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   550篇
  免费   80篇
  国内免费   26篇
电工技术   2篇
综合类   28篇
化学工业   442篇
金属工艺   2篇
机械仪表   1篇
建筑科学   4篇
矿业工程   10篇
能源动力   7篇
轻工业   7篇
水利工程   1篇
石油天然气   79篇
无线电   11篇
一般工业技术   49篇
冶金工业   5篇
原子能技术   5篇
自动化技术   3篇
  2023年   3篇
  2022年   19篇
  2021年   12篇
  2020年   13篇
  2019年   18篇
  2018年   16篇
  2017年   13篇
  2016年   26篇
  2015年   20篇
  2014年   40篇
  2013年   29篇
  2012年   33篇
  2011年   35篇
  2010年   23篇
  2009年   26篇
  2008年   23篇
  2007年   47篇
  2006年   43篇
  2005年   40篇
  2004年   32篇
  2003年   26篇
  2002年   21篇
  2001年   16篇
  2000年   18篇
  1999年   16篇
  1998年   5篇
  1997年   6篇
  1996年   11篇
  1995年   6篇
  1994年   2篇
  1993年   5篇
  1992年   2篇
  1991年   2篇
  1990年   3篇
  1985年   1篇
  1984年   2篇
  1983年   1篇
  1982年   1篇
  1977年   1篇
排序方式: 共有656条查询结果,搜索用时 31 毫秒
1.
The methanol‐to‐olefins reaction (MTO) was studied in a small‐scale fluidized‐bed reactor over synthesized silicoaluminophosphate (SAPO‐34) catalysts. Mesoporous nanocrystalline SAPO‐34 molecular sieves were synthesized hydrothermally by ultrasonic and microwave‐assisted aging processes in the presence of hexadecyltrimethylammonium bromide (CTAB) and tetradecyldimethyl(3‐trimethoxysilylpropyl)ammonium chloride (TPOAC) as surfactant agents. The Box‐Behnken experimental design method was applied to determine the optimum operating parameters of this process conducted in the fluidized‐bed reactor. The optimum conditions in terms of reaction temperature, ratio of inlet gas velocity to minimum fluidizing velocity, and MeOH weight fraction were evaluated.  相似文献   
2.
Manganese oxides having a tunnel structure (OMS-2) have been utilized as selective catalysts for alcohol oxidation. In this study manganese oxide catalysts were synthesized in different media and modified by exchanging the tunnel cation by H+, using acid treatment or exchanging with NH4+ followed by thermolysis. Various alcohol oxidations were performed using these catalysts to ascertain the influence of synthesis method on their activity. A correlation is made between lattice oxygen instability and activity of the catalysts, which indicates involvement of the lattice oxygen in the mechanism. The exchange of the tunnel cation with the smaller H+ ions leads to weakening of the Mn–O bond, as verified by temperature programmed desorption (TPD) results. Only the chemisorbed oxygen on the surface (O) and the lattice oxygen in the layers close to the surface is involved in the oxygen transfer during the reaction.  相似文献   
3.
Silicoaluminophosphate (SAPO-5) molecular sieves have been synthesised from reaction mixtures having a molar composition of: 0.7–1.0 Al2O3:0.7–1.0 P2O5:0.01–2.0 SiO2:xR:40 H2O (where R = (C2H3)3N or (C2H3)4NOH and x = 1.5–2.5 for (C2H5)5N and 0.5 for (C2H5)4NOH, at 473 K using various sources of alumina and silica. The effects of (i) varying the crystallinity of the alumina source (boehmite) and (ii) the use of different silica sources such as freshly prepared silica either from sodium silicate or paddy husk extract, silica gel from commercial water-glass, and tetraethyl orthosilicate have been studied. The crystallinity of boehmite has been found to have a strong effect on its reactivity towards the formation of SAPO-5. The activity of boehmite for SAPO-5 formation increased with a decrease in its crystallinity (or with increase in its moisture content). Any silica source devoid of sodium ions could be employed for the synthesis of SAPO-5. The process of crystallisation started as early as within 1.5 h of reaction and incorporation of silicon into the AlPO4 framework has been noted at this stage. Formation of some tridymite phase as impurity has been observed under conditions such as (i) SiO2 concentration > 1.7 mole and (ii) x > 2.0 when R = (C2H5)3N.  相似文献   
4.
近年来铈(Ce)基脱硝催化剂成为低温脱硝领域的研究热点,按载体类型可分为金属氧化物催化剂、二氧化钛载体催化剂、分子筛载体催化剂、活性炭及氧化铝载体催化剂等。按催化剂种类分别介绍了掺杂改性、制备工艺、反应条件等对催化剂性能的影响,并阐述了可能的原因机理。目前,铈基催化剂大多处于实验室阶段,工业化应用尚存在问题,尤其作为低温脱硝催化剂,活性中心堵塞问题更加突出,并且催化剂成本较高。未来可从催化剂制备工艺入手解决催化剂成型问题,以实现工业应用。同时探讨催化剂中毒机理,进一步提升其抗中毒能力。另外,寻求适宜的材料与铈掺杂组合,达到高效脱硝和经济效益最大化。  相似文献   
5.
改性催化裂化催化剂研究进展   总被引:1,自引:0,他引:1  
对催化裂化催化剂的活性组分Y型分子筛的脱铝改性及抗重金属污染改性方法和改性后的含Y型沸石的性能进行了详细介绍。重点介绍了经特殊改性的催化裂化催化剂在脱硫、多产柴油及多产丙烯等方面的用途,指出应在现有技术基础上重点开发性能更为优良的多用途催化裂化催化剂。  相似文献   
6.
以三乙胺为模板剂,在合成过程中直接加入了硝酸铬及硅溶胶,水热合成了CrAPO-5和CrAPSO-5杂原子磷铝分子筛。以丙酮为溶剂,过氧化氢为氧化剂,考察了环己烷氧化制取环己酮的反应。反应12h、n(H2O2)/n(C6H12)=1.0、催化剂通量0.01-0.05g,环己烷的转化率最高可达到11.0%,酮醇比可达到1.39。  相似文献   
7.
负载型中孔分子筛催化剂的研究进展   总被引:4,自引:0,他引:4  
本文对M41S中孔分子筛作载体的负载试剂的研究进展进行了综述,主要介绍了负载酸型、负载碱型和负载氧化型催化剂的研究现状,以及对其应用和发展前景作了总结和评述。  相似文献   
8.
Carbon membranes from cellulose and metal loaded cellulose   总被引:1,自引:0,他引:1  
Jon Arvid Lie 《Carbon》2005,43(12):2600-2607
The focus of this work was to find a low-cost precursor for carbon molecular sieve (CMS) membranes, and a simple way of producing them. In addition, several ways of modifying a carbon material are described. The modification method used in this study was metal doping of carbon. CMS membranes were formed by vacuum carbonization of cellulose and metal loaded cellulose. Metal additives include oxides of Ca, Mg, Fe(III) and Si, and nitrates of Ag, Cu and Fe(III).The carbon membrane containing Fe-nitrate has promising separation performance for the gas pairs O2/N2 and CO2/CH4. Carbon containing nitrates of Cu or Ag show high selectivity, but reduced O2 and CO2 permeability compared to carbon with Fe-nitrate. Element analysis indicates that Cu migrates to the carbon surface, creating an extra layer resistance to gas transport. A silver mirror is also seen on the surface of Ag-nitrate-containing carbon. However, the Ag- and Cu-containing membranes show a high H2 permeability. Adding metal oxides makes the carbon membranes retard the transport of easily condensable gases (e.g. CO2). This can be exploited for enhanced H2/CO2 separation efficiency.  相似文献   
9.
碳沉积法制富氮用炭分子筛的研究   总被引:1,自引:0,他引:1  
本文提出的碳沉积法是用煤焦油馏分油的有机溶液浸渍煤炭化物,然后热解以进行“孔调变”。确定了最佳工艺条件,制得富氮性能良好的炭分子筛。并用D-A方程求取了各种样品的微孔结构参数。  相似文献   
10.
环己烷催化氧化催化剂的研究进展   总被引:1,自引:0,他引:1  
综述了国内外环己烷选择性氧化催化剂的研究进展,对目前环己烷氧化所用催化剂体系进行了总结及比较分析,重点介绍了分子筛催化剂体系中TS-1、MCM、SBA-15等分子筛催化体系.  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