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121.
Cellulose/polyethylene (CPE) mixture 3:1, w/w with and without three clay catalysts (K10 – montmorillonite K10, KSF – montmorillonite KSF, B – Bentonite) addition were subjected to pyrolysis at temperatures 400, 450 and 500 °C with heating rate of 100 °C/s to produce bio-oil with high yield. The pyrolytic oil yield was in the range of 41.3–79.5 wt% depending on the temperature, the type and the amount of catalyst. The non-catalytic fast pyrolysis at 500 °C gives the highest yield of bio-oil (79.5 wt%). The higher temperature of catalytic pyrolysis of cellulose/polyethylene mixture the higher yield of bio-oil is. Contrarily, increasing amount of montmorillonite results in significant, almost linear decrease in bio-oil yield followed by a significant increase of gas yield. The addition of clay catalysts to CPE mixture has a various influence on the distribution of bio-oil components. The addition of montmorillonite K10 to cellulose/polyethylene mixture promotes the deepest conversion of polyethylene and cellulose. Additionally, more saturated than unsaturated hydrocarbons are present in resultant bio-oils. The proportion of liquid hydrocarbons is the highest when a montmorillonite K10 is acting as a catalyst. 相似文献
122.
利用连续流釜式超临界水反应器,以聚乙二醇(PEG)模拟废水为研究对象,研究PEG浓度、反应温度、停留时间以及KOH催化剂对含PEG废水的超临界气化产H2特性的影响.结果表明,气体产物主要成分为H2,CH4,CO和CO2,在500℃,压力25MPa,停留时间50s的条件下,TOC去除率、碳气化率和氢气化率分别达到98.56%,98.33%和141.82%;PEG浓度的升高会导致气化效率下降,反应温度的上升和停留时间的延长对气化效率有正影响.KOH催化剂的加入可以温和反应条件,提高气化效率,消除CO的产生并使气体产物中部分CO2以无机盐形式固定,从而提高了产物中有效组分H2的相对含量.在450℃,压力25MPa,停留时间30s,KOH浓度800mg·l-1时,TOC去除率和氢气化率分别为91.08%和186.06%,含PEG废水在超临界状态下可转化为富氢气体. 相似文献
123.
海藻酸钠-聚氧化乙烯凝胶球去除废水中重金属离子的研究 总被引:1,自引:0,他引:1
研究了海藻酸钠浓度及固化时间对海藻酸钠-聚氧化乙烯(SA-PEO)凝胶球性能的影响以及采用SA-PEO凝胶球对溶液中3种重金属离子(Pb2 ,Cu2 、Cd2 )进行吸附实验的研究.结果表明,2.0%(质量分数)的SA溶液制成的凝胶球性能较好,固化时间对重金属去除率影响较小,但随着固化时间的增加,SA-PEO凝胶球的直径逐渐缩小,紧密程度和机械强度逐渐增加;在重金属离子溶液pH为4~6时,SA-PEO凝胶球对重金属离子去除率较高;SA-PEO凝胶球对不同重金属离子吸附效果为pb2 >Cu2 >Cd2 ;多种重金属离子共存使得SA-PEO凝胶球对Pb2 和Cd2 的吸附受一定程度的抑制,而对Cu2 吸附能力有所增强,说明SA-PEO凝胶球对重金属离子吸附有选择性;1.00 mol/L的HCl溶液对Pb2 的解吸效果较好,解吸再生后的SA-PEO凝胶球可以重复利用. 相似文献
124.
以聚乙二醇-6000(PEG-6000)为模板剂水热法制备碳酸氧铋(p-Bi2O2CO3)粉末,采用X射线衍射(XRD)、扫描电镜(SEM)、X射线光电子能谱(XPS)、透射电子显微镜(TEM)和紫外可见漫反射(DRS)对粉末进行了初步表征。在可见光(λ≥420 nm)照射下,以罗丹明B(RhB)和水杨酸(SA)光催化降解实验为探针反应,实验结果表明,p-Bi2O2CO3具有较高的光催化活性,对RhB和SA有较好的降解效果。通过紫外-可见光谱(UV-Vis)、红外光谱(IR)和测定总有机碳(TOC)含量,光催化反应35 h后RhB的矿化率为77%,同时对SA的降解率达到43%。同时,采用N,N-二乙基对苯二胺(DPD)分光光度法和对苯二甲酸荧光光度法分别测定了降解过程中H2O2和羟基自由基(·OH)的变化,表明p-Bi2O2CO3/Vis光催化降解机理涉及到·OH历程。 相似文献
125.
Raised beds are used to produce some high-value annual fruit and vegetable crops such as strawberry in California (CA) and tomato in Florida (FL), USA. Pre-plant soil fumigation is an important tool to control soil-borne pests in the raised beds. However, fumigant emissions have detrimental environmental consequences. Field trials were conducted to evaluate emissions of 1,3-dichloropropene (1,3-D) and chloropicrin (CP) in two different production systems with raised beds covered by different tarps. In the CA trial, InLine (60.8% 1,3-D and 33.3% CP) was drip-applied at 340 kg ha−1 to 5 cm deep in the beds (30 cm high and 107 cm wide) tarped with polyethylene (PE) or virtually impermeable film (VIF). In the FL trial, carbonated Telone C35 (63.4% 1,3-D and 34.7% CP) was shank-applied at 151 kg ha−1 to 20 cm deep in the beds (22 cm high and 76 cm wide) tarped with totally impermeable film (TIF). Emissions from tarped beds relative to furrows were contrary between the two trials. For the CA trial, the emission was 47% of applied 1,3-D and 27% of applied CP from PE tarped beds and 31% of applied 1,3-D and 15% of applied CP from VIF tarped beds, while that from uncovered furrows was <0.4% for both chemicals in both fields. In the FL trial, only 0.1% 1,3-D was emitted from the TIF tarped beds, but 27% was measured from the uncovered furrows. Factors contributing to the differences in emissions were chiefly raised-bed configuration, tarp permeability, fumigant application method, soil properties, soil water content, and fumigant carbonation. The results indicate that strategies for emission reduction must consider the differences in agronomic production systems. Modifying raised bed configuration and fumigant application technique in coarse textured soils with TIF tarping can maximize fumigation efficiency and emission reduction. 相似文献
126.
聚对苯二甲酸乙二醇酯(PET)饮料瓶属一次性塑料包装,应用广泛且周期短,废弃量大,从节约资源、减少碳排放和保护环境等方面看,废PET饮料瓶回收都具有重要的意义。基于PET瓶装的饮料产量和PET瓶消费量的正相关性,建立了饮料总产量-PET瓶装的饮料产量-废PET饮料瓶产生量(PET饮料瓶消费量)间的数量响应关系,结合灰色模型,预测2020—2025年我国废PET饮料瓶的产生量;根据国内PET饮料瓶回收现状和物质代谢定性分析,确定了废PET饮料瓶的主要流向;通过问卷调查和现场实测,测算出现阶段我国PET饮料瓶回收总体水平。结果表明:2020—2025年,我国废PET饮料瓶的年产生量预测值为370万~409万t,主要流向回收利用体系、餐厨垃圾处理厂、垃圾填埋场、垃圾焚烧发电厂以及海滩等地,其中流向餐厨垃圾处理厂、垃圾填埋场、垃圾焚烧发电厂、海滩等地的废PET饮料瓶所占比例总体低于5%,即全国废PET饮料瓶回收率在95%以上,处于较高的回收水平。 相似文献
127.
高压聚乙烯装置料仓闪燃隐患综合治理 总被引:1,自引:0,他引:1
阮赤宇 《安全.健康和环境》2005,5(8):28-31
介绍了茂名石化分公司化工事业部高压聚乙烯装置料仓闪燃隐患治理的情况.根据存在的问题从两个方面进行了改造:采用多重管重力掺混技术,降低气相粉尘浓度,减少静电积聚;在料仓底部增设通风口,增加氮气、空气反吹管等,减少可燃气体积聚. 相似文献
128.
129.
A home-made inexpensive passive diffusion bag (PDB) sampler, prepared by filling deionized water in low-density polyethylene (LDPE) tubes, was evaluated for volatile organic compounds (VOC) sampling in groundwater at industrial contamination sites. Impacts of environmentally relevant conditions on the sampling equilibration time and partitioning of VOCs between the sampler and the water sample were investigated. Sample salinity, agitation and temperature can influence the equilibration time, but generally sampling equilibration was obtained in 14 days under real field sampling of VOCs in groundwater. Both laboratory study and field testing in a contaminated site showed that the VOC concentrations in the developed sampler were equal to those in the water samples at equitibrium. Coupled with a purge and trap concentrator-gas chromatograph-mass spectrometer (P&T-GC-MS), the developed PDB sampler provided a low-cost sampling device for routine monitoring of VOCs in groundwater in wells, with LODs in the range of 2.9-10 μg/L. The proposed PDB was applied to determine VOCs in groundwater at an industrial contamination site, and the present results agreed well with those determined using conventional pump-and-sample monitoring. All the studied 13 VOCs were tested in the four wells in the industrial contamination sites, with their concentrations in the range of 12-73660 μg/L. In addition, while benzene and toluene were heavily contaminated up to a maximum concentration of 74000 μg/L and 6000 μg/L, respectively, 1,2,3-trichlorobenzene and bromobenzene had relatively low contamination levels (below 25 μg/L). 相似文献
130.