二氧化硫烟气碱吸收液低温催化歧化的研究

为实现低浓度二氧化硫烟气处理过程中硫的资源化,提出了一种新型二氧化硫烟气净化技术,即二氧化硫碱吸收-低温催化制备硫黄和硫酸氢钠工艺.该工艺首先采用碱液直接吸收净化二氧化硫烟气,再通过低温催化碱吸收液获得含硫产品,实现了硫的资源化.首先通过热力学计算证明了碱吸收液中亚硫酸氢钠的歧化反应在低温条件(＜100℃)下发生的可行性.然后研究了反应物浓度对吸收过程和歧化反应过程的影响,结果表明,增加反应物浓度可加快歧化反应速率.此外,研究了硫黄产品的脱稳过程,结果表明,当脱稳加热时间为6h时,硫黄产率可达到95.97％,所得硫黄产品为纯度较高的单斜硫.该催化过程为固—液—固反应,兼具了多相反应与均相反应的优点.     

钢厂石灰窑烟气CO_2的回收利用

简述了某钢厂将石灰窑烟气中的CO2回收,制成食品级CO2的工艺概况及其综合利用效益,为工业尾气CO2资源化循环利用提供了示范。     

Effects of introducing energy recovery processes to the municipal solid waste management system in Ulaanbaatar,Mongolia

Currently, most developing countries have not set up municipal solid waste management systems with a view of recovering energy from waste or reducing greenhouse gas emissions. In this article, we have studied the possible effects of introducing three energy recovery processes either as a single or combination approach, refuse derived fuel production,incineration and waste power generation, and methane gas recovery from landfill and power generation in Ulaanbaatar, Mongolia, as a case study. We concluded that incineration process is the most suitable as first introduction of energy recovery. To operate it efficiently,3Rs strategies need to be promoted. And then, RDF production which is made of waste papers and plastics in high level of sorting may be considered as the second step of energy recovery.However, safety control and marketability of RDF will be required at that moment.     

Effects of introducing energy recovery processes to the municipal solid waste management system in Ulaanbaatar,Mongolia

Currently, most developing countries have not set up municipal solid waste management systems with a view of recovering energy from waste or reducing greenhouse gas emissions. In this article, we have studied the possible effects of introducing three energy recovery processes either as a single or combination approach, refuse derived fuel production, incineration and waste power generation, and methane gas recovery from landfill and power generation in Ulaanbaatar, Mongolia, as a case study. We concluded that incineration process is the most suitable as first introduction of energy recovery. To operate it efficiently, 3Rs strategies need to be promoted. And then, RDF production which is made of waste papers and plastics in high level of sorting may be considered as the second step of energy recovery. However, safety control and marketability of RDF will be required at that moment.     

海南省城镇污泥处理处置对策建议

为了便于海南省实现污泥的有效处置,研究组对海南省全部污水处理厂相关运营数据进行了系统分析,基于前期资料分析、实地调查及典型污水处理厂污泥采样分析结果,本研究明确了污水收集管网覆盖面低、雨污不分流等海南省城镇污水处理厂运营现状,同时提出污泥产量低、污泥处理后部分指标不达标、现有处置方式单一、不尽合理等污泥处理处置现状及存在问题。最后,提出了加快城镇污水收集管网建设、强化污泥处理工作及加强投资与管理等建议。     

城市建筑垃圾的资源化利用

随着建设项目的增多,建筑垃圾也日益增多。本文对建筑垃圾资源化利用进行了初步分析,重点通过对建筑垃圾的分类研究,提出我国建筑垃圾资源化存在问题及建议。     

电磁水循环加热方式在稠油开采中的应用

分析了稠油开采过程中螺杆泵传统电缆加热方式的不足,提出新型电磁水循环加热方式,实现了现场安全、节能和环保的提升,且能提高原油日产量。     

流动注射在线UV消解测定环境水体中的总氮研究

采用San++流动分析仪在线UV消解测定环境水体中的总氮,样品浓度在0.00~5.0 mg/L与峰高有良好的线性关系(r=0.999 6)。进行了标准样品考核和实际水样的流动注射法和国标方法的比对分析。实验结果表明:采用流动注射在线消解测定水中TN,其标样测定值均在保证值范围内,相对标准偏差小于3%;两种方法测定实际水样的结果无显著性差异且具有很好的一致性,加标回收实验的回收率在90.0%~97.7%之间,能满足地表水及排放废水中TN监测要求。     

浅述汽车加油站油气回收系统监测研究

加油站油气回收系统是由卸油油气回收系统、汽油密闭储存、加油油气回收系统、在线监测系统和油气排放处理装置组成。该系统的作用是将加油站在卸油、储油和加油过程中产生的油气,通过密闭收集、储存和送入油罐汽车的罐内,运送到储油库集中回收变成汽油,以达到在汽车加油、油料储运过程中油汽不外泄,不污染周边环境的目的。根据中华人民共和国《加油站大气污染物排放标准》(GB 20952-2007)中第六条的规定,长三角地区的改造项目应在2010年1月1日进行,因此对加油站油气回收系统的监测显得十分紧迫。     

Anaerobic-aerobic treatment of purified terephthalic acid (PTA) effluent; a techno-economic alternative to two-stage aerobic process

This paper addresses the treatment of purified terephthalic acid (PTA) effluent using anaerobic and aerobic processes. Laboratory studies were carried out on flow proportionate composite wastewater generated from the manufacturing of PTA. An activated sludge process (ASP-two stage and single stage) and an upflow anaerobic fixed film fixed bed reactor (AFFFBR) were used, individually and in combination. The performance of a full-scale ETP under existing operating conditions was also studied. Full scale ETP studies revealed that the treatment of PTA effluent using a two-stage ASP alone does not meet treated effluent quality within the prescribed Indian Standards. The biomass produced in the two stage ASP was very viscous and fluffy and the sludge volume index (SVI) was very high (200-450 ml/g). However, pretreatment of PTA effluent using an upflow AFFFBR ensured substantial reduction in BOD (63%) and COD (62%) with recovery of biogas at 1.8-1.96 l/l effluent treated at a volumetric loading rate (VLR) 4-5 kg COD/m(3) d. The methane content in the biogas varied between 55% and 60%. The pretreated effluent from the upflow AFFFBR was then treated through a single stage ASP. The biomass produced in the ASP after anaerobic treatment had very good settlability (SVI: 75-90 ml/g) as compared to the two stage ASP and the treated effluent quality with respect to BOD, COD and SS was within the prescribed Indian Standards. The alternative treatment process comprising an upflow AFFFBR and a single stage ASP ensured net power saving of 257 kW and in addition generated 442 kW of power through the AFFFBR.