共查询到20条相似文献,搜索用时 46 毫秒
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国外已广泛应用液化石油气代替汽油做汽车的燃料并显示出很多优点,作者介绍了液化石油及汽油的性能以及用液化石油气做汽车燃料的实现方法。 相似文献
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液化石油气作汽车燃料浅议哈尔滨市燃气安全管理处鲍靖宇1问题的提出随着世界各国汽车工业迅速发展,汽车数量不断增加,燃料需求矛盾越来越大,世界性能源日益紧张,汽车尾气排放已成为公害。据国家环保部门测定,城市主要道路的一氧化碳、氮氢化物等对人体有毒气体都处... 相似文献
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汽油—液化石油气(LPG)双燃料在Santana2000发动机上的应用 总被引:1,自引:0,他引:1
本文通过Santana2000化油器发动机改燃LPG的试验,得到了Santana2000发动机燃烧LPG和汽油的性能对比结果,这些结果对今后进一步开发LPG汽车及其零部件提供了重要的依据。 相似文献
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液化石油气比其它气体燃料热值高又便于储存运输。它是一种优良的民用燃料,也是点燃式发动机理想的代用燃料。由于各种原因,我国在车辆上使用液化石油气的工作开展不广。为了更合理有效地利用液化石油气资源,作者探索在柴油发电机组上燃用液化石油气,将柴油机改装成液化石油气-柴油双燃料发动机。本文介绍了这种发动机双燃料供给系统的方案以及在2135柴油发电机组上进行试验的情况。 相似文献
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国外已广泛应用液化石油气代替汽油做汽车的燃料并显示出很多优点。作者介绍了液化石油气及汽油的性能以及用液化石油气做汽车燃料的实现方法。 相似文献
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对EQ6100发动机燃用LPG做外特性试验,发动机动力性有所降低,造成的原因有多个方面,通过科学的调整是可以补偿其动力性能的。 相似文献
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汽油—液化石油气(LPG)两用燃料发动机的研究 总被引:5,自引:2,他引:5
介绍了汽油-液化石油气(LPG)两用燃料发动机空燃比的调节和作者研制成功的无混合器式双蒸发器LPG供气系统,该供气系统取消了LPG发动机惯用的混合器,在原机双腔化油器的主、副腔喉管处钻孔,接入LPG主供气系和LPG加浓系,从而取消了混合器,解决了全负荷时动力性与部分负荷时燃料经济性、排放之间的矛盾,取得了良好的效果。用该系统改装的汽油-LPG两用燃料发动机,在燃用汽油时性能无任何变化,燃用LPG时取得了动力性、燃料经济性和排放指标俱佳的效果。 相似文献
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综述了液化石油气(LPG)汽车的环保优势,在发动机台架上评价了不同起配比的液化石油气与市售车用汽油在不同转速和负荷时的排放和动力性能指标等。车用LPG对油气而言有20%~30%的价格优势,无论从经济效率还是社会效益看,在我国大中城市推LPG车的条件已经成熟。 相似文献
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The effects of the length of the gas flow path from the exhaust outlet in the cylinder head to the catalyst inlet in the exhaust line, the ignition timing and the engine idle speed on the three-way catalyst light-off behavior in an electronically controlled inlet port LPG (liquefied petroleum gas) injection SI (spark-ignition) engine during cold start were investigated experimentally. The results showed that these factors affect the catalyst light-off behavior significantly during cold start. The reduction of the gas flow path length upstream the catalyst reduces the heat loss from the exhaust gases, increases the temperature of the catalyst, and results in faster catalyst light-off. Retarding the ignition timing from 0 to 15°CA ATDC decreases 22 and 8 s catalyst light-off time for HC and CO respectively. Increasing the engine idle speed from 1400 to 1800 rpm decreases 19 and 15 s the light-off time for HC and CO respectively. 相似文献
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Noel D. Uri 《国际能源研究杂志》1994,18(9):783-797
The paper begins by discussing the importance of accurate estimates of the price elasticity of demand and some of the problems frequently encountered in obtaining these estimates. To these problems is added that associated with inaccuracy in the measurement of the dependent variable and one or more of the independent variables that affect the quantity demanded. Two diagnostics, i.e. the regression coefficient bounds and the bias correction factor, have been introduced to assess the effect that such measurement error has on the estimated coefficients of demand relationships. The use of these diagnostics will aid in assessing the integrity of the estimates obtained. In considering the demand for natural gas and the demand for liquefied petroleum gas by farmers in the USA, both the quantity demanded and the price data available for demand model estimation purposes contain measurement error. The regression coefficient bounds diagnostic was used to indicate a range over which the true price responsiveness of farmers to changes in energy prices lies. The results suggest that each 1% increase (decrease) in the price of energy will result in a decrease (increase) of between 0.41 and 0.17% in the quantity of natural gas demanded and a decrease (increase) of between 0.48 and 0.07% in the quantity of liquefied petroleum gas demanded. The bias correction factor was computed to evaluate the magnitude of the underestimation of the responsiveness of the quantity of natural gas and liquefied petroleum gas demanded to a change in the number of acres irrigated. For natural gas, the under-estimation was 26.5%, whereas, for liquefied petroleum gas, it was 9.5%. 相似文献
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Kui ShenXueguang Wang Xiujing ZouXinxing Wang Xionggang LuWeizhong Ding 《International Journal of Hydrogen Energy》2011,36(8):4908-4916
A series of Ni/MgxAl catalysts with different Mg/Al molar ratios were prepared by impregnating Mg-Al mixed oxides with nickel nitrate aqueous solution and used for the pre-reforming of LPG in the temperature range of 400-500 °C. XRD and H2-TPR results showed that the Ni/MgxAl catalysts calcined at 800 °C mainly consisted of γ-Al2O3, Mg(Ni)Al2O4 and Mg(Ni)O phases varying with Mg/Al molar ratio without free NiO species observed. The effects of Mg/Al molar ratio, S/C molar ratio and reaction temperature on the catalytic behavior of the Ni/MgxAl catalysts were investigated in detail. The results revealed that the catalyst with Mg/Al molar ratio of 1.25 had the highest catalytic activity and stability. The increase in S/C molar ratio promoted both the steam reforming of LPG and the methanation of carbon oxides and hydrogen. The stability tests of 15%Ni/Mg1.25Al catalyst showed that the catalyst was stable for the pre-reforming of LPG, and the stability decreased with elevating the reaction temperature due to more coke deposition. 相似文献
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Xiujing Zou Xueguang WangKui Shen Xionggang LuWeizhong Ding 《International Journal of Hydrogen Energy》2010
The pre-reforming of commercial liquefied petroleum gas (LPG) was investigated over Ni–CeO2 catalysts at low steam to carbon (S/C) molar ratios less than 1.0. It was found that the catalytic activity and selectivity depended strongly on the nature of the support and the interaction between Ni and CeO2. The Ni–CeO2/Al2O3 catalysts, which were prepared by impregnating boehmite (AlOOH) with an aqueous solution of cerium and nickel nitrates, exhibited the optimal catalytic activity and remarkable stability for the steam reforming of LPG in the temperature range of 275–375 °C. The effects of CeO2 loading, reaction temperature and S/C ratio on the catalytic behavior of the Ni–CeO2/Al2O3 catalysts were discussed in detail. The results showed that the catalysts with 10 wt.% CeO2 had the highest catalytic activity, and higher S/C ratios contributed to LPG reforming and the methanation of carbon oxides and hydrogen. The XRD and H2-TPR analyses revealed that the strong interaction between Ni and CeO2 resulted in the formation of CeAlO3 in the Ni–CeO2/Al2O3 catalysts reduced. The stability tests of 15Ni–10CeO2/Al2O3 catalyst at 350 °C indicated that the catalyst was stable, and the stability could be enhanced by increasing S/C ratio. 相似文献
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