US1719349A - Process for producing soap - Google Patents
Process for producing soap Download PDFInfo
- Publication number
- US1719349A US1719349A US119225A US11922526A US1719349A US 1719349 A US1719349 A US 1719349A US 119225 A US119225 A US 119225A US 11922526 A US11922526 A US 11922526A US 1719349 A US1719349 A US 1719349A
- Authority
- US
- United States
- Prior art keywords
- soap
- content
- soaps
- milling
- grain
- 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 - Lifetime
Links
- 239000000344 soap Substances 0.000 title description 28
- 238000000034 method Methods 0.000 title description 13
- 235000014113 dietary fatty acids Nutrition 0.000 description 12
- 239000000194 fatty acid Substances 0.000 description 12
- 229930195729 fatty acid Natural products 0.000 description 12
- 150000004665 fatty acids Chemical class 0.000 description 12
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 9
- 238000003801 milling Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 235000019197 fats Nutrition 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000007127 saponification reaction Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 235000013162 Cocos nucifera Nutrition 0.000 description 3
- 244000060011 Cocos nucifera Species 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 235000017550 sodium carbonate Nutrition 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical group OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 239000003346 palm kernel oil Substances 0.000 description 2
- 235000019865 palm kernel oil Nutrition 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 235000021588 free fatty acids Nutrition 0.000 description 1
- -1 hydro-naphthaline Chemical compound 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
Classifications
-
- 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
- C11D13/00—Making of soap or soap solutions in general; Apparatus therefor
- C11D13/02—Boiling soap; Refining
Definitions
- This invention relates to processes for producing soap and more particularly durable soaps made by the milling process that do not change through influences of the air or 2 weather.
- the only soaps that will meet these requirements are the soaps made by the milling process; they are formed or cut into strips by being passed through pairs of rolls and then pressed into cakes. These soaps will keep for practically any length of time because they have a high content of fatty acid and a low content ofwater.
- powdered soap has consisted hitherto in milling.
- liquid high grade grain soap is first solidified, and then cu't'into slices or rolled into bands so as to make it present as large a surface as possible in the ensuing drying process.
- this drying process has recently been greatly improved by the use of ingeniously designed devices it still requires an amount of heat,
- fat solvents such as hydrocarbon bodies, for example naphtha, kerosene, or benzol, hydro-naphthaline, hydro-phenol, carbon-tetraohloride or the like may be used in the first stage of saponification or mixed with grain soap or soap paste to obtain milled soaps with a content of fat solvents.
- Example 1 1000 kgs. of palm kernel oil fatty acid or cocoanut oil fatty acid, containing more than 99% of free fatty acid, are mixed with 360 kgs. of water-free sodium carbonate. This gives a uniform substance which saponifies after a while by spontaneous heatin Before the process of saponification is en ed and before the substance has completely solidified, 700 to 800 kgs. of liquid grain soap, made from tallow or bone fat, is added. By stirring or mixing these ingredients an almost homogeneous soap is obtained in a short time which after one hour can be milled in a milling machine into ribbons. These ribbons can be formed immediately, or after they have been stored for a short period, into bars by a plodder or compressor and then cut into cakes or tablets.
- I claim A a process for producing air-resisting moulded soap consisting in mixing commercial fatty acids at about their melting point with a quantity of alkali carbonate free from water, sufiicient to saponify up to twice the quantity of fatty acids present, and after saponification, admixing grain soap there with and thereupon subjecting the product thus obtained to the milling process.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Detergent Compositions (AREA)
Description
Patented July '2,
UNITED STATES PATENT OFFICE.
ADOLF WELTER, OF DKEIRINGWERKE, GERMANY.
ITROC ESS FOR PRODUCING SOAP.
This invention relates to processes for producing soap and more particularly durable soaps made by the milling process that do not change through influences of the air or 2 weather.
Efl'ortshave long been made to produce soaps that will keep indefinitely, that do not become unsightly when stored for long periods, whose weight does not change appreciably and which retain their original shape even in the tropics. The only soaps that will meet these requirements are the soaps made by the milling process; they are formed or cut into strips by being passed through pairs of rolls and then pressed into cakes. These soaps will keep for practically any length of time because they have a high content of fatty acid and a low content ofwater. Theonly known method of producing them, apart from the compressing of pure, non-hydrous,
powdered soap, has consisted hitherto in milling. In the milling process liquid high grade grain soap is first solidified, and then cu't'into slices or rolled into bands so as to make it present as large a surface as possible in the ensuing drying process. Although this drying process has recently been greatly improved by the use of ingeniously designed devices it still requires an amount of heat,
time and labor that is high in proportion to the value of the soap obtained. After the content of water has been reduced by this. known method to such an extent that the content offatty acid is about 80% the hard soap is capable of being milled. The highest content of water at which the milling is pos sible at all is about 14 to 15% (see Schrauth,
- Medikamentose Seifen 1914, page 30).
Inpractice it is, however, not advisable 1:0
s to the content of fatty acid this must not be lower than 75% and the most favorable content for milling is 7980%. Now I have found that, if the water in a hydrous soap is partly or completely substituted by bicarbonate of sodium, it is possible to make easily millable and durable soaps even if the content of fatty acid is as low as 60 to 75%. The only process known up to the present by which such soaps containing bicarbonate of sodium can be made cheaply consists in allowing fatty acids that are free of neutral Drawing. Application fileii June 2a, 1926, Serial is. 119,225, and in Germany m s, 1925.
most one molecule of soda is used the followmg equation will hold:
' RCOOH+Na,GO
RCOONa+NaHCO Now it has been found that, if fatty acids free of neutral fat as described are made to react on a maximum of one molecule of soda atabout the melting temperature of the fatty acids and liquid or solid grain soap or even soappaste is added before, or even after, the sapomfication is quite complete, a soap mixture is obtained which can be easily and perfectly milled and which has all the desirable properties such as durability, uniformity of composition, immutability of weight and shape. Quite contrary to expectation this millability of the soap mixture was found to exist even when its content of fatty acid dropped to 60%,"and even then rigorous conditions could be maintained in the method of operation and imposed on the quality of the final product. It is, therefore, possible to produce high grade or grain soaps in this manner whose composition corresponds to that of ordinary grain soapbut which greatly surpass it in respect to external appearance and durability. My novel process has, however, further advantages which will now be gone into.
It is well known that in milling grain soap the palm kernel or cocoanut oil content can only be up to 15% if 20% is exceeded trouble ensues when milling. My' aforedescribed process, however, makes it possible not only'to greatly increase the content of cocoanut or palm kernel oil, but it even renders it possible to use this oil alone, which is extremely important as far as the solubility, foam forming qualities and the utility of the soap in seawater is concerned.
It is to be particularly noted that the aforedescribed process supercedes by far all hitherto known processes in regard to economy and simplicity and that it enables a large production to be achieved even with a small plant. Just as important is the fact that it enables marketable, nice-looking soap to be made from the prepared fatty acids in one to two hours,- whereas the time re uired with known processes even with a per ect plant was several days. My novel process also enables a part of the soda to be replaced by crystallized sodium carbonate (washing soda) or by potash and permits of the use of resin. Furthermore fat solvents such as hydrocarbon bodies, for example naphtha, kerosene, or benzol, hydro-naphthaline, hydro-phenol, carbon-tetraohloride or the like may be used in the first stage of saponification or mixed with grain soap or soap paste to obtain milled soaps with a content of fat solvents.
Example 1. 1000 kgs. of palm kernel oil fatty acid or cocoanut oil fatty acid, containing more than 99% of free fatty acid, are mixed with 360 kgs. of water-free sodium carbonate. This gives a uniform substance which saponifies after a while by spontaneous heatin Before the process of saponification is en ed and before the substance has completely solidified, 700 to 800 kgs. of liquid grain soap, made from tallow or bone fat, is added. By stirring or mixing these ingredients an almost homogeneous soap is obtained in a short time which after one hour can be milled in a milling machine into ribbons. These ribbons can be formed immediately, or after they have been stored for a short period, into bars by a plodder or compressor and then cut into cakes or tablets.
Example 2.
substance is a thin liquid and perfectl .homogeneous. After a short while it becomes warm and hardens, its temperature rising to 60 to 65 C. The saponification is complete in a few hours and the substance is then soluble in distilled water at a temperaure of fectly uniform and whose exterior does not differ in the least from the usual fine soap ribbons. These ribbons can be easily plodded, cut, and pressed, and their durability is in no wise inferiorto that of the finest soaps.
I claim A a process for producing air-resisting moulded soap consisting in mixing commercial fatty acids at about their melting point with a quantity of alkali carbonate free from water, sufiicient to saponify up to twice the quantity of fatty acids present, and after saponification, admixing grain soap there with and thereupon subjecting the product thus obtained to the milling process.
In testimony whereof I have afiixed my signature.
ADOLF WELTER.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEW0069799 | 1925-07-03 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1719349A true US1719349A (en) | 1929-07-02 |
Family
ID=7608476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US119225A Expired - Lifetime US1719349A (en) | 1925-07-03 | 1926-06-28 | Process for producing soap |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US1719349A (en) |
| FR (1) | FR618958A (en) |
| GB (1) | GB254755A (en) |
| NL (1) | NL19680C (en) |
-
0
- NL NL19680D patent/NL19680C/xx active
-
1926
- 1926-06-28 US US119225A patent/US1719349A/en not_active Expired - Lifetime
- 1926-07-01 FR FR618958D patent/FR618958A/en not_active Expired
- 1926-07-05 GB GB16844/26A patent/GB254755A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| GB254755A (en) | 1927-10-05 |
| FR618958A (en) | 1927-03-24 |
| NL19680C (en) |
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