GB2014473A – Reactor for liquid-phase oxidation and use thereof
– Google Patents
GB2014473A – Reactor for liquid-phase oxidation and use thereof
– Google Patents
Reactor for liquid-phase oxidation and use thereof
Info
Publication number
GB2014473A
GB2014473A
GB7904614A
GB7904614A
GB2014473A
GB 2014473 A
GB2014473 A
GB 2014473A
GB 7904614 A
GB7904614 A
GB 7904614A
GB 7904614 A
GB7904614 A
GB 7904614A
GB 2014473 A
GB2014473 A
GB 2014473A
Authority
GB
United Kingdom
Prior art keywords
reactor
liquid
phase oxidation
oxidation
phase
Prior art date
1978-02-13
Legal status (The legal status 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 status listed.)
Granted
Application number
GB7904614A
Other versions
GB2014473B
(en
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dynamit Nobel AG
Original Assignee
Dynamit Nobel AG
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.)
1978-02-13
Filing date
1979-02-09
Publication date
1979-08-30
1979-02-09
Application filed by Dynamit Nobel AG
filed
Critical
Dynamit Nobel AG
1979-08-30
Publication of GB2014473A
publication
Critical
patent/GB2014473A/en
1982-09-15
Application granted
granted
Critical
1982-09-15
Publication of GB2014473B
publication
Critical
patent/GB2014473B/en
Status
Expired
legal-status
Critical
Current
Links
Espacenet
Global Dossier
Discuss
239000007791
liquid phase
Substances
0.000
title
1
230000003647
oxidation
Effects
0.000
title
1
238000007254
oxidation reaction
Methods
0.000
title
1
Classifications
F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28—HEAT EXCHANGE IN GENERAL
F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
F28D7/1615—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium
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
B01J19/0006—Controlling or regulating processes
B01J19/0013—Controlling the temperature of the process
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
B01J19/24—Stationary reactors without moving elements inside
B01J19/245—Stationary reactors without moving elements inside placed in series
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
B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
B01J3/04—Pressure vessels, e.g. autoclaves
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
B01J8/1836—Heating and cooling the reactor
C—CHEMISTRY; METALLURGY
C07—ORGANIC CHEMISTRY
C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
C07C51/265—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting having alkyl side chains which are oxidised to carboxyl groups
F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28—HEAT EXCHANGE IN GENERAL
F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28—HEAT EXCHANGE IN GENERAL
F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
F28D7/0083—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
F28D7/0091—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium the supplementary medium flowing in series through the units
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
B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
B01J2208/00008—Controlling the process
B01J2208/00017—Controlling the temperature
B01J2208/00106—Controlling the temperature by indirect heat exchange
B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
B01J2208/00132—Tubes
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
B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
B01J2208/00008—Controlling the process
B01J2208/00017—Controlling the temperature
B01J2208/00106—Controlling the temperature by indirect heat exchange
B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
B01J2208/00141—Coils
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
B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
B01J2208/00796—Details of the reactor or of the particulate material
B01J2208/00823—Mixing elements
B01J2208/00831—Stationary elements
B01J2208/0084—Stationary elements inside the bed, e.g. baffles
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/00049—Controlling or regulating processes
B01J2219/00051—Controlling the temperature
B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
B01J2219/00081—Tubes
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/00049—Controlling or regulating processes
B01J2219/00051—Controlling the temperature
B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
B01J2219/00083—Coils
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/00049—Controlling or regulating processes
B01J2219/00051—Controlling the temperature
B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
B01J2219/00108—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/00761—Details of the reactor
B01J2219/00763—Baffles
B01J2219/00765—Baffles attached to the reactor wall
B01J2219/00768—Baffles attached to the reactor wall vertical
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/18—Details relating to the spatial orientation of the reactor
B01J2219/182—Details relating to the spatial orientation of the reactor horizontal
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/18—Details relating to the spatial orientation of the reactor
B01J2219/185—Details relating to the spatial orientation of the reactor vertical
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/19—Details relating to the geometry of the reactor
B01J2219/194—Details relating to the geometry of the reactor round
B01J2219/1941—Details relating to the geometry of the reactor round circular or disk-shaped
B01J2219/1943—Details relating to the geometry of the reactor round circular or disk-shaped cylindrical
GB7904614A
1978-02-13
1979-02-09
Reactor for liquid-phase oxidation and use thereof
Expired
GB2014473B
(en)
Applications Claiming Priority (1)
Application Number
Priority Date
Filing Date
Title
DE2805915A
DE2805915C3
(en)
1978-02-13
1978-02-13
Reactor for the oxidation of mixtures of p-xylene and p-toluic acid methyl ester with oxygen-containing gases in the liquid phase
Publications (2)
Publication Number
Publication Date
GB2014473A
true
GB2014473A
(en)
1979-08-30
GB2014473B
GB2014473B
(en)
1982-09-15
Family
ID=6031776
Family Applications (1)
Application Number
Title
Priority Date
Filing Date
GB7904614A
Expired
GB2014473B
(en)
1978-02-13
1979-02-09
Reactor for liquid-phase oxidation and use thereof
Country Status (18)
Country
Link
US
(1)
US4269805A
(en)
JP
(1)
JPS54117435A
(en)
AR
(1)
AR221484A1
(en)
BE
(1)
BE874097A
(en)
BG
(1)
BG48334A3
(en)
BR
(1)
BR7900837A
(en)
CS
(1)
CS217968B2
(en)
DE
(1)
DE2805915C3
(en)
FR
(1)
FR2416725A1
(en)
GB
(1)
GB2014473B
(en)
IT
(1)
IT1162612B
(en)
MX
(1)
MX149747A
(en)
NL
(1)
NL184771C
(en)
PL
(1)
PL120527B1
(en)
RO
(1)
RO77204A
(en)
SU
(1)
SU1056879A3
(en)
TR
(1)
TR20807A
(en)
YU
(1)
YU41848B
(en)
Cited By (15)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
EP0150835A2
(en)
*
1984-01-27
1985-08-07
Paul Dipl.-Ing. Bonsels
Process for the oxidation of liquid organic substances
WO1998027029A1
(en)
*
1996-12-18
1998-06-25
Twenty-First Century Research Corporation
Methods of preparing an intermediate oxidation product from a hydrocarbon by utilizing an activated initiator
US5877341A
(en)
*
1996-08-21
1999-03-02
Twenty-First Century Research Corporation
Methods and devices for controlling the reaction rate of a hydrocarbon to an intermediate oxidation product by pressure drop adjustments
US5908589A
(en)
*
1997-12-08
1999-06-01
Twenty-First Century Research Corporation
Methods for separating catalyst from oxidation mixtures containing dibasic acids
US5929277A
(en)
*
1997-09-19
1999-07-27
Twenty-First Century Research Corporation
Methods of removing acetic acid from cyclohexane in the production of adipic acid
US5939582A
(en)
*
1996-01-17
1999-08-17
Twenty-First Century Research Corporation
Reaction control by regulating internal condensation inside a reactor
US6037491A
(en)
*
1997-07-25
2000-03-14
Rpc Inc.
Methods and devices for controlling hydrocarbon oxidations to respective acids by adjusting the solvent to hydrocarbon ratio
US6039902A
(en)
*
1996-06-24
2000-03-21
Rpc Inc.
Methods of recycling catalyst in oxidations of hydrocarbons
US6129875A
(en)
*
1998-02-19
2000-10-10
Rpc Inc.
Process of separating catalyst from oxidation mixtures
US6143927A
(en)
*
1996-06-24
2000-11-07
Rpc Inc.
Methods for removing catalyst after oxidation of hydrocarbons
US6232495B1
(en)
1998-02-09
2001-05-15
Rpc Inc.
Methods for treating cobalt catalyst in oxidation mixtures resulting from oxidation of hydrocarbons to dibasic acids
US6288270B1
(en)
1996-06-24
2001-09-11
Rpc Inc.
Methods for controlling the reaction rate of a hydrocarbon to an acid by making phase-related adjustments
US6288274B1
(en)
1996-08-21
2001-09-11
Rpc Inc.
Methods and devices for controlling the reaction rate and/or reactivity of hydrocarbon to an intermediate oxidation product by adjusting the oxidant consumption rate
US6359173B1
(en)
1996-06-24
2002-03-19
Rpc Inc.
Methods and devices for oxidizing a hydrocarbon to form an acid
EP2626129A1
(en)
*
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2013-08-14
Heatric
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Families Citing this family (52)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
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EP0050030B1
(en)
*
1980-10-13
1985-01-09
Peter Spencer
Reactor for the thermal cracking of heavy hydrocarbons and a process and apparatus for the distillation and thermal cracking of a crude oil feedstock using such a reactor
US4519984A
(en)
*
1982-01-18
1985-05-28
Phillips Petroleum Company
Apparatus for carrying out sparged reaction
US4499029A
(en)
*
1983-06-15
1985-02-12
Ashland Oil, Inc.
Isobutyryl fluoride manufacture
US4550012A
(en)
*
1984-05-01
1985-10-29
Mobil Oil Corp.
Multi-phase countercurrent reactor system
US5380909A
(en)
*
1991-06-24
1995-01-10
The Dow Chemical Company
Captive carbonyl halide process for production of diaryl carbonates
US6153149A
(en)
*
1997-08-06
2000-11-28
The Trustees Of Princeton University
Adaptive feedback control flow reactor
US6433221B1
(en)
1998-07-02
2002-08-13
Rpc Inc.
Methods of separating catalyst in solution from a reaction mixture produced by oxidation of cyclohexane to adipic acid
US6340420B1
(en)
1998-07-06
2002-01-22
Rpc Inc.
Methods of treating the oxidation mixture of hydrocarbons to respective dibasic acids
CN1347397A
(en)
1999-04-20
2002-05-01
Rpc公司
Methods of replacing water and cyclohexanone with acetic acid in aqueous solutions of catalyst
US6949673B2
(en)
*
2000-01-12
2005-09-27
E.I. Du Pont De Nemours And Company
Process for producing carboxylic acids
US7060853B2
(en)
*
2000-01-12
2006-06-13
Invista North America S.A R.L.
Method for increasing oxidation reactor production capacity
GB2381764A
(en)
*
2001-11-08
2003-05-14
Farleydene Ltd
Autoclave suitable for heat treating parts
US20050256335A1
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*
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Ovidiu Marin
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KR20070057883A
(en)
*
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2007-06-07
셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이
Horizontal reactor vessel
US7381836B2
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*
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US7582793B2
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US7683210B2
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*
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CN101518726B
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*
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US7589231B2
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US7399882B2
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*
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US20080280892A1
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US7355068B2
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(en)
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2016-08-17
微波化学有限公司
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(en)
*
2011-11-11
2012-12-26
マイクロ波化学株式会社
Chemical reactor
US11229895B2
(en)
2011-11-11
2022-01-25
Microwave Chemical Co., Ltd.
Chemical reaction method using chemical reaction apparatus
FR3008627B1
(en)
2013-07-19
2017-02-24
Arkema France
THERMAL CONVERSION TANK USED IN ACETONE CYANOHYDRIN AMIDIFICATION PROCESS
CN114733451A
(en)
*
2022-04-15
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Continuous gas-liquid reaction device with adjustable residence time
Family Cites Families (8)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
US2760850A
(en)
*
1951-11-23
1956-08-28
Lummus Co
Tank reactor
US2920124A
(en)
*
1955-04-14
1960-01-05
Kellogg M W Co
Alkylation of hydrocarbons with improved mixing and emulsifying of catalyst and reactants
US3199959A
(en)
*
1958-03-04
1965-08-10
Sun Oil Co
Reactor for preparation of carboxylic aromatic acids
DE1767047U
(en)
*
1958-03-18
1958-05-22
Imhausen Werke G M B H
OXYDATION APPARATUS WITH INTERNAL COOLING SYSTEM FOR THE AIR OXYDATION OF ALKYL-SUBSTITUTED AROMATIC CARBON CARBONS TO DRAIN THE HEAT OF REACTION.
NL292245A
(en)
*
1962-05-11
US3271433A
(en)
*
1963-06-17
1966-09-06
Anderson Clayton & Co
Process for semi-continuous hydrogenation of fat
GB1398639A
(en)
*
1972-08-05
1975-06-25
Kanebo Ltd
Generation of gaseous formaldehyde from formaldehyde polymer
US3845117A
(en)
*
1972-12-14
1974-10-29
Halcon International Inc
Process for preparation of phthalic acids
1978
1978-02-13
DE
DE2805915A
patent/DE2805915C3/en
not_active
Expired
1978-04-18
AR
AR271824A
patent/AR221484A1/en
active
1979
1979-01-29
MX
MX176433A
patent/MX149747A/en
unknown
1979-02-08
RO
RO7996552A
patent/RO77204A/en
unknown
1979-02-09
GB
GB7904614A
patent/GB2014473B/en
not_active
Expired
1979-02-09
TR
TR20807A
patent/TR20807A/en
unknown
1979-02-12
FR
FR7903497A
patent/FR2416725A1/en
active
Granted
1979-02-12
YU
YU306/79A
patent/YU41848B/en
unknown
1979-02-12
IT
IT47968/79A
patent/IT1162612B/en
active
1979-02-12
PL
PL1979213379A
patent/PL120527B1/en
unknown
1979-02-12
BG
BG42443A
patent/BG48334A3/en
unknown
1979-02-12
BE
BE193403A
patent/BE874097A/en
unknown
1979-02-12
BR
BR7900837A
patent/BR7900837A/en
unknown
1979-02-12
NL
NLAANVRAGE7901105,A
patent/NL184771C/en
not_active
IP Right Cessation
1979-02-12
US
US06/011,656
patent/US4269805A/en
not_active
Expired – Lifetime
1979-02-13
JP
JP1442579A
patent/JPS54117435A/en
active
Granted
1979-02-13
CS
CS79959A
patent/CS217968B2/en
unknown
1981
1981-01-20
SU
SU813230705A
patent/SU1056879A3/en
active
Cited By (21)
* Cited by examiner, † Cited by third party
Publication number
Priority date
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Assignee
Title
EP0150835A2
(en)
*
1984-01-27
1985-08-07
Paul Dipl.-Ing. Bonsels
Process for the oxidation of liquid organic substances
EP0150835A3
(en)
*
1984-01-27
1987-04-08
Paul Dipl.-Ing. Bonsels
Process for the oxidation of liquid organic substances
US5939582A
(en)
*
1996-01-17
1999-08-17
Twenty-First Century Research Corporation
Reaction control by regulating internal condensation inside a reactor
US6039902A
(en)
*
1996-06-24
2000-03-21
Rpc Inc.
Methods of recycling catalyst in oxidations of hydrocarbons
US6288270B1
(en)
1996-06-24
2001-09-11
Rpc Inc.
Methods for controlling the reaction rate of a hydrocarbon to an acid by making phase-related adjustments
US6359173B1
(en)
1996-06-24
2002-03-19
Rpc Inc.
Methods and devices for oxidizing a hydrocarbon to form an acid
US6143927A
(en)
*
1996-06-24
2000-11-07
Rpc Inc.
Methods for removing catalyst after oxidation of hydrocarbons
US6294689B1
(en)
1996-06-24
2001-09-25
Rpc Inc.
Methods for removing catalyst after oxidation of hydrocarbons
US5877341A
(en)
*
1996-08-21
1999-03-02
Twenty-First Century Research Corporation
Methods and devices for controlling the reaction rate of a hydrocarbon to an intermediate oxidation product by pressure drop adjustments
US6288274B1
(en)
1996-08-21
2001-09-11
Rpc Inc.
Methods and devices for controlling the reaction rate and/or reactivity of hydrocarbon to an intermediate oxidation product by adjusting the oxidant consumption rate
US6183698B1
(en)
1996-08-21
2001-02-06
Rpc Inc.
Devices for controlling the reaction rate of a hydrocarbon to an intermediate oxidation product by pressure drop adjustments
US5824819A
(en)
*
1996-12-18
1998-10-20
Twenty-First Century Research Corporation
Methods of preparing an intermediate oxidation product from a hydrocarbon by utilizing an activated initiator
WO1998027029A1
(en)
*
1996-12-18
1998-06-25
Twenty-First Century Research Corporation
Methods of preparing an intermediate oxidation product from a hydrocarbon by utilizing an activated initiator
US6037491A
(en)
*
1997-07-25
2000-03-14
Rpc Inc.
Methods and devices for controlling hydrocarbon oxidations to respective acids by adjusting the solvent to hydrocarbon ratio
US6177053B1
(en)
1997-09-19
2001-01-23
Rpc Inc.
Devices for removing acetic acid from cyclohexane in the production of adipic acid
US5929277A
(en)
*
1997-09-19
1999-07-27
Twenty-First Century Research Corporation
Methods of removing acetic acid from cyclohexane in the production of adipic acid
US5908589A
(en)
*
1997-12-08
1999-06-01
Twenty-First Century Research Corporation
Methods for separating catalyst from oxidation mixtures containing dibasic acids
US6232495B1
(en)
1998-02-09
2001-05-15
Rpc Inc.
Methods for treating cobalt catalyst in oxidation mixtures resulting from oxidation of hydrocarbons to dibasic acids
US6326455B2
(en)
1998-02-09
2001-12-04
Rpc Inc.
Methods for treating cobalt catalyst in oxidation mixtures resulting from oxidation of hydrocarbons to dibasic acids
US6129875A
(en)
*
1998-02-19
2000-10-10
Rpc Inc.
Process of separating catalyst from oxidation mixtures
EP2626129A1
(en)
*
2005-09-23
2013-08-14
Heatric
Multiple reactor chemical production system
Also Published As
Publication number
Publication date
GB2014473B
(en)
1982-09-15
JPS54117435A
(en)
1979-09-12
IT1162612B
(en)
1987-04-01
DE2805915C3
(en)
1981-11-05
TR20807A
(en)
1982-09-16
NL7901105A
(en)
1979-08-15
AR221484A1
(en)
1981-02-13
FR2416725A1
(en)
1979-09-07
YU41848B
(en)
1988-02-29
SU1056879A3
(en)
1983-11-23
US4269805A
(en)
1981-05-26
BG48334A3
(en)
1991-01-15
NL184771C
(en)
1989-11-01
BR7900837A
(en)
1979-09-04
DE2805915A1
(en)
1979-08-16
RO77204A
(en)
1982-03-24
PL120527B1
(en)
1982-03-31
YU30679A
(en)
1982-08-31
NL184771B
(en)
1989-06-01
FR2416725B1
(en)
1983-07-08
BE874097A
(en)
1979-05-29
MX149747A
(en)
1983-12-15
CS217968B2
(en)
1983-02-25
DE2805915B2
(en)
1980-12-04
IT7947968D0
(en)
1979-02-12
JPS5758335B2
(en)
1982-12-09
PL213379A1
(en)
1979-10-22
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Legal Events
Date
Code
Title
Description
1995-10-04
PCNP
Patent ceased through non-payment of renewal fee
Effective date:
19950209
