2) liquefied petroleum gas
液化石油气体<冶>
3) liquefied petroleum gas
液化石油气
1.
Performance evaluation on new catalyst for producing aromatics from liquefied petroleum gas;
金属元素改性后的液化石油气制芳烃催化剂性能评价
2.
The evaluation of explosion accident of the liquefied petroleum gas warehouse in Lingxiang iron mine of WISCO;
武钢灵乡铁矿液化石油气库爆炸灾害评价
3.
Low temperature aromatization process for liquefied petroleum gas;
液化石油气低温芳构化工艺研究
4) LPG
[英][,el pi: 'dʒi:] [美]['ɛl 'pi 'dʒi]
液化石油气
1.
OPTIMIZATION OF LPG AMINE DESULFURIZATION;
炼油厂液化石油气胺法脱硫工艺设计优化
2.
APPLICATION OF FIBER LIQUID FILM CONTACTOR IN LPG SWEETENING PROCESS;
纤维液膜接触器在液化石油气脱硫工艺中的应用
3.
ANALYSIS OF REVAMP OF LPG CAUSTIC-FREE SWEETENING PROCESS;
液化石油气无碱脱硫醇工艺改造分析
5) liquified petroleum gas
液化石油气
1.
The stability of catalyst cobalt sulfonated phthalocyanine(CoSPc) used in liquified petroleum gas sweetening process was researched by ultraviolet-visible spectrometry method in alkaline solution.
利用紫外可见光谱方法对磺化酞菁钴催化剂在液化石油气脱硫醇工艺中的稳定性进行了研究。
2.
The underlying dangerous factors in the explosion elimination processing of LPG(liquified petroleum gas) tanks in a chemical plant in Xiangfan city, Hubei province, were systematically analyzed from the top tree event to the bottom tree event,and from the results to the causes by a fault tree taking a fire or explosion accident for the top.
采用事故树分析法,建立了以发生火灾或爆炸事故为顶上事件的事故树,从分析事故发生因果关系中的顶上事件开始,直到基本事件,由果到因、自上而下地分析了某化工厂液化石油气储罐销爆过程中的危险因素。
3.
In the cause of thiol removal from liquified petroleum gases by catalytic oxidization, peak values of thiol removal percentage were investigated in an operating cycle in the caustic pre-washing drum.
在液化石油气催化氧化脱硫醇生产中观察到预碱洗罐在碱液运行周期内脱硫醇率出现峰值，进而通过实验得出了在现有的脱硫醇装置工艺和设备条件下，向氢氧化钠溶液中加入0。
6) liquefied petroleum gas(LPG)
液化石油气
1.
Objective To compare the mutagenicities by combustion particulates from liquefied petroleum gas(LPG)and coal,and to know the model of their joint action.
目的比较液化石油气(LPG)燃烧颗粒物和蜂窝煤燃烧颗粒物的致突变性以及二者的联合作用。
2.
18 C1-C5 carbohydrate composition in liquefied petroleum gas(LPG) was separated by 30 m×0.
)HP PLOT/A l2O3石英毛细管柱,程序升温和分流进样技术对液化石油气的18种C1~C5烃类组分进行分离。
补充资料：低压液化气体
分子式：
CAS号：
性质：临界温度大于70℃的气体。区分为不燃无毒和不燃有毒，酸性腐蚀性气体；可燃无毒和可燃有毒、酸性腐蚀气体；易分解或聚合的可燃气体。此类气体在充装时以及在允许的工作温度下贮运和使用过程中均为液态。包括的气体品种有一氟二氯甲烷、二氟氯甲烷、二氟二氯甲烷、二氟溴氯甲烷、三氟氯乙烷、四氟二氯乙烷、五氟氯乙烷、八氟环丁烷、六氟丙烯、氯、三氯化硼、光气、氟化氢、溴化氢、二氧化硫、硫酰氟、二氧化氮、液化石油气、丙烷、环丙烷、丙烯、正丁烷、异丁烷、1-丁烯、异丁烯、(顺)2-丁烯、(反)2-丁烯、R-142b、R143-a、R152a、氯乙烷、二甲醚、氨、乙胺、一甲胺、二甲胺、三甲胺、甲硫醇、硫化氢、氯甲烷、溴甲烷、砷烷、1,3-丁二烯、氯乙烯、环氧乙烷、乙烯基甲醚、R-1113、溴乙烯。
CAS号：
性质：临界温度大于70℃的气体。区分为不燃无毒和不燃有毒，酸性腐蚀性气体；可燃无毒和可燃有毒、酸性腐蚀气体；易分解或聚合的可燃气体。此类气体在充装时以及在允许的工作温度下贮运和使用过程中均为液态。包括的气体品种有一氟二氯甲烷、二氟氯甲烷、二氟二氯甲烷、二氟溴氯甲烷、三氟氯乙烷、四氟二氯乙烷、五氟氯乙烷、八氟环丁烷、六氟丙烯、氯、三氯化硼、光气、氟化氢、溴化氢、二氧化硫、硫酰氟、二氧化氮、液化石油气、丙烷、环丙烷、丙烯、正丁烷、异丁烷、1-丁烯、异丁烯、(顺)2-丁烯、(反)2-丁烯、R-142b、R143-a、R152a、氯乙烷、二甲醚、氨、乙胺、一甲胺、二甲胺、三甲胺、甲硫醇、硫化氢、氯甲烷、溴甲烷、砷烷、1,3-丁二烯、氯乙烯、环氧乙烷、乙烯基甲醚、R-1113、溴乙烯。
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参考词条