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1)  post-hydrotreatment
后加氢
1.
D40 solvent naphtha and 3~# white oil were produced by pre-hydrotreatment and dewaxing over zeolite followed by post-hydrotreatment.
利用分子筛脱蜡预加氢和后加氢装置改产D40溶剂油和3#白油,现有原料条件下,生产出硫和氮含量均小于1μg。
2)  hydrogenated residuum
加氢后残渣
3)  hydrogenated coker naphtha
加氢后焦化汽油
4)  hydrogenation [,haidrədʒə'neiʃən]
加氢
1.
Advance and trend in glucose hydrogenation catalysts for sorbitol;
葡萄糖加氢催化剂研究现状及发展趋势
2.
Supported nickel catalyst for hydrogenation of p-nitrophenol to p-aminophenol;
负载型Ni催化剂上对硝基酚加氢合成对氨基酚的研究
3.
Modification of the Cu-Zn catalysts supporred on γ-Al_2O_3 for hydrogenation of furfural to furfuryl alcohol;
糠醛加氢制糠醇中γ-Al_2O_3负载Cu-Zn催化剂的改性研究
5)  Hydrofining ['haidrə,fainiŋ]
加氢
1.
Analysis Quality and Profit of Wax Hydrofining Production;
白土预精制在蜡加氢生产中效益分析
2.
Trial manufacture and application of LH-3 diesel oil hydrofining catalyst;
LH-03柴油加氢改性催化剂的试生产和应用
3.
Reformation of Feeding Pump for 4×10 5 t/a Hydrofining Unit;
40万吨/年加氢精制装置进料泵改造
6)  hydrotreating
加氢
1.
Comparison of residue oil ebullated-bed hydrotreating processes in China and abroad
国内外渣油沸腾床加氢技术的比较
2.
The effect of the pH of impregnating solution and the use of additives on the chemical and physical properties of Co-Mo/Al 2O 3 hydrotreating catalyst were discussed.
讨论了浸渍溶液pH以及在浸渍溶液中添加助剂等对Co -Mo加氢催化剂物化性质的影响 ,调整浸渍溶液 pH可以改变催化剂孔结构 ,在浸渍溶液中添加助剂可以改善活性金属在加氢催化剂表面的分布。
3.
Effects of Na +,heavy metal nickel and vanadium,sulfur and viscosity of residue on activity of catalyst for S-RHT were investigated on a residue hydrotreating pilot unit.
在中型渣油加氢试验装置上考察了钠离子、镍、钒、硫和渣油粘度对S-RHT催化剂活性的影响。
补充资料:C10-18-碳烯加氢甲酰化物蒸馏轻组分
CAS:97552-94-8
中文名称:C10-18-碳烯加氢甲酰化物蒸馏轻组分
英文名称:Alkenes, C10-18-hydroformylation products, distn. lights; Alkenes,C10-18-hydroformylation products,distn. lights
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