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Method for the separation of wax from crude wax and bitumen

机译:从粗蜡和沥青中分离蜡的方法

摘要

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.
机译:通过用碱金属氢氧化物加热溶解在沸点低于100℃的饱和脂族醇或其化合物中的粗蜡或沥青,并冷却,将皂化的蜡和树脂与粗蜡或含有皂化的蜡和树脂的沥青分离。当树脂皂保留在溶液中时,混合物会导致不溶性蜡酸皂,蜡醇和存在的任何蜡烃从醇中分离出来。然后从溶液中除去不溶性蜡质物质,并与过量的水溶性酸稀水溶液混合,该水溶液的亲和力比对蜡金属的亲和力更大,从而释放出游离的蜡酸,并将其与从水溶液中除去游离的蜡醇和任何蜡烃,并以已知方式进一步处理。从醇溶液中回收树脂皂和其他树脂物质以及可溶于冷醇的任何高级醇和烃,并用水或用有机溶剂如苯萃取。为了获得类似于天然蜡的蜡产品,可以将分离的蜡酸与来自该方法和/或其他来源的高级醇进行酯化。据指出,在皂化和冷却后从醇溶液中沉降出的任何沥青物质都以固体饼的形式这样做,其可以容易地与蜡状产物的沉淀物分离。在一个实例中,将从萃取过程获得的沥青溶解在乙醇中,并在压力下用氢氧化钾皂化。然后将混合物冷却,蜡酸的钾盐沉淀,等。形成的产物被滤出,用乙醇洗涤,与水混合,加入过量的硫酸,并由此形成游离蜡酸的沉淀与水溶液分离。通过蒸馏除去醇并保留在原始的冷碱性醇溶液中的溶液中的树脂物质,并用苯甲酚萃取。不可皂化的部分溶解在苯甲酸酯中,而树脂酸的钾盐保留为残留物。分离不皂化物部分的苯甲溶液后,树脂酸用硫酸从钾盐中释放出来。通过蒸馏除去溶剂,从苯甲溶液中回收不皂化物部分。在另一实例中,通过蒸馏除去醇并用溶解树脂酸的盐的冷水萃取残余物,从碱性醇溶液中回收树脂物质(在皂化和分离蜡状物质之后)。然后用硫酸从水性提取物中释放出树脂酸。不溶于冷水的残留物构成树脂物质的不可皂化部分。请参考规格5999/00,[Class 91]和402,751。

著录项

  • 公开/公告号GB645613A

    专利类型

  • 公开/公告日1950-11-01

    原文格式PDF

  • 申请/专利权人 ALBERT FERDINAND SUNDGREN;ERKKI EMIL EKMAN;

    申请/专利号GB19470003900D

  • 发明设计人

    申请日1947-02-10

  • 分类号C10G73/00;

  • 国家 GB

  • 入库时间 2022-08-24 02:03:53

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