GB889828A - Process for dehydrating the catalyst in deuterium exchange installations - Google Patents

Process for dehydrating the catalyst in deuterium exchange installations

Info

Publication number
GB889828A
GB889828A GB18357/58A GB1835758A GB889828A GB 889828 A GB889828 A GB 889828A GB 18357/58 A GB18357/58 A GB 18357/58A GB 1835758 A GB1835758 A GB 1835758A GB 889828 A GB889828 A GB 889828A
Authority
GB
United Kingdom
Prior art keywords
catalyst
water
passed
exchange
withdrawn
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
GB18357/58A
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.)
DEUTSCHE GOLD-UND SILBERSCHEIDEANSTALT
Evonik Operations GmbH
Original Assignee
DEUTSCHE GOLD-UND SILBERSCHEIDEANSTALT
Degussa GmbH
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 DEUTSCHE GOLD-UND SILBERSCHEIDEANSTALT, Degussa GmbH filed Critical DEUTSCHE GOLD-UND SILBERSCHEIDEANSTALT
Publication of GB889828A publication Critical patent/GB889828A/en
Expired legal-status Critical Current

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
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/90Regeneration or reactivation
    • B01J23/96Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the noble metals
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/18Carbon

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

<PICT:0889828/III/1> The catalyst, separated from water in a deuterium-exchange process between hydrogen and water containing a catalyst in suspension, is dehydrated by exposure to a stream of hydrogen having a lower D- content than the water adhering to the catalyst, and the hydrogen is passed into an exchange process with water. H2 generated from water in 21 is passed through exchange column 22 in countercurrent to water containing suspended catalyst. The water is withdrawn at 29 and passed to separator 23, whence the water is returned to the generator 21. The separated catalyst passed to dehydrator 24, whence it is returned through 212 to the water feed at 213. Part of the water containing suspended catalyst is withdrawn at 214 and passed through cold (5 DEG -100 DEG C.) column 27 and hot (150 DEG -250 DEG C.) column 25, of a dual temperature isotope exchange unit, and returned at 218 to the main stream. The hydrogen used to dehydrate the catalyst in 24 passes in closed circuit through columns 25, 27, in countercurrent to the water, and a part circulation is withdrawn at 222 to flow through further cold and hot columns 28, 26 and returned at 225. A closed circuit of water containing suspended catalyst flows countercurrent through 28, 26 and product is withdrawn at 228 or passed to additional stages. In a simpler arrangement (Fig. 1, not shown) a simple exchange occurs in an exchange column associated with H2 generator, catalyst separator, and dehydrator, wherein a part of the H2 from the exchange column is used in the dehydrator and is added to the gas passing to the exchange column.
GB18357/58A 1957-06-07 1958-06-09 Process for dehydrating the catalyst in deuterium exchange installations Expired GB889828A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE889828X 1957-06-07

Publications (1)

Publication Number Publication Date
GB889828A true GB889828A (en) 1962-02-21

Family

ID=6834729

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18357/58A Expired GB889828A (en) 1957-06-07 1958-06-09 Process for dehydrating the catalyst in deuterium exchange installations

Country Status (1)

Country Link
GB (1) GB889828A (en)

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