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NL6917651A - - Google Patents

Info

Publication number
NL6917651A
NL6917651A NL6917651A NL6917651A NL6917651A NL 6917651 A NL6917651 A NL 6917651A NL 6917651 A NL6917651 A NL 6917651A NL 6917651 A NL6917651 A NL 6917651A NL 6917651 A NL6917651 A NL 6917651A
Authority
NL
Netherlands
Application number
NL6917651A
Other versions
NL165072C (nl
NL165072B (nl
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
Priority to BE759284D priority Critical patent/BE759284A/xx
Application filed filed Critical
Priority to NL6917651.A priority patent/NL165072C/xx
Priority to US00089967A priority patent/US3759669A/en
Priority to GB5556670A priority patent/GB1329025A/en
Priority to SE15828/70A priority patent/SE370024B/xx
Priority to FR707041940A priority patent/FR2068611B1/fr
Priority to CA098,877A priority patent/CA949292A/en
Priority to DE2057528A priority patent/DE2057528C3/de
Publication of NL6917651A publication Critical patent/NL6917651A/xx
Priority to US00297099A priority patent/US3817856A/en
Publication of NL165072B publication Critical patent/NL165072B/xx
Application granted granted Critical
Publication of NL165072C publication Critical patent/NL165072C/xx

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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/14—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles
    • C10G45/16—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles suspended in the oil, e.g. slurries
    • 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
    • B01J8/226—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 internally, i.e. the particles rotate within the vessel

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (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)
  • Catalysts (AREA)
NL6917651.A 1969-11-24 1969-11-24 Werkwijze voor het met elkaar in aanraking brengen van vloeistof en vaste-stofdeeltjes. NL165072C (nl)

Priority Applications (9)

Application Number Priority Date Filing Date Title
BE759284D BE759284A (fr) 1969-11-24 Procede et appareil pour la mise en contact d'un liquide avec des particules solides
NL6917651.A NL165072C (nl) 1969-11-24 1969-11-24 Werkwijze voor het met elkaar in aanraking brengen van vloeistof en vaste-stofdeeltjes.
US00089967A US3759669A (en) 1969-11-24 1970-11-16 Apparatus for contacting liquid and solid particles
SE15828/70A SE370024B (de) 1969-11-24 1970-11-23
GB5556670A GB1329025A (en) 1969-11-24 1970-11-23 Process and apparatus for contacting a liquid with solid particles
FR707041940A FR2068611B1 (de) 1969-11-24 1970-11-23
CA098,877A CA949292A (en) 1969-11-24 1970-11-23 Process and apparatus for contacting a liquid with solid particles
DE2057528A DE2057528C3 (de) 1969-11-24 1970-11-23 Vorrichtung zur Durchführung von Reaktionen in Flüssigkeiten in Gegenwart von suspendierten Feststoffteilchen sowie Verwendung dieser Vorrichtung
US00297099A US3817856A (en) 1969-11-24 1972-10-12 Method for contacting liquid and solid particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL6917651.A NL165072C (nl) 1969-11-24 1969-11-24 Werkwijze voor het met elkaar in aanraking brengen van vloeistof en vaste-stofdeeltjes.

Publications (3)

Publication Number Publication Date
NL6917651A true NL6917651A (de) 1971-05-26
NL165072B NL165072B (nl) 1980-10-15
NL165072C NL165072C (nl) 1981-03-16

Family

ID=19808463

Family Applications (1)

Application Number Title Priority Date Filing Date
NL6917651.A NL165072C (nl) 1969-11-24 1969-11-24 Werkwijze voor het met elkaar in aanraking brengen van vloeistof en vaste-stofdeeltjes.

Country Status (8)

Country Link
US (2) US3759669A (de)
BE (1) BE759284A (de)
CA (1) CA949292A (de)
DE (1) DE2057528C3 (de)
FR (1) FR2068611B1 (de)
GB (1) GB1329025A (de)
NL (1) NL165072C (de)
SE (1) SE370024B (de)

Families Citing this family (103)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3844936A (en) * 1970-08-04 1974-10-29 Haldor Topsoe As Desulfurization process
BE788356R (fr) * 1971-09-06 1973-03-05 Knapsack Ag Procede continu pour la mise en oeuvre de reactions catalytiques heterogenes en phase
US3920552A (en) * 1973-06-28 1975-11-18 Elkern Jr Kenneth F Self-contained water treatment system
JPS5131239B2 (de) * 1974-09-13 1976-09-06
US4007016A (en) * 1975-03-06 1977-02-08 The Bethlehem Corporation Continuous-flow reactor for high viscosity materials
FR2315506A1 (fr) * 1975-06-27 1977-01-21 Rhone Poulenc Ind Procede et dispositif de fabrication d'alkylaluminiums
DE2538037C3 (de) * 1975-08-27 1988-11-10 Hüls AG, 4370 Marl Verfahren zur Hydroformylierung von Olefinen
US3998722A (en) * 1975-12-31 1976-12-21 Mayer Francis X High temperature hydroconversion without incompatibles formation
JPS531957A (en) * 1976-06-25 1978-01-10 Nippon Petrochemicals Co Ltd Method and apparatus for wet oxidative treating method of waste liquor
JPS5344483A (en) * 1976-09-29 1978-04-21 Chiyoda Chem Eng & Constr Co Ltd Wet desulfurizing apparatus for exhaust combustion gas
US4164541A (en) * 1976-11-22 1979-08-14 Lubas William Venturi mixer
US4081378A (en) * 1977-01-17 1978-03-28 John Zink Company Liquid aeration to reduce biological oxygen demand
DE2721298C3 (de) * 1977-05-12 1979-10-25 Kernforschungszentrum Karlsruhe Gmbh, 7500 Karlsruhe Verfahren zum Reinigen phosphathaltiger Abwasser
US4482524A (en) * 1978-01-31 1984-11-13 Ari Technologies, Inc. Autocirculation apparatus
DE2964898D1 (en) * 1978-07-19 1983-03-31 Ecolotrol Fluidized-bed reactor having excess growth control system
FR2446259A1 (fr) * 1979-01-12 1980-08-08 Degremont Procede et appareil pour l'elimination de la pollution azotee des eaux
US4329234A (en) * 1980-04-15 1982-05-11 Exxon Research & Engineering Co. Multi-stage gas liquid reactor
EP0096082A1 (de) * 1982-06-03 1983-12-21 Bechtel International Corporation Oxidationsreaktor
JPS59182203A (ja) * 1983-03-26 1984-10-17 Furukawa Electric Co Ltd:The 塩素水和物生成槽
SE446858B (sv) * 1983-05-30 1986-10-13 Atlas Copco Ab Anordning for att oka syrekoncentrationen i ett under ytan liggande skikt i en termiskt skiktad vattenkropp
US4640765A (en) * 1984-09-04 1987-02-03 Nippon Oil Co., Ltd. Method for cracking heavy hydrocarbon oils
US4648999A (en) * 1985-07-22 1987-03-10 M. W. Kellogg Company Apparatus for contacting fluid with solid
US4749552A (en) * 1986-08-06 1988-06-07 Ebara Densan Ltd. Automatic titration analysis apparatus
US4753721A (en) * 1986-10-24 1988-06-28 Amoco Corporation Process for resid hydrotreating employing feed distributor
US4740087A (en) * 1986-12-16 1988-04-26 Illinois Tool Works Inc. Magnetic particle bath suspension apparatus
US4820493A (en) * 1987-05-15 1989-04-11 Mobil Oil Corporation Apparatus for mixing fluid catalytic cracking hydrocarbon feed and catalyst
US4792391A (en) * 1987-06-11 1988-12-20 Amoco Corporation Floating recycle pan and process for ebullated bed reactors
CA2040995A1 (en) * 1990-05-16 1991-11-17 Robert D. Buttke Reduced gas holdup in catalytic reactor
US5139753A (en) * 1991-04-08 1992-08-18 Ari Technologies, Inc. Continuous process for mass transfer of a liquid reagent with two different gases
US5160714A (en) * 1991-04-08 1992-11-03 Ari Technologies, Inc. Continuous autocirculation, multiple zone mass transfer apparatus and method
US5126118A (en) * 1991-04-08 1992-06-30 Ari Technologies, Inc. Process and apparatus for removal of H2 S with separate absorber and oxidizer and a reaction chamber therebetween
DE4117592A1 (de) * 1991-05-29 1992-12-03 Huels Chemische Werke Ag Reaktor fuer phasenheterogene reaktionen
AU5800494A (en) * 1992-12-18 1994-07-19 Exxon Research And Engineering Company Draft tube for catalyst distribution
US5268344A (en) * 1992-12-18 1993-12-07 Exxon Research & Engineering Company Draft tube for catalyst rejuvenation and distribution
US5389238A (en) * 1993-03-17 1995-02-14 Texaco Inc. Ebullated bed process with recycle eductor
US5360535A (en) * 1993-09-02 1994-11-01 Texaco Inc. Ebullated bed process with recycle eductor
NL9301792A (nl) * 1993-10-15 1995-05-01 Biothane Systems Int Bv Reactor voor het aeroob zuiveren van afvalwater en werkwijze voor het aeroob zuiveren van afvalwater.
US5535931A (en) * 1994-12-09 1996-07-16 Prince Corporation Storage system
FR2751564B1 (fr) * 1996-07-26 2001-10-12 Inst Francais Du Petrole Procede et dispositif pour le fonctionnement d'une colonne a bulles triphasique avec application en synthese fischer-tropsch
ZA98586B (en) * 1997-02-20 1999-07-23 Sasol Tech Pty Ltd "Hydrogenation of hydrocarbons".
US6080372A (en) * 1998-09-11 2000-06-27 Air Products And Chemicals, Inc. Two stage reactor for continuous three phase slurry hydrogenation and method of operation
FR2795001B1 (fr) * 1999-06-17 2001-08-17 Cogema Procede et installation de mise en oeuvre d'une reaction chimique triphasique sous pression
US6790427B2 (en) * 2001-06-25 2004-09-14 Eka Chemicals, Inc. Process for producing chlorine dioxide
WO2003035258A1 (fr) * 2001-10-24 2003-05-01 Daikin Industries, Ltd. Procede et systeme pour la recuperation de catalyseurs et procede et unite pour la production de telomeres d'iodure de perfluoroalkyle
DE10329491A1 (de) * 2003-07-01 2005-01-27 Basf Ag Reaktor für gas/flüssig oder gas/flüssig/fest Reaktionen
US7267328B2 (en) * 2004-04-22 2007-09-11 Anthony John Witheridge Aeration of wastewater ponds using airlift pumps
US7390921B2 (en) 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) * 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) 2004-09-02 2009-01-27 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
US7972499B2 (en) 2004-09-10 2011-07-05 Chevron U.S.A. Inc. Process for recycling an active slurry catalyst composition in heavy oil upgrading
US7678732B2 (en) 2004-09-10 2010-03-16 Chevron Usa Inc. Highly active slurry catalyst composition
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7943036B2 (en) * 2009-07-21 2011-05-17 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7431823B2 (en) * 2005-12-16 2008-10-07 Chevron U.S.A. Inc. Process for upgrading heavy oil using a highly active slurry catalyst composition
US7431822B2 (en) * 2005-12-16 2008-10-07 Chevron U.S.A. Inc. Process for upgrading heavy oil using a reactor with a novel reactor separation system
US8372266B2 (en) * 2005-12-16 2013-02-12 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US8435400B2 (en) * 2005-12-16 2013-05-07 Chevron U.S.A. Systems and methods for producing a crude product
US7938954B2 (en) * 2005-12-16 2011-05-10 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US8048292B2 (en) * 2005-12-16 2011-11-01 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7431831B2 (en) * 2005-12-16 2008-10-07 Chevron U.S.A. Inc. Integrated in-line pretreatment and heavy oil upgrading process
US7390398B2 (en) * 2005-12-16 2008-06-24 Chevron U.S.A. Inc. Process for upgrading heavy oil using a highly active slurry catalyst composition
US7931796B2 (en) 2008-09-18 2011-04-26 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7358389B2 (en) * 2006-01-04 2008-04-15 Eastman Chemical Company Oxidation system employing internal structure for enhanced hydrodynamics
US7355068B2 (en) 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
JP2007197636A (ja) * 2006-01-30 2007-08-09 Nippon Steel Engineering Co Ltd 気泡塔型炭化水素合成反応器
US7931797B2 (en) * 2009-07-21 2011-04-26 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7897035B2 (en) 2008-09-18 2011-03-01 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7897036B2 (en) * 2008-09-18 2011-03-01 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7935243B2 (en) 2008-09-18 2011-05-03 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US20110017637A1 (en) * 2009-07-21 2011-01-27 Bruce Reynolds Systems and Methods for Producing a Crude Product
KR101592856B1 (ko) * 2008-09-18 2016-02-12 셰브런 유.에스.에이.인크. 원유제품의 제작 시스템 및 방법
US8236169B2 (en) * 2009-07-21 2012-08-07 Chevron U.S.A. Inc Systems and methods for producing a crude product
US20100155307A1 (en) * 2008-12-18 2010-06-24 Soto Jorge L Method and system for fines management in slurry processes
US8759242B2 (en) 2009-07-21 2014-06-24 Chevron U.S.A. Inc. Hydroprocessing catalysts and methods for making thereof
US9068132B2 (en) 2009-07-21 2015-06-30 Chevron U.S.A. Inc. Hydroprocessing catalysts and methods for making thereof
US8927448B2 (en) 2009-07-21 2015-01-06 Chevron U.S.A. Inc. Hydroprocessing catalysts and methods for making thereof
FI2658647T3 (fi) 2010-12-30 2024-07-10 Chevron Usa Inc Vetykäsittelykatalyyttejä ja menetelmiä niiden valmistamiseksi
US9687823B2 (en) 2012-12-14 2017-06-27 Chevron U.S.A. Inc. Hydroprocessing co-catalyst compositions and methods of introduction thereof into hydroprocessing units
US9321037B2 (en) 2012-12-14 2016-04-26 Chevron U.S.A., Inc. Hydroprocessing co-catalyst compositions and methods of introduction thereof into hydroprocessing units
JP2014136767A (ja) * 2013-01-17 2014-07-28 Japan Oil Gas & Metals National Corp 炭化水素合成反応装置
ITMI20130131A1 (it) * 2013-01-30 2014-07-31 Luigi Patron Processo a migliorata produttività per la conversione di olii pesanti
CN105694959B (zh) * 2016-02-03 2017-08-22 浙江大学 一种用于重油加氢裂化的喷射型内环流反应器
CN106345375B (zh) * 2016-10-26 2019-05-31 中国科学院青岛生物能源与过程研究所 一种同时带有反应和分离功能的内环流反应器

Also Published As

Publication number Publication date
NL165072C (nl) 1981-03-16
DE2057528B2 (de) 1980-04-03
CA949292A (en) 1974-06-18
BE759284A (fr) 1971-05-24
FR2068611B1 (de) 1973-02-02
NL165072B (nl) 1980-10-15
GB1329025A (en) 1973-09-05
SE370024B (de) 1974-09-30
FR2068611A1 (de) 1971-08-27
DE2057528A1 (de) 1971-05-27
US3817856A (en) 1974-06-18
DE2057528C3 (de) 1980-12-11
US3759669A (en) 1973-09-18

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