生物通风技术修复柴油污染土壤的土柱模拟实验

生物通风技术是将土壤气相抽提和生物降解结合起来的原位强迫氧化降解方法,对于修复因地下储油罐泄漏引起的土壤污染具有广阔的应用前景。通过室内土柱模拟柴油泄漏污染土壤,分析了不同历时残余总石油烃(total pe-troleum hydrocarbon,TPH)的平衡分布规律以及土壤中不同深度柴油量、总柴油量的变化。结果表明:(1)各柱残余TPH剖面分布差异的原因受土柱的初始装填情况的影响较大;(2)残余TPH平衡分布曲线呈双峰型的土柱,柴油的去除主要以挥发作用及生物降解作用为主;(3)挥发作用主要是由通风孔隙体积数及土壤含水率来影响的;重力作用则主要是由初始油浓度、土壤含水率、C∶N∶P影响的;除通风方式外,其余4个因素都对生物降解作用有影响;(4)初始油浓度较大,土壤含水率较小的柱8和柱11,生物降解作用最明显,柴油去除效果最好。该成果可为生物通风过程的强化提供理论依据。     

强化生物通风修复过程中柴油衰减规律及其影响因素研究

强化生物通风技术对于修复因地下储油罐泄漏引起的土壤污染具有很大的应用前景。通过室内土柱模拟柴油泄漏污染土壤,从土柱中总石油烃（total petroleum hydrocarbon,TPH）剖面分布随时间的变化及降解模式角度,分析了其自然衰减和强化生物通风过程。结果表明：初始柴油浓度直接影响着各柱在自然衰减和强化生物通风过程中柱内的残余TPH平衡分布曲线的形状和浓度峰值位置;在前期自然衰减过程中（约1个月）,当土壤中的柴油浓度为5 000～40 000 mg油/kg土时,整个柱内TPH变化的主要原因是重力扩散迁移的结果;当土壤中的柴油浓度≤5 000 mg油/kg土时,其TPH的变化不仅是重力扩散迁移作用的结果,生物降解作用也存在;通风约2个月后,抽提作用对于保持土柱上部柴油浓度稳定变化的意义较为突出。     

土壤柴油污染修复的抽气提取去除实验研究

为得到土壤气相抽提(SVE)去除柴油的优化条件,进行了一维土柱抽气提取去除柴油污染物的实验研究,研究不同初始含水率、不同抽气量对污染土壤中柴油去除率的影响及不同深度残留柴油的变化规律。结果表明：在本实验模拟的范围内,抽气量越大,SVE处理效果越好;初始含水率越低,处理效果越好;此外,不同深度去除率变化的规律基本上是随深度的增大而减小。实验结果可为土壤轻油污染实际治理提供实验数据基础。     

柴油污染包气带的气相抽提影响因素

气相抽提(SVE)是一种经济、高效的土壤原位修复技术。为了研究介质、介质含水率和通风方式对SVE去除效率的影响,并探讨实验运行过程中包气带不同深度柴油浓度的变化规律,实验利用了有机玻璃柱模拟包气带环境,开展柴油污染的SVE实验。结果表明,对于不同介质,SVE去除粗砂中柴油的效率高于中砂;不同含水率,含水率为1%的粗砂中柴油的去除率大于含水率为12%的粗砂;不同的通风方式,连续通风的效率大于间歇通风。此外,不同深度介质均出现柴油浓度先升高后降低的趋势。     

热强化气相抽提法修复半挥发性石油烃污染土壤的影响因素

热强化气相抽提技术(T-SVE)在修复半挥发性石油烃污染土壤方面极具应用潜力。本文基于实验室模拟T-SVE装置,研究了加热温度及土壤含水量、有机质对4种半挥发性石油烃(正十三烷、正十四烷、正十五烷和正十六烷)去除效率的影响,并对石油烃去除动力学进行了拟合。结果表明,温度决定性地影响了石油烃污染土壤的修复效率,污染土壤残留率与加热温度基本呈反比。石油烃去除过程符合Elovich和Freundlich热脱附动力学方程。加热温度为140℃时,土壤含水量(5%~30%)的增加降低了石油烃去除效率;当温度上升到180℃,石油烃去除率在土壤含水量5%~20%时也表现出降低趋势,但在土壤含水量为30%时反而达到最高值。土壤有机质含量增加明显降低了石油烃去除率,尤其对于辛醇-水分配系数值高的石油烃;当加热温度从140℃升高到220℃,土壤有机质对石油烃污染去除的限制明显降低。实验获得结果可为T-SVE技术修复石油烃污染的工程设计提供参考。     

土壤气相抽提法去除红壤中挥发性有机污染物的影响因素研究

土壤气相抽提技术(SVE)是一种安全、经济、高效的土壤治理技术,广泛应用于不饱和土壤中挥发性有机污染物的去除.本实验以我国南方典型土壤红壤(粘性较大的土壤)为实验土样,选用最常见的挥发性有机物苯作为污染物,采用一维土柱通风模拟SVE过程,研究了通风流量、土壤含水率以及间歇操作对苯污染红壤去污过程的影响.结果表明,在各土柱垂向气相中苯浓度变化趋势一致,通风初期浓度迅速降低后进入长时间的拖尾阶段,拖尾阶段初期进行间歇操作可降低能耗达到较经济的治理效果.通风流量与土壤含水率是影响净化时间和修复效果的重要因素,两者均存在最佳值.当通风流量为600 mL/min,含水率为17.2%时本实验净化时间降低为36 h,去除率为99.9%,达到了最佳的治理效果.     

土壤气相抽提技术去污规律及土层压力变化特征分析

土壤气相抽提(SVE)技术可有效去除包气带土壤中挥发性有机污染物(VOCs),是一种经济高效的土壤原位修复技术.对北京市某化工厂内进行SVE技术的现场应用,去除污染土壤中的VOCs,研究污染物的消减规律以及土层压力的变化特征.结果表明,抽出气体的污染物浓度随SVE的运行不断降低,群井抽气初期,VOCs浓度迅速下降,之后...     

EDTA在铅污染土壤治理中的优化处理方法

为了探究EDTA在土壤重金属污染治理中的优化处理方法,采用湿筛和水中重力沉降的方法,从人工Pb污染土壤(原土)中分离提取砂土、粉土和粘土,分析讨论了EDTA对土壤中Pb的去除效果,并从EDTA清洗前后土壤中Pb的BCR形态分布出发,分析了EDTA对不同粒径土壤中各形态Pb的去除效果。研究发现,实验用土壤中砂土、粉土和粘土含量分别为11.2%、75.6%和13.2%,EDTA浓度越高,土壤中Pb去除效果越好,且砂土中Pb最易被去除(~100%),粉土与原土其次(88.66%~96.50%),粘土最难被去除(64.78%~79.60%),但随着EDTA浓度增加,粒径对去除Pb的影响减弱。在土壤修复实践中,可通过利用不同浓度EDTA处理不同粒径土壤的方法达到优化效果。BCR形态分布说明外源性Pb进入土壤后主要以弱酸提取态和可还原态存在,EDTA清洗主要去除弱酸提取态和可还原态,粘土中的各形态去除率均最小。     

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。     

绝缘油污染土壤微波热脱附的影响因素

为探究绝缘油污染土壤微波热脱附的影响条件,考察了温度、停留时间、土壤含水率、污染物初始浓度和微波功率对土壤中绝缘油去除效果的影响.结果表明,温度和停留时间显著影响土壤中绝缘油的去除率,在400℃、微波处理时间5 min的条件下,土壤中绝缘油的去除率为98.6％.当土壤含水率为5％时,土壤中绝缘油的去除率达到最佳.在微波处理15 min内,土壤中绝缘油的去除率随着绝缘油初始浓度的升高逐渐降低.微波功率越高,土壤中绝缘油的微波热脱附效率越高,综合考虑能耗和去除率,微波功率为1 000 W时较优.绝缘油污染土壤微波热脱附机理研究表明,脂肪烃主要通过蒸汽蒸馏和热解吸两种方式从土壤中脱除.本研究结果可为高浓度绝缘油污染土壤微波热脱附技术应用提供参考.     

Experimental investigation of pneumatic soil vapor extraction

Soil Vapor Extraction (SVE) is a common remediation technique for removing volatile organic compounds from unsaturated contaminated soils. Soil heterogeneities can however cause serious limitations to the applicability of SVE due to air bypassing low permeable areas of the soil, leading to diffusion limitation of the remediation. To enhance removal from areas subject to diffusion limitation a new remediation technique, pneumatic soil vapor extraction, is proposed. In contrast to traditional SVE, in which soil vapor is extracted continuously by a vacuum pump, pneumatic SVE is based on enforcing a sequence of large pressure drops on the system to enhance the recovery from the low-permeable areas. The pneumatic SVE technique was investigated in the laboratory using TCE as a model contaminant. 2D-laboratory tank experiments were performed on homogeneous and heterogeneous sand packs. The heterogeneous packs consisted of a fine sand lens surrounded by a coarser sand matrix. As expected when using traditional SVE, the removal of TCE from the low permeable lens was extremely slow and subject to diffusion limitation. In contrast when pneumatic venting was used removal rates increased by up to 77%. The enhanced removal was hypothesized to be attributed to mixing of the contaminated air inside the lens and generation of net advective transport out of the lens due to air expansion.     

Petroleum mass removal from low permeability sediment using air sparging/soil vapor extraction: impact of continuous or pulsed operation

Air sparging and soil vapor extraction (AS/SVE) are innovative remediation techniques that utilize volatilization and microbial degradation to remediate petroleum spills from soils and groundwater. This in situ study investigated the use of AS/SVE to remediate a gasoline spill from a leaking underground storage tank (UST) in the low permeability, clayey soil of the Appalachian Piedmont. The objectives of this study were to evaluate AS/SVE in low permeability soils by quantifying petroleum mass removal rates, monitoring vadose zone contaminant levels, and comparing the mass extraction rates of continuous AS/SVE to 8 and 24 h pulsed operation. The objectives were met by collecting AS/SVE exhaust gas samples and vadose zone air from multi-depth soil vapor probes. Samples were analyzed for O₂, CO₂, BTEX (benzene, toluene, ethylbenzene, xylene), and total combustible hydrocarbon (TCH) concentrations using portable hand meters and gas chromatography. Continuous AS/SVE was effective in removing 608 kg of petroleum hydrocarbons from low permeability soil in 44 days (14.3 kg day⁻¹). Mass removal rates ranged from 2.6 times higher to 5.1 times lower than other AS/SVE studies performed in sandy sediments. BTEX levels in the vadose zone were reduced from about 5 ppm to 1 ppm. Ten pulsed AS/SVE tests removed 78 kg in 23 days and the mean mass removal rate (17.6 kg day⁻¹) was significantly higher than the last 15 days of continuous extraction. Pulsed operation may be preferable to continuous operation because of increased mass removal and decreased energy consumption.     

Model analysis of mechanisms controlling pneumatic soil vapor extraction

The efficiency of traditional soil venting or soil vapor extraction (SVE) highly depends on the architecture of the subsurface because imposed advective air flow tends to bypass low-permeable contaminated areas. Pneumatic SVE is a technique developed to enhance remediation efficiency of heterogeneous soils by enforcing large fluctuating pressure fronts through the contaminated area. Laboratory experiments have suggested that pneumatic SVE considerably improves the recovery rate from low-permeable units. We have analyzed the experimental results using a numerical code and quantified the physical processes controlling the functioning of the method. A sensitivity analysis for selected boundary conditions, initial conditions and parameters was carried out to examine how the method behaves under conditions different from the experimental set-up. The simulations show that at the laboratory level the pneumatic venting technology is superior to the traditional technique, and that the method is particularly efficient in cases where large permeability contrasts exist between soil units in the subsurface.     

吹脱法预处理皮革废水的实验研究

对某皮革厂综合废水进行吹脱预处理实验,综合考察了影响氨氮去除的各个因素(pH值、汽液比、吹脱温度、氨氮初始浓度),同时对该预处理工艺去除铬、SS(悬浮固体浓度)、COD和硫化物的条件进行了优化,并进行了能耗及运行成本估算。结果表明:该厂皮革废水的最佳吹脱工况为pH=11,气液比=1 800,温度25~35℃,在此条件下,当进水ρ(NH3-N)=304.7 mg/L、ρ(Cr)=65.0 mg/L、ρ(SS)=1 700 mg/L、ρ(COD)=2 700 mg/L、ρ(S2-)=112.3 mg/L时,相应的去除率可达78.1%~83.5%、96.4%、88.2%、45.6%和85.0%,且吹脱法对氨氮具有较高的抗冲击负荷能力,吨水处理成本约为3.61元,可作为皮革废水的预处理工艺。     

Biofiltration of gasoline vapor by compost media

Gasoline vapor was treated using a compost biofilter operated in upflow mode over 4 months. The gas velocity was 6 m/h, yielding an empty bed retention time (EBRT) of 10 min. Benzene, toluene, ethylbenzene and xylene (BTEX) and total petroleum hydrocarbon (TPH) removal efficiencies remained fairly stable approximately 15 days after biofilter start-up. The average removal efficiencies of TPH and BTEX were 80 and 85%, respectively, during 4 months of stable operation. Biodegradation portions of the treated TPH and BTEX were 60 and 64%, respectively. When the influent concentration of TPH was less than 7800 mg TPH/m3, approximately 50% of TPH in the gas stream was removed in the lower half of the biofilter. When the influent concentration of BTEX was less than 720 mg BTEX/m3, over 75% of BTEX in the gas stream was removed in the lower half of the biofilter. Benzene removal efficiency was the lowest among BTEX. A pressure drop could not be detected over a 1-m bed height at a gas velocity of 6 m/h after approximately 4 months of operation. Results demonstrated that BTEX in gasoline vapor could be treated effectively using a compost biofilter.     

Removal of polycyclic aromatic hydrocarbons from manufactured gas plant-contaminated soils using sunflower oil: laboratory column experiments

Laboratory column experiments were performed to remove PAHs (polycyclic aromatic hydrocarbons) from two contaminated soils using sunflower oil. Two liters of sunflower oil was added to the top of the columns (33 cm x 21 cm) packed with 1 kg of PAH-contaminated soil. The sunflower oil was applied sequentially in two different ways, i.e. five additions of 400 ml or two additions of 1l. The influence of PAH concentration and the volume of sunflower oil on PAH removal were examined. A soil respiration experiment was carried out and organic carbon contents of the soils were measured to determine degradability of remaining sunflower oil in the soils. Results showed that the sunflower oil was effective in removing PAHs from the two soils, more PAHs were removed by adding sunflower oil in two steps than in five steps, probably because of the slower flow rate in the former method. More than 90% of total PAHs was removed from a heavily contaminated soil (with a total 13 PAH concentration of 4721 mg kg(-1)) using 4 l of sunflower oil. A similar removal efficiency was obtained for another contaminated soil (with a total 13 PAH concentration of 724 mg kg(-1)), while only 2l was needed to give a similar efficiency. Approximately 4-5% of the sunflower oil remained in the soils. Soil respiration curves showed that remaining sunflower oil was degraded by allowing air exchange and supplying with nutrients. Organic carbon content of the soil was restored to original level after 180 d incubation. These results indicated that the sunflower oil had a great capacity to remove PAHs from contaminated soils, and sunflower oil solubilization can be an alternative technique for remediation of PAH contaminated soils.     

复合介质渗透反应格栅去除地下水中的氨氮

针对受低浓度氨氮污染的地下水,实验筛选组合了不同的反应介质,利用串联的多介质填充柱模拟渗透反应格栅,通过物理吸附及生物硝化-反硝化作用来实现氮的去除。结果表明,在进水氨氮浓度为10 mg/L、流速为0.5 m/d的条件下,模拟柱对氨氮的去除率达到98%以上,且不会出现亚硝酸盐及硝酸盐浓度的升高。水体经过释氧柱后溶解氧由2mg/L升高至10 mg/L以上,表明释氧材料可提供硝化细菌所需的好氧环境。好氧柱中填充易于生物挂膜的生物陶粒及对氨氮有较强吸附能力的沸石,二者联用通过生物硝化-物理吸附协同作用实现对氨氮的去除,其中生物作用实现的氨氮去除量占总去除量的50%左右。后续厌氧反应柱填充海绵铁除氧并利用松树皮颗粒作为碳源,创造反硝化菌生长条件,硝酸盐氮浓度可由10 mg/L降低至5 mg/L以下,实现对好氧反应阶段所产生的硝酸盐的去除,避免了地下水的二次污染。     

Batch washing of cadmium from soil and sludge by a mixture of Na2S2O5 and Na2EDTA

Washing of cadmium contaminated soil and sludge using a mixture of 0.1 M Na₂S₂O₅ and 0.01 M Na₂EDTA was investigated in the batch mode. Initial Cd concentration in samples was 500 mg kg⁻¹. The sequential extraction was conducted to study of what form that Cd was removed. SPSS program version 9.01 was performed to determine what soil parameter had the greatest influence on the washing. The organic matter in soil was found to be the main factor for the washing. Soil with low organic matter would have high percentage of removing Cd. When adding more washing solution, the Cd removal efficiency was lower. The highest removal efficiency was between 67.83% and 97.3% when using a 1 g:2.5 ml soil to washing solution ratio. The predominant form of the removed Cd was exchangeable form. By contrast for the sludge, the highest Cd removal efficiency was 17.13% when using sludge in washing solution at the ratio of 1 g:7.5 ml. Most of washed Cd was in reducible form.