EP0451159A1 - Verfahren zum kontinuierlichen granulieren - Google Patents
Verfahren zum kontinuierlichen granulierenInfo
- Publication number
- EP0451159A1 EP0451159A1 EP89912447A EP89912447A EP0451159A1 EP 0451159 A1 EP0451159 A1 EP 0451159A1 EP 89912447 A EP89912447 A EP 89912447A EP 89912447 A EP89912447 A EP 89912447A EP 0451159 A1 EP0451159 A1 EP 0451159A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- gel
- liquid
- solid
- time
- tends
- 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 17
- 238000005469 granulation Methods 0.000 title claims abstract description 13
- 230000003179 granulation Effects 0.000 title claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 27
- 239000000203 mixture Substances 0.000 claims abstract description 12
- 230000003068 static effect Effects 0.000 claims abstract description 5
- 239000002994 raw material Substances 0.000 claims abstract description 3
- 239000007787 solid Substances 0.000 claims description 15
- 229910021536 Zeolite Inorganic materials 0.000 claims description 10
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 10
- 239000010457 zeolite Substances 0.000 claims description 10
- 239000000440 bentonite Substances 0.000 claims description 6
- 229910000278 bentonite Inorganic materials 0.000 claims description 6
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims description 6
- 239000002736 nonionic surfactant Substances 0.000 claims description 4
- 239000008247 solid mixture Substances 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 2
- 239000012265 solid product Substances 0.000 abstract 2
- 239000008187 granular material Substances 0.000 description 4
- 235000019353 potassium silicate Nutrition 0.000 description 4
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000001879 gelation Methods 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- -1 B. Wessalith P Chemical compound 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
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
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/02—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
- B01J2/06—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a liquid medium
- B01J2/08—Gelation of a colloidal solution
-
- 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
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
Definitions
- the invention relates to a process for the continuous granulation of a mixture containing at least one solid and at least one liquid which tends to form gel.
- Such granulation takes place e.g. B. in the manufacture of detergents.
- Such granules have hitherto been produced as follows: The liquid ingredients have been sprayed onto a granulated carrier produced by spray drying or incorporated into a pre-prepared recipe using a granulation process. Solid ingredients, on the other hand, were either made into a slurry and spray-dried or directly mixed in as a powder.
- the invention has for its object to provide a method of the type mentioned, which works with a gel-like intermediate phase and can be operated continuously.
- This object is achieved according to the invention in a process of the type mentioned at the outset that a mixture containing liquid raw materials which does not tend to gel alone is used as the liquid which tends to gel formation and which is produced in a static mixer, the mean residence time in this Mixer is shorter than the gelation time that the liquid is then allowed to gel in a stirred tank, the mean residence time in the stirred tank being longer than the gelation time, and only then is the highly viscous mass obtained granulated together with the solid.
- the static mixer essentially consists of a tubular one Channel in which individual swirling elements are permanently installed, and when the liquid flows through this tubular element, it is thoroughly mixed.
- this viscosity can be influenced by using a coolable or heatable stirred tank.
- No special pelletizer is required for the invention.
- All commercially available granulating devices including, for example, continuous moistening mixers) are suitable for practicing the invention.
- a ploughshare mixer is used for granulating.
- the gel is granulated immediately after it has entered the granulating device is chopped and then swirled with the solid. The initial chopping results in a small particle size very soon after the gel has entered the granulator. This keeps the mass in the granulator free-flowing and does not cake into a large lump.
- a mixture of nonionic surfactants and what containing or. water-releasing substances such as B. Water glass or zeolite suspension is used. It is also advantageous if spray-dried zeolite and / or a layered silicate, in particular bentonite or. Solid mixtures of preferably non-polar or a few polar substances are used.
- the gel is continuously introduced and granulated by the liquids supplied to the stirred tank in a free-flowing manner or with the appropriate metering elements in the granulating device for producing the granules together with metered solids.
- nonionic surfactant e.g. B. Dehydol LST
- 20 parts water glass solution e.g. B. Water glass N
- 40 to 60 parts of zeolite suspension used.
- 35 to 55 parts of the gel described and 65 to 45 parts of solids or solid mixtures are used to form the granules.
- These solids consist of spray dried zeolite, e.g. B. Wessalith P, resp. Bentonite, or a mixture of zeolite and bentonite. It can also be a mixture of 30 to 70 parts of zeolite, 10 to 40 parts of bentonite and 10 to 30 parts of soda. The proportions are variable. However, soda should not make up more than 30 parts in the solid mixture.
- a specific example discloses a gel composed of 2.0 parts of nonionic surfactant, 10 parts of water glass and 20 parts of zeolite suspension, to which 50 parts of spray-dried zeolite are added. This gives a bulk density of 840 g / l, which is easy to pour.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Dispersion Chemistry (AREA)
- Detergent Compositions (AREA)
- Glanulating (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Medicinal Preparation (AREA)
- Saccharide Compounds (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
- Housing For Livestock And Birds (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Farming Of Fish And Shellfish (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Colloid Chemistry (AREA)
- Jellies, Jams, And Syrups (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE3844025A DE3844025A1 (de) | 1988-12-27 | 1988-12-27 | Verfahren zum kontinuierlichen granulieren |
| DE3844025 | 1988-12-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP0451159A1 true EP0451159A1 (de) | 1991-10-16 |
Family
ID=6370352
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP89912447A Pending EP0451159A1 (de) | 1988-12-27 | 1989-10-12 | Verfahren zum kontinuierlichen granulieren |
| EP89118963A Expired - Lifetime EP0375858B1 (de) | 1988-12-27 | 1989-10-12 | Verfahren zum kontinuierlichen Granulieren |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP89118963A Expired - Lifetime EP0375858B1 (de) | 1988-12-27 | 1989-10-12 | Verfahren zum kontinuierlichen Granulieren |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US5188786A (da) |
| EP (2) | EP0451159A1 (da) |
| JP (1) | JPH04502423A (da) |
| KR (1) | KR970010330B1 (da) |
| AT (1) | ATE91088T1 (da) |
| DE (2) | DE3844025A1 (da) |
| DK (1) | DK96391D0 (da) |
| ES (1) | ES2057050T3 (da) |
| RU (1) | RU1836137C (da) |
| TR (1) | TR24022A (da) |
| WO (1) | WO1990007375A1 (da) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB9513327D0 (en) * | 1995-06-30 | 1995-09-06 | Uniliver Plc | Process for the production of a detergent composition |
| DE19533790A1 (de) * | 1995-09-13 | 1997-03-20 | Henkel Kgaa | Verfahren zur Herstellung eines amorphen Alkalisilikats mit Imprägnierung |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4059538A (en) * | 1972-10-20 | 1977-11-22 | Lever Brothers Company | Method for preparing granulated detergent formulations |
| GB8329880D0 (en) * | 1983-11-09 | 1983-12-14 | Unilever Plc | Particulate adjuncts |
| DE3617756C2 (de) * | 1985-05-29 | 1995-01-19 | Lion Corp | Verfahren zum Herstellen einer granularen Detergentien-Zusammensetzung mit hoher Schüttdichte |
| US4925585A (en) * | 1988-06-29 | 1990-05-15 | The Procter & Gamble Company | Detergent granules from cold dough using fine dispersion granulation |
-
1988
- 1988-12-27 DE DE3844025A patent/DE3844025A1/de not_active Withdrawn
-
1989
- 1989-10-12 JP JP1511554A patent/JPH04502423A/ja active Pending
- 1989-10-12 EP EP89912447A patent/EP0451159A1/de active Pending
- 1989-10-12 KR KR1019900701221A patent/KR970010330B1/ko not_active Expired - Lifetime
- 1989-10-12 ES ES89118963T patent/ES2057050T3/es not_active Expired - Lifetime
- 1989-10-12 WO PCT/EP1989/001205 patent/WO1990007375A1/de not_active Ceased
- 1989-10-12 AT AT89118963T patent/ATE91088T1/de not_active IP Right Cessation
- 1989-10-12 DE DE8989118963T patent/DE58904842D1/de not_active Expired - Fee Related
- 1989-10-12 EP EP89118963A patent/EP0375858B1/de not_active Expired - Lifetime
- 1989-10-12 US US07/720,468 patent/US5188786A/en not_active Expired - Fee Related
- 1989-11-08 TR TR89/0953A patent/TR24022A/xx unknown
-
1991
- 1991-05-22 DK DK91963A patent/DK96391D0/da not_active Application Discontinuation
- 1991-06-25 RU SU914895801A patent/RU1836137C/ru active
Non-Patent Citations (1)
| Title |
|---|
| See references of WO9007375A1 * |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0375858A1 (de) | 1990-07-04 |
| US5188786A (en) | 1993-02-23 |
| TR24022A (tr) | 1991-02-01 |
| DK96391A (da) | 1991-05-22 |
| DK96391D0 (da) | 1991-05-22 |
| EP0375858B1 (de) | 1993-06-30 |
| KR970010330B1 (ko) | 1997-06-25 |
| ATE91088T1 (de) | 1993-07-15 |
| JPH04502423A (ja) | 1992-05-07 |
| ES2057050T3 (es) | 1994-10-16 |
| KR900701385A (ko) | 1990-12-01 |
| DE3844025A1 (de) | 1990-06-28 |
| WO1990007375A1 (de) | 1990-07-12 |
| DE58904842D1 (de) | 1993-08-05 |
| RU1836137C (ru) | 1993-08-23 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
| 17P | Request for examination filed |
Effective date: 19910619 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE FR GB IT LI LU NL SE |
|
| XX | Miscellaneous (additional remarks) |
Free format text: VERFAHREN ABGESCHLOSSEN INFOLGE VERBINDUNG MIT 89118963.1/0375858 (EUROPAEISCHE ANMELDENUMMER/VEROEFFENTLICHUNGSNUMMER) VOM 08.11.91. |