当代化工
噹代化工
당대화공
CONTEMPORARY CHEMICAL INDUSTRY
2014年
3期
340-343
,共4页
李金瑞%张聪%闫锋%张树丰
李金瑞%張聰%閆鋒%張樹豐
리금서%장총%염봉%장수봉
焦化柴油%脱硫%脱氮%氧化萃取%萃取剂
焦化柴油%脫硫%脫氮%氧化萃取%萃取劑
초화시유%탈류%탈담%양화췌취%췌취제
Coker diesel%Desulfurization%Denitrification%Oxidation extraction%Extraction agent
以过氧化氢为氧化剂,磷钨酸为催化剂,四乙基溴化铵为相转移催化剂,糠醛为萃取剂,采用催化氧化反应与溶剂萃取相结合的试验方法对焦化柴油进行硫氮脱除反应,并对工艺条件进行优化。结果表明,以50 mL焦化柴油为基础,在H2O2体积为7 mL、磷钨酸用量为0.28 g/L、四乙基溴化铵质量为0.10 g、反应温度60℃、氧化反应70 min、25 mL糠醛萃取三次的最优工艺条件下,柴油中硫质量分数由647μg/g降至62.58μg/g,脱硫率达90.33%;而氮质量分数由775.26μg/g降至29.85μg/g,脱氮率高达96.15%。氧化溶液与萃取剂回收后经处理均可重复利用。
以過氧化氫為氧化劑,燐鎢痠為催化劑,四乙基溴化銨為相轉移催化劑,糠醛為萃取劑,採用催化氧化反應與溶劑萃取相結閤的試驗方法對焦化柴油進行硫氮脫除反應,併對工藝條件進行優化。結果錶明,以50 mL焦化柴油為基礎,在H2O2體積為7 mL、燐鎢痠用量為0.28 g/L、四乙基溴化銨質量為0.10 g、反應溫度60℃、氧化反應70 min、25 mL糠醛萃取三次的最優工藝條件下,柴油中硫質量分數由647μg/g降至62.58μg/g,脫硫率達90.33%;而氮質量分數由775.26μg/g降至29.85μg/g,脫氮率高達96.15%。氧化溶液與萃取劑迴收後經處理均可重複利用。
이과양화경위양화제,린오산위최화제,사을기추화안위상전이최화제,강철위췌취제,채용최화양화반응여용제췌취상결합적시험방법대초화시유진행류담탈제반응,병대공예조건진행우화。결과표명,이50 mL초화시유위기출,재H2O2체적위7 mL、린오산용량위0.28 g/L、사을기추화안질량위0.10 g、반응온도60℃、양화반응70 min、25 mL강철췌취삼차적최우공예조건하,시유중류질량분수유647μg/g강지62.58μg/g,탈류솔체90.33%;이담질량분수유775.26μg/g강지29.85μg/g,탈담솔고체96.15%。양화용액여췌취제회수후경처리균가중복이용。
Taking hydrogen peroxide as oxidant, phosphotungstic acid as catalyst, tetraethyl-ammonium bromide as phase transfer catalyst, furfural as extraction agent, desulphurization and denitrification of the coking diesel were carried out by using combined process of catalytic oxidation reaction and solvent extraction, and the process conditions were optimized. The results show that ,under the optimal process conditions of hydrogen peroxide 7 mL , phosphotungstic acid 0.28 g/L,tetraethyl-ammonium bromide 0.10 g,reaction temperature 60℃,reaction time 70 min,furfural extraction three times based on the 50 mL coking diesel, the desulfurization rate is as high as 90.33%and the sulphur content decreases from 647 μg/g to 62.58 μg/g;the denitrification rate is as high as 96.15% and the nitrogen content decreases from 775.26μg/g to 29.85μg/g. The oxidation solution and extraction agent can be reused after processing.