US2172265A - Preparation of saponins - Google Patents
Preparation of saponins Download PDFInfo
- Publication number
- US2172265A US2172265A US138006A US13800637A US2172265A US 2172265 A US2172265 A US 2172265A US 138006 A US138006 A US 138006A US 13800637 A US13800637 A US 13800637A US 2172265 A US2172265 A US 2172265A
- Authority
- US
- United States
- Prior art keywords
- solvent
- saponin
- saponins
- extraction
- alcohol
- 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
- 229930182490 saponin Natural products 0.000 title description 30
- 150000007949 saponins Chemical class 0.000 title description 30
- 235000017709 saponins Nutrition 0.000 title description 30
- 238000002360 preparation method Methods 0.000 title description 3
- 238000000034 method Methods 0.000 description 22
- 239000002904 solvent Substances 0.000 description 20
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 18
- 235000013311 vegetables Nutrition 0.000 description 14
- 238000000605 extraction Methods 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000003513 alkali Substances 0.000 description 9
- 241001454523 Quillaja saponaria Species 0.000 description 8
- 235000009001 Quillaja saponaria Nutrition 0.000 description 8
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N methanol Natural products OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 150000001875 compounds Chemical class 0.000 description 6
- 239000003960 organic solvent Substances 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 241000219287 Saponaria Species 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000002244 precipitate Substances 0.000 description 5
- 230000001376 precipitating effect Effects 0.000 description 5
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 235000019441 ethanol Nutrition 0.000 description 4
- 150000002484 inorganic compounds Chemical class 0.000 description 4
- 229910010272 inorganic material Inorganic materials 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical group OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000000706 filtrate Substances 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- XXROGKLTLUQVRX-UHFFFAOYSA-N allyl alcohol Chemical compound OCC=C XXROGKLTLUQVRX-UHFFFAOYSA-N 0.000 description 2
- 239000000908 ammonium hydroxide Substances 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- 229920001864 tannin Polymers 0.000 description 2
- 239000001648 tannin Substances 0.000 description 2
- 235000018553 tannin Nutrition 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- SZIFAVKTNFCBPC-UHFFFAOYSA-N 2-chloroethanol Chemical compound OCCCl SZIFAVKTNFCBPC-UHFFFAOYSA-N 0.000 description 1
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 description 1
- 239000004348 Glyceryl diacetate Substances 0.000 description 1
- 241000362909 Smilax <beetle> Species 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 235000019445 benzyl alcohol Nutrition 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- HPNMFZURTQLUMO-UHFFFAOYSA-N diethylamine Chemical compound CCNCC HPNMFZURTQLUMO-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 235000019443 glyceryl diacetate Nutrition 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 150000007529 inorganic bases Chemical class 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 229940032007 methylethyl ketone Drugs 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 239000013557 residual solvent Substances 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 239000004328 sodium tetraborate Substances 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
- 229910000406 trisodium phosphate Inorganic materials 0.000 description 1
- 235000019801 trisodium phosphate Nutrition 0.000 description 1
- 229960004418 trolamine Drugs 0.000 description 1
- 239000005418 vegetable material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H15/00—Compounds containing hydrocarbon or substituted hydrocarbon radicals directly attached to hetero atoms of saccharide radicals
- C07H15/20—Carbocyclic rings
- C07H15/24—Condensed ring systems having three or more rings
- C07H15/256—Polyterpene radicals
Definitions
- This invention relates to the extraction of saponins from vegetable matter.
- This invention has for its object to overcome the above difficulties. Another object it to provide a process whereby saponins may be prepared in improved 'form by means. of a simple solvent extraction process, A further object is to provide an improved process for extracting saponins from vegetable matter by means of an organic solvent. Other objects will appear hereinafter. These and other objects are accomplished by the herein described invention which comprises' extracting a saponin fromvegetable matter by means of an organic solvent while in the presence of a compound having an alkaline reaction.
- Material to be extracted such as soap bark
- an organic solvent while in the' presence of an alkaline compound. Contact between the substance extracted and the solvent.
- the two components may be brought about in conventional, solvent extraction apparatus or the two components may merely be placed in a container and allowed to' soak for a period of time, such as over night.
- the soaking procedure is preferred, since it results in a better recovery of the desired constituent. Repeated extraction with successive plete the recovery.
- the alkali may be added to the solvent before it is contacted with the vegetable matter. This procedure is preferred since the alkali is present during the entire period of extraction. Equivalent procedure would be to add the alkali to the vegetable matter prior to the, addition of the solvent.
- the solvent may be added to the vegetable matter and the alkali added subsequently, but extraction of coloring matter and tannin will take place until the alkali has been added.
- the amount of alkali used can be varied greatly without materially affecting the extraction process. Proportions of between .1 to 20% of alkaline compound based on the amount of solvent used are generally most useful, and amounts of between 1 and are preferred. With strong alkali proportions in the lower portion of the range mentioned are best while with weaker bases the higher concentrations are more useful. 5 Any substance having an alkaline reaction, such as sodium hydroxide, ammonia, ammonium hydroxide, borax, trisodium phosphate, methyl amine (33% in water), diethyl amine, triethanol amine, etc. may be used. 1
- the mixture may be heated to boiling temperature and the solvent then separated and filtered to remove suspended vegetable matter.
- a hot or boiling solvent may be used.
- the extract or filtrates from the successive extractions are preferably combined and are then treated by any one of a number of different methods to recover the dissolved saponin.
- One method of recovery is to completely or partially remove the solvent by evaporation or distillation, preferably under reduced pressure.
- the evaporation may be continued to dryness, butit is desirable to proceed only to a point where a precipitate-first forms.
- This first precipitate is often of a resinous nature and may be undesirable, in which case, it is removed from the hot solution by filtration.
- Super cooling may be 36 employed to increase the precipitation.
- the solubility of the saponin in the solvent is such that cooling does not cause much, if any precipitation.
- a precipitating agent is added.
- the precipitating 40 agent should be one which is soluble in the particular solvent containing the saponins but which has little or no solvent action for the saponins.
- the temperature of the solution at the time of addition of the .precipitating agent has a marked 5 effect on the physical properties of the saponin precipitated. Precipitationfrom a cold solution produces a finely divided precipitate, while that obtained from a hot solution is granular.
- the I former dries to a chalky mass, while the latter dies .to a resinous mass.
- the precipitated saponins are separated from the residual solvent by filtration and dried. If desired,- they may be washed with one of the precipitating agents, prior to the drying step.
- the saponin is .dried either in air or, when an especially light colored product is desired, drying in theabsence 01- air, such as in the presence or an inert atmosphere or in vacuo, is recommended.
- inert gases such as carbon dioxide, nitrogen, or vapors of solvents, such as carbon tetrachloride, may be employed.
- the product may be ground to fine powder if desired and is ready for immediate use,
- the extraction of the saponin from the vegetable matter can or a mixture of a large number of organic sumbles for the saponin.
- a preferred type of solvent is a low molecular weight aliphatic alcohol, such as methyl or ethyl alcohol, but other solvents,
- glycerine such as glycerine, ethylene glycol, allyl alcohol, iurfuryl alcohol, benzyl alcohol, diacetin, pyridine and ethylene chlorohydrin may be employed.
- Proportions of solvent may vary greatly as may also the number 01 extractions made. For the initial extraction proportions of five parts of solvent to one of vegetable matter have been found to be satisfactory. Smaller amounts of solvent can be used for the subsequent extractions.
- a process which comprises extracting a be accomplished using any one Examples of other materials are soapwort, soaproot and members of the Smilax group consisting of soap-bark.
- saponin which is substantially tree of water and which contains a compound having an alkaline reaction which is more than feeble.
- a process of preparing saponins which comprises extracting a member of the group consisting of soap bark, soapwort, and soaproot with an alcohol, which is substantially free of water and which contains an inorganic compound having an alkaline reaction.
- a process which comprises extracting vegetable matter containing a saponin with'an ali-' phatic alcohol, which is substantially free of water and which contains a basic substance.
- a process which comprises extracting soap bark with an aliphatic alcohol, which is substantially free of water and which contains an inorganic compound having analkaline reaction, adding a precipitating agent to the extract and separating precipitated saponin.
- a process which comprises extracting a I member of the group consisting of soap bark, soapwort and soaproot with methyl alcohol, which is substantially free of water and to which has been added an inorganic-compound having an alkaline reaction.
- the process of preparing a saponin which comprises extracting vegetable matter containing a saponin with an organic solvent, which is substantially free of water and which contains between about .1 and per cent of a compound having an alkaline reaction.
- a process which comprises extracting a member of the group consisting of soap bark, soapwort, and soaproot with an aliphatic alcohol, which is substantially free of water and which contains 1l0 per cent of an inorganic compound having an alkaline reaction.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Molecular Biology (AREA)
- Saccharide Compounds (AREA)
Description
Patented Sept. 5, i939 PREPARATION OF SAPONINS Fredrick H. Waltz, Roc Eastman Kodak Com hester, N. Y., assignor to pany, Rochester, N. Y., a
corporation of New Jersey No Drawing. Application April 20, 1937, I
. Serial No. 138,006
11 Claims.
This invention relates to the extraction of saponins from vegetable matter.
The ordinary methods for extracting saponins from vegetable matter also result in the extraction of large proportions of tannins and coloring substances at the same time. The
' presence of these latter substances in the product portions of solvent may be made in order to commake it unfit for many intended uses. To purify mixtures thus obtained, it is necessary to employ a number of complicated purification steps such as precipitation, recrystallization and the use of decolorizing agents.
This invention has for its object to overcome the above difficulties. Another object it to provide a process whereby saponins may be prepared in improved 'form by means. of a simple solvent extraction process, A further object is to provide an improved process for extracting saponins from vegetable matter by means of an organic solvent. Other objects will appear hereinafter. These and other objects are accomplished by the herein described invention which comprises' extracting a saponin fromvegetable matter by means of an organic solvent while in the presence of a compound having an alkaline reaction.
Material to be extracted, such as soap bark, is contacted in a chopped, macerated or finely divided form with an organic solvent while in the' presence of an alkaline compound. Contact between the substance extracted and the solvent.
may be brought about in conventional, solvent extraction apparatus or the two components may merely be placed in a container and allowed to' soak for a period of time, such as over night. The soaking procedure is preferred, since it results in a better recovery of the desired constituent. Repeated extraction with successive plete the recovery. I
The alkali may be added to the solvent before it is contacted with the vegetable matter. This procedure is preferred since the alkali is present during the entire period of extraction. Equivalent procedure would be to add the alkali to the vegetable matter prior to the, addition of the solvent. The solvent may be added to the vegetable matter and the alkali added subsequently, but extraction of coloring matter and tannin will take place until the alkali has been added.
It is, therefore, desirable to have the alkali present as soonfas the extraction starts. The amount of alkali used can be varied greatly without materially affecting the extraction process. Proportions of between .1 to 20% of alkaline compound based on the amount of solvent used are generally most useful, and amounts of between 1 and are preferred. With strong alkali proportions in the lower portion of the range mentioned are best while with weaker bases the higher concentrations are more useful. 5 Any substance having an alkaline reaction, such as sodium hydroxide, ammonia, ammonium hydroxide, borax, trisodium phosphate, methyl amine (33% in water), diethyl amine, triethanol amine, etc. may be used. 1
It is desirable to heat the mixture of solvent, alkali and vegetable material after it has soaked for a period of time, since this procedure increases the yield. For instance the mixture may be heated to boiling temperature and the solvent then separated and filtered to remove suspended vegetable matter. When the soaking procedure is not employed and the material is directly extracted with a solvent, a hot or boiling solvent may be used.
The extract or filtrates from the successive extractions are preferably combined and are then treated by any one of a number of different methods to recover the dissolved saponin. One method of recovery is to completely or partially remove the solvent by evaporation or distillation, preferably under reduced pressure. The evaporation may be continued to dryness, butit is desirable to proceed only to a point where a precipitate-first forms. This first precipitate is often of a resinous nature and may be undesirable, in which case, it is removed from the hot solution by filtration. When the concentrated extract is cooled, a portion of the dissolved saponin separates out. Super cooling may be 36 employed to increase the precipitation.
In some cases, the solubility of the saponin in the solvent is such that cooling does not cause much, if any precipitation. In such cases a precipitating agent is added. .The precipitating 40 agent should be one which is soluble in the particular solvent containing the saponins but which has little or no solvent action for the saponins. The temperature of the solution at the time of addition of the .precipitating agent has a marked 5 effect on the physical properties of the saponin precipitated. Precipitationfrom a cold solution produces a finely divided precipitate, while that obtained from a hot solution is granular. The I former dries to a chalky mass, while the latter dies .to a resinous mass. The precipitated saponins are separated from the residual solvent by filtration and dried. If desired,- they may be washed with one of the precipitating agents, prior to the drying step. Examples of suitable 66 .precipitati x agents at acetone, methyl-ethyl ketone, ethyl ether, and isopropyl ether.
'The saponin is .dried either in air or, when an especially light colored product is desired, drying in theabsence 01- air, such as in the presence or an inert atmosphere or in vacuo, is recommended. To provide an inert atmosphere inert gases, such as carbon dioxide, nitrogen, or vapors of solvents, such as carbon tetrachloride, may be employed. The product may be ground to fine powder if desired and is ready for immediate use,
The extraction of the saponin from the vegetable matter can or a mixture of a large number of organic soivents for the saponin. A preferred type of solvent is a low molecular weight aliphatic alcohol, such as methyl or ethyl alcohol, but other solvents,
such as glycerine, ethylene glycol, allyl alcohol, iurfuryl alcohol, benzyl alcohol, diacetin, pyridine and ethylene chlorohydrin may be employed.
Proportions of solvent may vary greatly as may also the number 01 extractions made. For the initial extraction proportions of five parts of solvent to one of vegetable matter have been found to be satisfactory. Smaller amounts of solvent can be used for the subsequent extractions.
' Example Pour 5 lbs. of methanol, containing 25 gms, of ammonium hydroxide (28% NHa), over 1 1b. of
soap bark. Allow this mixture to stand 15 hours.
Heat to boiling and filter while hot. Evaporate the filtrate to one-fifth its original volume, and
filter off and discard the precipitate which appears. Heat the filtrate to 120 F. and add an equal volume of acetone. The precipitated saponin settles out rapidly. Decant the supernatant liquor, add more acetone and decent again. Filter and place; the precipitate in a desiccator in an atmosphere'oi carbon dioxide. Evacuate the desiccator and allow the precipitate to dry over night. Grind the dry mass to a powder and the product is ready for use.
While I have given specific examples of materials which could be extracted, the procedure is applicable to other vegetable substances containing saponins.
having an alkaline reaction.
2. A process which comprises extracting a be accomplished using any one Examples of other materials are soapwort, soaproot and members of the Smilax group consisting of soap-bark.
member of the soapwort and soaproot with an organic solvent,
for the saponin, which is substantially tree of water and which contains a compound having an alkaline reaction which is more than feeble.
3. The process for the preparation of saponin which comprises extracting soap bark with an .organic solvent for the saponin, which is substantially free of water and which contains'a substance having an alkaline reaction.
4. The process of extracting saponins which comprises extracting vegetable mattercontaining a saponin with an alcohol, which is substantially free of water and which contains a compound having a basic reaction which is more than Ieeble.
5. A process of preparing saponins which comprises extracting a member of the group consisting of soap bark, soapwort, and soaproot with an alcohol, which is substantially free of water and which contains an inorganic compound having an alkaline reaction.
6. A process which comprises extracting vegetable matter containing a saponin with'an ali-' phatic alcohol, which is substantially free of water and which contains a basic substance.
'7. A process which comprises extracting soap bark with an aliphatic alcohol, which is substantially free of water and which contains an inorganic compound having analkaline reaction, adding a precipitating agent to the extract and separating precipitated saponin.
8. A process which comprises extracting a I member of the group consisting of soap bark, soapwort and soaproot with methyl alcohol, which is substantially free of water and to which has been added an inorganic-compound having an alkaline reaction.
9. The process of preparing a saponin which comprises extracting vegetable matter containing a saponin with an organic solvent, which is substantially free of water and which contains between about .1 and per cent of a compound having an alkaline reaction.
10. The process which comprises extracting vegetable matter containing a saponin with an aliphatic alcohol, which issubstantially free of water and which contains 1-10 per cent of an inorganic base.
11. A process which comprises extracting a member of the group consisting of soap bark, soapwort, and soaproot with an aliphatic alcohol, which is substantially free of water and which contains 1l0 per cent of an inorganic compound having an alkaline reaction.
FREDRICK H. wAL'r z.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US138006A US2172265A (en) | 1937-04-20 | 1937-04-20 | Preparation of saponins |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US138006A US2172265A (en) | 1937-04-20 | 1937-04-20 | Preparation of saponins |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2172265A true US2172265A (en) | 1939-09-05 |
Family
ID=22480016
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US138006A Expired - Lifetime US2172265A (en) | 1937-04-20 | 1937-04-20 | Preparation of saponins |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2172265A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2533546A (en) * | 1948-03-08 | 1950-12-12 | Union Oil Co | Water drive |
| US3883425A (en) * | 1973-12-10 | 1975-05-13 | Wadley Res Inst & Blood Bank | Detoxification of saponins |
-
1937
- 1937-04-20 US US138006A patent/US2172265A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2533546A (en) * | 1948-03-08 | 1950-12-12 | Union Oil Co | Water drive |
| US3883425A (en) * | 1973-12-10 | 1975-05-13 | Wadley Res Inst & Blood Bank | Detoxification of saponins |
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