全文获取类型
收费全文 | 1397篇 |
免费 | 167篇 |
国内免费 | 1011篇 |
专业分类
安全科学 | 61篇 |
废物处理 | 119篇 |
环保管理 | 118篇 |
综合类 | 1587篇 |
基础理论 | 174篇 |
污染及防治 | 420篇 |
评价与监测 | 90篇 |
社会与环境 | 6篇 |
出版年
2024年 | 1篇 |
2023年 | 12篇 |
2022年 | 64篇 |
2021年 | 58篇 |
2020年 | 72篇 |
2019年 | 72篇 |
2018年 | 95篇 |
2017年 | 82篇 |
2016年 | 93篇 |
2015年 | 124篇 |
2014年 | 168篇 |
2013年 | 163篇 |
2012年 | 174篇 |
2011年 | 149篇 |
2010年 | 129篇 |
2009年 | 129篇 |
2008年 | 136篇 |
2007年 | 138篇 |
2006年 | 147篇 |
2005年 | 91篇 |
2004年 | 76篇 |
2003年 | 62篇 |
2002年 | 52篇 |
2001年 | 40篇 |
2000年 | 39篇 |
1999年 | 29篇 |
1998年 | 27篇 |
1997年 | 34篇 |
1996年 | 32篇 |
1995年 | 24篇 |
1994年 | 17篇 |
1993年 | 17篇 |
1992年 | 9篇 |
1991年 | 11篇 |
1990年 | 3篇 |
1989年 | 2篇 |
1987年 | 1篇 |
1986年 | 2篇 |
1979年 | 1篇 |
排序方式: 共有2575条查询结果,搜索用时 31 毫秒
171.
172.
173.
厌氧膨胀床处理低浓度污水的污泥颗粒和生物活性变化 总被引:1,自引:0,他引:1
污泥的聚集形态和活性,是影响厌氧反应器处理效率的关键因素。通过对厌氧膨胀床反应器(anaerobicex—pandedblanketreactor,AEBR)处理低浓度城镇污水在启动和稳定运行期的污泥活性研究,AEBR在启动运行期内,接种颗粒污泥为适应低浓度基质条件,污泥粒径经历从大变小,再重新颗粒化粒径变大的过程。在运行期第103天,粒径小于1000μm污泥的体积比达到44.7%,平均粒径为952μm,到运行期第173天,粒径小于1000μm污泥的体积比降为28%,平均粒径达1179μm,污泥重新颗粒化完成。颗粒污泥适应新的环境后,单位重量污泥的最大比产甲烷活性(specificmetha.nogensisactivity,SMA)值和胞外聚合物含量增加,分别达到112mLCH4/(gVSS·d)和215mg/gVSS。在处理实际城镇污水的AEBR反应器内,辅酶F420含量可以有效指示污泥样品的产甲烷活性,AEBR反应器不同高度位置的污泥活性不一样,反应器底部污泥活性低于中上部区域污泥的活性。 相似文献
174.
175.
A. Chiumenti F. da Borso R. Chiumenti F. Teri P. Segantin 《Waste management (New York, N.Y.)》2013,33(6):1339-1344
Vacuum evaporation consists in the boiling of a liquid substrate at negative pressure, at a temperature lower than typical boiling temperature at atmospheric conditions. Condensed vapor represents the so called condensate, while the remaining substrate represents the concentrate.This technology is derived from other sectors and is mainly dedicated to the recovery of chemicals from industrial by-products, while it has not been widely implemented yet in the field of agricultural digestate treatment. The present paper relates on experimental tests performed in pilot-scale vacuum evaporation plants (0.100 and 0.025 m3), treating filtered digestate (liquid fraction of digestate filtered by a screw-press separator). Digestate was produced by a 1 MWe anaerobic digestion plant fed with swine manure, corn silage and other biomasses. Different system and process configurations were tested (single-stage and two-stage, with and without acidification) with the main objectives of assessing the technical feasibility and of optimizing process parameters for an eventual technology transfer to full scale systems.The inputs and outputs of the process were subject to characterization and mass and nutrients balances were determined.The vacuum evaporation process determined a relevant mass reduction of digestate.The single stage configuration determined the production of a concentrate, still in liquid phase, with a total solid (TS) mean concentration of 15.0%, representing, in terms of mass, 20.2% of the input; the remaining 79.8% was represented by condensate. The introduction of the second stage allowed to obtain a solid concentrate, characterized by a content of TS of 59.0% and representing 5.6% of initial mass.Nitrogen balance was influenced by digestate pH: in order to limit the stripping of ammonia and its transfer to condensate it was necessary to reduce the pH. At pH 5, 97.5% of total nitrogen remained in the concentrate. This product was characterized by very high concentrations of total Kjeldhal nitrogen (TKN), 55,000 mg/kg as average.Condensate, instead, represented 94.4% of input mass, containing 2.5% of TKN. This fraction could be discharged into surface water, after purification to meet the criteria imposed by Italian regulation. Most likely, condensate could be used as dilution water for digestion input, for cleaning floor and surfaces of animal housings or for crop irrigation.The research showed the great effectiveness of the vacuum evaporation process, especially in the two stage configuration with acidification. In fact, the concentration of nutrients in a small volume determines easier transportation and reduction of related management costs. In full scale plants energy consumption is estimated to be 5–8 kWhe/m3 of digestate and 350 kWht/m3 of evaporated water. 相似文献
176.
环境生物样品预处理中的微波溶样技术 总被引:2,自引:1,他引:2
微波溶样是近年产生的一种崭新的有前途的样品预处理技术,本文评述这一技术在环境、生物样品消解方面的近期应用。 相似文献
177.
178.
179.
以低温短时(90℃、30 min)水热预处理后的混合及初沉污泥为研究对象,分别进行了高温((55±1)℃)厌氧消化连续性试验.研究了该预处理条件下这两类污泥在水力停留时间(HRT)为20 d时的产气量、有机物分解率及物料平衡等,探讨了低温短时水热预处理对提高污泥厌氧消化性能的效果.结果表明:TS约为35 g·L-1的预处理混合污泥与初沉污泥经高温厌氧消化后,投加单位VS的产气量分别为(343.00±9.86)m L·g-1和(365.00±7.61)m L·g-1,VS去除率分别为38.9%和45.8%.COD物料平衡计算结果表明,混合和初沉污泥中分别有33.6%和43.9%的固体有机物被分解转化,生物气中CH4含量均在70%左右. 相似文献
180.
麦秆酸预处理后与猪粪混合发酵提高产气量的效应研究 总被引:1,自引:0,他引:1
为了研究不同水平的酸处理对麦秆混合发酵过程中各指标变化的影响,本试验通过测定不同醋酸浓度、时间处理后的麦秆与猪粪混合厌氧发酵进程中还原糖、挥发性脂肪酸(VFA)含量,以及p H值变化和甲烷产量,探究各指标的关系并优化得出最佳醋酸处理组合,以期为酸预处理混合发酵实现高甲烷产量提供可靠的理论依据.结果表明,醋酸处理后的麦秆通过与猪粪混合发酵可明显提高甲烷单位产量,增幅为124.28%~207.40%.发酵过程中还原糖、VFA、p H值间相互影响.通过响应面法建立模型,得到醋酸处理的最优组合为浓度3.35%、时间6.75d,最大甲烷单位产量751.97 m L·g-1(以VS计). 相似文献