IE39884B1 - Fluidisable charge of oxyhalogenation catalyst - Google Patents

Fluidisable charge of oxyhalogenation catalyst

Info

Publication number
IE39884B1
IE39884B1 IE1823/74A IE182374A IE39884B1 IE 39884 B1 IE39884 B1 IE 39884B1 IE 1823/74 A IE1823/74 A IE 1823/74A IE 182374 A IE182374 A IE 182374A IE 39884 B1 IE39884 B1 IE 39884B1
Authority
IE
Ireland
Prior art keywords
catalyst
oxyhalogenation
particles
charge
fluidisable
Prior art date
Application number
IE1823/74A
Other versions
IE39884L (en
Original Assignee
Rhone Progil
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 Rhone Progil filed Critical Rhone Progil
Publication of IE39884L publication Critical patent/IE39884L/en
Publication of IE39884B1 publication Critical patent/IE39884B1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical 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
    • B01J8/32Chemical 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 introduction into the fluidised bed of more than one kind of moving particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06Halogens; Compounds thereof
    • B01J27/08Halides
    • B01J27/10Chlorides
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/093Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/15Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

1474258 Oxyhalogenation catalyst RHONEPROGIL SA 2 Sept 1974 [4 Sent 19731 38272/74 Heading B1E [Also in Division C2] A pulverluent fluidisable oxyhalogenation catalyst charge comprises 5 to 50% wt of particles of an oxyhalogenation catalyst and 95 to 50% wt of particles of at least one solid substance that is catalytically and chemically inert in the oxyhalogenation reaction and that acts to stabilise the granulometry but not as a support for the catalyst, the average diameter of the catalyst particles being greater than the average diameter of the particles of the inert solid substance. The diluent may be alphaalumina, glass beads or siliceous sand. The catalyst may comprise an inorganic copper salt, e.g. the chloride, deposited on an activated alumina support of surface area 150-400 sq. m/gm. The charge may be of a particle size 20-200 microns with a mean diameter of 40-90 microns. [GB1474258A]
IE1823/74A 1973-09-04 1974-09-03 Fluidisable charge of oxyhalogenation catalyst IE39884B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR7331837A FR2242143B1 (en) 1973-09-04 1973-09-04

Publications (2)

Publication Number Publication Date
IE39884L IE39884L (en) 1975-03-04
IE39884B1 true IE39884B1 (en) 1979-01-17

Family

ID=9124596

Family Applications (1)

Application Number Title Priority Date Filing Date
IE1823/74A IE39884B1 (en) 1973-09-04 1974-09-03 Fluidisable charge of oxyhalogenation catalyst

Country Status (21)

Country Link
JP (1) JPS5324045B2 (en)
AR (1) AR201883A1 (en)
AU (1) AU7293474A (en)
BE (1) BE819480A (en)
BR (1) BR7407330D0 (en)
CA (1) CA1024998A (en)
DK (1) DK151007C (en)
EG (1) EG11251A (en)
ES (1) ES429752A1 (en)
FR (1) FR2242143B1 (en)
GB (1) GB1474258A (en)
IE (1) IE39884B1 (en)
IN (1) IN143087B (en)
IT (1) IT1019186B (en)
NL (1) NL189855C (en)
NO (1) NO141358C (en)
PH (1) PH12560A (en)
PL (1) PL96475B1 (en)
RO (1) RO72689A (en)
SU (1) SU567397A3 (en)
TR (1) TR18376A (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MX152427A (en) * 1979-09-12 1985-07-15 Mexicano Inst Petrol IMPROVED REACTOR AND PROCEDURE FOR ETHYLENE OXYCHLORATION
FR2641779B1 (en) * 1988-12-26 1991-04-19 Atochem OXYCHLORATION PROCESS AND CATALYST, THEIR APPLICATION TO THE PRODUCTION OF 1-2 DICHLOROETHANE
DE68918258T2 (en) * 1988-12-29 1995-05-04 Monsanto Co Fluidized bed process.
US5079379A (en) * 1988-12-29 1992-01-07 Monsanto Company Fluid bed process
JPH0414509U (en) * 1990-05-29 1992-02-05
US5243111A (en) * 1990-06-25 1993-09-07 Atochem Catalytic oxychlorination of hydrocarbons to produce chlorocarbons
FR2663629B1 (en) * 1990-06-25 1992-12-18 Atochem OXYCHLORATION PROCESS AND CATALYST, THEIR APPLICATION TO THE PRODUCTION OF 1-2 DICHLOROETHANE.
TWI341218B (en) * 2005-11-14 2011-05-01 Oxy Vinyls Lp Catalyst compositions and process for oxychlorination
CN112469499B (en) 2018-06-28 2023-08-01 奥升德功能材料运营有限公司 Method and system for using silica particles in a fluidized bed reactor

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2866830A (en) * 1956-05-31 1958-12-30 Dow Chemical Co Fixed bed oxychlorination of hydrocarbons
DE1142161B (en) * 1958-06-24 1963-01-10 Pittsburgh Plate Glass Co Process for the oxychlorination of aliphatic saturated hydrocarbons with 1 to 4 carbon atoms
GB894138A (en) * 1958-06-24 1962-04-18 Columbia Southern Chem Corp Process for the production of chlorinated hydrocarbons
NL135564C (en) * 1961-07-13

Also Published As

Publication number Publication date
PL96475B1 (en) 1977-12-31
FR2242143B1 (en) 1978-03-24
SU567397A3 (en) 1977-07-30
NO743162L (en) 1975-04-01
DK151007B (en) 1987-10-12
TR18376A (en) 1977-05-01
NO141358B (en) 1979-11-19
JPS5324045B2 (en) 1978-07-18
IN143087B (en) 1977-10-01
ES429752A1 (en) 1976-11-01
AU7293474A (en) 1976-03-11
GB1474258A (en) 1977-05-18
DE2442182A1 (en) 1975-03-27
NL189855B (en) 1993-03-16
FR2242143A1 (en) 1975-03-28
RO72689A (en) 1981-03-30
BE819480A (en) 1975-03-03
NO141358C (en) 1980-02-27
DE2442182B2 (en) 1976-06-16
CA1024998A (en) 1978-01-24
DK151007C (en) 1988-02-29
PH12560A (en) 1979-06-15
NL7411646A (en) 1975-03-06
AR201883A1 (en) 1975-04-24
BR7407330D0 (en) 1975-07-01
IT1019186B (en) 1977-11-10
IE39884L (en) 1975-03-04
EG11251A (en) 1977-01-31
NL189855C (en) 1993-08-16
JPS5070306A (en) 1975-06-11
DK464874A (en) 1975-05-05

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