当代化工
噹代化工
당대화공
CONTEMPORARY CHEMICAL INDUSTRY
2014年
7期
1202-1204
,共3页
吴阳春%王泽%夏大寒%王国兴%张先茂
吳暘春%王澤%夏大寒%王國興%張先茂
오양춘%왕택%하대한%왕국흥%장선무
裂解 C9%加氢催化剂%汽油调和组分%芳烃溶剂油
裂解 C9%加氫催化劑%汽油調和組分%芳烴溶劑油
렬해 C9%가경최화제%기유조화조분%방경용제유
Cracking c9%Hydrogenation catalyst%Composition of gasoline%Aromatic solvent oil
采用两段加氢工艺对裂解 C9进行了加氢处理,一段采用 Ni 系催化剂将易结焦的二烯烃、链烯基芳烃等热敏物质除去,并使部分单烯烃加氢饱和;二段采用 CoMoNi 系催化剂进行加氢脱硫同时将单烯烃加氢饱和。重点考查了反应温度、压力、氢油比、空速对一段加氢效果的影响,并初步探讨了二段反应温度对加氢性能的影响,研究结果表明两段加氢后的产品溴值小于2.0 g Br/100 g,总硫小于1.0μg/g,胶质含量小于5 mg/100 mL,可用于汽油调和组分或芳烃溶剂油。
採用兩段加氫工藝對裂解 C9進行瞭加氫處理,一段採用 Ni 繫催化劑將易結焦的二烯烴、鏈烯基芳烴等熱敏物質除去,併使部分單烯烴加氫飽和;二段採用 CoMoNi 繫催化劑進行加氫脫硫同時將單烯烴加氫飽和。重點攷查瞭反應溫度、壓力、氫油比、空速對一段加氫效果的影響,併初步探討瞭二段反應溫度對加氫性能的影響,研究結果錶明兩段加氫後的產品溴值小于2.0 g Br/100 g,總硫小于1.0μg/g,膠質含量小于5 mg/100 mL,可用于汽油調和組分或芳烴溶劑油。
채용량단가경공예대렬해 C9진행료가경처리,일단채용 Ni 계최화제장역결초적이희경、련희기방경등열민물질제거,병사부분단희경가경포화;이단채용 CoMoNi 계최화제진행가경탈류동시장단희경가경포화。중점고사료반응온도、압력、경유비、공속대일단가경효과적영향,병초보탐토료이단반응온도대가경성능적영향,연구결과표명량단가경후적산품추치소우2.0 g Br/100 g,총류소우1.0μg/g,효질함량소우5 mg/100 mL,가용우기유조화조분혹방경용제유。
The cracking C9 was hydrogenated by two-step hydrotreating.Nickel catalyst was used in the first-stage to eliminate heat sensitive materials such as diene and alkenyl aromatics,and some monoolefine was hydrogenated partially. The Co-Mo-Ni catalyst was used in the second-stage to carry out hydrodesulfurization, and residual monoolefine was hydrogenated. Effects of temperature, pressure, hydrogen-oil ratio and air speed on the hydrogenation reaction were investigated. The results shows that the cracking C9 after two-step hydrotreating can be used as composition of gasoline and aromatic solvent oil because its bromine number is less than 2.0 g Br/100 g, total sulfur is less than 1.0μg/g and the colloid content is less than 5 mg/100 mL.