GB1168052A - Process for the Dealkylation of Alkylaromatics - Google Patents

Process for the Dealkylation of Alkylaromatics

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Publication number
GB1168052A
GB1168052A GB32240/68A GB3224068A GB1168052A GB 1168052 A GB1168052 A GB 1168052A GB 32240/68 A GB32240/68 A GB 32240/68A GB 3224068 A GB3224068 A GB 3224068A GB 1168052 A GB1168052 A GB 1168052A
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GB
United Kingdom
Prior art keywords
reaction
pressure
alkanes
containing gas
alkylaromatics
Prior art date
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.)
Expired
Application number
GB32240/68A
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.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Priority to GB32240/68A priority Critical patent/GB1168052A/en
Priority to FR6922571A priority patent/FR2012373A1/en
Priority to NL6910207A priority patent/NL6910207A/xx
Priority to DE19691933897 priority patent/DE1933897A1/en
Priority to BE735573D priority patent/BE735573A/xx
Publication of GB1168052A publication Critical patent/GB1168052A/en
Expired legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/08Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule
    • C07C4/12Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule from hydrocarbons containing a six-membered aromatic ring, e.g. propyltoluene to vinyltoluene
    • C07C4/14Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule from hydrocarbons containing a six-membered aromatic ring, e.g. propyltoluene to vinyltoluene splitting taking place at an aromatic-aliphatic bond
    • C07C4/16Thermal processes
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    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
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    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/40Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts characterised by the catalyst
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/48Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
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    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/0205Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
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    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0415Purification by absorption in liquids
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465Composition of the impurity
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    • C01B2203/048Composition of the impurity the impurity being an organic compound
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    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
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    • C01B2203/14Details of the flowsheet
    • C01B2203/146At least two purification steps in series
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

1,168,052. Hydrodealkylation. SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V. 5 July, 1968, No. 32240/68. Heading C5E. A process for the dealkylation of alkylaromatics comprises (1) converting one or more alkylaromatics with a H 2 -containing gas into one or more aromatics and one or more alkanes at elevated temperature and pressure in a first reaction zone; (2) converting one or more alkanes with steam into a H 2 -containing gas at elevator termperature and pressure in a second reaction zone, and (3) exchanging heat between the first and second reaction zones. The alkanes produced in (1) may be converted in (2), and the H 2 -containing gas produced in (2) may be used in (1). The feedstock for the first reaction zone may be toluene, xylenes, ethylbenzene, mono-, di- and trimethylnaphthalenes or mixtures thereof. Reaction (1) may be carried out at 600-800‹ C. and 35-45 kg/cm.<SP>2</SP> pressure. Reaction (2) may be carried out at 600-800‹ C. and 30-45 kg/cm.<SP>2</SP> pressure in the presence of a nickel or rhenium containing catalyst supported on a carrier and optionally containing 0À1-10% by wt. alkali metal. The example describes the production of benzene from toluene. CO and steam contained in the effluent of reaction (1) or (2) may be converted to CO 2 and H 2 at 300-450‹ C. using a iron oxide-chromium oxide catalyst.
GB32240/68A 1968-07-05 1968-07-05 Process for the Dealkylation of Alkylaromatics Expired GB1168052A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
GB32240/68A GB1168052A (en) 1968-07-05 1968-07-05 Process for the Dealkylation of Alkylaromatics
FR6922571A FR2012373A1 (en) 1968-07-05 1969-07-03 Exothermic dealkylation of toluene
NL6910207A NL6910207A (en) 1968-07-05 1969-07-03
DE19691933897 DE1933897A1 (en) 1968-07-05 1969-07-03 Process for the dealkylation of alkyl aromatics
BE735573D BE735573A (en) 1968-07-05 1969-07-03

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB32240/68A GB1168052A (en) 1968-07-05 1968-07-05 Process for the Dealkylation of Alkylaromatics

Publications (1)

Publication Number Publication Date
GB1168052A true GB1168052A (en) 1969-10-22

Family

ID=10335516

Family Applications (1)

Application Number Title Priority Date Filing Date
GB32240/68A Expired GB1168052A (en) 1968-07-05 1968-07-05 Process for the Dealkylation of Alkylaromatics

Country Status (5)

Country Link
BE (1) BE735573A (en)
DE (1) DE1933897A1 (en)
FR (1) FR2012373A1 (en)
GB (1) GB1168052A (en)
NL (1) NL6910207A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1950271A1 (en) * 2007-01-26 2008-07-30 Linde Aktiengesellschaft Method for separating the gaseous reaction products of steam dealkylation

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008148807A1 (en) * 2007-06-08 2008-12-11 Basf Se Improved method for reacting hydrocarbons on a catalyst in the presence of steam

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1950271A1 (en) * 2007-01-26 2008-07-30 Linde Aktiengesellschaft Method for separating the gaseous reaction products of steam dealkylation

Also Published As

Publication number Publication date
FR2012373A1 (en) 1970-03-20
DE1933897A1 (en) 1970-01-08
NL6910207A (en) 1970-01-07
BE735573A (en) 1970-01-05

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