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Improvements in or relating to the extraction of sulphonic acids from acid sludge by-products of mineral oils

机译:从矿物油的酸性污泥副产物中提取磺酸的改进或与之有关的改进

摘要

Sulphonic acids are extracted from acid-sludge obtained as a by-product in the refining of mineral oils with sulphuric acid or oleum by washing the sludge at a temperature of between 20 DEG and 60 DEG C. with 100 to 400 per cent by weight, relative to the sludge, of a mineral oil having a Redwood I viscosity at 100 DEG F. of between 50 and 200 seconds, and separating the wash oil containing the sulphonic acids from the sludge. If the wash oil has a viscosity-gravity constant not exceeding 0.875 and an aniline point not less than 60 DEG C., the sodium salts of the extracted sulphonic acids will have a preponderance of sodium salts preferentially soluble in hydrocarbon oil; if the wash oil has a viscosity-gravity constant not less than 0.900 and an aniline point not exceeding 50 DEG C., the sodium salts of the extracted sulphonic acids will have a preponderance of sodium salts preferentially soluble in water. The sulphonic acids may be recovered from the wash-oil by means of an aqueous alcoholic solution of an alkali such as caustic soda and the resulting sodium sulphonates may be isolated and the free sulphonic acids obtained by treatment with, e.g. sulphuric acid. The acid sludge may be prepared by reacting a naphthenic type lubricating oil distillate with 10 per cent fuming sulphuric acid at 40 DEG C. In examples: (1) sulphonic acids yielding sodium salts predominantly preferentially oil-soluble are recovered from an acid sludge using as wash oil a mineral oil distillate of viscosity-gravity constant 0.831 and aniline point 97 DEG C.; (2) sulphonic acids yielding predominantly preferentially water-soluble salts are extracted from the same acid sludge by means of an Edeleanu aromatic petroleum extract from mineral oil and having a viscosity-gravity constant of 0.909 and an aniline-point of 26 DEG C. U.S.A. Specification 1,087,888 is referred to. According to the Provisional Specification, the wash oil may be any raw or refined oil, e.g. a naphthenic base oil of viscosity 70-150 seconds at 100 DEG F.
机译:从硫酸或发烟硫酸精制矿物油中作为副产物获得的酸性污泥中提取磺酸,方法是在20至60℃的温度下用100%至400%的重量洗涤污泥,相对于污泥,是在100°F下具有Redwood I粘度在50到200秒之间的矿物油,并从污泥中分离出含有磺酸的洗涤油。如果洗涤油的粘度-重力常数不超过0.875,苯胺点不低于60℃,则提取的磺酸的钠盐将具有优先溶于烃油的钠盐。如果洗涤油的粘度-重力常数不小于0.900且苯胺点不大于50℃,则提取的磺酸的钠盐将具有优先溶于水的钠盐。可以通过碱例如苛性钠的水溶液从洗涤油中回收磺酸,并且可以分离得到的磺酸钠,并通过用例如碳酸氢钠处理获得游离磺酸。硫酸。可以通过使环烷型润滑油馏出物与10%的发烟硫酸在40℃下反应来制备酸性污泥。在实例中:(1)从酸性污泥中回收主要产生油溶性钠盐的磺酸,使用洗涤油是粘度-重力常数为0.831和苯胺点为97℃的矿物油馏出物; (2)通过从矿物油中得到的Edeleanu芳族石油提取物,从相同的酸性污泥中提取主要产生水溶性盐的磺酸,其粘度-重力常数为0.909,苯胺点为26 CUSA规格1,087,888被称为。根据临时规范,洗涤油可以是任何原油或精制油,例如在100°F下粘度为70-150秒的环烷基基础油。

著录项

  • 公开/公告号GB699341A

    专利类型

  • 公开/公告日1953-11-04

    原文格式PDF

  • 申请/专利号GB19490026255

  • 发明设计人

    申请日1949-10-12

  • 分类号C07C303/00;C10G17/10;

  • 国家 GB

  • 入库时间 2022-08-24 00:21:17

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