GB645613A - Method for the separation of wax from crude wax and bitumen - Google Patents

Method for the separation of wax from crude wax and bitumen

Info

Publication number
GB645613A
GB645613A GB3900/47D GB390047D GB645613A GB 645613 A GB645613 A GB 645613A GB 3900/47 D GB3900/47 D GB 3900/47D GB 390047 D GB390047 D GB 390047D GB 645613 A GB645613 A GB 645613A
Authority
GB
United Kingdom
Prior art keywords
wax
solution
alcohol
acids
recovered
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
Application number
GB3900/47D
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ALBERT FERDINAND SUNDGREN
Original Assignee
ALBERT FERDINAND SUNDGREN
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ALBERT FERDINAND SUNDGREN filed Critical ALBERT FERDINAND SUNDGREN
Publication of GB645613A publication Critical patent/GB645613A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G73/00Recovery or refining of mineral waxes, e.g. montan wax

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)
  • Extraction Or Liquid Replacement (AREA)

Abstract

Saponifiable waxes and resins are separated from crude waxes or bitumens containing saponifiable waxes and resins by heating the crude wax or bitumen dissolved in a saturated aliphatic alcohol or a compound thereof having a boiling point below 100 DEG C. with an alkali metal hydroxide, and cooling the mixture to cause insoluble wax acid soaps, wax alcohols and any wax hydrocarbons present to separate out from the alcohol while the resin soaps remain in solution. The insoluble waxy substances are then removed from the solution and mixed with an excess of a dilute aqueous solution of a water-soluble acid having a greater affinity than the wax acids for the soap metal, thereby liberating the free wax acids, which together with the free wax alcohols and any wax hydrocarbons are removed from the aqueous solution and treated further in a known manner. The resin soaps and other resinous substances and any higher alcohols and hydrocarbons which are soluble in cold alcohol are recovered from the alcoholic solution and extracted either with water or with an organic solvent such as benzene. For the purpose of obtaining wax products resembling natural waxes, the separated wax acids may be esterified with higher alcohols from the process and/or of some other origin. It is stated that any asphaltic matter settling out from the alcoholic solution after saponification and cooling does so in the form of a solid cake which can readily be separated from the precipitate of wax-like products. In an example, bitumen obtained from an extraction process is dissolved in ethyl alcohol and saponified under pressure with potassium hydroxide. The mixture is then cooled, the precipitate of potassium salts of wax acids, &c. which forms, is filtered off, washed with ethyl alcohol, mixed with water, an excess of sulphuric acid added, and the precipitate of free wax acids thereby formed separated from the aqueous solution. The resinous substances which have remained in solution in the original cold alkaline alcohol solution are recovered by distilling off the alcohol and extracted with benzol. The unsaponifiable portion dissolves in the benzol while the potassium salts of the resin acids remain as a residue. After the separation of the benzol solution of the unsaponifiable portion, the resin acids are liberated from their potassium salts with sulphuric acid. The unsaponifiable portion is recovered from the benzol solution by distilling off the solvent. In the other example the resinous substances are recovered from the alkaline alcohol solution (after saponification and separation of the wax-like substances) by distilling off the alcohol and extracting the residue with cold water which dissolves the salts of the resin acids. The resin acids are then liberated from the aqueous extract with sulphuric acid. The residue insoluble in cold water constitutes the unsaponifiable portion of the resinous substances. Specifications 5999/00, [Class 91], and 402,751 are referred to.
GB3900/47D 1946-02-09 1947-02-10 Method for the separation of wax from crude wax and bitumen Expired GB645613A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE645613X 1946-02-09

Publications (1)

Publication Number Publication Date
GB645613A true GB645613A (en) 1950-11-01

Family

ID=20313907

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3900/47D Expired GB645613A (en) 1946-02-09 1947-02-10 Method for the separation of wax from crude wax and bitumen

Country Status (1)

Country Link
GB (1) GB645613A (en)

Similar Documents

Publication Publication Date Title
US2240365A (en) Method of treating tall oil
US2662893A (en) Extraction of valuable products from bark
US2652410A (en) Esters of alpha-hydroxy acids and their estolides
GB645613A (en) Method for the separation of wax from crude wax and bitumen
US1943427A (en) Production of organic acids
US2153302A (en) Saponification of oxidized hydrocarbons
US2248346A (en) Method for the recovery of phytosterol
US2193321A (en) Process for the recovery of high molecular weight carboxylic acids or their salts
US2729655A (en) Production of sterols
US2232331A (en) Process of recovering high-molecular aliphatic carboxylic acids from their salts
US2571221A (en) Method of extracting organic acids and their salts from cork and products resulting from this extraction
US2437643A (en) Separation of neutral fat from tall oil
US2394615A (en) Method of obtaining sterol and the like from tall oil
US2166812A (en) Process for the separation of the constituents of organic mixtures containing both resin acids and fatty acids, particularly tall oil
US2225246A (en) Method of producing a resin acid lactone
US2380412A (en) High iodine value oils
US2371307A (en) Purification of organic compounds
US2276517A (en) Treatment of tall oil
GB324538A (en) Improvements in the manufacture and production of organic acids and their salts
US2532101A (en) Method for separating rosin acids from mixed materials
SU15374A1 (en) Hydroxy acid release method
DE748194C (en) Process for the production of high quality soap fatty acids
US1817686A (en) Process for the manufacture of physiologically active substances from female internal secretory sex organs
SU48963A1 (en) The method of obtaining tall oil
US2259726A (en) Method of producing refined, noncrystallizable rosin