广州化工
廣州化工
엄주화공
GUANGZHOU CHEMICAL INDUSTRY AND TECHNOLOGY
2012年
15期
126-128
,共3页
焦化蜡油,非加氢脱碱氮,酸精制%糠醛精制
焦化蠟油,非加氫脫堿氮,痠精製%糠醛精製
초화사유,비가경탈감담,산정제%강철정제
coker gas oil%basic nitrogen%non-hydrogenation basic nitrogen removal%acid refining%furfural treatment
以辽河石化焦化蜡油对象,对甲酸精制、乙醇-FeCl3络合、白土吸附、硅胶氧化铝吸附、沸石吸附以及糠醛精制等非加氢脱碱氮技术进行了筛选和评价。研究表明,甲酸精制对焦化蜡油中碱氮的脱除效果显著,剂油比在1∶7时就能使碱氮从1766 mg/kg降至800 mg/kg以下,蜡油收率95%以上;FeCl3的络合作用有利于碱氮的脱除,但乙醇-FeCl3的脱氮效果并不明显,白土、硅胶氧化铝、沸石等吸附脱碱氮效果不佳;糠醛萃取也可将辽河石化蜡油中的碱氮脱至800 mg/kg以下,尽管抽余油收率相对较低(70%左右),但抽出油可作为化工原料使用,在经济成本及技术可行性上由于甲酸精制。
以遼河石化焦化蠟油對象,對甲痠精製、乙醇-FeCl3絡閤、白土吸附、硅膠氧化鋁吸附、沸石吸附以及糠醛精製等非加氫脫堿氮技術進行瞭篩選和評價。研究錶明,甲痠精製對焦化蠟油中堿氮的脫除效果顯著,劑油比在1∶7時就能使堿氮從1766 mg/kg降至800 mg/kg以下,蠟油收率95%以上;FeCl3的絡閤作用有利于堿氮的脫除,但乙醇-FeCl3的脫氮效果併不明顯,白土、硅膠氧化鋁、沸石等吸附脫堿氮效果不佳;糠醛萃取也可將遼河石化蠟油中的堿氮脫至800 mg/kg以下,儘管抽餘油收率相對較低(70%左右),但抽齣油可作為化工原料使用,在經濟成本及技術可行性上由于甲痠精製。
이료하석화초화사유대상,대갑산정제、을순-FeCl3락합、백토흡부、규효양화려흡부、비석흡부이급강철정제등비가경탈감담기술진행료사선화평개。연구표명,갑산정제대초화사유중감담적탈제효과현저,제유비재1∶7시취능사감담종1766 mg/kg강지800 mg/kg이하,사유수솔95%이상;FeCl3적락합작용유리우감담적탈제,단을순-FeCl3적탈담효과병불명현,백토、규효양화려、비석등흡부탈감담효과불가;강철췌취야가장료하석화사유중적감담탈지800 mg/kg이하,진관추여유수솔상대교저(70%좌우),단추출유가작위화공원료사용,재경제성본급기술가행성상유우갑산정제。
Non-hydrogenation basic nitrogen removal technologies of methanoic acid refining,ethanol-FeCl3 complexation,adsorption by carclazyte,silica gel-aluminum oxide and zeolite,and furfural treatment for coker gas oil were evaluated.During the methanoic acid refining test,the basic nitrogen was decreased from 1766 mg/kg to below 800 mg/kg only at the acid oil ratio of 1:7,and the oil recovery was obtained over 95%.The complexing action of FeCl3 provided a good favor on basic nitrogen removal,but the ethanol-FeCl3 complexation performed poor.Neither of the carclazyte,silica gel-aluminum oxide or zeolite adsorption proved accepted ability on basic nitrogen removal.Furfural treatment also decreased the basic nitrogen content to below 800 mg/kg.Although the oil recovery was relatively not high(about 70%),the raffinate oil was valuable as chemical raw materials,and the economic cost and the technical feasibility was better than that of methanoic acid refining.