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排序方式: 共有863条查询结果,搜索用时 15 毫秒
1.
本文以NH3-H2O系统Gibbs自由能、熵、焓和汽液相平衡的热力学模型为基础,用松弛法进行了无水氨精馏塔的模拟计算。改变无水氨采出比、回流比(直汽量)和进料板位置均影响蒸馏效果。 相似文献
2.
Non-pinched, minimum energy solutions are important class of distillation designs that offer the potential advantage of a better trade-off between capital investment and operating costs. In this paper, two important tasks associated with non-pinched distillation designs are studied. Thus the novel contributions of this work to the literature are
- (1) A comprehensive methodology for finding non-pinched minimum energy designs.
- (2) Understanding of the reasons for the existence of non-pinched distillation designs.
3.
本文对采用S1和S2的混合物作为萃取剂的三聚甲醛萃取-精馏新工艺进行了模拟计算,得到了使总费用最低的三聚甲醛精制工艺的联合操作参数。模拟计算结果成功地指导了小试操作,并可为大型工程设计提供可靠的基础数据。 相似文献
4.
This paper addresses the application of Genetic Programming (GP) to the synthesis of multicomponent product nonsharp distillation
sequences. Combined with the domain knowledge of chemical engineering, some evolutionary factors are improved, and a set of
special encoding method and solving strategy is proposed to deal with this kind of problem. The system structural variable
is optimized by GP and the continuous variable is optimized by the simulated annealing algorithm simultaneously. Because GP
has an automatic searching function, the optimal solution can be found including distillation, splitting, blending and bypassing
operations automatically without any superstructures of nonsharp distillation sequences. Three illustrative examples are presented
to demonstrate the effective computational strategies. 相似文献
5.
Unusual extended corrosion phenomena were detected in a distillation column made in AISI type 316 stainless steel (UNS S31600) of a plant for natural pectins extraction from citrus. The column was the first of a series of two distillation columns representing the unit core. Corrosion problems were observed only in that column and mainly along the surface of the trays located in the lower section of the column. The phenomenon was observed subsequently to a modification of the original plant layout that caused an increase of the operating temperatures and turbulence of the process stream inside the column. 相似文献
6.
采用非平衡级METSH方程组,对丙烯精馏过程进行了模拟计算和优化,提出了一种全新的、实用的塔板组成的圆整归一方法,摸索出了一套行之有效的计算程式,大大提高了模型方程组迭代计算的收敛性,求解更加稳定。本文还以精馏塔利润为目标,建立了优化目标函数,进行了优化计算,计算结果对丙烯塔生产具有一定意义。 相似文献
7.
Six distillation column models have been used in studies of the usefulness of the Inverse Nyquist Array (INA) method for design of dual composition control for distillation. Five of the column models are experimental, one describing an industrial column, the others four pilot plants. One column model is obtained by modeling from first principles.
The control strategies investigated and compared are multiloop SISO, 2-way decoupling and l-way decoupling. The control variables are the standard ones, i.e. reflux flow and boilup.
In most of the cases INA has been found to be a useful tool for design of the loops and for comparison of the different control approaches. INA has also been found to be useful for simultaneous tuning of the decouplers and the feedback controllers.
For 2-way decoupling the criterion to minimize interaction at the critical frequency for each primary feedback loop has been found useful in most, but not all, cases. The scheme can be designed by pure gains in the decouplers and there is no reason to introduce dynamics into the decouplers—the systems studied are already sufficiently rich in dynamics.
INA has been found to be a suitable vehicle for the choice between the two possible l-way decoupling schemes.
With the design approach taken, l-way decoupling has been found to provide considerably better control quality than 2-way decoupling in two of the six systems, the differences in control quality being small in the other cases.
The effect of model mismatching on the results, caused e.g. by process nonlinearities, is discussed and simple rules to decrease the parameter sensitivity for 2-way decoupling schemes are given. When model mismatching is considered, the advantage of l-way decoupling over 2-way decoupling seems to increase.
One deficiency of the INA design as used in this paper is that it does not single out the design which is to be preferred on the grounds of robustness. 相似文献
The control strategies investigated and compared are multiloop SISO, 2-way decoupling and l-way decoupling. The control variables are the standard ones, i.e. reflux flow and boilup.
In most of the cases INA has been found to be a useful tool for design of the loops and for comparison of the different control approaches. INA has also been found to be useful for simultaneous tuning of the decouplers and the feedback controllers.
For 2-way decoupling the criterion to minimize interaction at the critical frequency for each primary feedback loop has been found useful in most, but not all, cases. The scheme can be designed by pure gains in the decouplers and there is no reason to introduce dynamics into the decouplers—the systems studied are already sufficiently rich in dynamics.
INA has been found to be a suitable vehicle for the choice between the two possible l-way decoupling schemes.
With the design approach taken, l-way decoupling has been found to provide considerably better control quality than 2-way decoupling in two of the six systems, the differences in control quality being small in the other cases.
The effect of model mismatching on the results, caused e.g. by process nonlinearities, is discussed and simple rules to decrease the parameter sensitivity for 2-way decoupling schemes are given. When model mismatching is considered, the advantage of l-way decoupling over 2-way decoupling seems to increase.
One deficiency of the INA design as used in this paper is that it does not single out the design which is to be preferred on the grounds of robustness. 相似文献
8.
Tiina Komulainen Mauri Sourander Sirkka-Liisa Jms-Jounela 《Computers & Chemical Engineering》2004,28(12):2611-2619
9.
在对旋转填料床精馏特性研究的基础上,以塑料多孔板为填料,乙醇-水为体系,在全回流操作条件下,进一步研究了气相动能因子F、超重力因子β和回流量L对旋转填料床流体力学特性的影响,证明了旋转填料床的低耗能特性。 相似文献
10.
塔板效率包括:点效率、莫夫里效率和全塔效率,它们的值主要受流体多相流动时的动力学体系特性的影响;点效率可由双膜理论推出,莫夫里效率和全塔效率存在一定的内在关系。 相似文献