BR9904084A - Reator de dois estágios para sistema de hidrogenação de lamas em três fases contìnuas e processo de funcionamento - Google Patents

Reator de dois estágios para sistema de hidrogenação de lamas em três fases contìnuas e processo de funcionamento

Info

Publication number
BR9904084A
BR9904084A BR9904084-0A BR9904084A BR9904084A BR 9904084 A BR9904084 A BR 9904084A BR 9904084 A BR9904084 A BR 9904084A BR 9904084 A BR9904084 A BR 9904084A
Authority
BR
Brazil
Prior art keywords
sludge
operating process
stage reactor
continuous phases
hydrogenation system
Prior art date
Application number
BR9904084-0A
Other languages
English (en)
Inventor
Reinaldo Mario Machado
Original Assignee
Air Prod & Chem
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Air Prod & Chem filed Critical Air Prod & Chem
Publication of BR9904084A publication Critical patent/BR9904084A/pt

Links

Classifications

    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • 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
    • B01J8/222—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 in the presence of a rotating device only
    • 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
    • B01J8/18—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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

REATOR DE DOIS ESTáGIOS PARA SISTEMA DE HIDROGENAçãO DE LAMAS EM TRêS FASES CONTìNUAS E PROCESSO DE FUNCIONAMENTO. Um reator de tanque de agitação contínua é emparelhado com um reator de coluna de bolhas para aumentar a conversão em um processo contínuo, e.g. hidrogenação, no qual um reagente gasoso é mistuado com um líquido. O reator de agitação contínua é equipado com um sistema de impulsor especializado para circular líquido e aumentar o contato do líquido com o gás reagente trazido da coluna de bolhas.
BR9904084-0A 1998-09-11 1999-09-08 Reator de dois estágios para sistema de hidrogenação de lamas em três fases contìnuas e processo de funcionamento BR9904084A (pt)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US09/151,625 US6080372A (en) 1998-09-11 1998-09-11 Two stage reactor for continuous three phase slurry hydrogenation and method of operation

Publications (1)

Publication Number Publication Date
BR9904084A true BR9904084A (pt) 2000-10-17

Family

ID=22539562

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9904084-0A BR9904084A (pt) 1998-09-11 1999-09-08 Reator de dois estágios para sistema de hidrogenação de lamas em três fases contìnuas e processo de funcionamento

Country Status (12)

Country Link
US (1) US6080372A (pt)
EP (1) EP0985446B1 (pt)
JP (1) JP3244229B2 (pt)
KR (1) KR100349476B1 (pt)
CN (1) CN1134292C (pt)
AT (1) ATE235958T1 (pt)
BR (1) BR9904084A (pt)
CA (1) CA2281398C (pt)
DE (1) DE69906439T2 (pt)
MY (1) MY118463A (pt)
SG (1) SG74164A1 (pt)
TW (1) TW497990B (pt)

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FR2834984B1 (fr) * 2002-01-21 2005-08-19 Rhodia Polyamide Intermediates Procede continu d'hydrogenation de nitriles ou composes nitres en amines
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) * 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) * 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) * 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) * 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) * 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) * 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) * 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7884232B2 (en) * 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7358389B2 (en) * 2006-01-04 2008-04-15 Eastman Chemical Company Oxidation system employing internal structure for enhanced hydrodynamics
US20070155987A1 (en) * 2006-01-04 2007-07-05 O'meadhra Ruairi S Oxidative digestion with optimized agitation
US7355068B2 (en) * 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
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
US20110137083A1 (en) 2008-05-27 2011-06-09 Basf Se Continuous method and reactor for hydrogenating organic compounds
EP2147932A1 (en) 2008-07-24 2010-01-27 LANXESS Inc. Process for the continuous hydrogenation of carbon-carbon double bonds in an unsaturated polymer to produce a hydrogenated polymer
EP2147931A1 (en) 2008-07-24 2010-01-27 LANXESS Inc. Process for the continuous hydrogenation of carbon-carbon double bonds in an unsaturated polymer
US9849434B2 (en) * 2010-09-22 2017-12-26 Grupo Petrotemex, S.A. De C.V. Methods and apparatus for enhanced gas distribution
CN102653691B (zh) * 2012-02-29 2014-01-01 东南大学 一种生物油催化转化制备含氧液体燃料的装置和方法
JP6674911B2 (ja) * 2014-06-24 2020-04-01 ノヴァ ケミカルズ（アンテルナショナル）ソシエテ アノニム 攪拌反応器内の局所流体齢の制御
CN104437272B (zh) * 2014-12-05 2016-06-01 安徽师范大学 一种气固相全混流反应器及其使用方法
KR101593207B1 (ko) * 2015-05-20 2016-02-15 한국생산기술연구원 고분산 합성반응 방법, 이를 이용한 고분산 담지 촉매의 제조방법 및 고분산 합성반응 장치
CN106422990A (zh) * 2016-12-05 2017-02-22 南京东擎科技有限公司 一种适用于三相介质的反应装置
CN107398227A (zh) * 2017-08-30 2017-11-28 中国恩菲工程技术有限公司 可调节的给料搅拌系统
KR102500508B1 (ko) * 2017-12-28 2023-02-16 한화솔루션 주식회사 사이클로도데센의 제조 방법 및 이의 합성 장치
CN108745213B (zh) * 2018-07-09 2020-04-24 安徽昊源化工集团有限公司 一种加氢反应器
CN112638854B (zh) 2018-09-05 2023-10-27 巴斯夫欧洲公司 通过不对称氢化连续制备光学活性羰基化合物
CN109999746A (zh) * 2019-05-10 2019-07-12 海安艾拉新材料有限公司 固液循环反应装置
CN110252272B (zh) * 2019-06-17 2022-04-22 万华化学集团股份有限公司 一种连续大规模制备烯烃环氧化催化剂的方法及装置
CN110394126A (zh) * 2019-08-27 2019-11-01 如皋市涤诺皂业有限公司 一种氢化反应釜
KR102371310B1 (ko) * 2019-10-22 2022-03-07 주식회사 엔엘씨 양자점 합성 장치 및 이의 합성 방법
CN113694860B (zh) * 2021-08-25 2022-05-13 宁波昊德化学工业股份有限公司 一种甲基烯丙醇的生产工艺及设备
CN113956301B (zh) * 2021-11-24 2023-06-27 浙江大学 一种用于糖醇生产的多釜串联连续加氢的方法及装置

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Also Published As

Publication number Publication date
JP2000093790A (ja) 2000-04-04
EP0985446B1 (en) 2003-04-02
DE69906439D1 (de) 2003-05-08
EP0985446A3 (en) 2000-04-19
TW497990B (en) 2002-08-11
MY118463A (en) 2004-11-29
SG74164A1 (en) 2000-07-18
KR20000022975A (ko) 2000-04-25
CN1248484A (zh) 2000-03-29
CN1134292C (zh) 2004-01-14
KR100349476B1 (ko) 2002-08-21
ATE235958T1 (de) 2003-04-15
US6080372A (en) 2000-06-27
CA2281398A1 (en) 2000-03-11
JP3244229B2 (ja) 2002-01-07
CA2281398C (en) 2003-01-14
EP0985446A2 (en) 2000-03-15
DE69906439T2 (de) 2003-10-23

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Legal Events

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B07A Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]
B09B Patent application refused [chapter 9.2 patent gazette]

Free format text: INDEFIRO O PRESENTE PEDIDO DE ACORDO COM O ART. 8O DA LPI.

B09B Patent application refused [chapter 9.2 patent gazette]

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