BR9809353A - Processo de sìntese de hidrocarboneto em pasta fluida - Google Patents
Processo de sìntese de hidrocarboneto em pasta fluidaInfo
- Publication number
- BR9809353A BR9809353A BR9809353-3A BR9809353A BR9809353A BR 9809353 A BR9809353 A BR 9809353A BR 9809353 A BR9809353 A BR 9809353A BR 9809353 A BR9809353 A BR 9809353A
- Authority
- BR
- Brazil
- Prior art keywords
- slurry
- gas
- hydrocarbon synthesis
- catalyst
- fluid paste
- Prior art date
Links
Classifications
-
- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
-
- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
- C10G2/34—Apparatus, reactors
- C10G2/342—Apparatus, reactors with moving solid catalysts
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/006—Separating solid material from the gas/liquid stream by filtration
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
- B01J8/224—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
- B01J8/228—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement externally, i.e. the particles leaving the vessel and subsequently re-entering it
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Catalysts (AREA)
Abstract
''PROCESSO DE SìNTESE DE HIDROCARBONETO EM PASTA FLUIDA'' Um catalisador de síntese de hidrocarboneto reversivelmente desativado em uma pasta fluida de síntese de hidrocarboneto é rejuvenescido pela passagem da pasta fluida dentro de um tubo de elevação externamente ao reator no qual ela contata um gás de rejuvenescimento que contém hidrogênio. O hidrogênio rejuvenesce as partículas do catalisador na pasta fluida e forma uma mistura de um gás de saída de rejuvenescimento o qual pode conter as espécies desativadoras do catalisador e uma pasta fluida do catalisador rejuvenescido. Essa mistura é passada dentro de um vaso de separação e remoção de gás no qual o gás de saída é separado e removido da pasta fluida, a qual é então retornada de volta para dentro do reator ou para um outro lugar. O gás rejuvenescedor também atua como um gás de elevação para criar uma circulação de pasta fluida de modo ascendente através do tubo de elevação e dentro do vaso de remoção de gás.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/850,357 US5958986A (en) | 1997-05-02 | 1997-05-02 | Slurry hydrocarbon synthesis process with catalyst rejuvenation in external lift pipe (law544) |
PCT/US1998/008789 WO1998050490A1 (en) | 1997-05-02 | 1998-04-29 | Slurry hydrocarbon synthesis process with catalyst rejuvenation in external lift pipe |
Publications (1)
Publication Number | Publication Date |
---|---|
BR9809353A true BR9809353A (pt) | 2000-07-04 |
Family
ID=25307910
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR9809353-3A BR9809353A (pt) | 1997-05-02 | 1998-04-29 | Processo de sìntese de hidrocarboneto em pasta fluida |
Country Status (12)
Country | Link |
---|---|
US (1) | US5958986A (pt) |
EP (1) | EP1015528B1 (pt) |
JP (1) | JP2002512651A (pt) |
KR (1) | KR20010020437A (pt) |
AU (1) | AU721351B2 (pt) |
BR (1) | BR9809353A (pt) |
CA (1) | CA2288173A1 (pt) |
DE (1) | DE69807507T2 (pt) |
MY (1) | MY132796A (pt) |
TW (1) | TW474838B (pt) |
WO (1) | WO1998050490A1 (pt) |
ZA (1) | ZA983687B (pt) |
Families Citing this family (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100241083B1 (ko) * | 1996-04-19 | 2000-02-01 | 야마오카 요지로 | 디메틸에테르 제조용 촉매와 그 제조방법 및 디메틸에테르의 제조방법 |
US6147125A (en) * | 1996-05-13 | 2000-11-14 | Nkk Corporation | Method and apparatus for producing dimethyl ether |
US6800665B1 (en) * | 1996-05-13 | 2004-10-05 | Jfe Holdings, Inc. | Method for producing dimethyl ether |
US6486220B1 (en) | 1999-11-17 | 2002-11-26 | Conoco Inc. | Regeneration procedure for Fischer-Tropsch catalyst |
US6869978B2 (en) | 1999-11-17 | 2005-03-22 | Conocophillips Company | Pressure swing catalyst regeneration procedure for Fischer-Tropsch catalyst |
US6323248B1 (en) | 2000-06-02 | 2001-11-27 | Exxonmobil Research And Engineering Company | Slurry hydrocarbon synthesis with fresh catalyst activity increase during hydrocarbon production |
US6696502B1 (en) | 2000-06-02 | 2004-02-24 | Exxonmobil Research And Engineering Company | Slurry hydrocarbon synthesis with fresh catalyst activity increase during hydrocarbon production |
CN1223555C (zh) * | 2001-07-13 | 2005-10-19 | 埃克森美孚研究工程公司 | 直接生产高纯度的费-托蜡 |
US6590002B2 (en) * | 2001-07-13 | 2003-07-08 | Exxonmobil Research And Engineering Company | Temperature controlled in situ wax purification |
US6649803B2 (en) * | 2001-11-06 | 2003-11-18 | Exxonmobil Research And Engineering Company | Slurry hydrocarbon synthesis with isomerization zone in external lift reactor loop |
US6900151B2 (en) * | 2001-11-13 | 2005-05-31 | Exxonmobil Research And Engineering Company | In situ catalyst regeneration/activation process |
US6774148B2 (en) * | 2002-06-25 | 2004-08-10 | Chevron U.S.A. Inc. | Process for conversion of LPG and CH4 to syngas and higher valued products |
WO2004026796A2 (en) * | 2002-09-20 | 2004-04-01 | Conocophillips Company | Slurry activation of fischer-tropsch catalyst with carbon monoxide co-feed |
US7045554B2 (en) * | 2003-09-03 | 2006-05-16 | Conocophillips Company | Method for improved Fischer-Tropsch catalyst stability and higher stable syngas conversion |
US20050154069A1 (en) * | 2004-01-13 | 2005-07-14 | Syntroleum Corporation | Fischer-Tropsch process in the presence of nitrogen contaminants |
US20070155987A1 (en) * | 2006-01-04 | 2007-07-05 | O'meadhra Ruairi S | Oxidative digestion with optimized agitation |
US7816556B2 (en) * | 2006-03-01 | 2010-10-19 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced multistage oxidative digestion |
US20070208194A1 (en) * | 2006-03-01 | 2007-09-06 | Woodruff Thomas E | Oxidation system with sidedraw secondary reactor |
US7772424B2 (en) * | 2006-03-01 | 2010-08-10 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion |
US7501537B2 (en) * | 2006-03-01 | 2009-03-10 | Eastman Chemical Company | Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange |
JP4808688B2 (ja) * | 2006-08-25 | 2011-11-02 | 新日本製鐵株式会社 | 合成ガスから炭化水素を製造する触媒、触媒の製造方法、触媒の再生方法、及び合成ガスから炭化水素を製造する方法 |
KR101430775B1 (ko) | 2006-08-25 | 2014-08-18 | 신닛떼쯔 수미킨 엔지니어링 가부시끼가이샤 | 합성 가스로부터 탄화 수소를 제조하는 촉매, 촉매의 제조 방법, 촉매의 재생 방법 및 합성 가스로부터 탄화 수소를 제조하는 방법 |
US20080260631A1 (en) | 2007-04-18 | 2008-10-23 | H2Gen Innovations, Inc. | Hydrogen production process |
KR101932328B1 (ko) * | 2016-12-29 | 2018-12-26 | 효성화학 주식회사 | 탈수소 반응 촉매재생장치 |
CN110124753B (zh) * | 2019-06-10 | 2022-05-24 | 新疆中泰化学阜康能源有限公司 | 低汞触媒在线活化再生方法及装置 |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5283216A (en) * | 1992-09-24 | 1994-02-01 | Exxon Research And Engineering Company | Rejuvenation of hydrocarbon synthesis catalyst |
US5382748A (en) * | 1992-12-18 | 1995-01-17 | Exxon Research & Engineering Co. | Hydrocarbon synthesis reactor employing vertical downcomer with gas disengaging means |
US5268344A (en) * | 1992-12-18 | 1993-12-07 | Exxon Research & Engineering Company | Draft tube for catalyst rejuvenation and distribution |
US5260239A (en) * | 1992-12-18 | 1993-11-09 | Exxon Research & Engineering Company | External catalyst rejuvenation system for the hydrocarbon synthesis process |
US5821270A (en) * | 1997-05-02 | 1998-10-13 | Exxon Research And Engineering Company | Slurry hydrocarbon synthesis process with multistage catalyst rejuvenation |
-
1997
- 1997-05-02 US US08/850,357 patent/US5958986A/en not_active Expired - Fee Related
-
1998
- 1998-04-23 MY MYPI98001809A patent/MY132796A/en unknown
- 1998-04-29 AU AU72720/98A patent/AU721351B2/en not_active Ceased
- 1998-04-29 WO PCT/US1998/008789 patent/WO1998050490A1/en not_active Application Discontinuation
- 1998-04-29 EP EP98920072A patent/EP1015528B1/en not_active Expired - Lifetime
- 1998-04-29 BR BR9809353-3A patent/BR9809353A/pt not_active IP Right Cessation
- 1998-04-29 CA CA002288173A patent/CA2288173A1/en not_active Abandoned
- 1998-04-29 DE DE69807507T patent/DE69807507T2/de not_active Expired - Fee Related
- 1998-04-29 JP JP54822198A patent/JP2002512651A/ja active Pending
- 1998-04-29 KR KR1019997010068A patent/KR20010020437A/ko not_active Application Discontinuation
- 1998-04-30 ZA ZA983687A patent/ZA983687B/xx unknown
- 1998-08-24 TW TW087106816A patent/TW474838B/zh not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
DE69807507D1 (de) | 2002-10-02 |
ZA983687B (en) | 1998-11-06 |
AU721351B2 (en) | 2000-06-29 |
EP1015528A1 (en) | 2000-07-05 |
US5958986A (en) | 1999-09-28 |
AU7272098A (en) | 1998-11-27 |
KR20010020437A (ko) | 2001-03-15 |
TW474838B (en) | 2002-02-01 |
CA2288173A1 (en) | 1998-11-12 |
DE69807507T2 (de) | 2003-01-16 |
MY132796A (en) | 2007-10-31 |
WO1998050490A1 (en) | 1998-11-12 |
EP1015528B1 (en) | 2002-08-28 |
JP2002512651A (ja) | 2002-04-23 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
B08F | Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette] |
Free format text: REFERENTE A 7A E 8A ANUIDADES. |
|
B08K | Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette] |
Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 1892 DE 10/04/2007. |