GB1072722A - Improvements in or relating to chemical reactors - Google Patents

Improvements in or relating to chemical reactors

Info

Publication number
GB1072722A
GB1072722A GB4153163A GB4153163A GB1072722A GB 1072722 A GB1072722 A GB 1072722A GB 4153163 A GB4153163 A GB 4153163A GB 4153163 A GB4153163 A GB 4153163A GB 1072722 A GB1072722 A GB 1072722A
Authority
GB
United Kingdom
Prior art keywords
column
phase
heavy phase
electrolysis
heavy
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
GB4153163A
Inventor
Marcel Matricon
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.)
Commissariat a lEnergie Atomique et aux Energies Alternatives CEA
Original Assignee
Commissariat a lEnergie Atomique CEA
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 Commissariat a lEnergie Atomique CEA filed Critical Commissariat a lEnergie Atomique CEA
Publication of GB1072722A publication Critical patent/GB1072722A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/04Solvent extraction of solutions which are liquid
    • B01D11/0419Solvent extraction of solutions which are liquid in combination with an electric or magnetic field or with vibrations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18Absorbing units; Liquid distributors therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D59/00Separation of different isotopes of the same chemical element
    • B01D59/28Separation by chemical exchange
    • B01D59/32Separation by chemical exchange by exchange between fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D59/00Separation of different isotopes of the same chemical element
    • B01D59/38Separation by electrochemical methods
    • B01D59/40Separation by electrochemical methods by electrolysis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D59/00Separation of different isotopes of the same chemical element
    • B01D59/50Separation involving two or more processes covered by different groups selected from groups B01D59/02, B01D59/10, B01D59/20, B01D59/22, B01D59/28, B01D59/34, B01D59/36, B01D59/38, B01D59/44
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/32Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32282Rods or bars

Landscapes

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

Abstract

<PICT:1072722/C6-C7/1> In a chemical reactor comprising a stationary column for effecting chemical exchange between two liquids of different densities, e.g. in isotopic enrichment processes, means are located in annular chambers at spaced levels in the column for effecting electrolysis of the lighter phase between anode members contacting the lighter phase and the heavy phase which is employed as cathode and spreads out in sheet like form in the annular chambers. Typically the heavy phase is an amalgam of isotopic elements and the light phase contains ionized compounds of such elements. The electrolytic action may assist or effect the exchange or inhibit or compensate for perturbative side reactions, or the applied voltage may be insufficient to effect electrolysis but sufficient to prevent undesired side reactions. As shown, a column 1 containing packing 2 is divided into sections by assemblies including annular chambers 3, the light phase following the ascending path G, H while the heavy phase 5 descends through the column and is spread out within an apertured packing support member 4, baffles 8 rendering the heavy phase quiescent. Electrolysis is effected at 6 between hollow anodes 7 traversed by a temperature-regulating fluid and the heavy phase contacting the cathodic members 12, 13. Gas evolved is extracted via orifices 10, 11. Additional anodes may be provided by packing elements comprising porous insulating flattened rods each containing an electrode core and stacked in crossing layers with the longer axes of the rods in alternate layers being oppositely inclined Fig.5 (not shown). In an alternative arrangement Figs. 2, 3 (not shown), the column is of annular form and the whole of both phases passes through the electrolysis chamber each of which is formed by plates (41, 43) carried alternately by the inner and outer column walls (40, 42) to define a plurality of intercommunicating levels, the plates including insulators (44) to prevent contact of the heavy phase with the anodes. Insulating baffles (45) are disposed on the plates at each level to define sectors (47, 49) which are alternately plain and provided with vertical peripheral channels (48) for passage in counter-current of the light and heavy phases, the channels of one level being disposed over the plain sectors of the next lower level. Helicoidal guide members e.g. of cruciform cross-section may be located adjacent the exchange surface of the two phases parallel to the directions of flow for accelerating renewal of the exchange surface.
GB4153163A 1962-10-22 1963-10-21 Improvements in or relating to chemical reactors Expired GB1072722A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR913043A FR1345052A (en) 1962-10-22 1962-10-22 Chemical reactor

Publications (1)

Publication Number Publication Date
GB1072722A true GB1072722A (en) 1967-06-21

Family

ID=8789232

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4153163A Expired GB1072722A (en) 1962-10-22 1963-10-21 Improvements in or relating to chemical reactors

Country Status (5)

Country Link
BE (1) BE639013A (en)
FR (1) FR1345052A (en)
GB (1) GB1072722A (en)
LU (1) LU44662A1 (en)
NL (1) NL299532A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8629681D0 (en) * 1986-12-11 1987-01-21 British Nuclear Fuels Plc Electrolytic reaction

Also Published As

Publication number Publication date
NL299532A (en)
FR1345052A (en) 1963-12-06
LU44662A1 (en) 1963-12-19
BE639013A (en) 1964-02-17

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