RU2015109699A - Способ и установка для получения жидкого топлива и выработки энергии - Google Patents
Способ и установка для получения жидкого топлива и выработки энергии Download PDFInfo
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Abstract
1. Способ получения жидкого топлива из углеводородного газа и выработки энергии, в котором:осуществляют риформинг углеводородного газа для получения газа риформинга путем реакции парового риформинга углеводородного газа;осуществляют синтез бензина, диметилового эфира, или дизельного топлива из газа риформинга через метанол;извлекают тепло термической энергии газа риформинга для получения насыщенного водяного пара, имеющего температуру не более 180°C, до использования указанного газа риформинга на стадии синтеза;осуществляют перегревание указанного насыщенного водяного пара с использованием теплового источника, имеющего температуру по меньшей мере 200°C, образовавшегося в указанном способе, чтобы получить перегретый водяной пар; иосуществляют выработку энергии с использованием указанного перегретого водяного пара.2. Способ по п. 1, в котором в качестве теплового источника для перегревания на стадии перегревания используют водяной пар, образовавшийся за счет экзотермической реакции на стадии синтеза.3. Способ по п. 1, в котором в качестве теплового источника для перегревания на стадии перегревания используют часть газа риформинга, полученного на стадии риформинга.4. Способ по п. 1, в котором в качестве теплового источника для перегревания на стадии перегревания используют дымовой газ, образовавшийся на стадии риформинга.5. Установка для получения жидкого топлива из углеводородного газа и для выработки энергии, содержащая:устройство парового риформинга для получения газа риформинга путем реакции риформинга углеводородного газа;колонну синтеза для получения бензина, диметилового эфира, или дизельного топлива из газа
Claims (8)
1. Способ получения жидкого топлива из углеводородного газа и выработки энергии, в котором:
осуществляют риформинг углеводородного газа для получения газа риформинга путем реакции парового риформинга углеводородного газа;
осуществляют синтез бензина, диметилового эфира, или дизельного топлива из газа риформинга через метанол;
извлекают тепло термической энергии газа риформинга для получения насыщенного водяного пара, имеющего температуру не более 180°C, до использования указанного газа риформинга на стадии синтеза;
осуществляют перегревание указанного насыщенного водяного пара с использованием теплового источника, имеющего температуру по меньшей мере 200°C, образовавшегося в указанном способе, чтобы получить перегретый водяной пар; и
осуществляют выработку энергии с использованием указанного перегретого водяного пара.
2. Способ по п. 1, в котором в качестве теплового источника для перегревания на стадии перегревания используют водяной пар, образовавшийся за счет экзотермической реакции на стадии синтеза.
3. Способ по п. 1, в котором в качестве теплового источника для перегревания на стадии перегревания используют часть газа риформинга, полученного на стадии риформинга.
4. Способ по п. 1, в котором в качестве теплового источника для перегревания на стадии перегревания используют дымовой газ, образовавшийся на стадии риформинга.
5. Установка для получения жидкого топлива из углеводородного газа и для выработки энергии, содержащая:
устройство парового риформинга для получения газа риформинга путем реакции риформинга углеводородного газа;
колонну синтеза для получения бензина, диметилового эфира, или дизельного топлива из газа риформинга через метанол;
устройство теплообмена для получения насыщенного водяного пара, имеющего температуру не более 180°C, за счет теплообмена газа риформинга до введения указанного газа риформинга в колонну синтеза;
устройство перегревания для перегревания насыщенного водяного пара с использованием теплового источника, имеющего температуру по меньшей мере 200°C, образовавшегося внутри указанной установки, чтобы получить перегретый водяной пар; и
устройство выработки энергии для генерации энергии с использованием указанного перегретого водяного пара.
6. Установка по п. 5, в которой тепловой источник, используемый в устройстве перегревания, представляет собой водяной пар, образовавшийся за счет экзотермической реакции в колонне синтеза.
7. Установка по п. 5, в которой тепловой источник, используемый в устройстве перегревания, представляет собой часть газа риформинга, полученного с помощью устройства парового риформинга.
8. Установка по п. 5, в которой тепловой источник, используемый в устройстве перегревания, представляет собой дымовой газ, образовавшийся в устройстве парового риформинга.
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| JP2012-208105 | 2012-09-21 | ||
| JP2012208105A JP6057643B2 (ja) | 2012-09-21 | 2012-09-21 | 液体燃料を製造するとともに発電する方法およびシステム |
| PCT/JP2013/073810 WO2014045871A1 (ja) | 2012-09-21 | 2013-09-04 | 液体燃料を製造するとともに発電する方法およびシステム |
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| WO2018004994A1 (en) | 2016-07-01 | 2018-01-04 | Res Usa, Llc | Fluidized bed membrane reactor |
| CN108825364B (zh) * | 2018-06-22 | 2021-05-04 | 中船动力有限公司 | 天然气发电机组余热及二氧化碳利用装置 |
| US11885266B2 (en) | 2021-04-14 | 2024-01-30 | J Ray Mcdermott S.A. | Steam cycle methods, systems, and apparatus for efficiently reducing carbon footprints in plant systems |
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| DE2846693C2 (de) | 1978-10-26 | 1987-03-26 | Metallgesellschaft Ag, 6000 Frankfurt | Verfahren zur Erzeugung von Benzin aus Synthesegas |
| JPS5714685A (en) | 1980-06-30 | 1982-01-25 | Mitsubishi Heavy Ind Ltd | Recovering method for heat of reaction |
| JPH08312310A (ja) * | 1995-05-19 | 1996-11-26 | Hitachi Ltd | 廃棄物発電システム |
| JP3366807B2 (ja) * | 1996-07-11 | 2003-01-14 | 株式会社日立製作所 | 廃棄物焼却システム及びその運転・制御方法 |
| JPH11257093A (ja) * | 1998-03-06 | 1999-09-21 | Hitachi Ltd | 発電プラント及びその運用方法 |
| JPH11257094A (ja) * | 1998-03-16 | 1999-09-21 | Electric Power Dev Co Ltd | 石炭ガス化発電システム |
| JP2000054852A (ja) | 1998-06-05 | 2000-02-22 | Nippon Steel Corp | ガスタ―ビン複合サイクル発電システム |
| JP4533515B2 (ja) * | 2000-08-16 | 2010-09-01 | 三菱重工業株式会社 | 合成ガスの製造方法 |
| MY128179A (en) | 2001-10-05 | 2007-01-31 | Shell Int Research | System for power generation in a process producing hydrocarbons |
| GB0200891D0 (en) | 2002-01-16 | 2002-03-06 | Ici Plc | Hydrocarbons |
| GB0405786D0 (en) * | 2004-03-16 | 2004-04-21 | Accentus Plc | Processing natural gas to form longer-chain hydrocarbons |
| JP4981439B2 (ja) * | 2006-12-28 | 2012-07-18 | 三菱重工業株式会社 | 固体燃料ガス化ガス利用プラント |
| US20090084035A1 (en) * | 2007-09-28 | 2009-04-02 | General Electric Company | Polygeneration systems |
| JP4823297B2 (ja) * | 2008-11-26 | 2011-11-24 | 三菱重工業株式会社 | スチームシステム及びその制御方法 |
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| CA2884175C (en) | 2017-04-04 |
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| AU2013319303A1 (en) | 2015-03-26 |
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