集成膜法回收钛白废酸中硫酸

对扩散渗析回收钛白废酸中硫酸与减压膜蒸馏联合浓缩废酸进行了实验研究。结果表明,扩散渗析的酸回收率、回收酸浓度和亚铁泄漏率随料液流量的增大而减小,而酸渗析速度及酸对硫酸亚铁的分离系数却随之增大;随水料比的增大,酸回收率、酸渗析速率和亚铁泄漏率增大,回收酸浓度及酸对硫酸亚铁的分离系数减小;在选定实验条件下,硫酸浓度为1.92 mol/L的钛白废酸,先经扩散渗析进行酸盐分离,然后经减压膜蒸馏浓缩,可得到硫酸质量百分浓度为65%以上的浓缩废酸,达到了返回钛白生产使用的要求。     

清洗液和阻垢剂对疏水膜接触角的影响

研究了采用不同pH的酸、碱清洗液及阻垢剂溶液静态浸泡对聚偏氟乙烯(PVDF)和聚四氟乙烯(PTFE)疏水平板膜接触角的影响.实验结果表明:随pH 2.5盐酸和pH2.0草酸浸泡PVDF膜和PTFE膜时间的延长,两种疏水膜的接触角均小幅度减小,说明酸性清洗液对两种疏水膜性能的影响较小;随pH11.5NaOH溶液浸泡膜时间...     

不饱和聚酯树脂高浓度废水共沸精馏资源化与治理技术

针对不饱和聚酯树脂生产高浓度废水的特点,采用新型共沸精馏技术进行资源化预处理。实验结果表明,共沸精馏几乎将废水中的原料、聚合中间体等有机物全部浓缩于釜液中,釜底浓缩液COD可高达120万mg／L左右,有机物回收率达93％～96％。将COD约120万nq-g／L的釜液以20％比例投入不饱和聚酯树脂合成反应中,制得了一种新型高性能树脂,且树脂的得率由常规生产的93．4％提高至99．77％。对与共沸剂分离后的COD约为1万mg／L的馏出液采用新型多技术协同催化氧化技术进行预处理,使废水B／C由0．021提高至0．3以上;再采用EGSB＋MBBR生化处理和活性炭吸附深度处理,出水可稳定达标排放,并能满足循环冷却水要求。     

炼油厂延迟焦化装置冷焦水密闭脱臭处理

通过对焦化冷焦水性质的分析,并结合目前其它炼油厂的经验,自行设计建成了一套冷焦水密闭脱臭装置,该套装置具有投资省,操作方便的优点。装置建成投用至今已连续正常运行9个月,脱臭效果明显,周围环境状况大为改善。     

珠江广州河段漂浮垃圾分布特点及治理策略

通过对珠江广州河段水上漂浮垃圾不同时间打捞量、来源分布、及其构成成份的调查和分析,提出水上垃圾总量模型和打捞削减模型,并根据广州地区的特点,提出水上垃圾的治理必须加强源头宏观管理;增加河涌拦网设置;扩大江面垃圾打捞区域;强化水上环卫管理队伍监管能力等策略意见。     

试论空分装置的防爆技术

空分装置的安全运行是工业制氧安全生产的关键环节 ,也是最难控制的危险源。本文从空分爆炸原理入手 ,系统阐述了碳氢化合物在液氧中的积聚机理 ,激发能源的种类与形成 ,并提出了综合控制空分爆炸的若干措施     

Using NDVI to Assess Vegetative Land Cover Change in Central Puget Sound

We used the Normalized Difference Vegetation Index (NDVI) in the rapidly growing Puget Sound region over three 5-year time blocks between 1986–1999 at three spatial scales in 42 Watershed Administrative Units (WAUs) to assess changes in the amounts and patterns of green vegetation. On average, approximately 20% of the area in each WAU experienced significant NDVI change over each 5-year time block. Cumulative NDVI change over 15 years (summing change over each 5-year time block) was an average of approximately 60% of each WAU, but was as high as 100% in some. At the regional scale, seasonal weather patterns and green-up from logging were the primary drivers of observed increases in NDVI values. At the WAU scale, anthropogenic factors were important drivers of both positive and negative NDVI change. For example, population density was highly correlated with negative NDVI change over 15 years (r = 0.66, P < 0.01), as was road density (r = 0.71, P < 0.01). At the smallest scale (within 3 case study WAUs) land use differences such as preserving versus harvesting forest lands drove vegetation change. We conclude that large areas within most watersheds are continually and heavily impacted by the high levels of human use and development over short time periods. Our results indicate that varying patterns and processes can be detected at multiple scales using changes in NDVIa values.     

基于控制单元的农村生活污水处理优化模型

基于系统动力学(SD)模拟模型和Powell优化模型,建立了农村生活污水污染物削减量与治理费用的SD-Powell模拟优化耦合模型,该模型可模拟预测污染物排放量,建立污染物削减量与治理费用函数关系.在此基础上,以污水治理费用最小为目标,以污水处理量为约束条件,对区域污染物削减量进行空间优化,得到最小治理费用下的最大污染物削减量.以常州市为例进行实证分析,模拟结果显示,2020年常州市农村生活污水COD和NH3-N排放量将达到16583t和2551t,分别比2008年增长4.60%和4.59%.采用聚类方法将常州市51个乡镇划分为4类控制单元,得到4类地区COD、NH3-N治理费用函数.各单位治理资金削减量存在明显差异,COD削减率的排序依次为:I类控制单元413kg/万元、IV类控制单元 380kg/万元、II类控制单元352kg/万元、III类控制单元348kg/万元,NH3-N削减率的排序依次为:III类控制单元65kg/万元、I类控制单元64kg/万元、IV类控制单元58kg/万元、II类控制单元54kg/万元,全区域削减率达到100%需要的治理费用约为16870万元.污染物削减空间优化结果显示,基于控制单元空间优化的削减效率高于平均分配的结果,治理费用在1000 -16870万元/a范围,COD、NH3-N的削减率分别提高6.4%和7.4%,4类地区的优先排序顺序依次为I类,IV类,II类和III类.     

Biomass waste gasification - can be the two stage process suitable for tar reduction and power generation?

A pilot scale gasification unit with novel co-current, updraft arrangement in the first stage and counter-current downdraft in the second stage was developed and exploited for studying effects of two stage gasification in comparison with one stage gasification of biomass (wood pellets) on fuel gas composition and attainable gas purity. Significant producer gas parameters (gas composition, heating value, content of tar compounds, content of inorganic gas impurities) were compared for the two stage and the one stage method of the gasification arrangement with only the upward moving bed (co-current updraft). The main novel features of the gasifier conception include grate-less reactor, upward moving bed of biomass particles (e.g. pellets) by means of a screw elevator with changeable rotational speed and gradual expanding diameter of the cylindrical reactor in the part above the upper end of the screw. The gasifier concept and arrangement are considered convenient for thermal power range 100-350 kW_th. The second stage of the gasifier served mainly for tar compounds destruction/reforming by increased temperature (around 950 °C) and for gasification reaction of the fuel gas with char. The second stage used additional combustion of the fuel gas by preheated secondary air for attaining higher temperature and faster gasification of the remaining char from the first stage. The measurements of gas composition and tar compound contents confirmed superiority of the two stage gasification system, drastic decrease of aromatic compounds with two and higher number of benzene rings by 1-2 orders. On the other hand the two stage gasification (with overall ER = 0.71) led to substantial reduction of gas heating value (LHV = 3.15 MJ/Nm³), elevation of gas volume and increase of nitrogen content in fuel gas. The increased temperature (>950 °C) at the entrance to the char bed caused also substantial decrease of ammonia content in fuel gas. The char with higher content of ash leaving the second stage presented only few mass% of the inlet biomass stream.     

关于在用电梯安全管理中主体责任的思考

本文通过从电梯行业的流通各环节进行讨论,介绍各环节涉及主体、各主体存在的问题及各主体间的联系,重点探讨关于在居民公用电梯使用中业主安全主体责任不明晰、未能有效落实的问题.并为如何有效落实业主在电梯安全管理中的主体责任提出几点对策,以期为降低电梯带病运行的可能、最大程度消除潜藏安全隐患提供一定的参考,从而规范电梯行业安全管理.