GB240803A - An improved manufacture of petrolatum and petrolatum oils - Google Patents
An improved manufacture of petrolatum and petrolatum oilsInfo
- Publication number
- GB240803A GB240803A GB21272/25A GB2127225A GB240803A GB 240803 A GB240803 A GB 240803A GB 21272/25 A GB21272/25 A GB 21272/25A GB 2127225 A GB2127225 A GB 2127225A GB 240803 A GB240803 A GB 240803A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oil
- per cent
- acid
- solvent
- petrolatum
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G73/00—Recovery or refining of mineral waxes, e.g. montan wax
- C10G73/36—Recovery of petroleum waxes from other compositions containing oil in minor proportions, from concentrates or from residues; De-oiling, sweating
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Highly purified petrolatum and petrolatum oils are obtained by heating the crude products with fuming sulphuric acid until the impurities are converted into undissolved solid or semi-solid carbonaceous matter, and dissolving the purified petrolatum &c. from the mass. In an example, 1000 kilograms of crude hydrocarbon grease are heated to 120-180 DEG C. for 24-48 hrs. with 1500 kilograms of 20 per cent oleum, and then extracted with naphtha or benzol. The solution is treated with alkali to remove acidity, and is distilled to remove the solvent. The carbonaceous matter is pulverized and calcined at a dull red heat to produce a decolorizing carbon. Any sulphur dioxide evolved is absorbed in alkali to produce sulphite. According to the Specification as open to inspection under Sect. 91 (3) (a), petroleum residues and heavy oils are purified by treatment with strong sulphuric acid at an elevated temperature. Preferably the material is first treated below 100 DEG C., and then at over 200 DEG C., e.g. 160-170 DEG C., sulphur trioxide is added to the acid, a hydrocarbon that is liquid at the temperature employed and unacted upon by the acid is mixed with the crude material, and the product is neutralized by treatment with calcium carbonate and filtration through porous clay. Oil that has been treated once with acid as above may be freed from sulphonated compound by extraction with alcohols, light naphtha, or other solvent of the pure oil, or by further treatment with 20 per cent oleum. In an example black cylinder oil is mixed with an equal weight of petroleum jelly that has already been treated with acid, and agitated with 1.5 parts by weight of 20 per cent oleum at 120-160 DEG C. for 24 hours. The liquid is drawn off, neutralized by agitation at 120 DEG C. for 3-4 hours with 10 per cent of porous clay and 1.5 per cent of calcium carbonate, and filtered hot through porous clay. The carbonaceous residue in the acid-treatment vessel is broken up and treated with naphtha, benzol, tetrachlorethylene, or other solvent of the purified oil. The solution is withdrawn, the solvent distilled off, and the oil neutralized and filtered. Alternatively the solution is chilled and the precipitated oil or jelly allowed to settle out. The carbonaceous residue is afterwards heated to about 400 DEG C. to Q remove volatile impurities, ground in a ball mill, and maintained red hot in contact with air until about half is consumed. A highly adsorbent carbon results. Sulphur dioxide evolved during the operations is absorbed in a 28 per cent solution of sodium carbonate. The porous clay is revivified in known manner after treatment at about 50 DEG C. with naptha or other solvent of the oil. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR240803X | 1924-10-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB240803A true GB240803A (en) | 1926-10-07 |
Family
ID=8883256
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB21272/25A Expired GB240803A (en) | 1924-10-04 | 1925-08-25 | An improved manufacture of petrolatum and petrolatum oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB240803A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112158989A (en) * | 2020-09-24 | 2021-01-01 | 山东天智信息科技有限公司 | Casting wastewater purification treatment method |
-
1925
- 1925-08-25 GB GB21272/25A patent/GB240803A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112158989A (en) * | 2020-09-24 | 2021-01-01 | 山东天智信息科技有限公司 | Casting wastewater purification treatment method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2168315A (en) | Method for the purification of petroleum mahogany sulphonates | |
GB240803A (en) | An improved manufacture of petrolatum and petrolatum oils | |
US1785270A (en) | Process of preparing petrolatum and the like and product obtained thereby | |
US2121032A (en) | Detergent and wetting agent and process of producing the same | |
US1836429A (en) | Manufacture of water soluble sulphonic acids of mineral oils | |
DE539551C (en) | Process for the production of high molecular weight water-soluble sulfonic acids or salts thereof suitable as cleaning, emulsifying and wetting agents | |
GB259442A (en) | An improved manufacture of petrolatum and petrolatum oils | |
US1766304A (en) | Process for separating and purifying sulpho-acids of high molecular weight | |
US1963257A (en) | Separation and purification of sulphonates with ammonia | |
US1960348A (en) | Filtration of acid sludge | |
US2133765A (en) | Process for purifying naphthenic acids | |
US1940372A (en) | Method of obtaining phytosterol, fatty acids and resin acids from raw soap or liquidresin obtained in the manufacture of cellulose according to the sulphate method | |
US1733597A (en) | Process and apparatus for making white petrolatum | |
US1938513A (en) | Process for working up naphthenic acid soap-containing oily residues | |
US2324012A (en) | Extraction of organic materials | |
US1425883A (en) | Process of treating hydrocarbon oils | |
US1443983A (en) | Process for obtaining paraffin and highly-viscous lubricating oils from bituminous masses | |
US1445668A (en) | Process of producing cresol | |
US3142636A (en) | Guanidine naphthenates and process for making them | |
US1339310A (en) | Producing resinous bases prom tar | |
US2108901A (en) | Production of assistants for the | |
US2154616A (en) | Grease-setting agent | |
GB459078A (en) | A process for the production of alkyl ester salts | |
US1578235A (en) | Gilsonitic product and its manufacture | |
AT147147B (en) | Process for the extraction of pure sulfur. |