非法废物贸易机制及相关对策研究

针对国际上某些发达国家向发展中国家越境转移废物这一倍受关注的现象,阐述了废物贸易,尤其是非法废物贸易产生的机制和发生的后果,对目前有关废物越境转移的国际公约作了介绍,并着重探讨了中国对于非法废物贸易相应国内立法及应采取的措施。      

工业废水处理装置中的废气治理技术

工业废水中排出的废气对环境的污染,是石化及化工行业需关注的新焦点,本文介绍了国外工业废水处理装置排出的废气情况及国内外相关治理技术的发展概况和最新进展,并探讨了国内开发废气治理技术的紧迫性、可行性及应优先考虑的方向。      

氢氟酸生产过程中石膏废渣的利用研究

在分析了石膏废渣熟料、石灰以及复合缓凝剂等主要物质作用机理的基础上,着重讨论了它们对加气砌块试样性能的影响,并通过试验确定了熟料的最佳引入量为65%~70%,饱和石灰掺量为12%,复合缓凝剂的用量不超过4.5%。      

综合利用石墨化废旧辅料的新方法

炭素石墨制品生产过程中产生的石墨化废旧辅料,在炭素行业是最有开发潜力的固体废物。通过初加工可实现回收利用,经研制开发新产品可实现综合利用。该综合利用方法表明,在实现综合利用中可获得大的经济效益和可观的社会效益。      

气力管道输送在垃圾收运领域的应用研究

气力管道输送应用于垃圾收运在国内尚处于起步阶段,开发该项技术目前还存在一定的技术困难,但若该技术能在环境领域成功应用,它将完全改变传统的垃圾收运模式,大大提高垃圾收集的效率,减小垃圾收运过程中对环境造成的影响。本文主要对该技术的优势及在国内应用的技术困难进行探讨,并在此基础上提出了解决方法。     

Influence of bromine on metal volatilization in waste combustion

Co-combustion tests of municipal solid waste and bromine-containing waste plastics have been performed in the TAMARA test incinerator in order to investigate the fate of bromine in waste combustion. HBr is the main bromine combustion product. Approximately 50% of the bromine inventory stays in the grate ashes, which is much more than is found for chlorine. The percentage of bromine transferred into the fly ash also exceeds that of chlorine. There is a strong indication that bromine has a promoting effect upon the volatility of most of the heavy metals that are typically mobilized by chlorine. Received: February 2, 2000 / Accepted: March 3, 2000     

垃圾焚烧炉预处理系统设计与优化

论述了垃圾预处理系统的一些关键设备和技术要点,分析了垃圾焚烧炉预处理系统的流程设计和不同的设备组合方式,并介绍了一种用于循环流化床焚烧炉的预处理系统流程和试验结果。     

废橡胶制备燃料油和炭黑

介绍了由废旧橡胶通过催化裂解制备燃料油和炭黑的方法,着重探讨了影响燃料油产率的因素,结果表明在优化条件下燃料油收率达42％,炭黑纯度在97％以上。     

生活垃圾厌氧堆肥产甲烷特性研究

为了更好地利用厌氧处理产生的气体,在介绍模拟厌氧堆肥试验的基础上,对厌氧堆肥产甲烷的基本特性进行了研究。结果表明,在厌氧堆肥开始阶段20d左右,甲烷只有7．8％（质量分数,下同）左右,远远低于32．8％的二氧化碳;而随着反应的进行,二氧化碳呈下降趋势,甲烷先升高后降低,直到反应进行到第70天左右时,甲烷才逐渐高于二氧化碳,片于第90天左右时达到最高值42．0％;此后二氧化碳及甲烷都逐渐降低,但甲烷始终高于二氧化碳。     

Two-stage thermal gasification of polyolefins

Plastic pellets of polyethylene (PE), polypropylene (PP), and polystyrene (PS) were gasified in a two-stage thermal degradation process. The first stage is the conversion of polyolefins to distilled oils using a melting vessel. In the second stage, the oils from the first stage are gasified using a tubular reactor. The distilled oil yields of PE, PP, and PS in the first stage were 84, 89, 92 wt%, respectively, each at 470°C. The total gas yields of PE, PP, and PS in the second stage were 80, 74, and 6.2 wt%, respectively, each at 800°C. The main components of the product gas for PE and PP were methane and olefins such as ethene and propene. Some aromatic oils, including benzene, toluene, and xylene, were also produced as by-products. The amount of carbonaceous residue, or coke, was very low (less than 1 wt%). By dividing the process into two stages, the coking rate was considerably reduced compared with direct gasification of the polyolefins. Received: July 19, 2000 / Accepted: September 17, 2000