RU2017145757A - METHOD OF OBTAINING SYNTHETIC LIQUID HYDROCARBON - Google Patents

METHOD OF OBTAINING SYNTHETIC LIQUID HYDROCARBON Download PDF

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Publication number
RU2017145757A
RU2017145757A RU2017145757A RU2017145757A RU2017145757A RU 2017145757 A RU2017145757 A RU 2017145757A RU 2017145757 A RU2017145757 A RU 2017145757A RU 2017145757 A RU2017145757 A RU 2017145757A RU 2017145757 A RU2017145757 A RU 2017145757A
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RU
Russia
Prior art keywords
liquid hydrocarbon
production
fuel
synthetic liquid
cavitator
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RU2017145757A
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Russian (ru)
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RU2017145757A3 (en
Inventor
Алексей Сергеевич Архипов
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Алексей Сергеевич Архипов
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Priority to RU2017145757A priority Critical patent/RU2017145757A/en
Publication of RU2017145757A3 publication Critical patent/RU2017145757A3/ru
Publication of RU2017145757A publication Critical patent/RU2017145757A/en

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Claims (4)

1. Способ получения синтетического жидкого углеводорода, включающий реакцию гидрополимеризации СОх, отличающийся тем, что СОх в газообразном либо в жидком виде, образующуюся при: генерации тепла и/или электроэнергии от сжигания углеводородного ископаемого топлива или твердых бытовых отходов; производстве цветных (алюминия) и черных металлов; работе двигателя внутреннего сгорания (ДВС); очистке природного метана или попутного нефтяного газа; производстве извести и цемента; производстве биогаза; переработке свалочного газа, вводят в зону кавитации воды, имеющей рН=7,5…10,5 ед., при этом температура смеси газов и воды, циркулирующей через проточное гидродинамическое кавитационное устройство, выполненное в виде насоса-кавитатора, составляет не более +50°С, непрореагировавшую СОх повторно подают в насос-кавитатор, а после реакции гидрополимеризации СОх, смесь разделяют, выделяя синтетический жидкий углеводород.1. A method of producing a synthetic liquid hydrocarbon, comprising the reaction of hydropolymerizing CO x , characterized in that the CO x in gaseous or liquid form, formed during: the generation of heat and / or electricity from the combustion of fossil hydrocarbon fuel or solid household waste; production of non-ferrous (aluminum) and ferrous metals; operation of the internal combustion engine (ICE); purification of natural methane or associated petroleum gas; lime and cement production; biogas production; processing of landfill gas is injected into the zone of cavitation of water having a pH = 7.5 ... 10.5 units, while the temperature of the mixture of gases and water circulating through a flow hydrodynamic cavitation device, made in the form of a pump cavitator, is no more than +50 ° C, unreacted CO x re-fed into the pump-cavitator, and after the reaction of hydropolymerization CO x , the mixture is separated, releasing a synthetic liquid hydrocarbon. 2. Способ по п. 1, отличающийся тем, что синтезированный жидкий углеводород используют в качестве энергетического рециклового топлива на объекте - источнике СОх или на отдельном, энергогенерирующем объекте.2. The method according to p. 1, characterized in that the synthesized liquid hydrocarbon is used as an energy recycle fuel at the facility - the source of CO x or on a separate, power generating facility. 3. Способ по п. 1, отличающийся тем, что синтезированный жидкий углеводород фракционируют, с получением моторного топлива : бензина и дизельного топлива.3. The method according to p. 1, characterized in that the synthesized liquid hydrocarbon is fractionated, with the production of motor fuel: gasoline and diesel fuel. 4. Способ по пп. 1, 2, 3, отличающийся тем, что его осуществляют по периодической либо по непрерывной схеме.4. The method according to paragraphs. 1, 2, 3, characterized in that it is carried out according to a periodic or continuous scheme.
RU2017145757A 2017-12-25 2017-12-25 METHOD OF OBTAINING SYNTHETIC LIQUID HYDROCARBON RU2017145757A (en)

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RU2017145757A RU2017145757A (en) 2017-12-25 2017-12-25 METHOD OF OBTAINING SYNTHETIC LIQUID HYDROCARBON

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Application Number Priority Date Filing Date Title
RU2017145757A RU2017145757A (en) 2017-12-25 2017-12-25 METHOD OF OBTAINING SYNTHETIC LIQUID HYDROCARBON

Publications (2)

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RU2017145757A3 RU2017145757A3 (en) 2019-06-25
RU2017145757A true RU2017145757A (en) 2019-06-25

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RU2017145757A3 (en) 2019-06-25

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