DSTE工艺及其应用实例

DSTE工艺是近年来开发的一种以厌氧为主,好氧为辅去除有机物的新型组合式污水处理系统.本文重点介绍该工艺的工艺流程、反应机理及优缺点;并介绍该工艺在澄江县禄充旅游度假区、江川县小马沟旅游度假区的工程应用实例.     

CITY OF TUCSON WASTE WATER EFFLUENT DELIVERY FACILITY1

ABSTRACT: The Tucson area is totally dependent on ground water, which is in increasingly short supply due to excessive overdrafts. Tucson area waste water treatment plants discharge material quantities of secondary effluent downstream, which is lost to evapotranspiration and recharge of the ground water basin. The city and the four large mining companies who share the common Santa Cruz basin ground water, recognized the common water supply problem and agreed to fund a feasibility study for mining process use of the effluent to partly alleviate the overdraft of ground water. The study analyzed the projected waste water effluent resources, potential mining company demand for waste water effluent and possible interface of an effluent delivery facility with the proposed Central Arizona Project. The effluent resources were analyzed with respect to potential demand. An optimum alignment was selected. An optimum system was detailed through design schematics, amortized cost and finance requirements, and an implementation schedule. It was concluded that a waste water effluent delivery facility could be implemented which would utilize reclaimed effluent in quantities approximating 35 percent of basin overdraft and which would provide revenue for full cost recovery over a 20 year operation period. The mining companies are studying the internal economic impacts of the project.     

时变条件下的有害物品运输的人口风险分析

随着工业的发展 ,有害物品运输量在逐年增加 ,有害物品对于人类威胁也在加大 ,有害物品运输的风险问题受到了广泛的关注。由于有害物品运输中 ,路径周围的人口密度随着时间的变化而变化 ,进而影响在运输过程中的人口风险。笔者在有时变情况下 ,对有害物品运输人口风险进行了分析 ;建立了估计人口风险的模型 ;获得了有害物品运输中的最小人口风险以及最佳出发时间 ;进一步完善了有害物品的运输的风险分析 ;为如何减少有害物品运输的人口风险提供了依据。     

Influence of sewage inputs and fish farm effluents on dissolved nitrogen species in a chalk river

Nitrate, ammonium and dissolved organic nitrogen (DON) concentrations were measured in the lower reaches of the River Test in Hampshire to assess the impact of two effluent point sources. An 18-month survey from July 2001 to December 2002 was carried out at locations above and below fish farm inputs and a sewage effluent outfall. The concentration of nitrate exceeded 400 M at the four sites on all sample dates. A consistent increase in ammonium concentration was measured downstream of the fish farm, but not the sewage effluent input. DON samples collected downstream of the fish farm did not show a consistent increase in concentration, compared with the upstream sampling location, whereas the sewage effluent input at Romsey was a point source of DON to the River Test with a mean increase of 15 M. Nitrate was the major component of dissolved nitrogen in this aquifer-fed chalk-bed river system, with up to 10% being DON and ammonium comprising <1%.     

变速循环流化床烟气脱硫实验和机理分析

以循环流化床原理为基础,在变速循环流化床试验台上进行了烟气脱硫小试研究． 烟气流量为５００ｍ³／ｈ 时,气体在脱硫系统中的理论停留时间为３．２ｓ． 用干消化石灰得到的熟石灰粉末作为脱硫剂,在Ｃａ／Ｓ摩尔比为１．１,喷水量为１１ｋｇ／ｈ,保持趋近绝热饱和温度ΔＴ＝ １２℃时,系统脱硫效率可以达到８９％ ． 对影响脱硫效率的主要因素进行了分析,认为喷水量是影响脱硫效率的最关键因素,并对脱硫机理进行了初步探讨．     

固体微粒气溶胶灭火剂的改性研究

固体微粒气溶胶灭火剂作为一种新型灭火剂具有优越的抑制火灾的性能,但其应用和推广的关键在于降低灭火气溶胶形成时的温度.本文利用TG方法分析了灭火剂的热分解过程,并通过测定固体微粒气溶胶灭火剂的释放速度、释放区温度分布及灭火性能,研究了固体微粒气溶胶灭火剂的降温消焰技术.同时对气溶胶的成分和固体粒子粒度分布进行了分析.     

Replacement of a multiple hearth by a fluid bed incinerator the Greensboro case history

The incinerator at the T.Z. Osborne Plant in Greensboro, North Carolina burns sludge from its own waste water treatment plant and sludge pumped from the nearby North Buffalo plant. The two plants have a combined capacity of 36 million gallons per day of wastewater. Because of the age of and increasing high maintenance on the existing multiple hearth incinerator, and the need to increase treatment capacity, the Osborne plant concluded a study in 1992 evaluating its options for future municipal sewage sludge disposal. Options which were evaluated during the study included; (i) rehabilitation of the existing eight-year old multiple hearth unit; (ii) addition of a new multiple hearth; (iii) addition of a new fluid bed system; (iv) drying, composting, or land application. The chosen option, based on both economic and environmental considerations, was a new fluid bed system with a capacity of 2.55 tons per hour, approximately double that of the existing multiple hearth. Design of the new fluid bed system began in December 1994 and equipment delivery for the incineration system was begun in April 1995. Initial operation occurred in August 1996. Primary and secondary sludge, dewatered to 28% dry solids by centrifuge, is delivered by piston pumps to the twenty-foot freeboard ID incinerator. A shell and tube heat exchanger recuperates heat from the exhaust gas and preheats the combustion air to 1250°F, resulting in minimal auxiliary fuel use. The air pollution control device is a high-energy Tandem Nozzle® scrubber. Greensboro was the initial installation of this scrubber design on a fluid bed incinerator and its characteristics and performance are discussed. Ash is dewatered in an ash thickener/belt press system prior to disposal to landfill. The system includes a state of the art Programmable Logic Controller (PLC) system for computer control of the operation. The unit was commissioned in August 1996 and has been in continuous operation since that time except for a one week inspection and maintenance shutdown in February 1999. The plant operates 24 h/day, 7 days per week. The initial performance test showed the system to readily meet federal and state air emission standards. Particulate released was 0.002 grains per dry standard cubic foot, carbon monoxide was 22.5 parts per million volumetric (ppmv) and opacity was 0.4%. These results show a significant emission reduction with the fluid bed when compared to the multiple hearth. Annual tests conducted since then and continuous emission monitoring have shown the unit to be in consistent compliance. Since the fluid bed system became operational, the old multiple hearth system has been maintained on standby as a backup, but its use has not been required. Operational experience is discussed, the most interesting of which is the relatively trouble-free operation. The minor problems which occurred and their solutions are detailed. Also included is a comparison of operation and maintenance experience of the fluid bed and the multiple hearth. Current sludge disposal actual cost data are also provided including the average cost per ton of dry solids treated. The almost three years of operational experience to date has shown that the decision to install a new fluid bed system was the correct one on both an environmental and economic basis. It has provided benefits to all interested parties — the wastewater treatment plant, the regulators, the taxpayers, and the surrounding community.     

利用磷渣熔制饰面玻璃

介绍了用磷渣熔饰面玻璃的试验过程。对试验中出现的工艺问题进行了探讨,并讨论经济效益进行了初步分析。     

Genotoxicity of substances extracted from construction materials

Construction waste such as road pavement and concrete is estimated to constitute about 50% of the total industrial waste in Japan, and the recycling of such material has recently become a prominent topic among construction engineers. It has also been suggested that various types of industrial waste be utilized as components of construction materials. This paper investigates the environmental safety of certain materials in terms of the elutions and genotoxicities of these substances. The substances extracted from some materials, such as emulsifier, ash, and sediment, were found to have genotoxic characteristics. The dose-related responses of the various materials and their genotoxic strengths are shown. Received: June 16, 1998 / Accepted: September 7, 1999     

大气中多环芳烃气固相分配与颗粒物粒径的关系

采集了2005年5月16日～6月3日上海市桃浦地区气相样品、TSP样品及不同粒径的颗粒物样品.用GC-MS对各样品中美国EPA规定优先控制的16种多环芳烃(PAHs)做了定量分析.结果表明,大气中PAHs的气固相分配系数(KP)和各物质的过冷饱和蒸气压(pl⁰)呈良好的线性相关.多元线性回归分析表明,PAHs的气固相分配受颗粒物粒径大小的影响,粒径越大,对PAHs的气固相分配影响越大;过冷饱和蒸气压越高,气固相分配越易受到粒径大小的影响.