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    Study of Miscibility of Lower Alcohols with Gasoline
    低碳燃料醇与汽油掺合性的研究
    Synthesis gasoline process from CO+H_2 in high-speed fixed bed
    高速固定床CO+H_2合成汽油
    Mathematical Models for the First Stage Hydrogenation Reaction of Cracked Gasoline
    裂解汽油加氢—段绝热反应器的数学模型
    DEVELOPMENT OF TWO-STAGE MODIFIED FT(MFT) GASOLINE SYNTHESIS PROCESS FROM SYNGAS
    CO+H_2两段法合成汽油(MFT)过程开发
    STUDY ON KINETICS OF METHANOL TO GASOLINE REACTION
    甲醇制汽油反应及动力学研究
    DEVELOPMENT OF CHINA'S AUTOMOBILE GASOLINE VARIETIES AND QUALITY
    我国车用汽油产品质量发展
    The saturation sulfur capacity of CuY-135-500 type zeolite absorbent which was prepared under above optimum conditions for model gasoline could reached 8.61%(mass fraction) at the conditions of atmospheric pressure,room temperature and LHSV 10h1.
    在上述条件下制得的分子筛吸附剂对模型汽油在常压、室温、液体时空速为10 h-1时的饱和硫容量为8.61%(质量分数)。
    The thermal properties of the modified PVA, as well as the effect of the content of the modifiers on the gasoline barrier property of the modified PVA blown tubes were studied, and the permeation resistance of PVA and HDPE blown tubes against gasoline was compared.
    研究了改性PVA的热性能及改性剂含量对PVA吹塑管坯汽油阻隔性能的影响,并比较了PVA与HDPE吹塑管坯的汽油阻隔性。
    SBA-15-SO3 Ag obtained via ion exchange with Ag+ is used to remove dibenzothiophene from a model gasoline such as octane. The adsorption capacity reaches 12.15 mg/g for sulfide under the same conditions at DBT concentration of 4 000 mg/L.
    SBA-15-SO3H具有较高的Ag+交换率,在正辛烷和二苯并噻吩(DBT)组成的汽油模拟体系中,吸附载体用量不变的情况下,DBT的初始浓度为4000 mg/L时,测得SBA-15-SO3Ag对硫吸附量达到了12.15 mg/g.
    Results show that the contents of C5= and C6= in FCC gasoline can be enhanced via using the ZSM-5 catalyst in catalytic cracking.
    结果表明,催化裂化过程添加ZSM-5催化剂可提高汽油中C=5、C=6的质量分数。
    The effects of temperature and flow velocity of N2 on propylene yields of cracking light gasoline and 2M-1-C5= are nearly the same,namely propylene yield increases when temperature increases or flow velocity of N2 decreases.
    在脉冲色谱装置上,反应温度和载气流量对轻汽油和2M-1-C=5裂化生产丙烯的影响一致,即反应温度升高,载气流量降低,丙烯收率增加。
    Inverse emulsion copolymerization of C 16 DMAAC and AM was carried out using Span-80 and OP-10 as emulsifying agent,K 2S 2O 8-Na 2S 2O 4 and W-044 as initiator, gasoline as oil-phase medium The particles size distribution in inverse emulsion and the molecular weight were studied;
    以Span - 80、OP - 10为乳化剂,K2 S2 O8、Na2 S2 O4 、W - 0 4 4为引发剂,以12 0 #汽油为分散介质,用反相乳液聚合法制备出二甲基十六烷基烯丙基氯化铵/丙烯酰胺共聚物,并且用粒度分布仪进行了表征。
    The mesoporous silica MCM-41 with large pore volume and pore diameter of 0. 96 cm3/g and 4. 74 nm, respectively, can be obtained by adding proper amount of 90# gasoline to original reactive formulation, which indicated that the added gasoline played a role of pore diameter expander.
    向反应体系中添加适量的90#商用汽油,可以起到扩孔的作用,使得介孔MCM-41的孔体积和孔径变大,分别为0.96 cm3/g和4.74 nm。
    APPLICATION OF FIBER-FILM CONTACTOR IN GASOLINE CAUSTIC WASHING
    纤维膜接触器在汽油碱洗中的应用
    Study on The Synthesis of 4 - Aminotoluene - 3 - Sulphonic Acid by Solvent Naphtha
    在溶剂汽油中合成4-氨基甲苯-3-磺酸的研究
    Design and industrial application of DOCP(jl)catalyst for PHV upgrading
    提高汽油辛烷值催化剂DOCP(jl)配方设计及工业应用
    Development of a Co-Mo-Ni/Al_2O_3 pyrolysis gasoline hydrogenation catalyst
    Co-Mo-Ni/Al_2O_3型裂解汽油加氢催化剂的研制
    Carbonylation of C_6~C_8 olfins from waxcracking to C_7~C_9 mixed fatty acid esters
    石油裂解汽油烯羰化酯化制C_7~C_9混合脂肪酸酯
    Formula Design of Catalysts Matching Petrol Vehicles
    匹配汽油车的催化剂配方设计
    SIMULATION OF GASOLINE FRACTIONATOR SYSTEM BY ASPEN PLUS
    用Aspen Plus模拟汽油分馏塔系统
 

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