GB2180835A - A method for the production of sodium stearate or magnesium stearate - Google Patents
A method for the production of sodium stearate or magnesium stearate Download PDFInfo
- Publication number
- GB2180835A GB2180835A GB08523739A GB8523739A GB2180835A GB 2180835 A GB2180835 A GB 2180835A GB 08523739 A GB08523739 A GB 08523739A GB 8523739 A GB8523739 A GB 8523739A GB 2180835 A GB2180835 A GB 2180835A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stearate
- sodium
- magnesium stearate
- magnesium
- sodium stearate
- 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.)
- Granted
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/41—Preparation of salts of carboxylic acids
- C07C51/412—Preparation of salts of carboxylic acids by conversion of the acids, their salts, esters or anhydrides with the same carboxylic acid part
Abstract
A method for the production of sodium stearate or magnesium stearate, which method comprises mixing sodium hydroxide and stearic acid, and magnesium nitrate only when the magnesium stearate is being prepared, causing the sodium stearate or the magnesium stearate to crystallise out, and obtaining the crystallised sodium stearate or the crystallised magnesium stearate.
Description
SPECIFICATION
A method for the production of sodium stearate or magnesium stearate
This invention relates to a method for the production of sodium stearate or magnesium stearate.
Sodium stearate and magnesium stearate are used in the coating of tablets. It is an aim of the present invention to provide a method of the production of the sodium stearate or the magnesium stearate, which method is simple and lends itself to bulk preparation of the sodium stearate or the magnesium stearate.
Accordingly, this invention provides a method for the production of sodium stearate or magnesium stearate, which method comprises mixing sodium hydroxide and stearic acid, and magnesium nitrate only when the magnesium stearate is being prepared, causing the sodium stearate or the magnesium stearate to crystallise out, and obtaining the crystallised sodium stearate or the crystallised magnesium stearate.
Preferably, the method is one in which the sodium hydroxide is in the form of sodium hydroxide pellets, and in which the sodium hydroxide pellets are dissolved in a solvent prior to admixture with the stearic acid.
The solvent is preferably a mixture of rectified spirits and toluene. The mixture of rectified spirits and toluene may be in equal mixtures by volume, and such an equal volume mixture solvent is available commercially under the trade mark Kensol. Other solvents may be employed if desired.
Usually, the magnesium nitrate will be magnesium nitrate hexahydrate.
The sodium stearate may be caused to crystallise out by cooling the mixture of sodium hydroxide and stearic acid to 35-40"C, seeding the cooled mixture with powdered crystalline sodium stearate, cooling the seeded mixture to ambient temperature, and chilling the cooled mixture to cause the sodium stearate to crystallise out.
The magnesium stearate may be caused to crystallise out by cooling the mixture of sodium hydroxide, stearic acid and magnesium nitrate to ambient temperature.
The crystallised sodium stearate or the crystallised magnesium stearate may be obtained by filtering.
The filtering will usually be effected using suction.
The filtered sodium stearate or magnesium stearate may be dried with hot air or, alternatively, air dried and then further dried in an open oven.
The present invention also provides the sodium stearate or the magnesium stearate when produced by the method of the invention.
The present invention also provides tablets whenever coated with the sodium stearate or the magnesium stearate produced by the method of the invention.
In order to facilitate a full understanding of the present invention, reference will now be made to the following Examples.
EXAMPLE I
PREPARATION OF SODIUM STEARATE RA W MA TERIALS: 1. Sodium Hydroxide pellets 98%.
2. Stearic Acid 96% mp 69"-710C.
3. "Kensol" solvent. This is made from equal mixtures v/v of rectified spirits and toluene 99%. The Kensol solvent boils at 72"C, its wt. per ml. is 0.83g, and it dissolves plastics.
4. Thermolyne Type 1000 stir plate.
PRODUCTION:
Place 9.0g sodium hydroxide pellets into a 5 litre beaker. Add 4.5 litres of Kensol solvent.
Warm slowly with stirring on the stir plate until the temperature reaches 50"C (15 minutes). Switch off the heater and continue stirring until the pellets dissolve completely (10 minutes). The temperature should stay below 65"C. The solution will become slightly turbid.
Add 64.0g of stearic acid in a siow stream and continue stirring. Some bubbling will occur. Continue stirring for about 2 minutes.
Turbidity disappears and the solution becomes clear.
Remove the beaker from the heater and allow to stand for 5 minutes. A small amount of particulate matter settles. Decant slowly into a 7 litre steel beaker containing 2.5 litres of Kensol so as to leave the particulate matter behind.
Allow to cool to 35 -40 C. Seed liberally with powdered crystalline sodium stearate and allow to cool to ambient. Chill overnight at -5"C. Sodium stearate crystallises out.
Filter with suction on a 33cm diameter bench top porcelain buchner using a 32cm filter paper and drain as dry as possible. Dry the product by passing hot air through it. Alternatively, allow to dry in the air on filter paper or other porous material and then in an open oven at 45"C. Kensol vapours may ignite in a closed oven. Finally, dry to constant weight at 105"C.
The dry product is in the form of shiny plates. The solvent is re-used for the next run, and may be re-used ten times before purification by distillation. The following yields were obtained in four consecutive runs: 82.7%, 85.7%, 94.6%, 96.2%. Minimum purity is 99%. The dry product may be milled to the desired particle size.
All operations with Kensol solvent should be carried out under a fume hood.
EXAMPLE II
PREPARATION OF MAGNESIUM STEARATE RA W MA TERIALS: 1. Sodium Hydroxide pellets 98%.
2. Stearic Acid 96% m.p. 69"-71"C.
3. Magnesium nitrate hexahydrate 99%.
4. Kensol solvent.
PRODUCTION:
Place 20.09 sodium hydroxide pellets in a 5 litre beaker. Add 3.5 litres of Kensol solvent.
Warm slowly on a stir plate until the temperature reaches 45"C. Switch off the heater and continue stirring until the pellets dissolve completely. The temperature will now have risen to 62 C.
Add 142.29. of stearic acid and stir until it dissolves. The temperature falls to 60"C.
At 60"C, add 64.0g. of magnesium nitrate hexahydrate and continue stirring until it dissolves. The solution goes turbid. Stir for 3 minutes more, remove from the stir plate and cool the solution overnight at room temperature. Magnesium stearate crystallises out.
Filter using the same apparatus as with the sodium stearate described above in Example I, but with the filter plate wrapped up with nylon cloth over the filter paper. Wash the product twice with 96% ethanol and then several times with water until it is free from sodium nitrate. The nylon cloth aids in the washing because it does not tear.
Dry initially at 60 then to constant weight at 105"C. The yield is over 99%.
All operations with Kensol solvent should be carried out under a fume hood.
It is to be appreciated that the embodiments of the invention described above in the
Examples have been given for illustrative purposes only and modifications may be effected.
In particular, it will be appreciated that the described production methods in the Examples will be scaled up for commercial bulk production.
Claims (14)
1. A method for the production of sodium stearate or magnesium stearate, which method comprises mixing sodium hydroxide and stearic acid, and magnesium nitrate only when the magnesium stearate is being prepared, causing the sodium stearate or the magnesium stearate to crystallise out, and obtaining the crystallised sodium stearate or the crystallised magnesium stearate.
2. A method according to Claim lin which the sodium hydroxide is in the form of sodium hydroxide pellets, and in which the sodium hydroxide pellets are dissolved in a solvent prior to admixture with the stearic acid.
3. A method according to Claim 2 in which the solvent is a mixture of rectified spirits and toluene.
4. A method according to Claim 3 in which the mixture of rectified spirits and toluene is in equal mixtures by volume.
5. A method according to any one of the preceeding Claims in which the magnesium nitrate is magnesium nitrate hexahydrate.
6. A method according to any one of the preceeding Claims in which the sodium stearate is caused to crystallise out by cooling the mixture of sodium hydroxide and stearic acid to 35-4O0C, seeding the cooled mixture with powdered crystalline sodium stearate, cooling the seeded mixture to ambient temperature, and chilling the cooled mixture to cause the sodium stearate to crystallise out.
7. A method according to any one of
Claims 1-5 in which the magnesium stearate is caused to crystallise out by cooling the mixture of sodium hydroxide, stearic acid and magnesium nitrate to ambient temperature.
8. A method according to any one of the preceeding Claims in which the crystallised sodium stearate or the crystallised magnesium stearate is obtained by filtering.
9. A method according to Claim 8 in which the filtering is effected using suction.
10. A method according to Claim 8 or
Claim 9 in which the filtered sodium stearate or magnesium stearate is dried with hot air.
11. A method according to Claim 8 or
Claim 9 in which the filtered sodium stearate or magnesium stearate is air dried and then further dried in an open oven.
12. A method for the production of sodium stearate or magnesium stearate, substantially as herein described with reference to the examples.
13. Sodium stearate or magnesium stearate when produced by a method as claimed in any one of the preceeding Claims.
14. Tablets whenever coated with sodium stearate or magnesium stearate produced by the method claimed in any one of Claims 1-12.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8523739A GB2180835B (en) | 1985-09-26 | 1985-09-26 | A method for the preparation of sodium and magnesium stearate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8523739A GB2180835B (en) | 1985-09-26 | 1985-09-26 | A method for the preparation of sodium and magnesium stearate |
Publications (3)
Publication Number | Publication Date |
---|---|
GB8523739D0 GB8523739D0 (en) | 1985-10-30 |
GB2180835A true GB2180835A (en) | 1987-04-08 |
GB2180835B GB2180835B (en) | 1989-10-18 |
Family
ID=10585746
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8523739A Expired GB2180835B (en) | 1985-09-26 | 1985-09-26 | A method for the preparation of sodium and magnesium stearate |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB2180835B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100391927C (en) * | 2005-10-28 | 2008-06-04 | 天津理工大学 | Method for synthesizing ferrous stearate |
CN106187745A (en) * | 2016-07-29 | 2016-12-07 | 温州吉象化学股份有限公司 | A kind of sodium stearate and continuous production technology thereof and production line |
CN110028401A (en) * | 2019-05-29 | 2019-07-19 | 连云港华明泰材料科技有限公司 | A kind of preparation method and application of plant acid rouge magnesium stearate |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB674164A (en) * | 1949-01-26 | 1952-06-18 | George Judson Chertoff | Heat stabilizer for vinyl resins |
GB1397020A (en) * | 1972-06-14 | 1975-06-11 | Merck & Co Inc | Aluminium monostearate |
GB1573367A (en) * | 1976-08-31 | 1980-08-20 | Tenneco Chem | Production of metal salts of organic acids |
-
1985
- 1985-09-26 GB GB8523739A patent/GB2180835B/en not_active Expired
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB674164A (en) * | 1949-01-26 | 1952-06-18 | George Judson Chertoff | Heat stabilizer for vinyl resins |
GB1397020A (en) * | 1972-06-14 | 1975-06-11 | Merck & Co Inc | Aluminium monostearate |
GB1573367A (en) * | 1976-08-31 | 1980-08-20 | Tenneco Chem | Production of metal salts of organic acids |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100391927C (en) * | 2005-10-28 | 2008-06-04 | 天津理工大学 | Method for synthesizing ferrous stearate |
CN106187745A (en) * | 2016-07-29 | 2016-12-07 | 温州吉象化学股份有限公司 | A kind of sodium stearate and continuous production technology thereof and production line |
CN106187745B (en) * | 2016-07-29 | 2019-02-12 | 温州吉象化学股份有限公司 | A kind of odium stearate and its continuous production technology and production line |
CN110028401A (en) * | 2019-05-29 | 2019-07-19 | 连云港华明泰材料科技有限公司 | A kind of preparation method and application of plant acid rouge magnesium stearate |
Also Published As
Publication number | Publication date |
---|---|
GB2180835B (en) | 1989-10-18 |
GB8523739D0 (en) | 1985-10-30 |
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Legal Events
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PCNP | Patent ceased through non-payment of renewal fee |