国产AV丝袜美腿丝袜_日韩国产欧美在线_成年人网站免费在线观看_国产男女羞羞视频免费一区_亚洲图片另类综合小说_青青草原在线免费观看_亚洲欧美另类制服丝袜_国产欧美日本亚洲_尤物视频在线观看_欧美成年免费一区二区

1. Introduction

Catalytic reforming oil is rich in a small amount of olefin. As the reforming severity becomes higher and higher, the olefin content in the reformed oil also increases significantly. Olefin in aromatic hydrocarbon in qualified reforming oil must be removed, or it will affect bromine index, corrosivity, or acid pickling color of aromatic products. A small amount of olefin in the reformed oil has different effects on aromatics extraction and performance of downstream, adsorbent, and catalyst. Thus, how to reduce the olefin content in the reformed oil is a difficult problem to be solved in the industry. Olefin in reforming oil can be removed by the ways of granular argil adsorption, selective hydrogenation and molecular sieve catalytic refining.

2. Performance index of TOR-1 catalyst

TOR-1 deolefination catalyst adopts special molecular sieve, with unique pore structure and acid strength distribution, as active component. Single pass life of the catalyst is 8 times that of industrial argil. Compared with argil, TOR-1 has longer life cycle, lower labour intensity, and lower waste emission.

List 1 Physical chemical index of deolefination catalyst TOR-1

List 2 Operating condition and performance guarantee of deolefination catalyst TOR-1