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 processesInfo
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J49/00—Regeneration or reactivation of ion-exchangers; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J47/00—Ion-exchange processes in general; Apparatus therefor
- B01J47/02—Column or bed processes
- B01J47/026—Column 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.
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)
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)
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 |
-
0
- BE BE516816D patent/BE516816A/xx unknown
- NL NL79196D patent/NL79196C/xx active
-
1953
- 1953-01-08 DE DEST5821A patent/DE958019C/en not_active Expired
- 1953-01-13 CH CH313763D patent/CH313763A/en unknown
- 1953-01-15 US US331473A patent/US2751280A/en not_active Expired - Lifetime
- 1953-01-15 GB GB1284/53A patent/GB725660A/en not_active Expired
- 1953-01-16 FR FR1069599D patent/FR1069599A/en not_active Expired
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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