摘要
在广州石化分公司进行了催化C4精脱硫工业侧线试验,试验结果表明,在压力1.6MPa,温度为常温,液空速1.0h-1的条件下,该工艺能将催化C4中总硫含量从10mg/m3~80mg/m3脱除至1.0mg/m3以下,所使用的吸附剂可以再生,再生性能好,可用于催化C4中硫化物的精脱。
Industrial side stream test for fine desulfurization of FCC C4 fraction was carried out in SINOPEC Guangzhou Company.The results showed that under pressure of 1.6MPa,atmospheric temperature and LHSV of 1.0h-1,total sulfur content in FCC C4 fraction was reduced to below 1.0 mg/m3 from 10 mg/m3~80mg/m3 and the used adsorbents could be well regenerated,which indicated this adsorptive desulfurization process could be used for deep removal of sulfur in FCC C4 fraction.
出处
《天然气化工—C1化学与化工》
CAS
CSCD
北大核心
2011年第3期30-33,共4页
Natural Gas Chemical Industry
关键词
催化C4
吸附脱硫
工业侧线试验
1-丁烯
吸附剂
FCC C4 fraction
adsorptive desulfurization
industrial side stream test
1-butene
adsorbent
