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51.
金水河流域矿物元素生物地球化学交换模式 总被引:1,自引:0,他引:1
通过对金水河流域矿物元素生物地球化学交换模式的研究,得到以下结论:(1)在不同空间位置的矿物元素对河水的水质贡献率不相同。河水成分贡献主要来源于硅酸盐风化,在金水河流域生态系统不同空间位置矿物元素对河水水质贡献率方程为:YRiverwater=0.242+0.203 XRain+0172 XLitter+0.471 XSoilwater(r2=0.55)。(2)固-液相界面(土壤-土壤水溶液)离子交换过程拟合表明:离子交换过程符合二、三次曲线模型。(3)区域内碳酸盐岩含较少的Na+和K+,且受酸雨等影响。Na+在土壤-土壤溶液之间的分配行为可能加重土壤盐碱化的趋势。土壤和枯枝落叶层HCO3-和TDS值均处于稳定的范围内。(4)输入性污染分析表明,流域内土壤基本表现出物理性质改善;但却表现出贫养化和生物地球化学性质恶化的极化趋势。人为活动输入污染物影响显著,在全球变化背景下,酸雨和干旱加剧了水溶液组成的变化。 相似文献
52.
云南高原典型林分林下枯落物持水特征研究 总被引:19,自引:0,他引:19
森林枯落物具有重要生态水文功能,通过实地调查与实验分析,对云南高原湖泊纳帕海流域3种典型林分枯落物储量、持水量和持水过程进行了研究。结果表明:高山松(pinus densata)林下枯落物储量最大,白桦林(Betula platyphylla Suk.)次之,川滇高山栎(Quercus aquifolioides)灌丛最小,林下枯落物储量最大持水量和有效拦蓄量大小排序表现出和枯落物储量相同的顺序;不论是储量、最大持水量还是有效拦蓄量,各林分枯落物都表现出半分层大于未分解层。3种林下枯落物在0~2 h内吸水较快,在10 h后吸水速明显减缓,用对数方程对3种林下枯落物未分解层和半分解层持水量与浸水时间进行拟合,用幂函数方程对吸水速率与浸水时间进行拟合,结果显示相关系数都较高。 相似文献
53.
Calculating ecological carrying capacity of shellfish aquaculture using mass-balance modeling: Narragansett Bay, Rhode Island 总被引:1,自引:0,他引:1
Increasing growth in the aquaculture industry demands ecosystem-based techniques for management if that growth is to be ecologically sustainable and promote equity among users of the ecosystems in which it occurs. Models of carrying capacity can be used to responsibly limit the growth of aquaculture in increasingly crowded coastal areas. Narragansett Bay, Rhode Island, USA is one such crowded coastal region experiencing a rapid increase in bivalve aquaculture. An ecosystem mass-balance model was used to calculate the ecological carrying capacity of bivalve aquaculture. Cultured oyster biomass is currently at 0.47 t km−2 and could be increased 625 times without exceeding the ecological carrying capacity of 297 t km−2. This translates to approximately 38,950 t of harvested cultured oysters annually which is 4 times the total estimated annual harvest of finfish. This potential for growth is due to the high primary productivity and large energy throughput to detritus of this ecosystem. Shellfish aquaculture has potential for continued growth and is unlikely to become food limited due, in part, to the large detritus pool. 相似文献
54.
水热法制备玉米叶基生物炭对亚甲基蓝的吸附性能研究 总被引:7,自引:0,他引:7
以农业废弃物玉米叶和玉米秆为原材料,采用水热法制备生物炭,通过批试验方法考察了接触时间、污染物初始浓度、生物炭投加量、反应体系温度及溶液p H值等因素对2种生物炭吸附亚甲基蓝的影响,并对吸附规律进行了探讨.吸附动力学拟合结果发现,准二级动力学能更好地拟合吸附过程(R~2=0.9986~0.9999);颗粒内扩散方程拟合结果表明,2种生物炭对亚甲基蓝的吸附由液膜扩散和颗粒内扩散2个过程控制.玉米叶基生物炭对亚甲基蓝的吸附可以通过Freundlich方程来进行拟合(R~2=0.9898),说明吸附在生物炭表面是多分子层吸附过程;而玉米杆基生物炭对亚甲基蓝的吸附更符合Langmuir方程(R~2=0.9825),说明吸附在生物炭表面是单分子层吸附过程.与玉米杆基生物炭相比,玉米叶基生物炭具有更好的吸附性能,拟合理论最大吸附量为玉米杆基生物炭的1.25倍. 相似文献
55.
Shixiang Li Xulan Zhang Er Bei Huihui Yue Pengfei Lin Jun Wang Xiaojian Zhang Chao Chen 《环境科学学报(英文版)》2017,29(8):331-339
N-nitrosodimethylamine(NDMA) precursors consist of a positively charged dimethylamine group and a non-polar moiety, which inspired us to develop a targeted cation exchange technology to remove NDMA precursors. In this study, we tested the removal of two representative NDMA precursors, dimethylamine(DMA) and ranitidine(RNTD), by strong acidic cation exchange resin. The results showed that pH greatly affected the exchange efficiency, with high removal(DMA 78% and RNTD 94%) observed at pH pk_a-1 when the molar ratio of exchange capacity to precursor was 4. The exchange order was obtained as follows: Ca~(2+) Mg~(2+) RNTD~+ K~+ DMA~+ NH_4~+ Na~+. The partition coefficient of DMA~+to Na~+was 1.41 ± 0.26, while that of RNTD~+to Na~+was 12.1 ± 1.9. The pseudo second-order equation fitted the cation exchange kinetics well. Bivalent inorganic cations such as Ca~(2+)were found to have a notable effect on NA precursor removal in softening column test. Besides DMA and RNTD, cation exchange process also worked well for removing other 7 model NDMA precursors. Overall, NDMA precursor removal can be an added benefit of making use of cation exchange water softening processes. 相似文献
56.
Perfluorooctane sulfonate(PFOS) has attracted increasing concern in recent years due to its world-wide distribution, persistence, bioaccumulation and potential toxicity. The influence of sorbent properties on the adsorptive elimination of PFOS from wastewater by activated carbons, polymer adsorbents and anion exchange resins was investigated with regard to their isotherms and kinetics. The batch and column tests were combined with physicochemical characterization methods, e.g., N_2 physisorption, mercury porosimetry, infrared spectroscopy, differential scanning calorimetry, titrations, as well as modeling. Sorption kinetics was successfully modelled applying the linear driving force(LDF) approach for surface diffusion after introducing a load dependency of the mass transfer coefficient βs.The big difference in the initial mass transfer coefficient βs,0, when non-functionalized adsorbents and ion-exchange resins are compared, suggests that the presence of functional groups impedes the intraparticle mass transport. The more functional groups a resin possesses and the longer the alkyl moieties are the bigger is the decrease in sorption rate.But the selectivity for PFOS sorption is increasing when the character of the functional groups becomes more hydrophobic. Accordingly, ion exchange and hydrophobic interaction were found to be involved in the sorption processes on resins, while PFOS is only physisorptively bound to activated carbons and polymer adsorbents. In agreement with the different adsorption mechanisms, resins possess higher total sorption capacities than adsorbents. Hence, the latter ones are rendered more effective in PFOS elimination at concentrations in the low μg/L range, due to a less pronounced convex curvature of the sorption isotherm in this concentration range. 相似文献
57.
Simultaneous removal of Cu(II) and Cr(VI) by Mg–Al–Cl layered double hydroxide and mechanism insight
Mg–Al–Cl layered double hydroxide (Cl-LDH) was prepared to simultaneously remove Cu(II) and Cr(VI) from aqueous solution. The coexisting Cu(II) (20 mg/L) and Cr(VI) (40 mg/L) were completely removed within 30 min by Cl-LDH in a dosage of 2.0 g/L; the removal rate of Cu(II) was accelerated in the presence of Cr(VI). Moreover, compared with the adsorption of single Cu(II) or Cr(VI), the adsorption capacities of Cl-LDH for Cu(II) and Cr(VI) can be improved by 81.05% and 49.56%, respectively, in the case of coexisting Cu(II) (200 mg/L) and Cr(VI) (400 mg/L). The affecting factors (such as solution initial pH, adsorbent dosage, and contact time) have been systematically investigated. Besides, the changes of pH values and the concentrations of Mg2+ and Al3+ in relevant solutions were monitored. To get the underlying mechanism, the Cl-LDH samples before and after adsorption were thoroughly characterized by X-ray powder diffraction, transmission electron microscopy, Fourier transform infrared spectroscopy, and X-ray photoelectron spectroscopy. On the basis of these analyses, a possible mechanism was proposed. The coadsorption process involves anion exchange of Cr(VI) with Cl− in Cl-LDH interlayer, isomorphic substitution of Mg2+ with Cu2+, formation of Cu2Cl(OH)3 precipitation, and the adsorption of Cr(VI) by Cu2Cl(OH)3. This work provides a new insight into simultaneous removal of heavy metal cations and anions from wastewater by Cl-LDH. 相似文献
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60.
基于生态系统供给及净化服务功能的贵州省水生态占用研究 总被引:1,自引:0,他引:1
针对传统及现有水生态足迹理论及其模型存在的缺陷与不足,本文提出了基于生态系统供给及净化服务功能的贵州省水生态占用概念与模型,将其划分为生物生产和非生物生产的水生态占用两部分,建立水产品、水资源、水环境3类账户,并在此基础上以2000—2014年的贵州省为例进行计算分析,结果表明:(1)水产品账户中,贵州省水产品消费的水生态占用总体呈上升趋势,水生态承载力波动变化较小,水产品消费呈生态赤字状态,且其生态压力较大;(2)水资源账户中,贵州省淡水资源的水生态占用整体呈逐渐上升趋势,水生态承载力则呈明显波动的趋势,且变化幅度较大,淡水资源消费处于生态盈余状态,且其与水生态承载力的变化态势一致,淡水资源消费的生态压力较小;(3)水环境账户中,水环境生态压力主要来源于氮污染,2000—2010年消纳污染的水生态占用变化不大,2011—2014年波动较大,历年生活水污染账户值均大于工业,今后要注重加强生活水污染防治,消纳污染的水生态承载力呈波动变化的趋势,水环境处于生态赤字状态,且其生态压力较高;(4)与现有生态足迹模型的比较分析可知:该模型核算更为全面;不考虑均衡因子,并以最大水生态压力指数来评价区域水生态系统所承受的压力状态具有合理性,更能准确反映贵州水生态的实际情况和水生态文明建设的需要. 相似文献