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Simulation of DME synthesis from coal syngas by kinetics model 总被引:1,自引:0,他引:1
Hyun Min Shim Seung Jong Lee Young Don Yoo Yong Seung Yun Hyung Taek Kim 《Korean Journal of Chemical Engineering》2009,26(3):641-648
DME (Dimethyl Ether) has emerged as a clean alternative fuel for diesel. There are largely two methods for DME synthesis.
A direct method of DME synthesis has been recently developed that has a more compact process than the indirect method. However,
the direct method of DME synthesis has not yet been optimized at the face of its performance: yield and production rate of
DME. In this study it is developed a simulation model through a kinetics model of the ASPEN plus simulator, performed to detect
operating characteristics of DME direct synthesis. An overall DME synthesis process is referenced by experimental data of
3 ton/day (TPD) coal gasification pilot plant located at IAE in Korea. Supplying condition of DME synthesis model is equivalently
set to 80 N/m3 of syngas which is derived from a coal gasification plant. In the simulation it is assumed that the overall DME synthesis
process proceeds with steadystate, vapor-solid reaction with DME catalyst. The physical properties of reactants are governed
by Soave-Redlich-Kwong (SRK) EOS in this model. A reaction model of DME synthesis is considered that is applied with the LHHW
(Langmuir-Hinshelwood Hougen Watson) equation as an adsorption-desorption model on the surface of the DME catalyst. After
adjusting the kinetics of the DME synthesis reaction among reactants with experimental data, the kinetics of the governing
reactions inner DME reactor are modified and coupled with the entire DME synthesis reaction. For validating simulation results
of the DME synthesis model, the obtained simulation results are compared with experimental results: conversion ratio, DME
yield and DME production rate. Then, a sensitivity analysis is performed by effects of operating variables such as pressure,
temperature of the reactor, void fraction of catalyst and H2/CO ratio of supplied syngas with modified model. According to simulation results, optimum operating conditions of DME reactor
are obtained in the range of 265–275 °C and 60 kg/cm2. And DME production rate has a maximum value in the range of 1–1.5 of H2/CO ratio in the syngas composition. 相似文献
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SIMULATION STUDIES OF THE REMOVAL OF WATER FROM ETHANOL BY A CATALYTIC DISTILLATION PROCESS 总被引:1,自引:0,他引:1
Christina B. Dirk-Faitakis Karl T. Chuang 《Chemical Engineering Communications》2005,192(11):1541-1557
A new approach based on catalytic distillation (CD) technology was proposed to remove water from ethanol. Isobutylene was introduced to react with water in the CD column. The commercial software simulation tool Aspen Plus was used to investigate the effects of key design factors such as operating pressure and temperature, reactant ratios, reflux and distillate to feed ratios, number of separation and reaction stages, and feed and reaction zone location. It was found that the CD technology offers potential advantages of reduced energy consumption and reduced capital cost over traditional approaches for the removal of water from ethanol. 相似文献
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基于Aspen Plus工作平台,运用Gibbs自由能最小化原理,对气流床粉煤气化过程进行了数值模拟,并对流程算法进行了改进。研究了氧煤比、蒸气煤比、压力及粉煤粒径对气化炉出口气体组成、温度、冷煤气效率、碳转化率及有效气产率的影响。结果表明:模拟值和实验值有良好的相似性;氧煤比对气化进程的影响较蒸汽煤比及其它操作条件更为显著;并确定了模拟煤种的最佳氧煤比是0.70~0.80kg/kg,气化炉出口CO+H2的最大干基体积分数为96.48%,冷煤气效率最高为83.56%,最大有效气产率为1.74m^3/kg;氧煤比每升高0.1kg/kg,气化炉出口温度升高约40℃,而蒸汽煤比每升高0.1kg/kg,气化炉出口温度降低约8℃。 相似文献
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Matlab语言强大的运算、仿真能力,被广泛用在液压控制系统中。利用Matlab语言可以进行液压特性曲线的绘制,液压控制系统稳定性的检测,也可以进行液压控制系统的仿真。这里以两个实例,即单、双喷嘴挡板阀压力流量特性曲线的绘制,以及液压转矩放大器系统稳定性的检测,来说明它的强大的功能。 相似文献
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目的建立篮式生物反应器制备Vero细胞乙型脑炎灭活疫苗的工艺。方法利用7.5L篮式生物反应器和片状载体培养Vero细胞,接种乙型脑炎病毒P3V2株毒种,根据葡萄糖的消耗量,分析细胞的生长情况及调节病毒培养时的灌流速度,每24h取样,检测病毒滴度。收获的病毒液经纯化后,制备乙脑灭活疫苗,检测各项指标。结果Vero细胞培养至96h,葡萄糖消耗量达高峰,细胞密度达峰值;接种病毒后72h,葡萄糖消耗量达高峰,灌流量为7L/d,连续收获7~9d,共可收获(40±5)L病毒液;96h病毒滴度达高峰,为10.0LgLD50/ml;制备的乙型脑炎灭活疫苗各项指标均达到《中国药典》三部(2005版)要求。结论已建立了篮式生物反应器制备Vero细胞乙型脑炎灭活疫苗的工艺。 相似文献
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应用Polymers Plus和Aspen Dynamics软件建立聚丙烯装置稳态及动态模型.详细介绍了建立稳态模型的主要步骤,对建模过程的难点和影响模型准确程度的因素进行了分析。指出聚丙烯装置建模过程的关键在于确定物性参数及应该包含的反应;难点在于多牌号单活性中心稳态模型的优化。 相似文献
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