全文获取类型
收费全文 | 1588篇 |
免费 | 135篇 |
国内免费 | 35篇 |
专业分类
电工技术 | 10篇 |
综合类 | 147篇 |
化学工业 | 911篇 |
金属工艺 | 7篇 |
机械仪表 | 8篇 |
建筑科学 | 298篇 |
矿业工程 | 14篇 |
能源动力 | 47篇 |
轻工业 | 122篇 |
水利工程 | 31篇 |
石油天然气 | 30篇 |
无线电 | 4篇 |
一般工业技术 | 93篇 |
冶金工业 | 13篇 |
原子能技术 | 3篇 |
自动化技术 | 20篇 |
出版年
2024年 | 2篇 |
2023年 | 8篇 |
2022年 | 17篇 |
2021年 | 26篇 |
2020年 | 28篇 |
2019年 | 27篇 |
2018年 | 26篇 |
2017年 | 34篇 |
2016年 | 48篇 |
2015年 | 31篇 |
2014年 | 67篇 |
2013年 | 101篇 |
2012年 | 107篇 |
2011年 | 113篇 |
2010年 | 123篇 |
2009年 | 119篇 |
2008年 | 104篇 |
2007年 | 130篇 |
2006年 | 130篇 |
2005年 | 118篇 |
2004年 | 75篇 |
2003年 | 69篇 |
2002年 | 43篇 |
2001年 | 31篇 |
2000年 | 23篇 |
1999年 | 30篇 |
1998年 | 21篇 |
1997年 | 23篇 |
1996年 | 14篇 |
1995年 | 18篇 |
1994年 | 13篇 |
1993年 | 11篇 |
1992年 | 5篇 |
1991年 | 11篇 |
1990年 | 3篇 |
1989年 | 3篇 |
1987年 | 2篇 |
1986年 | 2篇 |
1984年 | 1篇 |
1951年 | 1篇 |
排序方式: 共有1758条查询结果,搜索用时 15 毫秒
1.
2.
Jean‐Marc Aldric Philippe Thonart 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2008,83(10):1401-1408
BACKGROUND: In the framework of biological processes used for waste gas treatment, the impact of the inoculum size on the start‐up performance needs to be better evaluated. Moreover, only a few studies have investigated the behaviour of elimination capacity and biomass viability in a two‐phase partitioning bioreactor (TPPB) used for waste gas treatment. Lastly, the impact of ethanol as a co‐substrate remains misunderstood. RESULTS: Firstly, no benefit of inoculation with a high cellular density (>1.5 g L?1) was observed in terms of start‐up performance. Secondly, the TPPB was monitored for 38 days to characterise its behaviour under several operational conditions. The removal efficiency remained above 63% for an inlet concentration of 7 g isopropylbenzene (IPB) m?3 and at some time points reached 92% during an intermittent loading phase (10 h day?1), corresponding to a mean elimination capacity of 4 × 10?3 g L?1 min?1 (240 g m?3 h?1) for a mean IPB inlet load of 6.19 × 10?3 g L?1 min?1 (390 g m?3 h?1). Under continuous IPB loading, the performance of the TPPB declined, but the period of biomass acclimatisation to this operational condition was shorter than 5 days. The biomass grew to approximately 10 g L?1 but the cellular viability changed greatly during the experiment, suggesting an endorespiration phenomenon in the bioreactor. It was also shown that simultaneous degradation of IPB and ethanol occurred, suggesting that ethanol improves the biodegradation process without causing oxygen depletion. CONCLUSION: A water/silicone oil TPPB with ethanol as co‐substrate allowed the removal of a high inlet load of IPB during an experiment lasting 38 days. Copyright © 2008 Society of Chemical Industry 相似文献
3.
Claudio Garibay‐Orijel Elvira Ríos‐Leal Jaime García‐Mena Hctor Mario Poggi‐Varaldo 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2005,80(10):1180-1187
A fluidized bed bioreactor (FBBR) was operated for more than 575 days to remove 2,4,6‐trichlorophenol (TCP) and phenol (Phe) from a synthetic toxic wastewater containing 80 mg L?1 of TCP and 20 mg L?1 of Phe under two regimes: Methanogenic (M) and Partially‐Aerated Methanogenic (PAM). The mesophilic, laboratory‐scale FBBR consisted of a glass column (3 L capacity) loaded with 1 L of 1 mm diameter granular activated carbon colonized by an anaerobic consortium. Sucrose (1 g COD L?1) was used as co‐substrate in the two conditions. The hydraulic residence time was kept constant at 1 day. Both conditions showed similar TCP and Phe removal (99.9 + %); nevertheless, in the Methanogenic regime, the accumulation of 4‐chlorophenol (4CP) up to 16 mg L?1 and phenol up to 4 mg L?1 was observed, whereas in PAM conditions 4CP and other intermediates were not detected. The specific methanogenic activity of biomass decreased from 1.01 ± 0.14 in M conditions to 0.19 ± 0.06 mmolCH4 h?1 gTKN?1 in PAM conditions whereas the specific oxygen uptake rate increased from 0.039 ± 0.008 in M conditions to 0.054 ± 0.012 mmolO2 h?1 gTKN?1, which suggested the co‐existence of both methanogenic archaea and aerobic bacteria in the undefined consortium. The advantage of the PAM condition over the M regime is that it provides for the thorough removal of less‐substituted chlorophenols produced by the reductive dehalogenation of TCP rather than the removal of the parent compound itself. Copyright © 2005 Society of Chemical Industry 相似文献
4.
Namoi Shibasaki Ryousuke Obika Toshikuni Yonemoto Teiriki Tadaki 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》1995,63(3):201-208
Suspension cultures of tobacco cells were studied using airlift and rotary-drum bioreactors. The effect of initial concentrations of a major substrate, sucrose, on the growth and production of a secondary metabolite, phenolic compounds, was investigated. The dry weights and total concentrations of the phenolic compounds increased with the initial sucrose concentration in both bioreactors. Both bioreactors were found to have the same tendency for the effect of initial sucrose concentration. The structured model, presented previously was modified by considering that sucrose was hydrolyzed to glucose and fructose by an enzymatic reaction. The previous and the new models were applied to the above two sets of experimental data obtained with two bioreactors, independently. The hydrolysis of sucrose was elucidated to contribute slightly to the overall kinetics of growth and secondary metabolite production in these cultures. Furthermore, the levels of shear damage in each bioreactor were quantitatively compared based on the death rate constant, ki, which is one of the model constants. 相似文献
5.
纳滤膜技术及其应用的研究进展 总被引:6,自引:0,他引:6
随着膜技术的发展,20世纪80年代出现的纳滤膜弥补了反渗透与超滤之间的空白。纳滤膜(nanofiltration membrane,NF)又称“疏松型”反渗透膜。通常情况下,膜的截留相对分子质量界限为200~1 000。与截留相对分子质量相对应的膜孔径为1~3 nm,故将这类膜称为纳滤膜。纳滤膜可以截留糖类等低相对分子质量有机物和高价无机盐(MgSO4等),但对单价无机盐的截留率低(仅为10%~80%),具有相当大的透过能力。由于单价盐可以自由透过纳滤膜,使得膜两侧因离子浓度不同而造成的渗透压差远远低于反渗透膜。在相同通量条件下,纳滤膜所要求的驱动压力比反渗透膜要低得多。一般纳滤的操作压力为0.5~1.5 MPa。由于纳滤膜的这种独特分离性能,确定了它在水软化和低相对分子质量有机物纯化浓缩的地位。此外,纳滤膜能有效去除许多中等相对分子质量溶质,如消毒副产物的前驱物、残留农药和某些色素等,因而在水净化处理和脱色中得到广泛应用。 相似文献
6.
7.
8.
9.
10.
膜生物反应器(MBR)是膜分离与生物反应器相结合的新型水处理技术。焦化污水是一种高浓度、难降解的工业污水,应用传统的生化方法处理焦化污水存在费用大、效率低的缺点。作者采用一体浸没式膜生物反应器处理焦化污水,调整合适的操作参数,污水中主要污染物COD、NH2-N的去除率分别达到80%、98%以上,操作简单,出水水质稳定,且远好于国家一级排放标准,取得了良好的效果,有一定的推广意义。 相似文献