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Development and Application of the CGP-2 Catalyst in the MIP-CGP Process

机译:CIP-2催化剂在MIP-CGP工艺中的开发与应用

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摘要

The research and development of the CGP-2 catalyst, which was used in the MIP-CGP process for reducing the olefin and sulfur contents of FCC naphtha and enhancing the propylene yield, were introduced. A specific type of metal compound was added into the matrix to provide active centers for reactions including catalytic conversion and selective adsorption of sulfur containing compounds. The CGP-2 catalyst possessed excellent hydrothermal stability to meet the requirements of the 2nd reaction zone of the MIP-CGP process. The commercial test of the said catalyst at the SINOPEC Cangzhou refinery showed that in comparison with the base case (using the CGP-1Z catalyst) the CGP-2 catalyst could reduce the sulfur content of FCC naphtha by 30.32% and increase the propylene yield along with good coke selectivity. Thus, the naphtha produced by the MIP-CGP process at the Cangzhou refinery can meet the new gasoline standard enforced in July 2005.
机译:介绍了在MIP-CGP工艺中用于降低FCC石脑油的烯烃和硫含量并提高丙烯收率的CGP-2催化剂的研发。将特定类型的金属化合物添加到基质中,为包括催化转化和含硫化合物的选择性吸附在内的反应提供活性中心。 CGP-2催化剂具有出色的水热稳定性,可以满足MIP-CGP工艺第二反应区的要求。在中石化沧州炼油厂对上述催化剂进行的商业测试表明,与基本情况(使用CGP-1Z催化剂)相比,CGP-2催化剂可以将FCC石脑油的硫含量降低30.32%,并提高丙烯的收率。具有良好的焦炭选择性。因此,在沧州炼油厂通过MIP-CGP工艺生产的石脑油可以满足2005年7月实施的新汽油标准。

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