US1721958A - Dibasic-acid salts and method of making same - Google Patents
Dibasic-acid salts and method of making same Download PDFInfo
- Publication number
- US1721958A US1721958A US549567A US54956722A US1721958A US 1721958 A US1721958 A US 1721958A US 549567 A US549567 A US 549567A US 54956722 A US54956722 A US 54956722A US 1721958 A US1721958 A US 1721958A
- Authority
- US
- United States
- Prior art keywords
- acids
- dibasic
- soaps
- oxidation
- salts
- 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
- 239000002253 acid Substances 0.000 title description 37
- 150000003839 salts Chemical class 0.000 title description 13
- 238000004519 manufacturing process Methods 0.000 title description 9
- 150000007513 acids Chemical class 0.000 description 30
- 239000000344 soap Substances 0.000 description 22
- 238000000034 method Methods 0.000 description 17
- 238000007254 oxidation reaction Methods 0.000 description 16
- 230000003647 oxidation Effects 0.000 description 14
- -1 aldehyde fatty acids Chemical class 0.000 description 12
- 235000014113 dietary fatty acids Nutrition 0.000 description 11
- 239000000194 fatty acid Substances 0.000 description 11
- 229930195729 fatty acid Natural products 0.000 description 11
- 239000000203 mixture Substances 0.000 description 10
- 230000001590 oxidative effect Effects 0.000 description 10
- 239000000047 product Substances 0.000 description 7
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 6
- 239000002480 mineral oil Substances 0.000 description 5
- 235000019645 odor Nutrition 0.000 description 5
- 150000007524 organic acids Chemical class 0.000 description 5
- 235000005985 organic acids Nutrition 0.000 description 5
- 235000010446 mineral oil Nutrition 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 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 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 3
- 239000003518 caustics Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000007800 oxidant agent Substances 0.000 description 3
- 239000011591 potassium Substances 0.000 description 3
- 229910052700 potassium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 125000001931 aliphatic group Chemical class 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000007859 condensation product Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 239000002385 cottonseed oil Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 150000001261 hydroxy acids Chemical class 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/29—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with halogen-containing compounds which may be formed in situ
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/215—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups
- C07C51/225—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups of paraffin waxes
Definitions
- JOSEPH 111px JAMES or PITTSBURGH, riEnnsYLvANIA.
- the liquid hydrocarbon containing gas in regulated proportions, near the theoretical combining proportion or preferably in excess thereof, and the hot mixture is passed, with or without the addition of a dilutlng gas, such as steam, through a relatively thin layer or through successive relatively thin layers of catalytic material under a regulated temperature, preferably below 500 C.
- the catalysts'employed are preferably complex oxides 'or compounds of metals havin a varying valence, such for example, as the Inc oxides of molybdenum.
- the prod nets of this partial-combustion or partialoxidation process arethen condensed, giving amixture of partial-oxidation products, ranging from alcohols through, aldehydes to aldehyde fatty acids.
- the process may be varied to produce more or less of the alde hyde fatty acids and of aldehydes.
- the condensed product contains aldehyde fatty acids of varying mo- I 4 v brown in color and has an aldehydic odor, and
- I take the condensation product formed by my vapor-phase partial-oxidation process, above referred to, and form soaps, preferably sodium or potassium soaps, from the aldehyde fatty acids contained in the mixture.
- the original solution of the aldehyde fatty acid soaps is usually dark cases,'entirely white; and the resulting soaps have little or none of the objectionable aldehydic odor.
- soaps are produced of the dibasic acids of varying molecular weight corresponding to the aldehyde acids in the original mixture. These soaps are usually of sufficient purity to be salted out,
- dibasic acids may, after the oxidation step, be liberatedfrom the sodium or potassium soaps by mineral acids, and then purified by any of the well known methods of purifying organic compounds, such as by vacuum distillation.
- I may use another solvent which is not appreciably attacked by the oxidizing agent, such as alcohol.
- I may use either the soaps or the free acids in carrying out the step of oxidation.
- I may also dissolve the original condensation product of the vaporphase oxidation in a solvent, such as alcohol, not appreciably attacked by the oxidizing agent, and then introduce the oxidizing agent, preferably the hydrochlorite solution.
- a solvent such as alcohol
- the oxidizing agent preferably the hydrochlorite solution.
- I will oxidize the aldehydes to true fatty acids and the aldehye alcohols to hydroxy-acids. Then the saponifying step may be carried out, giving a mixture of different soaps.
- My new step of oxidizing these aldehyde fatty acids may also be applied to the oxygenated acids obtained in the cotton seed oil industry and other industries, such oxygenated acids probably containing aldehyde acids in all or in most cases. Attempts have been made to utilize such oxygenated acids by reducing them, but such attempts have failed, so far as I am aware. My step is the opposite of this, since it oxidizes these acids to dibasic acids. Any of the methods herein described may be applied to such oxygenated acids, as well as to those obtained by my preferred method of manufacture from mineral oils.
- the mixture of salts of dibasic acids of different molecular weights produced by oxidizing the oxygenated organic acids present in the product obtained by gaseous partial oxidation of aliphatic hydrocarbons, the mixture also containing other salts produced by said further oxidation of said partial oxidation product.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
is vaporized, mixed with air or an oxygen Patented July 23, 1929.-
i U ED STATES.
PATENT OFFICE.
JOSEPH 111px JAMES, or PITTSBURGH, riEnnsYLvANIA.
mBAsrc-Aom SALTS AND METHOD OF'MAKING SAME.
N'o Drawing. Application filed April 4, 1922, Serial No. 549,567, Renewe dDecember 5, 1928.
dibasic acid salts or soaps and the method of aldehyde fatty acids.
In the said process, the liquid hydrocarbon containing gas in regulated proportions, near the theoretical combining proportion or preferably in excess thereof, and the hot mixture is passed, with or without the addition of a dilutlng gas, such as steam, through a relatively thin layer or through successive relatively thin layers of catalytic material under a regulated temperature, preferably below 500 C. The catalysts'employed are preferably complex oxides 'or compounds of metals havin a varying valence, such for example, as the Inc oxides of molybdenum. The prod nets of this partial-combustion or partialoxidation process arethen condensed, giving amixture of partial-oxidation products, ranging from alcohols through, aldehydes to aldehyde fatty acids. The process may be varied to produce more or less of the alde hyde fatty acids and of aldehydes.
As the liquid hydrocarbon is usually a certain fraction or cut of mineral oil, such as petroleum containing hydrocarbons of verying molecular'weight, the condensed product contains aldehyde fatty acids of varying mo- I 4 v brown in color and has an aldehydic odor, and
as the chlorine causes the oxidation, the color changes finally becoming lighter, and in many lecular weights in admixture.
her 5, 1919, I'have describeda certain method of making soaps and metallic salts of the aldehyde' fatty acid thus produced. I have, however, experienced much difiicult-y 1n obtaining soaps or compounds by the methods of thelast named applications, of light color and free from aldehydic odor. My present invention isde signed to overcome this difficulty, and it consists in oxidizing these aldehyde fatty acids, preferably by using one of the halogens to make a lighter colored product, free or substantially free from the aldehydic odors. The soaps may be made either by the method described in the above copending applications, or by any ordlnarymethod of soap manufacture, and the oxidation may be carried on either during or after such soap formation. The acids are thus preferably taking oxidized to dibasic acids, thus in many cases obtaining soaps of a white color and free from aldehydic odors.
While many chemical methods may be used for oxidizing the aldehyde acids into dibasic acids, I will now set forth a preferred process 3 I therefor.
I take the condensation product formed by my vapor-phase partial-oxidation process, above referred to, and form soaps, preferably sodium or potassium soaps, from the aldehyde fatty acids contained in the mixture.
To the heated water solution of the sodium or potassium soaps of these acids, I add sufficient caustic soda or caustic potash or other carbonates, to keep the bath alkaline during the oxidation. That is, I add the caustic, preferably gradually, in sutficient amount to have enough caustic present to react with the acid groups formed by theox'idation of the aldehyde groupsin the aldehyde acid soaps and keep a slight excess, by successive addithe solution (keeping the caustic in slight eX- cess) and the course of the reaction may be easily followed by noting the color changes place. The original solution of the aldehyde fatty acid soaps is usually dark cases,'entirely white; and the resulting soaps have little or none of the objectionable aldehydic odor.
' In this method, as above outlined, when the oxidation is complete, soaps are produced of the dibasic acids of varying molecular weight corresponding to the aldehyde acids in the original mixture. These soaps are usually of sufficient purity to be salted out,
after concentrating the solution by evaporation, if necessary.
If in any case it IS desired to further purify the dibasic acids, they may, after the oxidation step, be liberatedfrom the sodium or potassium soaps by mineral acids, and then purified by any of the well known methods of purifying organic compounds, such as by vacuum distillation. p
. cient method is afforded for producing dibasic acids. I
Instead of using a water solution of the soaps, I may use another solvent which is not appreciably attacked by the oxidizing agent, such as alcohol. In this case, I may use either the soaps or the free acids in carrying out the step of oxidation. I may also dissolve the original condensation product of the vaporphase oxidation in a solvent, such as alcohol, not appreciably attacked by the oxidizing agent, and then introduce the oxidizing agent, preferably the hydrochlorite solution. In this case, in addition to oxidizing the aliphatic fatty acids, I will oxidize the aldehydes to true fatty acids and the aldehye alcohols to hydroxy-acids. Then the saponifying step may be carried out, giving a mixture of different soaps.
Many variations may be-made in the reagents employed, and the steps may be varied without departing from my invention, as defined in the broader claims.
My new step of oxidizing these aldehyde fatty acids may also be applied to the oxygenated acids obtained in the cotton seed oil industry and other industries, such oxygenated acids probably containing aldehyde acids in all or in most cases. Attempts have been made to utilize such oxygenated acids by reducing them, but such attempts have failed, so far as I am aware. My step is the opposite of this, since it oxidizes these acids to dibasic acids. Any of the methods herein described may be applied to such oxygenated acids, as well as to those obtained by my preferred method of manufacture from mineral oils.
I make no claim herein to the mixtureo-f dibasic acids or the method of producing them, as claims thereon are nresent'in my acids and forming chemical salts of said dibasic acids.
2. In the treatment of liquid oxygenated organic acids derived from mineral oil, the steps consisting of oxidizing them into dibasic acids and forming chemical salts of said dibasic acids.
3. The process consisting in oxidizing oxygenated acids derived from mineral oil into dibasic acids and then converting a part of the dibasic acids into soap.
4. In the treatment of a mixture of oxygenated organic acids derived from mineral oil, the steps consistingof oxidizing them into dibasic acids and forming chemical salts of said dibasic'acids. i
5. As a new article of manufacture, a soap containing the salts of aliphatic dibasic acids of different molecular weights.
6. As a new article. of manufacture, a soap containing the ammonium salts of aliphatic dibasic acids of different molecular weights.
7. As a new article of manufacture, the mixture of salts of dibasic acids produced by oxidizing oxygenated organic acids obtained by gaseous partial oxidation of aliphatic hydrocarbons.
8. As a new article of manufacture, the mixture of salts of dibasic acids produced by oxidizing the oxygenated organic acids present in the'product obtained by gaseous partial oxidation of aliphatic hydrocarbons, the mixture also containing other salts produced by said further oxidation of said partial oxidation product. p
9. As a new article of manufacture, the mixture of salts of dibasic acids of different molecular weights produced by oxidizing the oxygenated organic acids present in the product obtained by gaseous partial oxidation of aliphatic hydrocarbons, the mixture also containing other salts produced by said further oxidation of said partial oxidation product.
In testimony whereof I have hereunto set my hand.
JOSEPH HIDY JAMES.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US549567A US1721958A (en) | 1922-04-04 | 1922-04-04 | Dibasic-acid salts and method of making same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US549567A US1721958A (en) | 1922-04-04 | 1922-04-04 | Dibasic-acid salts and method of making same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1721958A true US1721958A (en) | 1929-07-23 |
Family
ID=24193521
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US549567A Expired - Lifetime US1721958A (en) | 1922-04-04 | 1922-04-04 | Dibasic-acid salts and method of making same |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1721958A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2437410A (en) * | 1943-11-20 | 1948-03-09 | Distillers Co Yeast Ltd | Manufacture of hydroxy acids |
| US2559147A (en) * | 1949-05-24 | 1951-07-03 | Monsanto Chemicals | Preparation of dibasic aromatic acids by oxidation |
| US2862942A (en) * | 1957-10-01 | 1958-12-02 | Jordan P Snyder | Method of oxidizing and cleaving compounds to form acidic products |
-
1922
- 1922-04-04 US US549567A patent/US1721958A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2437410A (en) * | 1943-11-20 | 1948-03-09 | Distillers Co Yeast Ltd | Manufacture of hydroxy acids |
| US2559147A (en) * | 1949-05-24 | 1951-07-03 | Monsanto Chemicals | Preparation of dibasic aromatic acids by oxidation |
| US2862942A (en) * | 1957-10-01 | 1958-12-02 | Jordan P Snyder | Method of oxidizing and cleaving compounds to form acidic products |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2287803A (en) | Direct conversion of alcohols to acids | |
| US1721958A (en) | Dibasic-acid salts and method of making same | |
| US2156737A (en) | Process of preparing octadecadiene acid | |
| US2011199A (en) | Treatment of aliphatic and cyclic saturated hydrocarbons | |
| US1418448A (en) | Manufacture of butyric aldehyde | |
| US1517968A (en) | Cracking and oxidizing petroleum oil to make gasoline and useful products of oxidation | |
| US2226378A (en) | Oxidation of hydrocarbons | |
| US2302468A (en) | Process of oxidizing menthanes and products therefrom | |
| US1681185A (en) | Joseph hidy james | |
| US1595299A (en) | Manufacture of phenols | |
| US1895799A (en) | Treating partial oxidation products | |
| US2302463A (en) | Process of oxidizing menthanes | |
| US1753517A (en) | Method of treating liquid partial-oxidation products | |
| US1636854A (en) | Catalytic oxidation of aromatic hydrocarbons | |
| US2085501A (en) | Manufacture of alkyl acid salts | |
| US1697264A (en) | Making organic acids and other products from petroleum | |
| US1516756A (en) | Producing aromatic substances from petroleum | |
| US2824142A (en) | Process of producing alcohols by oxidatively polymerizing ethylene and subsequently hydrogenating | |
| US1912484A (en) | Method of treating mixtures of partially oxidized hydrocarbons | |
| US1992691A (en) | Process of oxidizing cracked petroleum | |
| US1518339A (en) | Refining and deodorizing isopropyl alcohol | |
| US2042410A (en) | Sulphonic acid bodies and process of making same | |
| US2251819A (en) | Preparation of salts of oxidized petroleum acids | |
| US1782963A (en) | Manufacture of solvents | |
| US1876454A (en) | humphkjey |