TiO2光催化氧化脱除模拟烟气中的NOx

采用P25纳米TiO2为催化剂,对NOx浓度360 mg/m3的模拟烟气进行了光催化氧化实验研究,以期为此种方法在电厂烟气脱硝方面的应用提供依据。经SEM、XRD等表征手段,探讨了催化剂晶型尺寸对光催化的作用。实验考察了光催化反应过程规律以及负载量、光照度、NO初始浓度、O2含量、相对湿度和停留时间对光催化氧化效率的影响。结果表明,光催化反应是瞬态到稳态的过程,其催化效率与上述影响因子有密切关系。实验最优条件下NOx的脱除率为46%,但只需适当提高氧化效能,便能达到理想的效果。     

Removal of SO2 from flue gas using blast furnace dust as an adsorbent

Environmental Science and Pollution Research - To control the SO2 emission and achieve the target of “waste controlled by waste”, a novel desulfurization method with blast furnace dust...     

等离子体协同光催化去除模拟烟气中SO2的实验研究

近年来,低温等离子体技术以及纳米TiO2光催化技术在烟气脱硫中的应用越来越引起人们的关注。利用填充床反应器将这2种技术有机地结合起来,进行了大量脱硫实验研究。研究结果表明,等离子体协同光催化去除烟气中的SO2与单独采用等离子体技术相比,其SO2的去除率可提高5%～20%。同时,探讨了等离子体协同TiO2光催化剂的脱硫机理,分别研究了外加电压、气体流量和SO2初始浓度等因素对脱硫效率的影响。实验结果表明,当SO2初始浓度为800 mg/m3,输入电压为17.5 kV,气体流量为0.2 m3/h时,SO2脱除率可以达到77.6%。     

强电离放电模拟烟气脱硫实验

应用强电离放电方法进行烟气脱硫 ,将烟气中大部分O2 、N2 和H2 O等气体分子电离后加工成OH等活性粒子 ,在高温、不加吸收剂的条件下 ,直接将SO2 氧化成H2 SO4。实验中分别研究了烟气在反应室内的停留时间、烟气中含水量和含氧量等因素对脱硫率的影响。实验结果表明 ,烟气在反应室内停留时间为 0 74s ,烟气中含水量和含氧量分别为2 8%和 2 0 8%时 ,SO2 脱除率可达到 10 0 %。     

脉冲放电烟气脱硫脱硝技术研究进展

综述了脉冲放电等离子体烟气脱硫脱硝技术的发展历史、研究现状、进展及其存在的问题.     

脉冲放电烟气脱硫脱硝技术研究进展

综述了脉冲放电等离子体烟气脱硫脱硝技术的发展历史、研究现状、进展及其存在的问题。     

超重力脱除模拟烟气中一氧化氮

以NO和N2的混合气作模拟烟气,以酸性尿素溶液为吸收剂,在超重力机中进行了脱除模拟烟气中NO实验研究。实验考察了混合气中NO初始含量、进气流量、吸收液流量、超重力机转速对NO脱除率的影响,确定了在超重力中尿素吸收NO的适宜条件。实验结果表明,在常温常压下,N2体积流量为1.0 m3/h,控制NO初始浓度为3 300 mg/m3,吸收液流量为250 L/h,超重力机转速为650 r/min时,NO脱除率可达89.5%。     

超重力脱除模拟烟气中一氧化氮简

以NO和N₂的混合气作模拟烟气,以酸性尿素溶液为吸收剂,在超重力机中进行了脱除模拟烟气中NO实验研究。实验考察了混合气中NO初始含量、进气流量、吸收液流量、超重力机转速对NO脱除率的影响,确定了在超重力中尿素吸收NO的适宜条件。实验结果表明,在常温常压下,N₂体积流量为1.0 m³/h,控制NO初始浓度为3 300 mg/m³,吸收液流量为250 L/h,超重力机转速为650 r/min时,NO脱除率可达89.5%。     

采用可再生胺法脱除烟气中SO2

为加快可再生胺法脱硫工艺的工业化进程,开发了一套撬装式脱硫再生中试装置,通过SO2连续吸收解吸实验验证装置性能。分别考察吸收剂质量分数、pH、液气比（L/G）、解吸温度、SO2进口含量对吸收和解吸效率的影响,结果表明：随吸收剂质量分数、pH、液气比的增大吸收率升高,而解吸率下降;解吸温度升高,吸收率变化不大,解吸率增速较快;SO2进口浓度增大,吸收率和解吸率迅速降低。确定适宜工艺条件为：吸收剂质量分数30%,pH=6~8,吸收温度30℃,解吸温度（90±5）℃,液气比L/G=5.0 L·m-3。通过微分法导出体积总传质系数KGa的计算公式,并与相关工艺参数进行关联拟合,回归出填料吸收塔KGa经验模型：KGa=0.081（L/G）0.232 0（8.91 w0.107 3pH0.248e-0.32yA-1）。     

改性半焦脱除烟气中SO2的研究

对内蒙工业副产褐煤半焦（比表面积49.187m^2／g,孔容0.0351cm^2／g）,采用加压水热化学活化法,HNO3活化法和高温煅烧相结合的方法制备出半焦烟气脱硫剂,并对脱硫剂的脱硫性能进行固定床活性评价。分析表明,其脱硫效果比较好,转化率维持在50％以上的累计硫容可达24．30％,脱硫时间长达35h,远远高于原料半焦的脱硫效果（硫容为0．68％,时间为1．5h）;同时采用水洗法对脱硫剂进行再生,其再生液可用来制备浓度为9.01％的稀硫酸。     

Removal of PCDD/F from incinerator flue gases by entrained-phase adsorption

The emission abatement of polychlorinated dioxins and furans (PCDD/F) Issued from municipal solid waste incineration is growing in importance because of more stringent emission standards and general concern about their toxic characteristics. These substances cannot be separated by conventional gas cleanup processes but are successfully removed through adsorption onto carbonaceous materials. The simplest technique is the entrained-phase injection of pulverized adsorbents in the flue gas, followed by fabric filter separation. The various related techniques are briefly reviewed here. Operating conditions and results obtained from Flemish MSWIs are given. The results illustrate the excellent overall removal efficiency. Furans are adsorbed to a slightly higher extent than dioxins. PCDD/F removal by carbonaceous adsorbents is thereafter modeled from first principles for the contribution of both entrained-phase (eta1) and cake filtration (eta2) to the overall efficiency (etaT). Application of the model equations and comparison of measured and predicted overall efficiencies for the Flemish municipal solid waste incinerators (MSWIs) demonstrate that the approach is meaningful and that the dominant parameters are the operating temperature, the dosage and activity of adsorbent, and the fraction of adsorbent in the filter cake. The model equations enable the MSWI operators to predict the adsorption efficiencies for any combination of operating parameters and to assess the sensitivity of the process to varying operating conditions.     

烟道式脱硫装置处理冶炼厂高浓度SO2烟气的工程实践

本文介绍了烟道式脱硫装置的特点及工艺原理 ,采用该装置处理某冶炼厂高浓度SO2 烟气 ,其脱硫率达 90 %以上 ,净化后的烟气可直接达标排放 ,并年产合格脱硫石膏近万吨。烟道式脱硫装置解决了常规脱硫除尘装置共同存在的结垢和堵塞问题 ,在冶炼烟气治理方面具有一定的推广应用价值。     

NaClO2/尿素复合吸收剂湿法脱除烟气中的SO2和NO

在自行设计的喷淋塔中对NaClO2/尿素复合吸收剂脱除烟气中的SO2和NO进行了实验研究,实验分析了NaClO2/尿素复合吸收剂脱除SO2和NO机理。结果表明：SO2被吸收液吸收的过程分为2个部分,一部分SO2溶于水被NaClO2氧化为SO42-,另一部分SO2溶于水与尿素和氧气反应生成（NH4）2SO4;难溶于水的NO被NaClO2主要氧化为NO3-,进而被尿素吸收,NO被还原为环境友好气体N2。此外,实验主要探索了NaClO2浓度、尿素浓度、NO进口浓度、SO2进口浓度、初始pH值、温度对脱除NO的影响,优化选择最佳工艺条件,NaClO2浓度为4 mmol·L-1,尿素浓度为0.5 mol·L-1,吸收液初始pH值为7.0,温度为50℃时,平均SO2和NO脱除率分别为100%和95.2%。     

Removal of SO2 from smelting flue gas by using copper tailings with MnSO4: factors optimization by response surface methodology

Environmental Science and Pollution Research - The abatement of SO2 and the utilization of copper tailings are identified as two attention-attracting environmental issues in the copper smelter. In...     

Removal of alpha-pinene from gases using biofilters containing fungi

Biofiltration is cost-effective for the treatment of gases containing low concentrations of volatile organic compounds $\text{(<3}\text{g}\text{m}{}^{\mathrm{-3}}\text{)}$. However, conventional biofilters, based on compost and bacterial activity, face problems with the elimination of hydrophobic compounds. Besides that, biofilter operational stability is often hampered by acidification and drying out of the filter bed. To overcome these problems, biofilters with fungi on inert packing material have been developed. Fungi are more resistant to acid and dry conditions than bacteria, and it is hypothesised that the aerial mycelia of fungi, which are in direct contact with the gas, can take up hydrophobic compounds faster than flat aqueous bacterial biofilm surfaces. Alpha-pinene was chosen as a model compound. It is an odorous compound emitted by the wood processing industry. In $\text{2}\text{l}$ biofilter columns four different packing materials were tested: perlite, expanded clay granules, polyurethane foam cubes and compost. The filters were inoculated with forest soil and ventilated with gas containing alpha-pinene. Start up took 1–2 months and removal efficiencies of more than 90% were observed, but mostly ranged from 50% to 90% due to overloading. In the filters containing perlite, clay, polyurethane and compost volumetric removal capacities of, respectively, 24, 33, 38 and $\text{24}\text{g}$ alpha-$\text{pinene}\text{m}{}^{\mathrm{-3}}$ filter $\text{bed}\text{h}{}^{\mathrm{-1}}$ were attained and the gas pressure drops in the $\text{60}\text{cm}$ high filter beds measured at a superficial gas velocity of $\text{35}\text{m}\text{h}{}^{\mathrm{-1}}$ were 70, 550, 180 and $\text{250}\text{Pa}$. The results indicate that it is possible to develop biofilters based on the action of fungi with higher elimination capacities for alpha-pinene as reported in literature for bacterial biofilters. The use of polyurethane foam cubes is preferred because of the low gas pressure drop in combination with a high volumetric elimination capacity.     

应用冷等离子体净化尾气中NO的研究

本文设计了轻便的电晕放电装置 ,并用其进行了冷等离子体去除NO的实验研究 ,得到了NO的去除率随放电管的输入功率、NO的初始浓度以及气体的流量而变化的对比曲线。在流量较小 (≤ 0 .0 5m3 /h)或者浓度较低 (≤ 15 0×10 -6)的情况下 ,本文所设计的装置去除NO的效果较好 (>80 % )。该装置体积小、重量轻、功耗低 ,加以改进 ,对于实际的汽车尾气排放控制 ,具有良好的应用前景     

Surface compositions of carbon sorbents exposed to simulated low-rank coal flue gases

Bench-scale testing of elemental mercury (Hg0) sorption on selected activated carbon sorbents was conducted to develop a better understanding of the interaction among the sorbent, flue gas constituents, and Hg0. The results of the fixed-bed testing under simulated lignite combustion flue gas composition for activated carbons showed some initial breakthrough followed by increased mercury (Hg) capture for up to approximately 4.8 hr. After breakthrough, the Hg in the effluent stream was primarily in an oxidized form (>90%). Aliquots of selected activated carbons were exposed to simulated flue gas containing Hg0 vapor for varying time intervals to explore surface chemistry changes as the initial breakthrough, Hg capture, and oxidation occurred. The samples were analyzed by X-ray photoelectron spectroscopy to determine changes in the abundance and forms of sulfur, chlorine, oxygen, and nitrogen moieties as a result of interactions of flue gas components on the activated carbon surface during the sorption process. The data are best explained by a competition between the bound hydrogen chloride (HCl) and increasing sulfur [S(VI)] for a basic carbon binding site. Because loss of HCl is also coincident with Hg breakthrough or loss of the divalent Hg ion (Hg2+), the competition of Hg2+ with S(VI) on the basic carbon site is also implied. Thus, the role of the acid gases in Hg capture and release can be explained.     

Removal of SO2 from O2-containing flue gas by activated carbon fiber (ACF) impregnated with NH3

Adsorption of SO(2) from the O(2)-containing flue gas by granular activated carbons (GACs) and activated carbon fibers (ACFs) impregnated with NH(3) was studied in this technical note. Experimental results showed that the ACFs were high-quality adsorbents due to their unique textural properties. In the presence of moisture, the desulphurization efficiency for the ACFs was improved significantly due to the formation of sulfuric acid. After NH(3) impregnation of ACF samples, nitrogen-containing functional groups (pyridyl C(5)H(4)N- and pyrrolyl C(4)H(4)N-) were detected on the sample surface by using an X-ray photoelectron spectrometer. These functional groups accounted for the enhanced SO(2) adsorption via chemisorption and/or catalytic oxidization.     

Removal mechanism of elemental mercury by using non-thermal plasma

The removal mechanism of elementary mercury (Hg(0)) by non-thermal plasma (NTP) has been investigated, where dielectric barrier discharge and O(3) injection methods as oxidation techniques are employed, together with the analysis of mercury species deposited on the reactor surface using temperature-programmed desorption and dissociation (TPDD) and scanning electron microscopy-energy dispersive spectroscopy. The removal of Hg(0) by NTP is found to be time-dependent and proceed through three domains; the Hg(0) concentration just slightly decreases as soon as NTP is initiated and then becomes constant for several minutes (Region 1), thereafter starts to decrease rapidly for 1h (Region 2) and, after passing fall-off region, very slowly decreases for about 4h (Region 3). The deposited mercury species on the reactor surface were conglomerated like islands, rather than dispersed uniformly, and their ratio of Hg(0) to O composition is observed to be 1:2. Additionally, the new peak in TPDD spectra observed in the region of 260-380°C is proposed as HgO(3). These results lead us to conclude that the deposited mercury species by NTP have extra O atoms to oxidize the adsorbed Hg(0), resulting in the acceleration of removal rate as the oxidation of Hg(0) proceeds.     

还原法二氧化硫脱除技术

介绍了催化还原法、CaS还原法、吸收还原法、碳还原法和生物还原法脱除烟气中二氧化硫技术的原理、特点以及研究和应用现状 ,指出了各种还原法脱除二氧化硫技术在工业应用中的限制因素和研究的方向。