AU3802300A - Method for controlling crystal size during continuous mass crystallisation - Google Patents
Method for controlling crystal size during continuous mass crystallisationInfo
- Publication number
- AU3802300A AU3802300A AU38023/00A AU3802300A AU3802300A AU 3802300 A AU3802300 A AU 3802300A AU 38023/00 A AU38023/00 A AU 38023/00A AU 3802300 A AU3802300 A AU 3802300A AU 3802300 A AU3802300 A AU 3802300A
- Authority
- AU
- Australia
- Prior art keywords
- crystallisation
- grain size
- product
- seed
- seed product
- 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.)
- Abandoned
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/24—Sulfates of ammonium
- C01C1/248—Preventing coalescing or controlling form or size of the crystals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0018—Evaporation of components of the mixture to be separated
- B01D9/0022—Evaporation of components of the mixture to be separated by reducing pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0036—Crystallisation on to a bed of product crystals; Seeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/005—Selection of auxiliary, e.g. for control of crystallisation nuclei, of crystal growth, of adherence to walls; Arrangements for introduction thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0059—General arrangements of crystallisation plant, e.g. flow sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0063—Control or regulation
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Fertilizers (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fodder In General (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Peptides Or Proteins (AREA)
Abstract
The invention relates to a method for controlling the crystal size during continuous mass crystallisation, especially with ammonium sulphate. According to said method, seed products are added, the seed product being produced independently of the current crystallisation process in terms of its parameters. The average grain size of the solid form of the seed product is 0.1 to 1.0 mm and is smaller than that of the desired crstallisate. The solid form of the seed product is produced from different technological sub-streams in the given grain size range, independently of the main crystallisation process. The temperature of the seed product when it is added is up to 40 DEG C, preferably 10 to 30 DEG C lower than the process temperature in the crystalliser and all other materials that are supplied or returned to the crystalliser are free of solids. By controlling the parameters of the seed product it is possible to influence the grain size distribution of the end product and significantly reduce the fluctuations in the distribution of the grain size of the end product. The method can be carried out with discontinuous or continuous addition of the seed product.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19912699A DE19912699A1 (en) | 1999-03-20 | 1999-03-20 | Method for controlling crystal size in continuous mass crystallization |
DE19912699 | 1999-03-20 | ||
PCT/DE2000/000747 WO2000056416A1 (en) | 1999-03-20 | 2000-03-09 | Method for controlling crystal size during continuous mass crystallisation |
Publications (1)
Publication Number | Publication Date |
---|---|
AU3802300A true AU3802300A (en) | 2000-10-09 |
Family
ID=7901840
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU38023/00A Abandoned AU3802300A (en) | 1999-03-20 | 2000-03-09 | Method for controlling crystal size during continuous mass crystallisation |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP1165198B1 (en) |
KR (1) | KR100592155B1 (en) |
AT (1) | ATE397481T1 (en) |
AU (1) | AU3802300A (en) |
CO (1) | CO5231207A1 (en) |
DE (3) | DE19912699A1 (en) |
ES (1) | ES2307499T3 (en) |
TW (1) | TWI250892B (en) |
WO (1) | WO2000056416A1 (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6657073B1 (en) | 1999-08-18 | 2003-12-02 | Daesang Corporation | Crystallization of α-L-aspartyl-L-phenylalanine methyl ester |
DE10026619A1 (en) * | 2000-05-29 | 2001-12-06 | Basf Ag | Device for the production of crystals |
WO2009077346A1 (en) * | 2007-12-14 | 2009-06-25 | Gea Messo Gmbh | Method and device for producing a coarse-grained ammonium sulfate product crystallisate |
DE102008007154B4 (en) * | 2008-02-01 | 2014-03-20 | Gea Messo Gmbh | Process for the preparation of a coarse ammonium sulfate product by crystallization |
DE102008007155B4 (en) | 2008-02-01 | 2014-04-30 | Gea Messo Gmbh | A method and apparatus for the continuous production of a coarse crystalline ammonium sulfate product |
DE102008029050A1 (en) | 2008-06-18 | 2009-12-24 | Gea Messo Gmbh | Process and apparatus for the continuous production of a crystallizate with constant particle size distribution |
DE102008059754A1 (en) * | 2008-12-01 | 2010-06-02 | Gea Messo Gmbh | Process for producing a coarse ammonium sulphate product |
DE102012101702B4 (en) | 2012-03-01 | 2017-10-05 | Gea Messo Gmbh | Process for the preparation of a coarse ammonium sulphate product by crystallisation and plant for carrying out the process |
WO2014040858A1 (en) * | 2012-09-11 | 2014-03-20 | Dsm Ip Assets B.V. | Process for initiating an ammonium sulfate crystallization process |
CN105197962A (en) * | 2015-09-30 | 2015-12-30 | 芜湖新兴铸管有限责任公司 | Ammonium sulfate crystallization equipment |
CN111408157B (en) * | 2020-04-14 | 2021-09-14 | 中石化南京工程有限公司 | Ammonium sulfate crystallization method and device thereof |
CN115520879B (en) * | 2021-06-24 | 2024-03-26 | 中国石油化工股份有限公司 | Method and device for continuously preparing granular ammonium sulfate by heterogeneous seed crystal |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1597729A (en) * | 1968-12-06 | 1970-06-29 | ||
GB1329316A (en) * | 1970-12-08 | 1973-09-05 | Kerr Mc Gee Chem Corp | Process for automatic control of crystal size distribution |
DE2320601A1 (en) * | 1973-04-24 | 1975-03-13 | Kramer Oskar Ernst Dipl Ing Ch | Rotating tube continuous crystalliser - with counter current flow between crystals and mother liquor, and with seeding |
FR2374067A1 (en) * | 1976-12-14 | 1978-07-13 | Fives Cail Babcock | PROCESS AND PLANT FOR THE PRODUCTION OF SELECTED CRYSTALLIZING GERM, APPLICABLE TO DISCONTINUOUS OR CONTINUOUS CRYSTALLIZING APPARATUS, PARTICULARLY FOR LOW SWEET PRODUCTS |
ES2015589B3 (en) * | 1986-08-01 | 1990-09-01 | Fives-Cail Babcock Soc Anonyme | PROCEDURE AND INSTALLATION FOR THE PRODUCTION OF A SEED MAGMA FOR A CONTINUOUS CRYSTALLIZATION APPARATUS. |
WO1993019826A1 (en) * | 1992-03-27 | 1993-10-14 | Allied-Signal Inc. | Process for crystallization in a draft tube baffle crystallizer |
-
1999
- 1999-03-20 DE DE19912699A patent/DE19912699A1/en not_active Withdrawn
-
2000
- 2000-03-09 KR KR1020017011994A patent/KR100592155B1/en not_active IP Right Cessation
- 2000-03-09 AT AT00916803T patent/ATE397481T1/en not_active IP Right Cessation
- 2000-03-09 AU AU38023/00A patent/AU3802300A/en not_active Abandoned
- 2000-03-09 DE DE10080665T patent/DE10080665B4/en not_active Expired - Lifetime
- 2000-03-09 DE DE50015193T patent/DE50015193D1/en not_active Expired - Lifetime
- 2000-03-09 ES ES00916803T patent/ES2307499T3/en not_active Expired - Lifetime
- 2000-03-09 WO PCT/DE2000/000747 patent/WO2000056416A1/en active IP Right Grant
- 2000-03-09 EP EP00916803A patent/EP1165198B1/en not_active Revoked
- 2000-03-17 TW TW089104870A patent/TWI250892B/en active
- 2000-03-17 CO CO00019717A patent/CO5231207A1/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
DE10080665D2 (en) | 2002-10-31 |
TWI250892B (en) | 2006-03-11 |
KR100592155B1 (en) | 2006-06-23 |
EP1165198B1 (en) | 2008-06-04 |
DE19912699A1 (en) | 2000-09-28 |
DE10080665B4 (en) | 2009-04-30 |
WO2000056416A1 (en) | 2000-09-28 |
KR20020003214A (en) | 2002-01-10 |
CO5231207A1 (en) | 2002-12-27 |
EP1165198A1 (en) | 2002-01-02 |
ES2307499T3 (en) | 2008-12-01 |
ATE397481T1 (en) | 2008-06-15 |
DE50015193D1 (en) | 2008-07-17 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MK6 | Application lapsed section 142(2)(f)/reg. 8.3(3) - pct applic. not entering national phase |