Application of DBD and DBCD in SO_2 Removal

The dielectric barrier corona discharge(DBCD) in a wire-cylinder configuration and the dielectric barrier discharge(DBD) in a coaxial cylinder configuration are studied. The discharge current in DBD has a higher pulse amplitude than in DBCD. The dissipated power and the gas-gap voltage are calculated by analyzing the measured Lissajous figure. With the increasing applied voltage, the energy utilization factor for SO2 removal increases in DBCD but decreases in DBD because of the difference in their electric field distribution. Experiments of SO2 removal show that in the absence of NH3 the energy utilization factor can reach 31 g/kWh in DBCD and 39 g/kWh in DBD.

Influence of Cr^(3+) Concentration on SO_2 Removal over TiO_2 Based Multi-walled Carbon Nanotubes

In this study, titanium dioxide supported by multi-walled carbon nano tubes(MWCNTs/TiO_2) and Cr-doped TiO_2 supported by MWCNTs(MWNTs/Cr-TiO_2) were synthesized by the sol-gel method. The prepared samples were characterized by transmission electron microscopy, X-ray photoelectron spectroscopy, X-ray diffraction, the BrunauerEmmett-Teller analysis, and the Raman spectroscopy. The oxidation and efficiency for removal of SO_2 in a simulated flue gas were investigated experimentally in a fixed-bed reactor. The 15% MWCNTs/Cr-Ti02 sample displayed excellent adsorption properties, and a SO_2 removal rate equating to 30.415 1 mg/g from the simulated flue gas containing 2 300 μg/g of SO_2, 8% of 02, and 5% of H20 was achieved under optimal conditions covering a temperature of 333.15 K, and a space velocity of 1 275 h^(-1). The adsorption process was enhanced because Cr doping modified the pore structure and inhibited the grain growth of TiO_2. In addition, the Freundlich and Langmuir models revealed that SO_2 was mainly adsorbed through chemical adsorption on the sample surfaces, and the thermodynamic model analysis indicated that the adsorption was a spontaneous, exothermic, and entropy-reducing process. The adsorption kinetics of SO_2 can be described by the pseudosecond-order kinetic and the Bangham dynamics models. The possible reaction mechanism involved in desulfurization process was also proposed.

Study on SO_2 Removal Efficiency by Nanosecond Rising Edge Pulse DBD Under Different Environmental Conditions

In this paper, an experimental study on SO2 removal by nanosecond rising edge pulse dielectric barrier discharge （DBD） plasma, generated by multi-needle-to-plane electrodes, is carried out. The mechanism of the effect of various factors, such as gap size between dielectric barrier and discharge needles, environmental humidity, and inlet speed of gas flow upon the removal efficiency of air purification is analyzed. The studies show that SOs removal efficiency improves with the increase in the gap size between dielectric barrier and discharge needles in the case of a fixed space between two electrodes, and also improves with the increase in the environmental humidity. For a mixed gas with a fixed concentration, there is an optimal inlet speed of gas flow, which leads to the best removal efficiency.

Experimental Study of SO_2 Removal by Pulsed DBD Along with the Application of Magnetic Field

Dielectric barrier discharge （DBD） for SOs removal from indoor air is investigated. In order to improve the removal efficiency, two novel methods are combined in this paper, namely by applying a pulsed driving voltage with nanosecond rising time and applying a magnetic field. For SOs removal efficiency, different matches of electric field and magnetic field are discussed. And nanosecond rising edge pulsed power supply and microsecond rising edge pulsed power supply are compared. It can be concluded that a pulsed DBD with nanosecond rising edge should be adopted, and electrical field and magnetic field should be applied in an appropriate match.

Removal of SO_2 and NO_x by Pulsed Corona Combined with in situ Ca(OH)2 Absorption

Removal of SO2 and NOx by pulsed corona combined with in situ alkali absorption was experimentally investigated.In the reactor,a plate-wire-plate combination is devised for generating pulsed corona and then alkaline absorbent slurries were introduced into the reactor by a continuous band conveying system to capture the gaseous reaction products.It was found that both SO2 and NO could be removed by corona combined with in situ alkali absorption.The removal of SO2 increased to 75%with the corona discharge,compared with 60%removal only with Ca(OH)2 absorption.About 40%removal of NO was reached by pulsed corona combined with in situ Ca(OH)2 absorption.It was found that SO2 and NO in the gas stream are oxidized to SO3 and NO2 by pulsed corona respectively,and then absorbed by the alkali in the reactor.The removals of SO2 as well as NO were higher with Ca(OH)2 as the absorbent,compared with using CaCO3 or ZnO.

Simultaneous removal of NO and SO_2 from dry gas stream using non-thermal plasma

In order to investigate the feasibility of sequential removal NO and SO2 using non-thermal plasma and adsorbent simultaneously, the removal of NO and SO2 from dry gas stream （NO/SO2/N2/O2） with very little O2 using non-thermal plasma was investigated using a coaxial dielectric barrier discharge. Comparative experiments were carried out in the dry gas stream with and without Ar respectively at O2 concentration of 0.1%. The results showed that NO could be removed remarkably and it would be enhanced in the presence of Ar in the dry gas stream. It seems that SO2 could not be removed unless there is Ar in the dry gas stream. The mechanism of removal of NO and SO2 in the dry gas stream was discussed.

SO_2/Hg removal from flue gas by dry FGD

To study the mechanism of SO2 and Hg removal from flue gas, an experimental packed bed reactor was designed to simulate the dry FGD, where a mixture of lime and fly ash in ratio 1：3 w/w was used as the S02 and Hg sorbent, and steam at temperature of 100 ℃ was applied for activation of the sorbent, while the activation time set to 20 rain. The experimental factors including the SO2/Hg sorbent characteristics, 50% breakthrough time for SO2/Hg removal, sorbent packed bed depth and reaction temperature were investigated. The experimental results show that after steam activation, the BET specific surface area and specific pore volume increased from 37.8 to 45.5 m^2/g and from 0.42 to 0.51 cm^3/g, respectively. With activation of the sorbent by steam, the 50% breakthrough times of SO2 and Hg removal increased from 34 to 42 rain and from 23 to 45 rain, respectively. When the packed bed depth was increased from 5 to 25 ram. the 50% breakthrough times for Hg and S02 removal increased from 12 to 52 rain and from 6 to 47 rain, respectively. With the increase of the reaction temperature, the 50% breakthrough of SO2/Hg removal decreased accordingly. Steam activation can efficiently improve SO2/Hg removal simultaneously.

Study on the Removal of SO_2 from Simulated Flue Gas Using Dry Calcium-Spray with DBD Plasma

In this study, lime-hydrate （Ca（OH）2） desulfurizer was treated by plasma with strong ionization discharge of a dielectric barrier. The removal of SO2 from simulated flue gas was investigated. The principles of SO2 removal are discussed. Several factors affecting the efficiency of SO2 removal were studied. They included the ratio of calcium to sulfur （Ca/S）, desulfurizer granularity, residence time of the flue gas, voltage applied to the discharge electrode in the plasma generator, and energy consumption. Experimental results indicate that the increase in Ca/S ratio, the applied voltage and discharge power, the residence time, and the reduction in the desulfurizer granularity all can raise the SO2 removal efficiency. The SO2 removal efficiency was up to 91.3% under the following conditions, namely a primary concentration of SO2 of 2262×10^-6 （v/v） in the emission gas, 21%（v/v） of oxygen, 1.8% （v/v） of water, a Ca/S ratio of 1.48, a residence time of 2.8 s, a 3.4 kV voltage and a 10kHz frequency power applied to the discharge electrodes in the plasma generator, and a flow rate of 100 m^3/h for emission gas.

Hierarchical Reduced Graphene Oxide-MnO_(2)@Polypyrrole Coaxial Nanotube Composite Hydrogel as a Potential Adsorbent for Cr(Ⅵ)Removal

A hierarchical reduced graphene oxide-MnO_(2)@polypyrrole coaxial nanotube composite hydrogel was prepared via oxidative polymerization of pyrrole in the presence of MnO_(2)nanotubes,followed by the hydrothermal treatment of graphene oxide and MnO_(2)@polypyrrole coaxial nanotubes.The stable composite hydrogel with a hierarchical network was composed of one-dimensional MnO_(2)@polypyrrole coaxial nanotube and two-dimensional graphene nanosheet and characterized by scanning electron microscope,Fourier transform infrared spectroscopy,X-ray diffraction,Brunauer-Emmett-Teller surface,and X-ray photoelectron spectroscopy measurements.The composite hydrogel can be used as an efficient adsorbent for Cr(Ⅵ)removal due to the synergistic interaction between graphene and MnO_(2)@polypyrrole and the hierarchical structure of the hydrogel.Moreover,the composite hydrogel is easily separated because of its stable monolith,and it is reusable(76.8%of removal ability remaining after five adsorption-desorption cycles).The simple fabrication and cost-effective separation process together with the excellent absorption performance endow the composite hydrogel with great potential for practical wastewater treatment.

Efficient removal of Al(Ⅲ)and P507 from high concentration MgCl_(2)solution based on in-situ reaction strategy

For a highly efficient recycling of a wastewater containing a high concentration of MgCl_(2),Al(Ⅲ)and P507 were scheduled to be removed in advance.In this study,the in-situ removal of Al(Ⅲ)and P507 from a high concentration MgCl_(2)solution at different pH values and Al/P molar ratios was investigated.The results showed that P507 formed organic complexes of Al_(x)(OH)_y^(Z+)-P507 at pH of 2.0-4.0.At pH of 4.0-5.0,Al(Ⅲ)precipitated and transferred into Al(OH)_(3)with a flocculent amorphous morphology.Active sites on the Al(OH)_(3)surface enhanced the removal efficiency of P507.At pH of 6.0-6.5,Al(Ⅲ)and Mg(Ⅱ)formed layered crystalline Al(OH)_(3)and MgAl_(2)(OH)_(8with)small pore channels and fewer active sites,resulting in a reduced removal efficiency of P507.When the Al/P molar ratio exceeded 13 and the pH was between 4.0 and 5.0,the removal rates of both Al(Ⅲ)and P507 were higher than98%,while the concentration loss of Mg(Ⅱ)was only 0.2%-0.9%.

TiO2-PES Fibrous Composite Material for Ammonia Removal Using UV-A Photocatalyst

This study focused on the development and characterization of TiO2-PES composite fibers with varying TiO2 loading amounts using a phase inversion process. The resulting composite fibers exhibited a sponge-like structure with embedded TiO2 nanoparticles within a polymer matrix. Their photocatalytic performance for ammonia removal from aqueous solutions under UV-A light exposure was thoroughly investigated. The findings revealed that PeTi8 composite fibers displayed superior adsorption capacity compared to other samples. Moreover, the study explored the impact of pH, light intensity, and catalyst dosage on the photocatalytic degradation of ammonia. Adsorption equilibrium isotherms closely followed the Langmuir model, with the results indicating a correlation between qm values of 2.49 mg/g and the porous structure of the adsorbents. The research underscored the efficacy of TiO2 composite fibers in the photocatalytic removal of aqueous under UV-A light. Notably, increasing the distance between the photocatalyst and the light source resulted in de-creased hydroxyl radical concentration, influencing photocatalytic efficiency. These findings contribute to our understanding of TiO2 composite fibers as promising photocatalysts for ammonia removal in water treatment applications.

中空纤维膜吸收法脱除SO_2的实验研究

利用聚丙烯中空纤维膜组件为吸收器 ,以SO2 /空气混合气—清水、SO2 /空气混合气—NaOH溶液 ( 0 .1mol/L ,0 .5mol/L)为实验体系 ,研究了吸收液浓度、气液两相流速和气液两相流程等操作条件对吸收率的影响 ;以传质单元高度 (HTU)为指标 ,与 3种常用填料吸收塔进行了比较 ;研究结果表明 :中空纤维膜吸收技术用于工业SO2

电气设备中保护气体监测用SO_2F_2气体标准物质研制

介绍了钢瓶装氦气中氟化硫酰（SO_2F_2）气体标准物质的研制过程。标准混合气是通过将SO_2F_2和氦气充装到钢瓶中制备而成，研究了气瓶内压力和保存时间对混合气稳定性的影响。对混合气配制的一致性进行了考察，并对引入的不确定度进行了评估，由结果可以看出，每个摩尔分数点混合气的量值一致性均较好。通过对称量法配气与稳定性导致的不确定度的评价，结果显示利用称量法制备的氦气中SO_2F_2气体标准物质在6个月内的稳定性良好，其相对扩展不确定度不大于2％。

冰温结合SO_2两段释放对‘玫瑰香’葡萄贮藏品质的影响

研究了冰温结合SO_2两段释放对‘玫瑰香’葡萄贮后品质及贮藏效果的影响。试验结果表明,与对照相比,冰温(-1.0、-1.5℃)结合SO_2两段释放避免了果梗褐枯和果粒漂白问题,腐烂减轻,贮藏120 d腐烂率分别为1.5%、0.9%,果粒SO_2残留不超过3.2 mg/kg,糖、酸含量接近于葡萄采收值。与-1.0℃相比,-1.5℃贮藏葡萄穗梗冷害率30%,表现为穗梗鲜绿色转暗并呈现水渍状,而前者未发生冷害,因此,-1.0℃结合SO_2两段释放处理更适合‘玫瑰香’葡萄低硫贮藏。

天然气净化厂尾气SO_2排放治理工艺探讨

随着国家新《环境保护法》的实施,越来越严格的尾气排放标准给天然气净化厂硫磺回收及尾气处理装置带来巨大的减排压力和技术升级的严峻挑战。为此,分析了国内外天然气净化厂尾气排放标准改进及国内尾气排放现状,对可用于现有装置升级改造的5种尾气处理工艺(还原吸收法、胺法SO_2吸收法、湿法制酸法、石灰石/石膏湿法和循环流化床干法)、液相氧化还原法和生物脱硫法进行了技术评价分析,并针对2种不同处理规模(原料气潜硫量大于等于1 t/d及原料气潜硫量小于1 t/d)进行了技术经济对比分析。结果表明:①现有天然气净化厂硫磺回收装置排放尾气具有SO_2排放浓度较高、总量小的特点,宜采用还原吸收法、胺法SO_2吸收法和循环流化床法用于尾气治理或采用液相氧化还原法直接处理;②对原料气中潜硫量较大的,尾气处理宜选用还原吸收类工艺,反之则宜采用液相氧化还原法直接处理;③对尾气中潜硫量为中等的,宜选用胺法SO_2吸收工艺,潜硫量较小的则宜选用循环流化床干法工艺。

SO_2在球状活性炭上的吸附转化研究

研究了不同比表面积的沥青基球状活性炭（ＰＳＡＣ）在Ｏ２和Ｈ２Ｏ存在下脱除ＳＯ２的能力．结果表明，比表面积较大的ＰＳＡＣ具有较强的脱除ＳＯ２能力．在本实验条件下，三种不同比表面积的ＰＳＡＣ对ＳＯ２及ＳＯ２＋Ｏ２的吸附量无明显区别，但对Ｈ２Ｏ的吸附量随比表面积增大而增大，与样品的脱硫活性随比表面积增大的变化规律相一致，表明较多的水有利于ＳＯ２的脱除．这可归因于水既有利于样品活性部位上的ＳＯｘ转化成Ｈ２ＳＯ４，又能洗脱所生成的Ｈ２ＳＯ４，减少活性位上的Ｈ２ＳＯ４量。

Salt-assisted Synthesis of Hollow Bi_2WO_6 Microspheres with Superior Photocatalytic Activity for NO Removal

Hollow Bi2WO6 microspheres are successfully synthesized by a facile ultrasonic spray pyrolysis（USP） method using NaCl as a salt template.The as-prepared hollow microspheres assembled as nanoplates with dimensions of approximately 41-148 nm and are dispersed with non-uniform pores on the template surface.By swapping the salt template with KC1 or Na2SO4,different morphologies of Bi2WO6 are obtained.The experimental results demonstrate that NaCl plays a key role on the formation of Bi2WO6 with hollow structures.The specific growth mechanism of hollow microspheres was studied in detail.The Bi2WO6 hollow microspheres exhibit an excellent photocatalytic efficiency for NO removal under solar light irradiation,which is 1.73 times higher than for the Bi2WO6 obtained in the absence of any salt template.This enhancement can be ascribed to the simultaneous improvement on the surface area and visible light-harvesting ability from the hollow structures.Electron spin resonance（ESR） results suggest that both radicals of ·OH and ·O2^- are involved in the photocatalytic process over the BWO-NaCl sample.The production of ·O2^- radicals offers better durability for NO removal.

氨与脉冲电晕等离子体脱除SO_2的协同效应

为了揭示氨与等离子体脱除ＳＯ２的协同效应，对比了脉冲电晕等离子体在氨气注入前后ＳＯ２脱除率的变化。实验结果表明，脉冲电晕等离子体单独作用时，ＳＯ２脱除率仅为９％～１５％，而氨与脉冲电晕等离子体共同作用时，ＳＯ２脱除率可达９０％以上（ｆ＝１．０）．并从化学热力学角度探讨了氨与脉冲电晕的协同效应能显著提高ＳＯ２脱除率的原因，还考察了氧含量。

煤粉等温燃烧挥发分、焦炭分阶段SO_2释放规律研究

利用自制SO_2测量系统,对煤粉及煤焦进行了等温燃烧实验,针对挥发分与焦炭分阶段SO_2释放规律研究了温度、煤质、氧浓度对SO_2释放的影响。结果表明:煤粉等温燃烧过程中,经历了挥发分SO_2的快速释放和焦炭SO_2的缓慢释放,挥发分SO_2和焦炭SO_2的释放存在一定的重叠时间。随着温度升高,焦炭SO_2转化率显著增大,挥发分SO_2转化率变化不大。不同煤种SO_2转化率差异明显,低阶煤挥发分S0_2的转化率较低,塔山煤和印尼煤的焦炭SO_2转化率显著低于阳泉煤。随着氧浓度升高,挥发分和焦炭SO_2释放速率加快,挥发分SO_2和焦炭SO_2转化率均升高,挥发分SO_2的释放对氧浓度的变化更为敏感。

SO_2在含氮沥青基活性炭纤维上的脱除 Ⅰ含氮沥青基活性炭纤维的脱硫能力研究

由水和氨混合物活化制得的不同比表面积及氮含量的含氮沥青基活性炭纤维［ＰＡＣＦ（ＮＨ３）］在Ｏ２和Ｈ２Ｏ存在下脱除ＳＯ２的能力进行了研究。ＸＰＳ结果表明，ＰＡＣＦ（ＮＨ３）表面的含氮官能团主要为类吡咯氮、类吡啶氮及铵盐，它们的主要作用是增强对水的吸附。当比表面积相近，氮含量增加时或者氮含量相近，比表面积增大时，均导致ＰＡＣＦ（ＮＨ３）的脱硫能力增强，这与ＰＡＣＦ（ＮＨ３）对水的吸附量增加有关。