全文获取类型
收费全文 | 1601篇 |
免费 | 140篇 |
国内免费 | 170篇 |
专业分类
电工技术 | 55篇 |
综合类 | 138篇 |
化学工业 | 150篇 |
金属工艺 | 87篇 |
机械仪表 | 288篇 |
建筑科学 | 81篇 |
矿业工程 | 26篇 |
能源动力 | 39篇 |
轻工业 | 93篇 |
水利工程 | 13篇 |
石油天然气 | 37篇 |
武器工业 | 11篇 |
无线电 | 57篇 |
一般工业技术 | 298篇 |
冶金工业 | 74篇 |
原子能技术 | 89篇 |
自动化技术 | 375篇 |
出版年
2024年 | 13篇 |
2023年 | 30篇 |
2022年 | 57篇 |
2021年 | 64篇 |
2020年 | 70篇 |
2019年 | 53篇 |
2018年 | 46篇 |
2017年 | 55篇 |
2016年 | 65篇 |
2015年 | 48篇 |
2014年 | 96篇 |
2013年 | 98篇 |
2012年 | 124篇 |
2011年 | 144篇 |
2010年 | 85篇 |
2009年 | 99篇 |
2008年 | 85篇 |
2007年 | 97篇 |
2006年 | 101篇 |
2005年 | 85篇 |
2004年 | 60篇 |
2003年 | 55篇 |
2002年 | 59篇 |
2001年 | 55篇 |
2000年 | 42篇 |
1999年 | 29篇 |
1998年 | 15篇 |
1997年 | 23篇 |
1996年 | 13篇 |
1995年 | 7篇 |
1994年 | 7篇 |
1993年 | 8篇 |
1992年 | 6篇 |
1991年 | 4篇 |
1990年 | 5篇 |
1989年 | 1篇 |
1988年 | 1篇 |
1985年 | 1篇 |
1982年 | 3篇 |
1980年 | 1篇 |
1975年 | 1篇 |
排序方式: 共有1911条查询结果,搜索用时 15 毫秒
981.
移动式容器中液体的晃动及其影响因素的研究 总被引:1,自引:0,他引:1
保证移动式压力容器的运行安全具有特殊重要性。结合典型移动式压力容器———罐式集装箱,数值模拟了罐体内液体的晃动过程,重点考察了冲击力、压强、雷诺数等物理量的变化。结果发现,晃动所产生的最大压强远大于初始最大静压强,晃动过程中流场湍动剧烈;加速度越大,充装率越大,容积越小,最大冲击力出现的时刻越早;当罐内充装一半液体,即充装率为0.5时,晃动最剧烈;在数值模拟基础上,以加速度、充装率、介质密度和罐体容积等变量为参数,拟合出液体晃动对罐体封头的最大冲击力计算公式,精度超过95%;对于湍流状态的晃动,黏度对最大冲击力的影响很小。 相似文献
982.
针对物位计普遍存在着灰尘对波的漫反射而导致误判断这一突出问题,在研究了仪表的构成与工作原理基础上,利用γ射线穿透的方法设计了测量密闭容器物位测量方案。该设计方案在物位测量领域有着较大的应用前景。 相似文献
983.
针对化工、制药、食品等行业中所用不锈钢容器表面质量不好、产品易污染的问题,设计并研制了简易、轻巧的小口径不锈钢圆桶容器内壁抛磨装置。经该装置抛磨后,可去除小桶内壁表面氧化层、降低表面粗糙度值,解决了传统工艺中的技术难题,对提高产品质量具有现实意义。 相似文献
984.
985.
986.
987.
Kyung Soo Lee Sung Woon Cha Sun Mo Koo 《Polymer-Plastics Technology and Engineering》2013,52(8):781-788
Food can be preserved for long periods in containers made of thermoformed multilayered plastic. However, nonsystematic techniques based on field experience and knowledge must be used to design and produce multilayered plastic products, and problems are typically resolved by trial-and-error rather than cause analysis. Therefore, we evaluated and analyzed existing manufacturing techniques and developed a new process by adapting axiomatic design to the design and development of thermoformed multilayered plastic product (container). The feasibility of our new process was validated through case studies that examined the stacking and shrinkage properties of the resulting plastic products. 相似文献
988.
989.
990.
C.G. Bailey D.S. Jayas R.A. Holley L.E. Jeremiah C.O. Gill 《Food research international (Ottawa, Ont.)》1997,30(10):743-753
In today's market, fresh red meat is cut and packaged at both the wholesale and retail level. Greater economies could result if the wholesaler prepared all consumer cuts centrally, but the short storage life of meat limits distribution. Use of CO2-controlled atmosphere, master packaging, and strict temperature control (−1.5±0.5°C) can enhance storage life and, therefore, distribution ease. An insulated shipping and storage container was designed and tested for its suitability to distribute master-packaged meat. Shelves in the container supported 36 master trays (508 × 381 × 60 mm), with the source of refrigeration being injected liquid nitrogen (N2). Electric fans dispersed the N2 gas throughout the container. To reduce costs, 36 saline water bags (10% w/v NaCl) were used to thermally simulate the meat. Temperatures of 20 bags were recorded during storage experiments. The container was tested at outside temperatures of 15, 0 and −15°C with 4 internal fans and at 30°C with 2, 4 and 6 fans. In all instances, bags cooled from 10°C to an equilibrium temperature of −1.5°C within 5.5 h. Minimum equilibrium temperatures during any 8 h trial were −2.6, −2.0 and −2.0°C for 2, 4 and 6 fans, respectively. Correspondingly, maximum temperatures were −0.2, −0.7 and −0.3°C. Initial chilling of the product required, on average, 19 kg of N2, while equilibrium was maintained at a N2 consumption rate of 5.5, 4.0, 2.6 and 0.93 kg/h at outside temperatures of 30, 15 0 and −15°C, respectively, with 4 fans. The N2 use for 2 and 6 fans was 5 and 6.3 kg/h, respectively, at an outside temperature of 30°C. During simulated power failure or when the N2-tank ‘ran dry', temperatures in the container rose 0.9 and 2.0°C/h, respectively. When the door to the container was opened long enough to remove three trays, temperature was restored within 5 min. Convective heat transfer coefficients between saline water bags and circulating N2 were in the range of 80–100, 115–135, and 140–155 W/(m2·K) for 2, 4 and 6 fans, respectively. Heat transfer to meat will be limited by conduction in master packaged meat if similar convection coefficients prevail. 相似文献