亚洲国产无码网站在线观看_日韩三级大片91热国产_一级黄色视频淫妇插_欧美亚洲国产aⅴ人妖_水蜜桃一区三区视频_亚洲中文字幕av天堂_日本激情字幕免费中文_在线观看国产成人AV天堂野外_国产激情午夜理伦片_成网站在线观看人免费

Welcome to Luoyang Kechuang Petrochemical Technology Development Co., Ltd Official website!

Luoyang Kechuang Petrochemical Technology Development Co., Ltd

Hotline:

0379-652810870379-65233989

Technology brief

Your current location:Home > Process technology and service > Technology brief
Technology (catalyst) of dehydrogenation of low carbon alkane to olefin Release time:2019-09-11 Browse times:1320

Technology brief

The catalyst developed by Luoyang Kechuang Petrochemical Co., Ltd. is suitable for fixed bed low-carbon alkane dehydrogenation to olefin technology. Propylene and isobutylene are produced directly from propane or mixture of propane and isobutane. With this technology, low value-added alkane liquefied gas such as oil and gas fields and refineries can be converted into high value-added propylene and isobutylene products, with small investment and high olefin yield, which provides a new way for refining enterprises to increase production of low-carbon olefins.


Technical characteristics

① fixed bed process is adopted, and unreacted propane and isobutane are recycled.

The dehydrogenation performance of the catalyst is stable when using non noble metal catalyst.

③ high one-way conversion rate and low circulation ratio of raw materials reduce investment and operation cost.


Technical index

The technical scheme is flexible, and the production scheme can be adjusted according to the market changes. It can not only produce propylene by propane dehydrogenation, but also produce propylene and isobutylene by mixed feed of propane and isobutane.

When the feedstock is propane, the one-way conversion rate is more than 45%, and the total yield of propylene is more than 85%; when the feedstock is a mixture of propylene and isobutane, the one-way conversion rate of alkane is more than 45%, and the total yield of alkene is more than 85%; the one-way cycle of catalyst is 18 ~ 24min, and the reaction regeneration is continuously switched; the total life of catalyst is 2 ~ 3 years.


image.png