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GB930606A - Process for the production of heavy water - Google Patents

Process for the production of heavy water

Info

Publication number
GB930606A
GB930606A GB3324459A GB3324459A GB930606A GB 930606 A GB930606 A GB 930606A GB 3324459 A GB3324459 A GB 3324459A GB 3324459 A GB3324459 A GB 3324459A GB 930606 A GB930606 A GB 930606A
Authority
GB
United Kingdom
Prior art keywords
excess
catalyst
heavy water
extracted
bed
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
GB3324459A
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.)
Ruhrchemie AG
Original Assignee
Ruhrchemie 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.)
Filing date
Publication date
Application filed by Ruhrchemie AG filed Critical Ruhrchemie AG
Publication of GB930606A publication Critical patent/GB930606A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B5/00Water
    • C01B5/02Heavy water; Preparation by chemical reaction of hydrogen isotopes or their compounds, e.g. 4ND3 + 7O2 ---> 4NO2 + 6D2O, 2D2 + O2 ---> 2D2O
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0455Reaction conditions
    • C07C1/046Numerical values of parameters
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74Iron group metals
    • C07C2523/745Iron
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B3/00Engines characterised by air compression and subsequent fuel addition
    • F02B3/06Engines characterised by air compression and subsequent fuel addition with compression ignition

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The enrichment factor of heavy water in the aqueous phase of the products obtained from the continuous catalytic hydrogenation of CO at an elevated temperature in the presence of catalysts comprising a metal of Group VIII is increased provided the space velocity is in excess of 250 v/v/hr, pressure in excess of 5 kg/sq. cm., temperature below 220 DEG C., and conversion is maintained below 15% of total CO and H2 present. The catalyst may be precipitated iron, and may be a fixed bed, slurry, fluidized bed, or moving bed. The recycle ratio should be low, e.g. 0,1:1 to 1:1, and once through operation is preferred. The H2:CO molar ratio should be greater than 1,5:1. The catalyst may be periodically extracted with a solvent for paraffins, e.g. Diesel oil, without interrupting the hydrogenation. The liquor may be distilled or extracted to remove O2-containing organic compounds.
GB3324459A 1958-10-11 1959-09-30 Process for the production of heavy water Expired GB930606A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DER24190A DE1082884B (en) 1958-10-11 1958-10-11 Process for increasing the enrichment factor of the heavy water in the reaction water of the catalytic caroxydrogenation

Publications (1)

Publication Number Publication Date
GB930606A true GB930606A (en) 1963-07-03

Family

ID=7401603

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3324459A Expired GB930606A (en) 1958-10-11 1959-09-30 Process for the production of heavy water

Country Status (3)

Country Link
BE (1) BE543487A (en)
DE (1) DE1082884B (en)
GB (1) GB930606A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107987906A (en) * 2016-10-26 2018-05-04 中国石油天然气股份有限公司 Method for producing methane

Also Published As

Publication number Publication date
DE1082884B (en) 1960-06-09
BE543487A (en)

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