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41.
Jochen Oexmann Christian Hensel Alfons Kather 《International Journal of Greenhouse Gas Control》2008,2(4):539
The simulation tool ASPEN Plus® is used to model the full CO2-capture process for chemical absorption of CO2 by piperazine-promoted potassium carbonate (K2CO3/PZ) and the subsequent CO2-compression train. Sensitivity analysis of lean loading, desorber pressure and CO2-capture rate are performed for various solvent compositions to evaluate the optimal process parameters. EbsilonProfessional® is used to model a 600 MWel (gross) hard coal-fired power plant. Numerical equations for power losses due to steam extraction for solvent regeneration are derived from simulation runs. The results of the simulation campaigns are used to find the process parameters that show the lowest specific power loss. Subsequently, absorber and desorber columns are dimensioned to evaluate investment costs for these main components of the CO2-capture process. Regeneration heat duty, net efficiency losses and column investment costs are then compared to the reference case of CO2-capture by monoethanolamine (MEA).CO2-capture by piperazine-promoted potassium carbonate with subsequent CO2-compression to 110 bar shows energetic advantages over the reference process which uses MEA. Additionally, investment costs for the main components in the CO2-capture process (absorber and desorber columns) are lower due to the enhanced reaction kinetics of the investigated K2CO3/PZ solvent which leads to smaller component sizes. 相似文献
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The effect of heating technologies on CO(2) and energy efficiency of Dutch greenhouse firms 总被引:1,自引:0,他引:1
This paper uses Data Envelopment Analysis to compute measures of the efficiency (relative to a frontier) in terms of the use of all inputs as well as for single inputs like CO(2) and energy for a sample of greenhouse firms in the Netherlands over the period 1991-1995. These efficiency measures are generated for different firms specialised in production of vegetables, flowers, and potplants and with different heating technologies. The empirical results indicate that firms use energy quite efficiently and are less efficient in terms of CO(2) emissions. Firms using conventional heating are overall less efficiently using energy and CO(2) than firms using more advanced heating technologies. Most differences in efficiency between firm types and firms using different heating technologies are statistically significant. Scale adjustments can provide an important contribution to further efficiency improvements. 相似文献
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Jochen Oexmann Alfons Kather Sebastian Linnenberg Ulrich Liebenthal 《Greenhouse Gases: Science and Technology》2012,2(2):80-98
The integration of a post‐combustion CO2 capture unit in a coal‐fired steam power plant leads to a reduction in net power output, where the largest contributors to the power loss are the heat requirement for the regeneration of the chemical solvent in the desorber of the CO2 capture unit (approx. 2/3) and the auxiliary power demand of the CO2 compressor (approx. 1/4). In this review, the layout of the overall process is explained and the interaction of the three sub‐processes power plant, CO2 capture process and CO2 compressor is discussed. The optimization of process parameters of the CO2 capture unit – such as solution flow rate and reboiler temperature – is intricate due to the complex interaction of the sub‐processes. It is shown that although the heat requirement for solvent regeneration has the largest impact on the power output of the overall process, the optimal process parameters that lead to the lowest possible heat requirement of the capture unit do not necessarily coincide with the optimal process parameters that make for the most energy efficient operation of the overall process. Therefore, when optimizing process parameters of CO2 absorption processes in power plants, one should focus on the minimization of the overall power loss instead of solely reducing the heat requirement for solvent regeneration. The described coherences are illustrated by the results of process simulations based on detailed models of a post‐combustion CO2 capture unit using 7 m (30 wt.‐%) monoethanolamine (MEA), of a supercritical, hard‐coal‐fired steam power plant and of a six‐stage, intercooled CO2 compressor. © 2012 Society of Chemical Industry and John Wiley & Sons, Ltd 相似文献
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Zhao Zhonghua Ni Mingjiang Li Xiaodong Chen Tong Buekens Alfons Yan Jianhua 《Environmental science and pollution research international》2017,24(29):23321-23330
Environmental Science and Pollution Research - Unintentional formation of polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/F) is observed and investigated during the thermal desorption in... 相似文献