首页> 外国专利> Decontamination of waste semi-synthetic or synthetic mineral oils comprises treatment with glycol, chelating agents, and barium hydroxide before ultimate fractional distillation and possible decoloration treatment

Decontamination of waste semi-synthetic or synthetic mineral oils comprises treatment with glycol, chelating agents, and barium hydroxide before ultimate fractional distillation and possible decoloration treatment

机译:废半合成或合成矿物油的去污包括在最终分馏之前进行乙二醇,螯合剂和氢氧化钡的处理,并可能进行脱色处理

摘要

The stages of treatment of the contaminated oil enables operation of the fractional distillation stage at a lower temperature and avoids the cracking of any polymers present. The decontamination of waste lubricating oils comprising mineral oils, semi-synthetic and synthetic oils comprises: (a) the addition of 1-2 wt.% glycol to the oil in a container, heating to 60 deg C, stirring then cooling and separating to obtain an aqueous phase containing glycol and phenolic products, suspended material, silicone oil residues and anti-foam agents; (b) withdrawal of the aqueous phase and addition of a chelating agent to the oily phase in stoichiometric amount, or above, relative to the compounds to eliminate, in a soda solution at pH not exceeding 7 (preferably 6) at 60-80 deg C, with stirring for 1 hour, and centrifugation to separate off the oily phase from the solution containing chelated heavy metals; (c) the stoichiometric addition of a coagulant to the oily phase to separate iron, and separation of the aqueous phase obtained; (d) the stoichiometric addition of barium hydroxide to the oily phase in suspension or solution to precipitate sulfate and phosphate ions as barium phosphate and sulfate and separation by centrifugation; and (e) fractional distillation to recover the base constituents of the oils, and optionally decoloration of the products obtained.
机译:处理受污染的油的阶段使得分馏阶段可以在较低的温度下运行,并且避免了存在的任何聚合物的裂解。包含矿物油,半合成油和合成油的废润滑油的去污包括:(a)向容器中的油中添加1-2 wt%的乙二醇,加热至60℃,搅拌,然后冷却并分离至获得含有乙二醇和酚类产品,悬浮物,硅油残留物和消泡剂的水相; (b)在60-80℃的pH值不超过7(优选6)的苏打溶液中,相对于所述化合物以化学计量量或更高的化学计量量或更高的量抽出水相并向油相中加入螯合剂。 C,在搅拌下搅拌1小时,并进行离心分离,从含有螯合重金属的溶液中分离出油相; (c)在油相中化学计量地添加凝结剂以分离铁,并分离得到的水相; (d)在悬浮液或溶液中向油相中化学计量加入氢氧化钡,以沉淀出硫酸根和磷酸根离子,成为磷酸钡和硫酸根,并通过离心分离; (e)分馏以回收油的基本成分,并任选使所得产物脱色。

著录项

  • 公开/公告号FR2795421A1

    专利类型

  • 公开/公告日2000-12-29

    原文格式PDF

  • 申请/专利权人 DEUTSCH RICHARD;

    申请/专利号FR19990008021

  • 发明设计人 DEUTSCH RICHARD;

    申请日1999-06-23

  • 分类号C10M175/02;

  • 国家 FR

  • 入库时间 2022-08-22 01:07:55

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号