首页 | 本学科首页   官方微博 | 高级检索  
文章检索
  按 检索   检索词:      
出版年份:   被引次数:   他引次数: 提示:输入*表示无穷大
  收费全文   113270篇
  免费   2632篇
  国内免费   540篇
电工技术   1290篇
综合类   2533篇
化学工业   16461篇
金属工艺   5567篇
机械仪表   3740篇
建筑科学   3014篇
矿业工程   710篇
能源动力   1820篇
轻工业   7849篇
水利工程   1481篇
石油天然气   493篇
武器工业   14篇
无线电   10822篇
一般工业技术   21547篇
冶金工业   9974篇
原子能技术   439篇
自动化技术   28688篇
  2023年   355篇
  2022年   348篇
  2021年   755篇
  2020年   588篇
  2019年   503篇
  2018年   15217篇
  2017年   14053篇
  2016年   10801篇
  2015年   1453篇
  2014年   1254篇
  2013年   2203篇
  2012年   4614篇
  2011年   10734篇
  2010年   9395篇
  2009年   6635篇
  2008年   7928篇
  2007年   8876篇
  2006年   973篇
  2005年   1920篇
  2004年   1662篇
  2003年   1651篇
  2002年   965篇
  2001年   447篇
  2000年   506篇
  1999年   507篇
  1998年   2350篇
  1997年   1415篇
  1996年   1019篇
  1995年   607篇
  1994年   488篇
  1993年   440篇
  1992年   190篇
  1991年   201篇
  1990年   158篇
  1989年   159篇
  1988年   164篇
  1987年   162篇
  1986年   141篇
  1985年   228篇
  1984年   192篇
  1983年   170篇
  1982年   134篇
  1981年   178篇
  1980年   175篇
  1979年   126篇
  1978年   110篇
  1977年   225篇
  1976年   482篇
  1973年   113篇
  1954年   104篇
排序方式: 共有10000条查询结果,搜索用时 31 毫秒
991.
李灵芝  李建渠 《应用化工》2006,35(8):613-614,631
以TiOSO4为原料,采用化学络合溶胶-凝胶法,结合自蔓燃工艺制备了纳米TiO2粉体和掺杂铁的光催化剂。并以甲基橙为模拟水样,研究了光催化剂的催化性能。结果表明,掺铁的光催化剂比纯纳米TiO2的光催化活性高,在pH=3,催化剂加入量1 g/L,掺铁量为0.5%,溶液浓度为40 mg/L的条件下降解率高达80%。  相似文献   
992.
山西金甲化工有限公司(简称“金甲化工公司”)经历两次增容扩产,目前有61台金属阳极8型电解槽,设计生产能力为年产100%烧碱7kt,2005年产100%烧碱8275t,但因内部原因停车21次,其中,仅因整流柜水系统问题停车达14次之多,因此,在2006年金甲化工公司决定对整流冷却水系统进行改造。1改造前整流冷却系统的工艺情况改造前整流冷却系统(见图1)用水为自来水。自来水内含有大量的受热易结垢和导电的Ca2 、Mg2 等金属阳离子。在循环泵的作用下,冷却水在设备和管道中循环,转移整流系统可控硅发出的热量。而原换热器换热面积只有7m2,因换热面积小,循环…  相似文献   
993.
介绍了使用反相高效液相色谱法对氯溴异氰尿酸烟剂进行定量分析。HPLC法使用C18柱,以V(甲醇)﹕V(水)﹕V(冰乙酸)=15﹕85﹕0.1为流动相,紫外检测波长215nm。方法的变异系数为0.44%,回收率在98%~102%之间。  相似文献   
994.
The maximization of the total surface area of Pt-SnO2/Al2O3 catalyst was studied by using the Taguchi method of experimental design. The catalysts were prepared by sol-gel method. The effects of HNO3, H2O and aluminum nitrate concentrations and the stirring rate on the total surface area were studied at three levels of each. L9 orthogonal array leading nine experiments was used in the experimental design. The parameter levels that give maximum total surface area were determined and experimentally verified. In the range of conditions studied it was found that, medium levels of HNO3 and H2O concentration and lower levels of aluminum nitrate concentration and stirring rate maximize the total surface area.  相似文献   
995.
Pyrolysis of peat obtained from Yeniça?a, Bolu, Turkey was conducted in a fixed-bed tube furnace under various conditions, and variations in the structure of the char, tar and gas products were examined. The chars produced were studied by proximate and ultimate analyses. The maximum tar yield of 20.41% was obtained at a heating rate of 20 °C/min, a temperature of 450 °C, a sweeping gas flow rate of 100 ml/min and a 0.5–2.0 mm size range. The chemical composition of the tar was examined by elemental analysis, FTIR spectroscopy, 1H-NMR spectroscopy and column chromatography. The chemical composition of the tar with dense aliphatic structure was established to be CH1.22O0.25N0.02. The composition of the gases obtained at a heating rate of 20 °C/min for the 0.5–2.0 mm size range was examined by gas chromatography.  相似文献   
996.
997.
998.
A bubbling fluidized bed reactor was used to study CO2 capture from flue gas by using a potassium-based solid sorbent, sorbKX35 which was manufactured by the Korea Electric Power Research Institute. A dry sorbent, sorbKX35, consists of K2CO3 for absorption and supporters for mechanical strength. To increase initial CO2 removal, some amount of H2O was absorbed in the sorbent before injecting simulated flue gas. It was possible to achieve 100% CO2 removal for more than 10 minutes at 60°C and a residence time of 2 s with H2O pretreatment. When H2O pretreatment time was long enough to convert K2CO3 of sorbKX35 into K2CO3 · 1.5H2O, CO2 removal was excellent. The results obtained in this study can be used as basic data for designing and operating a large scale CO2 capture process with two fluidized bed reactors. This work was presented at the 6 th Korea-China Workshop on Clean Energy Technology held at Busan, Korea, July 4–7, 2006.  相似文献   
999.
The coal partial gasification catalyzed by limestone, sodium carbonate and dolomite was studied using a bench-scale atmospheric fluidized bed in the presence of air and steam at 900 °C. The effects of limestone, sodium carbonate and dolomite on composition, heating value, gas yield of product gas and carbon conversion in the catalytic coal partial gasification have been examined. The experimental results show that the catalysts can effectively improve the gas quality, the heating value and the gas yield of product gas and carbon conversion. The catalytic effect of sodium carbonate is better than that of limestone and dolomite. The increase of limestone loading can enhance the quality of product gas, such as the content of combustible gas, the high heating value and the gas yield, during coal partial gasification. This work was presented at the 6 th Korea-China Workshop on Clean Energy Technology held at Busan, Korea, July 4–7, 2006.  相似文献   
1000.
The adsorption of ethyl pyruvate on Pt(111) has been studied by in situ XANES measurements in the presence and absence of hydrogen. Depending on the hydrogen and ethyl pyruvate pressure, the C and O K‐edge spectra exhibit distinctly different angular dependence. Without hydrogen ethyl pyruvate is oriented preferentially perpendicular to the surface, indicating bonding via the O lone pairs. In the presence of hydrogen the mean orientation is more tilted towards the surface. Likely, ethyl pyruvate also interacts with Pt via its π system under these conditions. The observed angle‐dependent shift of the energy of the π* and σ* resonances indicates the coexistence of differently adsorbed ethyl pyruvate species. The experimental findings demonstrate the importance of the in situ approach for unraveling the adsorption mode of ethyl pyruvate in the enantioselective hydrogenation over cinchona‐alkaloid‐modified Pt. This revised version was published online in July 2006 with corrections to the Cover Date.  相似文献   
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号