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1)  hydrogen-enriching reforming
富氢改质
1.
Considering the feasibility of hydrogen-enriching pre-reduction in two-step smelting reduction process,the effects of gas parameters and shaft heights on hydrogen-enriching reforming of gas in a imaginary carbon-based packed bed were simulated.
模拟结果表明,在碳基填充床内进行煤气富氢改质是可行的;相同的气体温度和气体流量下,碳消耗量随着碳基填充床的高度增加而先增加后减小,在碳基填充床高约2m时出现拐点,水蒸汽消耗量随着碳基填充床高度的增加而减小;待改质气体通过碳基填充床后,CO的体积分数随着碳基填充床高度增加而增加,H_2的体积分数随着碳基填充床高度的增加先增加后减小,在碳基填充床高约3m时出现拐点。
2.
Considering the feasibility of hydrogen-enriching pre-reduction in COREX smelting reduction process, and in order to make the effective utilization of gas high-temperature physical heat,the effect of gas flux and tem- perature on hydrogen-enriching reforming of gas in an imaginary carbon-based packed bed was simulated.
模拟结果表明,在碳基填充床内进行煤气富氢改质是可行的;水消耗量随气流通量或气体温度的提高而增加,碳消耗量随气体温度的提高而增大,但随气流通量的增加而减少;改质后(?)(CO)随气流通量或气体温度的提高而减少,(?)(H_2)随气体温度的提高而增加,但随气流通量的增加则先增加后减少。
2)  hydrogen-enriching reform of gas
煤气富氢改质
3)  perhydrous vitrinite
富氢镜质体
1.
Fourier infrared spetra,X ray diffraction and electron spin resonance are used to discuss the differences in chemical structure between the perhydrous vitrinite and the normal vitrinite,and their rules of change with the coal rank.
应用傅里叶红外光谱、X射线衍射和电子顺磁共振分析方法,探讨了富氢镜质体与正常镜质体在化学结构上的差异性和随煤阶的变化规律。
4)  hydrogenation upgrading
加氢改质
1.
With the medium pressure hydrogenation upgrading process,under the suited operating conditions,the hydrogenation upgrading base oil and its by-product were produced in SINOPEC Jingmen Branch.
采用中压加氢改质工艺的工艺条件,并选择合适的操作生产出荆门加氢改质基础油及其副产品,并以此为原料,辅加传统的发烟硫酸磺化工艺制取满足SH0007-90优级品标准要求的化妆品白油,并且具有酸加入量少、油收率高、污染小的特点,是制取高级化妆品白油的一条有效途径。
5)  hydro-upgrading
加氢改质
1.
Preparation and evaluation of ternary zeolite surported hydro-upgrading catalysts for fluid catalytic cracking gasoline;
三元沸石基载铂型催化裂化汽油加氢改质催化剂的制备及评价
2.
Industrial Test for FCC Gasoline Hydro-upgrading TMD Process;
FCC汽油加氢改质TMD技术工业应用试验
3.
Using the fractions of vacuum distillate LDAO with cut temperature more than 500℃ by hydro-upgrading at laboratory in SINOPEC Jingmen Branch as feedstock, process conditions of ketone-benzol dewaxing & deoiling were investigated at laboratory.
以中国石化荆门分公司实验室加氢改质轻脱>500℃馏分油为原料,在实验室考察了酮苯脱蜡脱油工艺条件。
6)  hydroupgrading
加氢改质
1.
FCC gas oil and straight-run diesel have been taken as the feedstock of diesel hydroupgrading-hydro visbreaking unit in Liaohe Petrochemical Company and the presulfiding technology together with the corresponding catalyst DN3100/SDD-800 developed by US Standard Co.
中国石油辽河石化公司柴油加氢改质临氢降凝装置,原料为催化裂化柴油和直馏柴油,该装置选用了美国标准公司的预硫化技术及对应的DN3100/SDD-800催化剂,并于2003年10月一次开车成功,通过生产运行和考核,达到了预期目标。
2.
Bifunctional catalysts for FCC gasoline hydroupgrading were synthesized using Hβ as support, Ni as the active component and P, Mg and La as promotor respectively in this experiment.
采用Hβ沸石为载体,以Ni为主剂,分别以P、Mg、La为助剂合成了FCC汽油加氢改质双功能催化剂。
3.
After middle pressure hydroupgrading(MHUG), various index of the cut gas oil meet requirements.
催化裂化柴油芳烃特别是稠环芳烃含量高 ,用中压加氢改质工艺处理后 ,生产的柴油各项指标符合世界燃料规范Ⅱ类标准 ,且其它产品如重石脑油可作催化重整原料 ,尾油可作蒸汽裂解制乙烯原料。
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