US424991A - Simultaneous manufacture of soap and carbonic acid - Google Patents
Simultaneous manufacture of soap and carbonic acid Download PDFInfo
- Publication number
- US424991A US424991A US424991DA US424991A US 424991 A US424991 A US 424991A US 424991D A US424991D A US 424991DA US 424991 A US424991 A US 424991A
- Authority
- US
- United States
- Prior art keywords
- soap
- carbonic acid
- digester
- simultaneous manufacture
- bicarbonate
- 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 26
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 title description 18
- 238000004519 manufacturing process Methods 0.000 title description 12
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 28
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 16
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 14
- 238000000034 method Methods 0.000 description 12
- 239000000203 mixture Substances 0.000 description 8
- 150000007524 organic acids Chemical class 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- UIIMBOGNXHQVGW-UHFFFAOYSA-M NaHCO3 Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 4
- 241000220317 Rosa Species 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000002238 attenuated Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
Images
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
- Figure 1 is a sectional elevation .of my apparatus, and Fig. 2 is a plan view of the distributing steam-pipe or rose.
- My invention consists of the process hereinafter described for making soap from alkaline, bicarbonate, or carbonate, preferably from bicarbonate of sodium, and at the same time utilizing the carbonic acid thus formed either for the carbonation of soap-lyes or for any other purpose.
- rosin For the manufacture of soap from carbonate or bicorbonate of soda or any other alkali rosin free fatty acids or any organic acids capable of forming a soap may be used. I prefer to use rosin, and proceed in the following manner:
- the bicarbonate of soda or other alkaline bicarbonate or carbonate is introduced into a cylindrical iron tank or reservoir A, which I term a digester, eitherin solution in water or as a solid and water added.
- the rosin is then introduced, and the mixture is gently warmed by allowing steam to spray through it, the steam being admitted through the pipe 0 and the perforated rose 0'.
- the steam as it circulates through the mixture causes the rosin to act upon thebicarbonate of sodium, setting free carbonic acid, a rosin soap being left in solution.
- the soap is then salted out from this solution, when the action is complete, or the solution may be mixedwith awater solution of a common soap, if preferable, the soap bein drawn off from the digester through the faucet D, communicating with the interior of the digester at some distance from the bottom thereof.
- the carbonic acid formed by the action accumulates in the upper part of the digester and is removed therefrom as fast as formed through the outlet-pipe B by means of a suitable pump or blower L, of any ap proved construction, connected with the pipe B, and the gas is thus conveyed to wherever it is desired to use it.
- the chemical action would naturally become so strong were it not for the balanced regulating-valve B as to cause violent frothing of the liquid in the digester, resulting in the pumping out of a part of the liquid, together with the gas.
- the balanced valve B which opens inward, is adjusted to open by reason ofthe difference in pressure and let in at times just enough atmospheric air from the outside to prevent the air within from becoming so attenuated as to produce the frothing action, as above explained, thus acting as an automatic regulator.
- the safety-valve G acts in the usual manner to allow the gas to escape should the pressure within the digester become too great.
- the lye is drawn off from the digester through the outlet-tap E at the bottom, while at the top of the tank is the opening A, which serves as a man-hole and as a means for introducing the various ingredients into the digester.
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- 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
(No Model.)
E. D. MELLBN. SIMULTANEOUS MANUFAOTURE 0F SOAP AND GARBONIG AGID. No. 424,991. I Patented Apr. 8,1890.
2 B, B B 3 F F J E Wz'ines sea W 9 VfWW- UNITED STATES PATENT OFFICE.
EDIVIN D. MELLEN, OF CAMBRIDGE, MASSACHUSETTS.
SIMULTANEOUS MANUFACTURE or SOAP AND CARBONIC ACID.
SPECIFICATION forming part of Letters Patent No. 424,991, dated April 8, 1890. Application filed September 20, 1889. Serial No. 324,543. (No model.)
To all whom it may concern.-
Be it known that I, EDWIN D. MELLEN, a citizen of the United States, residing at Cambridge, in the county of Middlesex and Commonwealth of Massachusetts, have invented a certain new and Improved Process for the Simultaneous Manufacture of Soap and Carbonic Acid from Alkaline Bicarbonate or Oarbonate, of which the following is a full specification, reference being made to the accompanying drawings, forming a part thereof.
Figure 1 is a sectional elevation .of my apparatus, and Fig. 2 is a plan view of the distributing steam-pipe or rose.
My invention consists of the process hereinafter described for making soap from alkaline, bicarbonate, or carbonate, preferably from bicarbonate of sodium, and at the same time utilizing the carbonic acid thus formed either for the carbonation of soap-lyes or for any other purpose.
For the manufacture of soap from carbonate or bicorbonate of soda or any other alkali rosin free fatty acids or any organic acids capable of forming a soap may be used. I prefer to use rosin, and proceed in the following manner:
The bicarbonate of soda or other alkaline bicarbonate or carbonate is introduced into a cylindrical iron tank or reservoir A, which I term a digester, eitherin solution in water or as a solid and water added. The rosin is then introduced, and the mixture is gently warmed by allowing steam to spray through it, the steam being admitted through the pipe 0 and the perforated rose 0'. The steam as it circulates through the mixture causes the rosin to act upon thebicarbonate of sodium, setting free carbonic acid, a rosin soap being left in solution. The soap is then salted out from this solution, when the action is complete, or the solution may be mixedwith awater solution of a common soap, if preferable, the soap bein drawn off from the digester through the faucet D, communicating with the interior of the digester at some distance from the bottom thereof. The carbonic acid formed by the action accumulates in the upper part of the digester and is removed therefrom as fast as formed through the outlet-pipe B by means of a suitable pump or blower L, of any ap proved construction, connected with the pipe B, and the gas is thus conveyed to wherever it is desired to use it.
I preferably use this process in. connection with my improved process for the recovery of alkali and glycerine in soap-lye, for which I have applied for United States Letters Patent, the serial number of which application is 324,544, in which the gas is pumped into a tower, as therein described, and used for the saturation of soap-lyes therein contained.
Owing to the tendency to a continual vacuum maintained within the digester by the action of the pump or blower L, the chemical action would naturally become so strong were it not for the balanced regulating-valve B as to cause violent frothing of the liquid in the digester, resulting in the pumping out of a part of the liquid, together with the gas. In order to prevent this frothing from taking place, the balanced valve B which opens inward, is adjusted to open by reason ofthe difference in pressure and let in at times just enough atmospheric air from the outside to prevent the air within from becoming so attenuated as to produce the frothing action, as above explained, thus acting as an automatic regulator.
The safety-valve G acts in the usual manner to allow the gas to escape should the pressure within the digester become too great. The lye is drawn off from the digester through the outlet-tap E at the bottom, while at the top of the tank is the opening A, which serves as a man-hole and as a means for introducing the various ingredients into the digester.
I claim 1. The herein-described process for the simultaneous manufacture of soap and carbonic acid from alkaline carbonate or bicarbonate, the same consisting of mixing the said carbonate or bicarbonate with rosin or any suitable organic acid in a digester provided with suitable means both for regulating the chemical action and for withdrawing the gas and spraying the mixture with fine jets of steam, substantially as described.
2. The herein-described process for the si inultaneous manufacture of soap and carbonic acid from alkaline carbonate or bicarbonate, the same consisting of mixing the said carbonate or bicarbonate with rosin or anysuitable organic acid in a digester provided with pressure -regulating devices whereby the chemical action is controlled, spraying the mixture with fine jets of steam, and removing hand.
EDWIN D. MELLEN. Witnesses:
W. B. H. DoWsE, ALBERT E. LEACH.
Publications (1)
Publication Number | Publication Date |
---|---|
US424991A true US424991A (en) | 1890-04-08 |
Family
ID=2493905
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US424991D Expired - Lifetime US424991A (en) | Simultaneous manufacture of soap and carbonic acid |
Country Status (1)
Country | Link |
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US (1) | US424991A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2855391A (en) * | 1956-10-12 | 1958-10-07 | American Cyanamid Co | Manufacture of dry rosin size |
US2964472A (en) * | 1955-11-08 | 1960-12-13 | Pennsalt Chemicals Corp | Metal forming lubricant and method of making same |
-
0
- US US424991D patent/US424991A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2964472A (en) * | 1955-11-08 | 1960-12-13 | Pennsalt Chemicals Corp | Metal forming lubricant and method of making same |
US2855391A (en) * | 1956-10-12 | 1958-10-07 | American Cyanamid Co | Manufacture of dry rosin size |
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