RU2008147909A - Улучшенный способ конверсии материала углеродного энергоносителя - Google Patents
Улучшенный способ конверсии материала углеродного энергоносителя Download PDFInfo
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- RU2008147909A RU2008147909A RU2008147909/04A RU2008147909A RU2008147909A RU 2008147909 A RU2008147909 A RU 2008147909A RU 2008147909/04 A RU2008147909/04 A RU 2008147909/04A RU 2008147909 A RU2008147909 A RU 2008147909A RU 2008147909 A RU2008147909 A RU 2008147909A
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- reaction products
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- carbon
- reactive gas
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Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/08—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
- C10G1/086—Characterised by the catalyst used
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/16—Clays or other mineral silicates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/16—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form
- C10B49/20—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form in dispersed form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/08—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Dispersion Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1. Способ конверсии твердого или высоковязкого материала углеродного энергоносителя в жидкие и газообразные продукты реакции, включающий стадии ! а) приведение в контакт материала углеродного энергоносителя с материалом катализатора в виде частиц; ! b) конверсия материала углеродного энергоносителя при температуре реакции 200 - 450°С, с образованием газообразных продуктов реакции; ! c) отделение газообразных продуктов реакции от материала катализатора в виде частиц в течение 10 с после образования указанных продуктов реакции; ! d) необязательно быстрое охлаждение продуктов реакции до температуры ниже 200°С. ! 2. Способ по п.1, включающий дополнительную стадию отделения продуктов реакции от материала катализатора в виде частиц. ! 3. Способ по п.1 или 2, включающий дополнительную стадию отжига нагара, образовавшегося на материале катализатора в виде частиц. ! 4. Способ по п.2, включающий дополнительную стадию рециркуляции материала катализатора в виде частиц на стадии а) или b). ! 5. Способ по п.1, при котором реакционноспособный газ присутствует на стадии b). ! 6. Способ по п.5, в котором реакционноспособный газ имеет окислительные или восстановительные свойства. ! 7. Способ по п.5, в котором реакционноспособный газ является активным в реакциях изомеризации или алкилирования. ! 8. Способ по п.6, в котором реакционноспособный газ включает кислород, водород, сероводород или монооксид углерода. ! 9. Способ по п.7, в котором реакционноспособный газ включает изобутан, нафтен или летучую органическую кислоту. ! 10. Способ по п.1, в котором каталитический материал включает катионные глины, анионные глины, природные глины, гидроталькитоподо�
Claims (29)
1. Способ конверсии твердого или высоковязкого материала углеродного энергоносителя в жидкие и газообразные продукты реакции, включающий стадии
а) приведение в контакт материала углеродного энергоносителя с материалом катализатора в виде частиц;
b) конверсия материала углеродного энергоносителя при температуре реакции 200 - 450°С, с образованием газообразных продуктов реакции;
c) отделение газообразных продуктов реакции от материала катализатора в виде частиц в течение 10 с после образования указанных продуктов реакции;
d) необязательно быстрое охлаждение продуктов реакции до температуры ниже 200°С.
2. Способ по п.1, включающий дополнительную стадию отделения продуктов реакции от материала катализатора в виде частиц.
3. Способ по п.1 или 2, включающий дополнительную стадию отжига нагара, образовавшегося на материале катализатора в виде частиц.
4. Способ по п.2, включающий дополнительную стадию рециркуляции материала катализатора в виде частиц на стадии а) или b).
5. Способ по п.1, при котором реакционноспособный газ присутствует на стадии b).
6. Способ по п.5, в котором реакционноспособный газ имеет окислительные или восстановительные свойства.
7. Способ по п.5, в котором реакционноспособный газ является активным в реакциях изомеризации или алкилирования.
8. Способ по п.6, в котором реакционноспособный газ включает кислород, водород, сероводород или монооксид углерода.
9. Способ по п.7, в котором реакционноспособный газ включает изобутан, нафтен или летучую органическую кислоту.
10. Способ по п.1, в котором каталитический материал включает катионные глины, анионные глины, природные глины, гидроталькитоподобные материалы, слоистые материалы, руды, минералы, оксиды металлов, гидроксиды и карбонаты щелочных или щелочноземельных металлов или их смеси.
11. Способ по п.1, в котором материал энергоносителя имеет ископаемое происхождение.
12. Способ по п.11, в котором материал углеродного энергоносителя является смолой, тяжелой нефтью или битумом.
13. Способ по п.1, в котором материалом углеродного энергоносителя является синтетический полимер.
14. Способ по п.1, в котором материал углеродного энергоносителя является твердой биомассой.
15. Способ по п.14, в котором твердая биомасса включает целлюлозу, лигнин или лигниноцеллюлозу.
16. Способ по п.14, в котором твердая биомасса имеет водное происхождение.
17. Способ по п.14, при котором для производства биомассы используют CO2.
18. Способ по п.16, при котором для производства водной биомассы используют CO2.
19. Способ по п.1, в котором стадия а) включает перемалывание материала углеродного энергоносителя в присутствии материала катализатора в виде частиц.
20. Способ по п.1, в котором стадия а) включает стадии
(i) помещение материала катализатора в виде частиц в поток газа-носителя;
(ii) приведение потока газа в движение таким образом, что материал катализатора в виде частиц достигает скорости, по меньшей мере, 1 м/с, предпочтительно, по меньшей мере 10 м/с
(iii) столкновение частиц катализатора с материалом углеродного энергоносителя.
21. Способ по п.17, в котором газ-носитель дополнительно содержит инертный материал в виде частиц.
22. Способ по п.17 или 18, в котором стадию а) выполняют в реакторе с псевдоожиженным слоем, реакторе с восходящим или нисходящим потоком.
23. Способ по п.1, в котором температура реакции на стадии b) составляет менее 350°С, предпочтительно менее 300°С, более предпочтительно менее 250°С.
24. Способ по п.1, в котором газообразные продукты реакции включают пар, углеводороды или их смесь.
25. Способ по п.3, в котором нагар отжигают при помощи воздуха.
26. Способ по п.3, включающий дополнительную стадию охлаждения материала катализатора в виде частиц после отжига нагара.
27. Способ по п.23, в котором тепло, полученное от материала катализатора в виде частиц, используют для получения пара, горячей воды или электричества.
28. Способ по п.1, в котором, по меньшей мере, стадию b) выполняют в ФКК устройстве.
29. Способ по п.1, в котором, по меньшей мере, стадию b) выполняют в реакторе с нисходящим потоком.
Applications Claiming Priority (11)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP06113545A EP1852490A1 (en) | 2006-05-05 | 2006-05-05 | Pretreatment of particulate carbon-based energy carrier material |
EP06113567.9 | 2006-05-05 | ||
EP06113567A EP1852491A1 (en) | 2006-05-05 | 2006-05-05 | Mild pyrolysis of carbon-based energy carrier material |
EP06113545.5 | 2006-05-05 | ||
US83122006P | 2006-07-17 | 2006-07-17 | |
US60/831,220 | 2006-07-17 | ||
EP07102737A EP1970425A1 (en) | 2007-02-20 | 2007-02-20 | Improved process for converting carbon-based energy carrier material |
EP07102737.9 | 2007-02-20 | ||
PCT/EP2007/054375 WO2007128798A1 (en) | 2006-05-05 | 2007-05-04 | Improved process for converting carbon-based energy carrier material |
US29931908A | 2008-11-03 | 2008-11-03 | |
US13/008,430 US8460541B2 (en) | 2006-05-05 | 2011-01-18 | Process for converting carbon-based energy carrier material |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2008147909A true RU2008147909A (ru) | 2010-06-10 |
RU2437917C2 RU2437917C2 (ru) | 2011-12-27 |
Family
ID=38283284
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2008147909/04A RU2437917C2 (ru) | 2006-05-05 | 2007-05-04 | Улучшенный способ конверсии материала углеродного энергоносителя |
Country Status (9)
Country | Link |
---|---|
US (3) | US7901568B2 (ru) |
EP (1) | EP2032675B1 (ru) |
JP (1) | JP2009536235A (ru) |
KR (1) | KR20090013818A (ru) |
BR (1) | BRPI0711564A2 (ru) |
CA (1) | CA2651463C (ru) |
MX (1) | MX2008014179A (ru) |
RU (1) | RU2437917C2 (ru) |
WO (1) | WO2007128798A1 (ru) |
Cited By (1)
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RU2741006C1 (ru) * | 2020-06-17 | 2021-01-22 | Федеральное государственное автономное образовательное учреждение высшего образования "Национальный исследовательский технологический университет "МИСиС" | Способ получения монооксида углерода из лигнина гидролизного под действием CO2 |
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US8460541B2 (en) | 2013-06-11 |
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CA2651463A1 (en) | 2007-11-15 |
EP2032675B1 (en) | 2018-02-28 |
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