ВОДОРОД И УГЛЕВОДОРОДЫ, ЗА СЧЕТ МАКСИМАЛЬНО УВЕЛИЧЕННОГО ДОСТАТОЧНОГО МАГНИТНОГО ВОЗДЕЙСТВИЯ, СОЗДАВАЕМОГО УСОВЕРШЕНСТВОВАННЫМ УСТРОЙСТВОМ НОВОГО ПОКОЛЕНИЯ (57) Формула изобретения 1. Упрощенное устройство нового поколения, отличающееся, в общем, наличием немагнитного цилиндрического наполненного латунью наружного цельного корпуса, который, в общем, состоит из 3 основных частей, в котором одна из основных частей, представляющая собой немагнитный цилиндрический наполненный латунью наружный полукорпус, имеет полную наружную длину, равную 183 мм (17, 18) и наружный ∅42 мм (9, 16), и состоит из 3 секций разного размера, где обычно первая секция основной части, образующая полностью закрытую сторону немагнитного цилиндрического наполненного латунью наружного корпуса (1), имеет сопло (6) (наружный ∅12 мм и внутренний ∅8 мм и длина 30 мм), используемое как выпускное отверстие (7), через которое жидкие и газообразные вещества, состоящие из водорода и углеводородов, такие как вода, и более конкретно, жидкие и газообразные углеводородные топлива, такие как бензин, бензоспирт, дизельное топливо, керосин, пропан, природный газ, масло, выходят из упрощенного устройства нового поколения, и вторая секция основной части, которая образует внутреннее цилиндрическое открытое ложе (3), имеет (наружный ∅42 мм и внутренний ∅31 мм и длину 148 мм) ( ...

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