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101.
我国经济高速发展的同时,出现了矿产资源大量消耗和环境严重污染的问题。许多学者认为是矿产资源国家所有权惹的祸,极力倡导所有权改制。从理性的角度出发分析,出现这种现象并不是国家所有权惹的祸,而是国家所有权的管理体制不再适应今天市场化的要求,应从管理体制和竞争方面来加强矿产资源的管理。 相似文献
102.
综合利用中药资源,开展中药生产中的废料综合利用工作,是保证中药资源永续利用的重要措施和手段。本文概述了中药生产中的综合利用及研究情况,探讨了中药生产中废料资源化技术的开发。 相似文献
103.
EC法处理选磷废水的研究 总被引:2,自引:0,他引:2
为解决磷矿浮选尾水的污染和回用问题,采用了EC法处理,结果表明,经处理的尾矿水可部分回用,并节省Na2CO3 43-65%,这一处理方法具有一定的实用价值。 相似文献
104.
矿产资源经济区划的理论与方法 总被引:2,自引:0,他引:2
矿产资源经济区划是保护与合理开发利用矿产资源、实现资源优化配置和区域经济可持续发展的基础。本文依据经典的区位理论和地域分工理论,应用系统分析的方法,建立了矿产资源经济区划的一般程序,并归纳了定量分析中必要的技术手段和方法路线。 相似文献
105.
在计划经济体制下.农业不是也不可能成为一个独立产业,其结果只能是社会效益可观、经济效益甚微甚至倒贴,吃苦的是农民。社会主义市场经济体制的逐步确立,为农业走向市场带来了希望,首要的是确立市场经济观念。丘陵地区大搞农业资源的综合开发是使农业走向市场的重要途径,综合开发上了水平,实现“三高”农业就大有希望。搞农业综合开发的途径很多,但都必须以市场为导向、科技为先导、经济效益为中心,大搞农业产加销一条龙、贸工农一体化是提高农业综合开发整体水平、实现“三高”农业的必要途径。 相似文献
106.
ABSTRACT: An integrated remotely sensed database was used as the basis for a hydrologic and sediment transport modeling effort for an agricultural area of western Puerto Rico. Classified spectral images of airborne radiance data provided ground cover information and were used in conjunction with topographic and soils data to guide model construction and provide input to the water balance and sediment yield simulations. Runoff and sediment discharge from hydrologically homogeneous regions were routed through the drainage network and combined at the basin outlet. The model was used to simulate four years of observed sediment discharge from the basin. Relative contributions to the total sediment yield of forested and agricultural areas were determined and compared. 相似文献
107.
我国矿产资源利用的环境问题及对策 总被引:4,自引:0,他引:4
徐强 《中国人口.资源与环境》1995,5(1):33-37
矿产资源利用过程中靠成的环境问题是我国经济建设速发展所面临的一个现实问题本文全面地分析了矿产资源利用对环境影响的各个方面,分析了我国矿产资源环境问题的一些特点,提出了八个方面的对策建议。 相似文献
108.
Hong?ZhengEmail author Yoshitaka?Nitta Isamu?Yokota 《Journal of Material Cycles and Waste Management》2004,6(2):153-161
In this article, the systems for the collection and intermediate processing of used beverage cans (UBCs) are compared and analyzed, focusing on the time taken and the cost of processing, the energy consumption, and the emissions of CO2, SO
x
, and NO
x
, during the process. We found that cases where the UBCs were crushed in the discharging process gave better results, and how the UBCs were collected was the most important factor. It was more desirable to treat UBCs in one place than in two places. When the transportation distance was longer, the pressed form of UBCs was more convenient. When the transportation distance was short, the original form, the crushed form, and the shredded form of UBCs were all suitable. That is, the contribution of the transportation process to the evaluation was large when the transport distance was long, and the contribution of the treatment process was large when the transport distance was short. 相似文献
109.
Utilization of red mud as catalyst in conversion of waste oil and waste plastics to fuel 总被引:4,自引:0,他引:4
A. Ihsan?Cakici Jale?YanikEmail author Suat?U?ar Tamer?Karayildirim Huseyin?Anil 《Journal of Material Cycles and Waste Management》2004,6(1):20-26
The aim of this study was to investigate the possibilities of using a by-product (red mud) from alumina production as a catalyst for recovery of waste. The conversion of waste mineral oil (WMO) and waste mineral oil/municipal waste plastic (WMO/MWP) blends over red mud (RM), a commercial hydrocracking catalyst (silica–alumina), and a commercial hydrotreating catalyst (Ni–Mo/alumina) to fuel has been studied. The effect of the catalyst and the temperature on the product distribution (gas, liquid, and wax) and the properties of liquid products were investigated. In the case of hydrotreatment of WMO, the liquids obtained over RM at both 400° and 425°C had larger amounts of low-boiling hydrocarbons than that of thermal or catalytic treatment with hydrotreating catalyst. Gas chromatography and nuclear magnetic resonance analysis of the liquid products showed that RM had hydrogenation and cracking activity in hydrotreatment of WMO. In coprocessing of WMO with municipal waste plastics, temperature had an important effect as well as the amount of MWP in the blend and the catalyst type. The hydrocracking at 400°C produced no liquid product. In hydrocracking at 425°C, the product distribution varied with catalyst type and MWP amount. The commercial hydrocracking catalyst had more cracking ability in the conversion of WMO/MWP to liquid and gas fuel than RM. In the case of hydrocracking over RM, the largest amount of liquid having satisfactory quality was obtained only from the blend containing 20% MWP. 相似文献
110.