利用UVC去除低浓度丁烷的实验研究

探讨了不同实验参数对丁烷在UVC下去除效果的影响,获得了丁烷的去除率与丁烷的初始浓度、气体流量、相对湿度、氧气含量等参数之间的关系。数据表明：在实验条件范围内,丁烷的去除率随其初始浓度和气体流量增大而减小;丁烷的去除率随相对湿度的增加呈现先快速升高后缓慢降低的关系,最佳相对湿度值在40%～60%之间;丁烷的去除率随氧气...     

TiO2薄膜气相光催化氧化低浓度三氯甲烷和三氯乙烯的研究

自行设计了气固相光催化实验系统。以铝材为担载体，TCM和TCE为模拟污染物，在常温，常压下，对辐射光源，气体相对湿度，污染物反应浓度等因素对TCM和TCE的光催化降解反应的影响进行了研究。结果表明，在研究所采用的实验条件下，辐射光源采用254nm时的降解效率要比采用365nm时高10%左右。气体相对湿度为40%时光催化降解效率最高；随着污染物反应浓度的增加，TCM的降解效率降低，而TCE的降解效率增加，初步的反应动力学研究结果表明，TCM和TCE在二氧化钛表面的光催化降解反应可采用Langmuir-Hinshelwood动力学方程来表征。     

新型管状光催化反应器降解VOCs特性

以一种新型折流式管状光催化反应器为研究对象,选择甲醛、苯和甲苯为目标污染物,以紫外光源、催化剂负载量和反应器内循环流量为关键影响因素,利用非密闭型环境舱,分析了反应器降解室内VOCs特性。结果表明,在254 nm和365 nm紫外光源照射下,VOCs的总衰减系数随初始浓度的增加而增大,且254 nm紫外光源照射下的总衰减系数更大。365 nm紫外光源照射时,VOCs的反应有效度随催化剂负载量的增加而增大;254 nm紫外光源照射时,反应有效度受催化剂负载量变化的影响很小。VOCs的转化率随循环流量的增加而增大,而反应速率受循环流量的影响较小;相同的循环流量下,转化率和反应速率均随着VOCs初始浓度增加而增大。由于增设肋片,折流式管状反应器比传统无肋片管状反应器的洁净空气量提升60%,且反应有效度更接近0.5,说明前者的传质-反应速率更加匹配,降解性能明显更优。     

铈离子光催化降解茜素绿的性能和机理

主要研究了简单铈离子（Ce3＋）在紫外光（uv）的作用下对蒽醌染料茜素绿（AG）的光催化降解效果和反应机理。结果表明，UV／Ce3＋体系能够有效降解AG，初始反应速率随AG浓度的倒数值和Ce3＋浓度的增加而线性增加，随初始溶液pH的增加先降低后增加，在酸性条件下有很高的TOC去除率。荧光探针实验表明，反应过程中可以产生·OH自由基。UV／Ce3＋体系对其他类型染料和对硝基苯酚都有较好的降解效果。     

臭氧洗消化学战剂模拟剂DPCP试验研究

用臭氧对神经性化学战剂的模拟剂氯磷酸二苯酯（DPCP）进行洗消，试验考察了初始酸度、O₂流量、放电功率、放电室压力、反应温度、初始浓度和O₃流量等因素对DPCP降解率的影响。碱性条件下DPCP降解率高于酸性条件下的降解率；反应温度、O₃流量、放电功率的增加，DPCP降解率上升；初始浓度增加，DPCP降解率下降；氧气流量和放电室压力增加，DPCP降解率先上升，后下降。在最佳反应条件下，50 mg/L的DPCP处理16 min降解率达到98%，矿化率40.1%。     

臭氧氧化深度处理某工业园的印染废水尾水

采用O_3氧化法深度处理印染废水尾水。单因素实验结果表明,提高O_3浓度有利于TOC与UV254的去除,提高至4 mg·L~(-1)后TOC与UV254去除率不再升高;TOC与UV254去除率随反应进程逐渐升高,前10 min为快速反应阶段,此后为慢速分解阶段;弱碱性环境有利于O_3的氧化作用。采用响应面法获得了O_3氧化在最佳条件(pH 8.76,O3浓度4.88mg·L~(-1),反应60 min)下印染废水尾水TOC和UV254去除率分别为22.85%和76.48%。TOC去除率远大于UV254去除率。该显著差异表明,O_3能有效破坏含C=C和C=O双键的简单芳香族化合物结构,但对有机物矿化能力较差。GC-MS分析结果表明,印染废水尾水中除含大量长链烷烃、卤代烷烃、环状烷烃外,还含有以甲苯,二甲苯为主以及少量难降解的萘、菲等苯系物;经O_3氧化后,水中仅存少量残留二甲苯,其余苯系物均未检出。     

TiO2薄膜气相光催化氧化低浓度三氯甲烷和三氯乙烯的研究

自行设计了气固相光催化实验系统,以铝材为担载体,TCM和TCE为模拟污染物,在常温、常压下,对辐射光源、气体相对湿度、污染物反应浓度等因素对TCM和TCE的光催化降解反应的影响进行了研究.结果表明,在研究所采用的实验条件下,辐射光源采用254 nm时的降解效率要比采用365 nm时高10%左右;气体相对湿度为40%时光催化降解效率最高;随着污染物反应浓度的增加,TCM的降解效率降低,而TCE的降解效率增加.初步的反应动力学研究结果表明,TCM和TCE在二氧化钛表面的光催化降解反应可采用Langmuir-Hinshelwood动力学方程来表征.     

低频超声协同Fe-Ni-Mn／Al2O3催化降解酸性绿B的研究

采用低频超声与Fe-Ni-Mn／Al2O3催化剂协同降解偶氮染料酸性绿B模拟废水，考察染料初始浓度和pH值、催化剂、饱和气体及H2O2等因素对酸性绿B降解效果的影响，结果表明：催化剂Fe-Ni-Mn／Al2O3与低频超声存在协同效应，催化剂的最佳投加量为6g／L；酸性条件有利于染料的超声降解，当pH=3．8时，可取得最佳的降解效果；酸性绿B降解率随初始浓度的增大而降低，其优化初始浓度为100mg／L，此外，在反应体系中鼓入饱和气体也可促进酸性B的降解，且影响顺序为混合气体（air＋Ar）〉氧气〉氩气；在反应过程中投加H2O2有利于染料降解率的提高。在优化实验条件下降解150min，酸性绿B色度去除率达到91．4％。     

铈离子光催化降解茜素绿的性能和机理简

主要研究了简单铈离子（Ce³⁺）在紫外光（UV）的作用下对蒽醌染料茜素绿（AG）的光催化降解效果和反应机理。结果表明，UV/Ce³⁺体系能够有效降解AG，初始反应速率随AG浓度的倒数值和Ce³⁺浓度的增加而线性增加，随初始溶液pH的增加先降低后增加，在酸性条件下有很高的TOC去除率。荧光探针实验表明，反应过程中可以产生·OH自由基。UV/Ce³⁺体系对其他类型染料和对硝基苯酚都有较好的降解效果。     

零价铁修复受三氯乙烯污染地下水的实验研究

通过批实验和柱实验研究了三氯乙烯（TCE）初始浓度、四氯乙烯(PCE)等对零价铁去除三氯乙烯的影响，并建立了三氯乙烯降解的反应动力学方程。结果表明：（1）零价铁对TCE具有较好的降解效果，反应符合准一级反应动力学方程，表观反应速率常数随TCE浓度的增加而减小；（2）在铁粉充足的条件下，TCE初始浓度对降解效果影响不显著，且TCE去除率皆可达到90%以上；（3）PCE的存在抑制了TCE的脱氯反应。PCE和TCE共存时，TCE的最大去除率仅为64.2%；TCE脱氯反应的表观反应速率明显降低，反应半衰期由TCE单独存在时的6.8～9.7 h增大到66 h～346.5 h。     

K2Cr2O7溶液同时脱硫脱硝实验研究

采用K2Cr2O7溶液作为吸收液,在自制的鼓泡反应器内,对模拟烟气进行同时脱硫脱硝的实验研究,考察多种因素对SO2脱除率(即脱硫率)和NO脱除率(即脱硝率)的影响。实验结果表明:K2Cr2O7浓度、反应温度、NO浓度、SO2浓度、烟气流量对脱硫率、脱硝率影响显著;当烟气流量为0.4L/min,气相中O2体积分数为6%,SO2体积分数为0.09%,NO体积分数为0.100%,K2Cr2O7摩尔浓度为10mmol/L,反应温度为40℃时,脱硫率、脱硝率分别达到100%和64.3%。     

微波协同霍加拉特剂催化氧化苯的影响因素

为了探索一种高效、快速处理典型挥发性有机物的方法,对微波协同作用下霍加拉特剂催化氧化苯的性能进行了研究,主要考查了微波作用模式、微波功率、苯初始浓度、气体流量、催化剂用量和气体湿度对处理苯效果的影响,并对影响规律进行总结。实验结果表明,微波功率70 W,苯初始浓度1 917 mg/m3,气体流量1.0 L/min,催化剂床层高度3.86 cm时,苯转化率可达99.2%。微波辐照条件下霍加拉特剂能够有效实现苯的催化氧化,并且比传统加热具有更高的能量利用率。     

介质阻挡放电氧化降解木质素磺酸钠的动力学研究

为了有效地处理难生物降解的造纸废水，采用气相介质阻挡放电产生氧化性物质，对木质素磺酸钠进行了氧化降解研究。在不同操作条件下，对其降解动力学及矿化程度进行了研究。结果表明，介质阻挡放电能有效地降解木质素磺酸钠，其氧化降解反应遵循准一级动力学反应。当峰值电压为20 kV，被水蒸气饱和的空气为气源，流量为7 L/min时，氧化处理60 min后，木质素磺酸钠降解率达到70％。其速率常数K随峰值电压、气源、气体流量和木质素磺酸钠的初始浓度的变化而不同。气体流量越大，木质素磺酸钠的初始浓度越低，速率常数K越大，降解效果越好。随着处理时间的增加，氧化性物质能将部分木质素磺酸钠矿化使溶液TOC降低，当被水蒸气饱和的空气作为气源时，氧化处理120min，21.38%的TOC被去除。     

Phototransformation of ibuprofen and ketoprofen in aqueous solutions

The UV (254 nm) and UV/VUV (254/185 nm) photolysis of two anti-inflammatory drugs, ibuprofen and ketoprofen, have been studied in aqueous solutions as a possible process for the removal of non-biodegradable compounds.We have examined the effects of dissolved oxygen and initial target concentration. Upon irradiation at 254 nm, the decomposition rate of ketoprofen is almost forty times higher as it of ibuprofen whilst VUV irradiation only increased the ibuprofen decomposition rate. The presence of dissolved oxygen accelerated the photodegradation of ibuprofen, whereas no effect was observed on the degradation of ketoprofen. The maximum quantum yield for the phototransformation was 0.2. The rate of mineralization in both cases was ∼60%, even after 1 h of treatment and this suggests the formation of stable by-products which were identified using GC-MS and HPLC-MS, respectively.     

生物过滤塔处理实验室废气

研究了生物过滤塔处理实验室排放的模拟混合废气,考察了反应器对苯、甲苯、二甲苯、乙醇、丙酮、乙酸乙酯和甲烷等废气的去除效果。运行结果表明,在设备稳定运行期间,进气中总挥发性有机物(TVOCs)的浓度为124～380 mg/m3,而出气浓度在10～40 mg/m3,去除效率保持在85%以上。实验室废气中的多种污染物在生物过滤塔中去除机理不同,亲水性污染物的去除效率高于疏水性污染物。通过系统关停后重启,污染物的去除效果在第2天就能恢复,这为生物过滤塔处理实验室废气过程的停运检修或者系统闲置提供了可行性。     

Degradation of trichloroethylene by photocatalysis in an internally circulating slurry bubble column reactor

The effects of initial trichloroethylene (TCE) concentration, recirculating liquid flow rate and gas velocity on photodegradation of TCE have been determined in an internally circulating slurry bubble column reactor (0.15m-ID x 0.85 m-high). Titanium dioxide (TiO2) powder was employed as a photocatalyst and the optimum loading of TiO2 in the present system is found to be approximately 0.2 wt%. The stripping fraction of TCE by air flow increases but photodegradation fraction of TCE decreases with increasing the initial TCE concentration, recirculating liquid flow rate and gas velocity. The average removal efficiency of TCE is found to be approximately 97% in an internally circulating slurry bubble column reactor.     

Study on particulates and volatile organic compounds removal with TiO2 nonwoven filter prepared by electrospinning

In this study, polyvinyl alcohol (PVA) and titania (TiO₂) Degussa P-25 were mixed to generate TiO₂ nonwoven filters using electrospinning. The wires of titanium dioxide and the nonwoven binding titania nanofibers were formed using 14 kV voltage and a distance of 15 cm. A single-factor experimental method was used to investigate the effects of parameters such as initial concentration, retention time, and light source on acetone removal by nonwoven binding titania nanofibers. Furthermore, the effects of parameters such as gas pressure, particle size, initial concentration, and retention time on the removal of particulates were also assessed. The results showed that the degradation efficiency increased with decreasing initial concentrations and increasing retention time. The best operational conditions during this study for the removal of acetone using the TiO₂ nonwoven filters were a retention time of 100 sec, initial acetone concentration of 250 ppm, and ultraviolet (UV) light source of 254 nm. Under those conditions, 99% acetone removal efficiency was obtained. In addition, 90% particulate matter removal efficiency was reached when the particulate size was greater than 200 nm and the reaction time was longer than 5 minutes. The prepared TiO₂/nanofiber has good performance for volatile organic compounds (VOCs) and particulate removal at the same time.

Implications: In this study, polyvinyl alcohol (PVA) and titania (TiO₂) Degussa P-25 were mixed to generate TiO₂ nonwoven filters using electrospinning. The results showed that the optimum operating conditions for the removal of acetone using the TiO₂ nonwoven filters were a retention time of 100 sec, initial acetone concentration of 250 ppm, and UV light source of 254 nm. Under those conditions, 99% acetone removal efficiency was obtained.     

聚合氯化铝与粉末活性炭联合强化混凝处理垃圾渗滤液

研究了联合粉末活性炭与聚合氯化铝(PAC)强化混凝对垃圾渗滤液原水的处理效果。结果表明,在原水COD为4 100 mg/L、浊度为147 NTU、UV254为20的条件下,粉末活性炭的加入可以有效增加垃圾渗滤液中有机物的去除率,PAC投加量为0.6 g/L时,投加0.6 g/L粉末活性炭,COD的去除率由21.6%提高到29.1%,UV254去除率由29.8%提高到39.9%,剩余浊度由138 NTU降到133 NTU。该强化混凝过程使原水中溶解性小分子有机物的去除率提高显著,PAC投加量为0.6 g/L时,投加0.6 g/L粉末活性炭,在分子量小于1 kDa的范围内,UV254去除率由2.9%上升为10%。     

Mathematical model for photocatalytic destruction of organic contaminants in air

Photocatalytic oxidation (PCO) was investigated in a bench-scale reactor for the abatement of two airborne organic contaminants: toluene and ethanol. A mathematical model that includes the impacts of light intensity, initial contaminant concentration, catalyst thickness, and relative humidity (RH) on the degradation of organic contaminants in a photocatalytic reactor was developed to describe this process. The commercially available catalyst Degussa-PtTiO2 was selected to compare with the MTU-PtTiO2-350 catalyst, which was synthesized by the sol-gel process, platinized, and calcined at 350 degrees C. For toluene removal using the MTU-PtTiO2-350 catalyst, the degradation rate increased with increases in light intensity from 0.2 to 2.2 mW/cm2 and in catalyst thickness from 0.00037 to 0.00361 cm. However, further increases in light intensity and catalyst thickness had only slight effect on the toluene degradation rate. Increasing the initial concentration from 6.29 to 127.9 microg/L and the RH from 10 to 85% resulted in decreases in the toluene degradation rate. For ethanol removal using the MTU-PtTiO2-350 catalyst, the degradation rate increased more rapidly with an increase in RH from 17 to 56%; the RH had little effect on the ethanol degradation rate while it further increased from 56% to 82%. We discuss applicability of the model to estimate the influence of process variables and to evaluate photocatalyst performance.     

Photolysis of low concentration H2S under UV/VUV irradiation emitted from microwave discharge electrodeless lamps

The photolysis of simulating low concentration of hydrogen sulfide malodorous gas was studied under UV irradiation emitted by self-made microwave discharge electrodeless lamps (i.e. microwave UV electrodeless mercury lamp (185/253.7 nm) and iodine lamp (178.3/180.1/183/184.4/187.6/206.2 nm)). Experiments results showed that the removal efficiency (eta H2S) of hydrogen sulfide was decreased with increasing initial H2S concentration and increased slightly with gas residence time; H2S removal efficiency was decreased dramatically with enlarged pipe diameter. Under the experimental conditions with pipe diameter of 36 mm, gas flow rate of 0.42 standard l s(-1), eta H2S was 52% with initial H2S concentration of 19.5 mg m(-3) by microwave mercury lamp, the absolute removal amount (ARA) was 4.30 microg s(-1), and energy yield (EY) was 77.3 mg kW h(-1); eta H2S was 56% with initial H2S concentration of 18.9 mg m(-3) by microwave iodine lamp, the ARA was 4.48 microg s(-1), and the EY was 80.5mg kW h(-1). The main photolysis product was confirmed to be SO4(2-) with IC.