KTI硫回收技术？ tail gas treatment main features 尾气处理的主要特征 a) hydrogenation reactor reheating gas system 氢化反应器再热气系统 the hydrogenation reactor shall be filled with hydrogenation catalyst capable to operate at low temperature (typically 230-240°c), not the conventional catalyst operating at 280-320°c. 氢化反应器内应加注氢化催化剂，并能够在较低的温度下工作（一般为230- 240摄氏度），不是传统的需要工作在280-320摄氏度温度下的催化剂。 the proposed catalyst has been tested by licensor in a commercial unit in p.r.c., which is in normal operation and is used in many new units under design/construction/ operation. 建议的催化剂已由德希尼布意大利动力学技术国际公司在中国境内的一套正 常运转的工业设备上测试过，很多正在设计/施工/运转的新设备也使用了该 催化剂。 the reheating system of the process gas to the hydrogenation reactor proposed is indirect using a shell and tube heat exchanger. the superheated mp steam produced in the plant shall be used for reheating. 对至氢化反应器工艺气体，建议的再热系统为使用管壳换热器的间接式加热 系统。再热使用的是车间内生产的高压过热蒸汽。 with the new catalyst and the proposed plant configuration the plant operation shall be simpler while the investment and operating cost shall be substantially reduced. 使用新型催化剂以及建议的车间配置，车间的运转应更简单，投资及运转成 本也应得到大幅削减。 因为涉及到保密原则，详细资料看我的资料进p群询问。见谅。 查看更多
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