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A method for the continuous by means of guidance of propylene and / or butylenes in within the gasoline boiling range boiling polymer olefins

机译:通过在汽油沸程内使丙烯和/或丁烯连续沸腾的方法来连续聚合烯烃的方法

摘要

532,381. Polymerization of olefines. UNIVERSAL OIL PRODUCTS CO. May 19, 1939, No. 14964. Convention date, June 15, 1938. Drawings to Specification. [Class 2 (iii)] Propylene and/or butylenes are polymerized to gasoline products by contact with a solid catalyst consisting of a pre-calcined mixture of a major proportion by weight of a phosphoric acid and a minor proportion by weight of a siliceous carrier such as kieselguhr, the temperature being maintained within the range of 204-288‹C. under a pressure exceeding 40 atmospheres but not exceeding 136 atmospheres. In the case of stabilizer refluxes composed principally of 3 and 4 carbon atom hydrocarbons, temperatures of 232-288‹C. and pressures of over 40 to about 54 atmospheres are employed. Fractions composed mainly of 3 carbon atom hydrocarbons require temperatures of . 232-260‹C. and pressures of more than 40 atmospheres even as high as 136 atmospheres, whilst in the case of butane-butene fractions temperatures of 204-260‹C. are used in conjunction with pressures of the order of 51 atmospheres. The pre-heated and purified olefine-containing gases are passed or circulated through a series of tubes containing the catalyst, each group of tubes being surrounded by a liquid cooling medium, preferably water, whereby the temperature is maintained constant at any point of the system. The gases may be first contacted with partly spent catalyst before reaching catalyst of higher activity. Specifications 477,128, 490,854, 490,855, 492,567, 496,676 and 511,181 are referred to. The Specification as open to inspection under Sect. 91 also describes the use of pressures down to a minimum of 27 atmospheres and includes a table of data relating to the production of octanes from butane-butene mixtures at temperatures ranging from 135‹C. to 171‹C. under pressures of 43.5 to 82 atmospheres. This subject-matter does not appear in the Specification as accepted.
机译:532,381。烯烃聚合。通用油品公司,1939年5月19日,编号14964。公约日期,1938年6月15日。 [2(iii)类]通过与固体催化剂接触将丙烯和/或丁烯聚合为汽油产品,该固体催化剂由预煅烧的混合物组成,该预煅烧的混合物中有按重量计主要比例的磷酸和按重量计少比例的硅质载体。例如硅藻土,温度保持在204-288℃。压力超过40个大气压,但不超过136个大气压。在稳定剂回流主要由3和4个碳原子烃组成的情况下,温度为232-288℃。使用的压力超过40至约54个大气压。主要由3个碳原子碳氢化合物组成的馏分的温度为70℃。 232-260 ‹C。压力大于40个大气压,甚至高达136个大气压,而丁烷-丁烯馏分的温度为204-260°C。与51个大气压的压力结合使用。使预热和纯化的含烯烃的气体通过或循环通过一系列装有催化剂的管,每组管均被液体冷却介质(优选为水)包围,从而在系统的任何位置保持温度恒定。在达到较高活性的催化剂之前,气体可以首先与部分用过的催化剂接触。参考规格477,128、490,854、490,855、492,567、496,676和511,181。该规范可供本节检查。 91也描述了使用低至至少27个大气压的压力,并包括与在135℃的温度下由丁烷-丁烯混合物生产辛烷有关的数据表。至171 ‹C。在43.5至82个大气压的压力下该主题未在接受的规范中出现。

著录项

  • 公开/公告号DE938248C

    专利类型

  • 公开/公告日1956-03-15

    原文格式PDF

  • 申请/专利权人 UNIVERSAL OIL PRODUCTS COMPANY;

    申请/专利号DE1939U000425D

  • 发明设计人 NELSON EDWIN F.;

    申请日1939-06-13

  • 分类号C07C2/18;

  • 国家 DE

  • 入库时间 2022-08-23 22:56:10

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