New HPPOa technology for propylene oxide production: from laboratory reactor to commercial pilot installation

I.V. Shchutskyi, V. Brei, M. Sharanda, Y.V. Kas’kov, О.Yu. Dagaev, I.M. Pidsadyuk, A. Mylin, Y.O. Mykhailenko, O.Yu. Zienchenko
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Abstract

The development of HPPOa technology on production of propylene oxide from propylene and hydrogen peroxide with the use of acetonitrile as a solvent instead of methanol is shortly described. Laboratory studies included the development of a new catalyst and its testing in a flow fixed bed (4-10 cm3) reactor at 40-550C/3.0 MPa. Proposed TIS-1 catalyst was synthesized using dispersed Newsil 115 silica instead of traditional TEOS for TS-1 zeolite obtaining. Silica Ludox 40 and starch were used in the synthesis of TIS-1 catalyst also. On the basis of determined molar composition of reaction 60% H2O2 - propylene- 85% acetonitrile mixture and a load on catalyst the HPPOa (hydrogen peroxide to propylene oxide in acetonitrile) technology for a pilot installation with capacity of 2000 t/y has been developed. The main equipment – 3 reactors, 6 distillation columns, absorber, heat exchangers were made in Ukraine by Techinservice Manufacturing Group Ltd. At the beginning 2019, the construction of HPPOa installation at the olefin plant of Karpatnaftochim Ltd in Kalush began. The first start of this installation took place in June 2020. That is, in a very short time, 3 years after the start of laboratory tests. Technological HPPOa scheme includes epoxidation of propylene, preliminary separation of the product mixture, purification of propylene oxide, propylene compression, purification of propylene from propane, absorption of propylene with acetonitrile, regeneration of acetonitrile. The installation is a rather complex engineering system, some elements of which operate under both high (30 atm) and low (0.1 atm) pressure at temperatures from -30 to 1500C. Now the installation is brought to design capacity with the production of commercial propylene oxide with a polymer purity of 99.95% without the use of traditional ammonia and hydrazine. Fully automated installation is serviced by 4 operators working in two shifts. Consumption of 100% H2O2 and propylene per 1 ton of propylene oxide consists 0.68 and 0.75 tons, respectively. Ltd ”Karpatnaftochim” intends to build a facility for production of propylene oxide with a capacity of 130,000 tons per year using HPPOa technology.
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环氧丙烷生产的新型HPPOa技术:从实验室反应器到商业中试装置
简述了以丙烯和过氧化氢为原料,用乙腈代替甲醇生产环氧丙烷的HPPOa技术的发展情况。实验室研究包括开发一种新的催化剂,并在40-550C/3.0 MPa的流动固定床(4-10 cm3)反应器中进行测试。采用分散型Newsil 115二氧化硅代替传统的正硅酸乙酯制备TS-1沸石,合成了TIS-1催化剂。二氧化硅- Ludox - 40和淀粉也用于TIS-1催化剂的合成。在确定60% H2O2 -丙烯- 85%乙腈混合物的摩尔组成和催化剂负载的基础上,开发了2000吨/年中试装置的过氧化氢制环氧丙烷工艺。主要设备- 3个反应器,6个精馏塔,吸收塔,热交换器由乌克兰Techinservice制造集团有限公司制造。2019年初,Karpatnaftochim有限公司位于Kalush的烯烃工厂开始建设HPPOa装置。该装置于2020年6月首次启动。也就是说,在很短的时间内,在实验室测试开始3年后。HPPOa工艺方案包括丙烯的环氧化、产品混合物的初步分离、环氧丙烷的提纯、丙烯压缩、丙烯从丙烷中提纯、乙腈吸收丙烯、乙腈再生。安装是一个相当复杂的工程系统,其中一些元件在高压(30 atm)和低压(0.1 atm)下工作,温度从-30℃到1500℃。现在该装置已达到设计能力,无需使用传统的氨和肼,即可生产聚合物纯度为99.95%的商用环氧丙烷。全自动安装由4名操作员分两班工作。每生产1吨环氧丙烷,100% H2O2和100%丙烯的消耗量分别为0.68和0.75吨。“Karpatnaftochim”有限公司打算使用HPPOa技术建造年产13万吨环氧丙烷的生产设施。
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