GB725660A - Improvements in or relating to the loading and regeneration of ion exchangers used in ion exchange processes - Google Patents

Improvements in or relating to the loading and regeneration of ion exchangers used in ion exchange processes

Info

Publication number
GB725660A
GB725660A GB1284/53A GB128453A GB725660A GB 725660 A GB725660 A GB 725660A GB 1284/53 A GB1284/53 A GB 1284/53A GB 128453 A GB128453 A GB 128453A GB 725660 A GB725660 A GB 725660A
Authority
GB
United Kingdom
Prior art keywords
column
solution
columns
loading
group
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
GB1284/53A
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.)
Stamicarbon BV
Original Assignee
Stamicarbon 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 Stamicarbon BV filed Critical Stamicarbon BV
Publication of GB725660A publication Critical patent/GB725660A/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
    • B01J49/00Regeneration or reactivation of ion-exchangers; Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J47/00Ion-exchange processes in general; Apparatus therefor
    • B01J47/02Column or bed processes
    • B01J47/026Column or bed processes using columns or beds of different ion exchange materials in series

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treatment Of Water By Ion Exchange (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)

Abstract

<PICT:0725660/III/1> <PICT:0725660/III/2> A method of loading and regenerating an ion exchange system comprising a set of columns arranged in a series packed with ion exchanger to be loaded and another series of columns containing ion exchanger to be regenerated, is characterized in that the series to be loaded is divided into two groups, the loading solution is passed through the two groups in succession, the solution discharged from the last column of the second group is freed by crystallization from a large part of the compound formed during loading, the mother lye is concentrated and returned to the first column of the second group. The regenerating solution passes through the regenerating series of columns in such amount that regeneration is incomplete but a virtually pure regenerated solution leaves the last column. In Fig. 1 the columns C1 to Cm and D1 to Dn constitute the first and second groups of the loading series. The loading solution B2A2 is passed through the columns in succession and the solution leaving the last column of the second group is freed from the B1A2 compounds formed, by crystallization at Cr, and the residual lye is evaporated at Ev and returned to the first column of the second group, that is, D1. The regeneration is shown in Fig. 2 where columns E1 to Ep are arranged in series and are transversed by the regenerating solution B1A1 the amount thereof being such that a virtually pure B2A1 solution leaves the last column. Periodically the columns are disconnected and switched over so that the first column E1 in the regenerating group becomes the last column of the first loading group; at the same time column C1 is added to the end of the regeneration group and column D1 becomes column Cm, the cycle is then repeated. The invention is illustrated by the production of potassium nitrate crystals and calcium chloride solution from calcium nitrate solution and potassium chloride solution, six columns in two groups of three being employed for loading and a single group of three for regenerating. During loading the columns, saturated with potassium ions, are treated with a calcium nitrate solution passed therethrough, until the final column of the first group is 100 per cent. saturated with calcium ions. After leaving the last column potassium nitrate is crystallized out and the residual lye returned to column D1. Regeneration is effected with potassium chloride solution to such an extent that the regenerated column is only 80 per cent. saturated with potassium ions.
GB1284/53A 1952-01-19 1953-01-15 Improvements in or relating to the loading and regeneration of ion exchangers used in ion exchange processes Expired GB725660A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL313763X 1952-01-19

Publications (1)

Publication Number Publication Date
GB725660A true GB725660A (en) 1955-03-09

Family

ID=19783729

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1284/53A Expired GB725660A (en) 1952-01-19 1953-01-15 Improvements in or relating to the loading and regeneration of ion exchangers used in ion exchange processes

Country Status (7)

Country Link
US (1) US2751280A (en)
BE (1) BE516816A (en)
CH (1) CH313763A (en)
DE (1) DE958019C (en)
FR (1) FR1069599A (en)
GB (1) GB725660A (en)
NL (1) NL79196C (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3059777A (en) * 1956-10-05 1962-10-23 Michigan Chem Corp Apparatus for the separation of metallic ions by the use of an ion exchange resin
DE1064080B (en) * 1958-06-14 1959-08-27 Basf Ag Process for the production of ballast-free potassium ammonium nitrate fertilizers
US3096153A (en) * 1960-10-17 1963-07-02 Standard Magnesium Corp Inc Ion exchange process for producing potassium sulfate and sulfuric acid
DE1442942A1 (en) * 1964-02-10 1968-12-19 Dynamit Nobel Ag Process for carrying out the process steps required for ion exchange reactions and for preventing harmful mixing
DE1283192B (en) * 1965-01-15 1968-11-21 Braunschweigische Maschb Ansta Device for cleaning sugar juice or other solutions
DE2800516A1 (en) * 1978-01-03 1979-07-12 Permutit Gmbh METHOD AND DEVICE FOR TREATMENT OF WATER, SUCH AS DRINKING AND / OR USED WATER
FI114791B (en) * 2002-08-21 2004-12-31 Kemira Oyj Manufacturing process for carboxylic acid salts

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1859738A (en) * 1929-09-28 1932-05-24 Firm Odda Smelteverk As Process of manufacturing fertilizers
DE624141C (en) * 1931-06-03 1936-01-14 Luxemburgeoise Mutosel Sa Process for the extraction of salts
GB415660A (en) * 1933-03-17 1934-08-30 Ig Farbenindustrie Ag Improvements in the manufacture and production of alkali metal nitrate from calcium nitrate and alkali metal chloride
DE628139C (en) * 1933-06-02 1936-04-01 Luxemburgeoise Mutosel Sa Process for the production and purification of salts using base exchangers
NL43492C (en) * 1933-06-22 1900-01-01 Norsk Hydro Elektrisk
DE650086C (en) * 1933-06-22 1937-09-14 Norsk Hydro Elek Sk Kvaelstofa Process for the production of salts, in particular sodium nitrate, using base-exchanging substances

Also Published As

Publication number Publication date
FR1069599A (en) 1954-07-09
NL79196C (en)
DE958019C (en) 1957-02-14
US2751280A (en) 1956-06-19
BE516816A (en)
CH313763A (en) 1956-05-15

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