燃料化学学报
燃料化學學報
연료화학학보
JOURNAL OF FUEL CHEMISTRY AND TECHNOLOGY
2001年
2期
104-107
,共4页
李文华%霍卫东%舒歌平%白向飞%戴和武
李文華%霍衛東%舒歌平%白嚮飛%戴和武
리문화%곽위동%서가평%백향비%대화무
加氢液化%煤岩显微组分%反应性
加氫液化%煤巖顯微組分%反應性
가경액화%매암현미조분%반응성
用Fe2O3作催化剂,硫黄为助催化剂,脱晶蒽油为循环溶剂,在反应温度为450℃,初始氢压为10MPa,反应时间为60min.的实验条件下,在微型高压釜内对马家塔原料煤及其显微组分的加氢液化特征进行了系统研究。镜质组的液化反应性高于惰质组,在原料煤、镜质组和惰质组这三种实验原料中,原料煤的液化反应性是最高的。对总转化率和油收率而言,原料煤>镜质组>惰质组,对沥青烯产率而言,原料煤>惰质组>镜质组,水产率则是镜质组>原料煤>惰质组,气产率为惰质组>镜质组>原料煤。原料煤、镜质组和惰质组在加氢液化过程中所产生的气体在组成上也是有所差异的。各显微组分在加氢液化过程中可能存在着协同作用。
用Fe2O3作催化劑,硫黃為助催化劑,脫晶蒽油為循環溶劑,在反應溫度為450℃,初始氫壓為10MPa,反應時間為60min.的實驗條件下,在微型高壓釜內對馬傢塔原料煤及其顯微組分的加氫液化特徵進行瞭繫統研究。鏡質組的液化反應性高于惰質組,在原料煤、鏡質組和惰質組這三種實驗原料中,原料煤的液化反應性是最高的。對總轉化率和油收率而言,原料煤>鏡質組>惰質組,對瀝青烯產率而言,原料煤>惰質組>鏡質組,水產率則是鏡質組>原料煤>惰質組,氣產率為惰質組>鏡質組>原料煤。原料煤、鏡質組和惰質組在加氫液化過程中所產生的氣體在組成上也是有所差異的。各顯微組分在加氫液化過程中可能存在著協同作用。
용Fe2O3작최화제,류황위조최화제,탈정은유위순배용제,재반응온도위450℃,초시경압위10MPa,반응시간위60min.적실험조건하,재미형고압부내대마가탑원료매급기현미조분적가경액화특정진행료계통연구。경질조적액화반응성고우타질조,재원료매、경질조화타질조저삼충실험원료중,원료매적액화반응성시최고적。대총전화솔화유수솔이언,원료매>경질조>타질조,대력청희산솔이언,원료매>타질조>경질조,수산솔칙시경질조>원료매>타질조,기산솔위타질조>경질조>원료매。원료매、경질조화타질조재가경액화과정중소산생적기체재조성상야시유소차이적。각현미조분재가경액화과정중가능존재착협동작용。
The hydroliquefacton characteristics of Majiata coal and its individual macerals were systematically investigated in a microautoclave at the following experimental conditions: reaction temperature of 450 ℃, initial H2 pressure of 10 MPa, residence time of 60min., decrystallized anthracene oil was used as a solvent, Fe2O3 plus sulfur as the catalyst. The hydroliquefaction reactivity of vitrinite is higher than that of inertinite, and the parent coal has the highest hydroliquefaction reactivity among these three feedstocks. The reactivity order for the total conversion and oil yield is: parent coal>vitrinite>inertinite, for asphaltene yield: parent coal>inertinite>vitrinite, for water yield: vitrinite>parent coal>inertinite, for gas yield: inertinite> vitrinite>parent coal. The composition of gas from hydroliquefaction of the parent coal, vitrinite and inertinite is different. Synergism between the individual macerals during hydroliquefaction process exists.