土壤粒径及有机质对多溴二苯醚热脱附的影响

在实验室条件下,研究了土壤粒径与土壤有机质含量对多溴二苯醚(PBDEs)热脱附的影响,以期为PBDEs污染土壤热脱附修复提供理论依据。实验结果表明,300℃停留30 min条件下,粒径为<75、75～125、125～250、250～425和425～850μm的土壤中PBDEs去除率分别为49.53%、73.88%、79.39%、83.56%和87.09%,PBDEs总去除率随粒径的增大而增大,土壤BDE209较BDE206、BDE207和BDE208更易于脱除。此外,温度低于450℃时,H2O2氧化部分去除有机质后土壤中PBDEs的去除率较原土高;表明,土壤有机质可能抑制土壤中PBDEs的热脱附。     

氯苯污染土壤低温原位热脱附修复

为了考察低温原位热脱附技术对土壤中氯苯的修复效果,以土壤中氯苯为目标污染物,控制热脱附设备设定温度、土壤粒径、土壤含水率,对不同条件下土壤中的氯苯进行测定分析,研究其对热脱附效果的影响。结果表明:原位热脱附过程中土壤温度变化以加热棒为中心,随着距离增加而呈现时间和空间上的滞后效应;原位热脱附设定温度越高,土壤修复效果越好,当土壤设定温度为100℃时,90%土壤样品氯苯去除率达99%以上,与设定温度130℃修复效果相当;土壤粒径越小,其比表面积大,对污染物吸附效率越高,所需热脱附时间越长;含水率影响氯苯在土壤中的挥发速率、有效孔隙率和透气率,含水率过高或过低都不利于氯苯污染土壤原位热脱附修复。热脱附设备设定温度、土壤粒径、土壤含水率对低温原位热脱附技术去除土壤中氯苯的效果具有较大的影响。     

4种碱基添加剂对1,2,4-三氯苯污染土壤热脱附效果的影响

含氯有机物是土壤中常见的污染物质,对人体危害大,采用热脱附修复技术去除。通过改变加热温度、加热时间及添加4种碱性物质(NaHCO3、NaOH、Ca(OH)2、CaCO3)等条件获取TCB的去除效率及污染土壤理化性质变化情况。实验结果表明,热脱附能有效去除土壤中TCB,当温度为350℃加热30 min时,污染土壤中TCB去除率为83.27%;碱性物质的添加能有效强化热脱附过程,添加1%的NaHCO3、NaOH、Ca(OH)2和CaCO3后,TCB去除率分别提高了28.28、26.13、20.28、18.19%。碱性物质的添加促进了TCB的脱氯和降解,相比于无碱性物质热脱附,添加1%NaHCO3和NaOH后尾气中DCBz增加了5.4 ug·L-1和3.65 ug·L-1。热脱附后土壤有机碳、有效磷质量分数和阳离子交换量减少,电导率增大;碱基协同热脱附前后土壤的总有机碳质量分数变化不大,土壤中有效磷质量分数和阳离子交换量明显增大,脱附条件为250℃、30 min以及1%的Ca(OH)2时,脱附前后有效磷由57.5 mg·kg-1增大至80.2 mg·kg-1,阳离子交换量由19.72 cmo...     

基于超声波-微波耦合效应的石油烃类污染土壤的热脱附规律与参数优化

以邻二甲苯为石油烃类污染物代表,以污染土壤质量的减少量以及冷凝液质量的增加量表征土壤污染物的平均脱附效率,研究了微波-超声波耦合热源处理石油烃类污染土壤的脱附规律。结果表明,在超声波功率恒定(800 W)情况下,增大微波功率(从200 W增到400 W),能显著提升装置内反应温度(从128.3℃增到270.1℃),显示了微波较强的热效应;在微波功率恒定(350 W)情况下,增大超声波功率(从600 W增到1 400 W),对装置升温效果影响不明显(从169.4℃增加到187.9℃),表明了超声波较弱的热效应。超声波/微波耦合热源修复壤土的最优工艺参数为土水比20∶1、超声波功率800 W、微波功率350 W、辐照10 min,相应的最高污染物平均脱附率为77.28%,处理效果优于单热源条件。对于不同的土壤粒径及有机质含量,不同类型土壤的平均脱附率排序为砂土(88.36%)壤土(64.29%)黏土(52.61%);综合考虑土壤介电损耗因子、土壤比热容、土壤通透性影响的结果,土水比最优值设为10∶1;综合考虑土壤颗粒单层吸附/多层吸附作用的结果,土壤污染物浓度最优值为8%(砂土)、4%(壤土、黏土)。     

有机质对污染土壤中DDTs热脱附行为的影响

采用2种不同性质土壤(黑土和棕壤)作为供试土壤,利用DDT农药自配滴滴涕类(DDTs,包括p,p'-DDT、o,p'-DDT、p,p'-DDD、p,p'-DDE)污染土壤.采用热脱附方法,研究了原土及去有机质后土壤中DDTs在300℃,6个停留时间(5、10、20、30、40和50 min)下的去除率以及脱附后土壤中D...     

天津某复杂有机污染地块原位热脱附修复技术中试研究

针对受到挥发性有机物、农药污染形成的复杂有机污染地块,采用原位热脱附修复技术开展中试试验,研究该技术在低渗透区(以粉质黏土/黏土为主)、污染程度复杂、污染严重条件下的技术有效性,同时研究该技术使用过程中的升温规律及影响半径。结果表明,原位热脱附前期,位于加热井所构成正三角形的中心点的测温井以5℃/d的速率升温,当土壤温度到达95～100℃,进入潜热阶段,此时土壤中水分大量汽化,当升温达到100℃左右时,土壤中毛细水未完全去除,升温进入瓶颈期;综合考虑该地块原位热脱附的影响半径为1.5 m。     

热脱附技术在修复石油烃污染土壤中的应用研究

采用热脱附技术处理实际石油烃污染土壤,考察影响热脱附效率的影响因素,并结合工程实际,初步确定热脱附技术的最优工艺参数.实验结果表明,热脱附技术可有效修复石油烃污染土壤,其中加热温度、停留时间是影响修复效果的关键因素.相同热脱附条件下,石油烃组分相对分子质量越大,饱和蒸气压越低,与土壤有机质结合能力越强,越不易脱附.当加...     

载气含氧量及污染物浓度对土壤石油烃热脱附效率的影响

石油烃(TPHs)在土壤中难以降解,并具有生物毒性,异位热脱附(ESTD)在修复石油烃污染土壤方面极具应用潜力。采用实验室模拟异位热脱附装置,研究了热脱附载气含氧量及土壤石油烃污染浓度对可萃取石油烃(EPHs)中柴油段(DRO)和重油段(ORO)的5种组分去除率的影响。结果表明:在初始浓度为5 000～20 000mg·kg~(-1)时,在20 min内的脱附率均不超过50%;当初始浓度增加到40 000 mg·kg~(-1)、脱附时间为20 min时脱附率可以达到68.2%。热脱附时间为50 min时,40 000 mg·kg~(-1)污染土壤的残余浓度为407.1 mg·kg~(-1)。DOR组分相同时间的脱附率随污染浓度的升高而升高,ORO组分在50 min之内不能完全脱附,脱附率随着污染物浓度上升会出现先增大后减小的趋势。在250℃时,DRO中3个组分的去除率均随着气氛含氧量的增加而呈现明显的增长趋势。在400℃条件下,ORO中2个组分分别在含氧量为12%和15%时达到最高的去除率。本研究结果可为ESTD技术修复不同浓度的石油烃污染土壤的工程设计参数提供参考。     

基于碳数分段法的石油烃污染土壤异位热脱附工艺的优化

针对石油烃污染土壤成分复杂、污染严重、修复难度高的问题,采用适用性广、效率高且去除彻底的异位热脱附技术修复石油烃污染土壤.利用碳数分段法及室内模拟实验,探究在热脱附过程中的土壤粒径、含水率和有机质对石油烃及各组分热解吸效率的影响;另外,还采用响应面法对各影响因素进行了优化,以获得异位热脱附修复石油烃污染土壤的最优工艺参...     

添加剂强化热脱附修复菲污染土壤

针对多环芳烃污染土壤热脱附能耗较高的问题，采用K₂CO₃、CaCO₃和Fe₂O₃等添加剂强化热脱附过程，以降低能耗。通过室内模拟实验研究了热脱附温度、停留时间、添加剂种类与投加量等对菲(Phe)去除效果的影响，分析了热脱附去除过程、能耗以及热脱附后土壤理化性质的变化。结果表明：在100、200℃下停留30 min,投加5.0%(质量分数)的K₂CO₃、CaCO₃和Fe₂O₃均能显著提高Phe的去除率(p<0.05),效果最好的是K₂CO₃。添加剂投加后土壤导热系数的提高可能是促进热脱附的重要原因。200℃停留30 min时，Phe去除率随K₂CO₃投加量增加呈现先增加后下降趋势，最优投加量为5.0%,此时去除率为85.90%,较无添加剂组提高了11.82百分点。200℃时，投加...     

脱水污泥热调质的特性

热调质方法是污泥深度脱水的有效办法之一。研究结果表明,污泥热调质过程中反应温度和反应时间对污泥热调质效果影响较大,搅拌速度影响较小。当反应温度从160℃升至180℃,反应时间从30 min增至60 min时,污泥溶液中挥发性悬浮固体(VSS)急剧溶解,释放出细胞里的结合水,表明污泥细胞破壁的温度条件为160～180℃,时间条件为45～60 min。热调质后污泥的比阻变化较大。随着反应温度的不断提高,比阻不断减小,污泥的脱水性能越来越好。实验确定了污泥热调质的最佳反应条件为:反应温度180℃,反应时间60 min,搅拌转速30 r/min。在此条件下,压滤后泥饼含水率约50%,滤液中COD浓度可达19 000 mg/L,有利于后续污泥的消化。     

The effect of atmospheric thermal conditions and urban thermal pollution on all-cause and cardiovascular mortality in Bangladesh

This study assessed the effect of temperature and thermal atmospheric conditions on all-cause and cardiovascular mortality in Bangladesh. In particular, differences in the response to elevated temperatures between urban and rural areas were investigated. Generalized additive models (GAMs) for daily death counts, adjusted for trend, season, day of the month and age were separately fitted for urban and rural areas. Breakpoint models were applied for determining the increase in mortality above and below a threshold (equivalent) temperature. Generally, a 'V'-shaped (equivalent) temperature-mortality curve with increasing mortality at low and high temperatures was observed. Particularly, urban areas suffered from heat-related mortality with a steep increase above a specific threshold. This adverse heat effect may well increase with ongoing urbanization and the intensification of the urban heat island due to the densification of building structures. Moreover, rising temperatures due to climate change could aggravate thermal stress.     

Products of thermal degradation of dielectric fluids

Polychlorinated dibenzofurans (PCDFs) are formed in the combustion of polychlorinated biphenyls (PCBs), trichlorobenzene, and tetrachloroethylene transformer dielectric fluids. Polychlorinated dibenzodioxins (PCDDs) are also observed, but at lower levels.     

Fingerprints of dioxin from thermal industrial processes

PCDD/F homologue profiles and 2,3,7,8 chlorine-substituted congener patterns are studied using principal component analysis and hierarchical cluster analysis. Measurement data from different industrial metallurgical processes such as iron and steel manufacturing, copper smelters and aluminium plants are compared. It appears that the PCDD/F homologue profiles from industrial metallurgical processes are similar to those from municipal solid waste incinerators. The 2,3,7,8 chlorine-substituted congener pattern from copper smelters is also very similar to that of municipal solid waste incinerators. However, the 2,3,7,8 chlorine-substituted congener pattern from an aluminum plant is very different, 2,3,7,8-TCDF being by far the most important TCDF congener.     

蓄热式热氧化器的改进与应用

为了解决城市周边小企业挥发性有机物空气污染问题,研发了一种新型多蓄热室旋转换向蓄热式热氧化器,对现有蓄热式热氧化器内不合理的流通截面积分配比例进行了改进,并在北京市郊某工厂建设了处理能力3 000 m3/h的应用示范装置.应用情况表明,新型蓄热式热氧化器对VOC的处理效率可达96%,同时比常规热力焚烧炉节能70%以上....     

Response of thermal stressed bobwhite to organophosphorus exposure

Constant and intermittent cold stressed juvenile northern bobwhite (Colinus virginianus) were exposed to chlorpyrifos, an organophosphorus insecticide, following avian dietary LC(50) test procedures. Chlorpyrifos concentrations ranged from 100 to 1000 ppm; ambient temperatures (T(a)) included 35.0 (control), 32.5, 30.0 and 27.5 degrees C. Survival decreased significantly under constant cold conditions. Non-survivors averaged 33% weight loss, but survivor weight dropped with increasing dose and decreasing T(a). Control quail at all temperatures maintained a constant body temperature (T(b)); however, T(b) of dosed quail fell with increasing dose and decreasing T(a). Non-surviving cold stressed quail had higher cholinesterase (ChE) activity that non-survivors at 35 degrees C; in addition, dead quail failed to average the 50% inhibition of ChE used to implicate a ChE depressant in death. Daily exposure of quail to 12 h of warmth increased survival. Survivors of intermittent cold stress experienced less weight loss than constant cold survivors due to reduced metabolic costs. Synergistic effects were evident in juvenile northern bobwhite exposed simultaneously to chlorpyrifos and cold stress; however, mortality and certain sublethal effects were mitigated when cold exposure was intermittent.     

飞灰热处理过程中基本特性研究

对不同粒径飞灰中重金属的分布情况进行了研究,并采用高温熔融管式电炉试验装置,对垃圾焚烧飞灰进行了高温热处理研究,探讨了热处理过程中飞灰减重率和重金属挥发率的变化规律,并对飞灰热处理后的收集物进行XRD实验。结果表明,Cd和Pb在小粒径飞灰中含量较高,Zn和Cu的分布与飞灰的粒径分布相似,Cr富集于相对较大粒径的飞灰中。热处理过程中,1 150 ℃和1 350 ℃时飞灰减重率增长快,而在650～1 050 ℃之间减重率增长缓慢,仅从8%增加至17%。飞灰中重金属经热处理后,挥发率依次为Pb＞Cd＞Cu＞Zn。XRD实验结果表明,Pb主要以双金属氯化物（KPb₂Cl₅）形式挥发。     

Pesticide residues in thermal mineral water in Greece

Eight different hot springs (SPA) in Greece were monitored over a one-year survey for priority pesticide residues. A specific and effective procedure including solid phase extraction in combination with HPLC and GC analytical methods were applied. Samples that were sensitive to nitrogen-phosphorus (NPD) and/or electron capture (ECD) detectors were analysed by capillary gas chromatography. From the twenty-six water samples, pesticide residues were detected in fourteen of them (54%) but no one exceeding the European Union Maximum Acceptable Concentration (MAC). Lindane (gamma-BHC) was the most frequently detected pesticide. It was found in nine samples (35%) in concentrations from < 0.005 to 0.01 microg/L. Other pesticides detected were phorate (in five samples), propachlor (in two samples) and chlorpyriphos ethyl (in three samples) but in concentrations far below the permissible levels.     

Conversion of concentrated solar thermal energy into chemical energy

When a concentrated solar beam is irradiated to the ceramics such as Ni-ferrite, the high-energy flux in the range of 1500-2500 kW/m(2) is absorbed by an excess Frenkel defect formation. This non-equilibrium state defect is generated not by heating at a low heating-rate (30 K/min), but by irradiating high flux energy of concentrated solar beam rapidly at a high heating rate (200 K/min). The defect can be spontaneously converted to chemical energy of a cation-excess spinel structure (reduced-oxide form) at the temperature around 1773 K. Thus, the O(2) releasing reaction (α-O(2) releasing reaction) proceeds in two-steps; (1) high flux energy of concentrated solar beam absorption by formation of the non-equilibrium Frenkel defect and (2) the O(2) gas formation from the O(2-) in the Frenkel defect even in air atmosphere. The 2nd step proceeds without the solar radiation. We may say that the 1st step is light reaction, and 2nd step, dark reaction, just like in photosynthesis process.