螺旋状中空纤维膜吸收器脱硫性能的研究

用自组装的膜吸收器试验研究了不同操作条件下的烟气脱硫特性。实验结果表明，脱硫过程传质阻力主要集中在气相和膜上，利用螺旋管技术可以强化气相的传质。     

基于气液悬浮旋切掺混的气动旋流塔脱硫性能测试与分析

为了研制低运行能耗和高脱硫效率的新型脱硫塔,以满足国家最新环保超低排放标准,采用基于气液悬浮旋切掺混的气动旋流塔脱除燃煤烟气中的SO_2污染物,对其内部气动旋流单元的强化传质脱硫性能进行探究,考察了空塔喷淋段和气动旋流段的喷淋层位置和液气比对脱硫效率及系统阻力的影响,并对气动旋流单元的脱硫效率进行了理论计算模拟。结果表明:喷淋层距浆液池高度越高,液滴在吸收区停留的时间越长,脱硫效率越高,系统运行阻力也越大;增加液气比,可显著提高系统的脱硫效率,单层喷淋层阻力约为150 Pa;在低pH工况下,SO_2吸收过程为液膜控制,气动旋流单元的脱硫效率较低;随着pH的增大,SO_2吸收过程逐渐由液膜控制转变为双膜甚至气膜控制,气动旋流单元的脱硫效率逐渐增强;当pH=5时,液气比=25 L·m~(-3),5层喷淋层运行工况下的脱硫效率高达99.82%。气动旋流单元的脱硫效率模拟计算结果表明:在高pH下,气动旋流单元的脱硫效率更高;当pH=5.5时,气动脱硫单元的脱硫效率为62.56%,阻力为360 Pa,实验数据与理论计算曲线吻合较好。以上研究结果可为新型高效燃煤机组脱硫超低排放改造技术的开发及其在环境污染控制领域的应用提供参考。     

旋流塔板叶片仰角对湿钙法烟气脱硫过程的影响

实验研究了旋流塔板叶片仰角对钙基湿法烟气脱硫工艺的影响。结果表明 ,一般情况下 ,叶片仰角增大 ,脱硫率有所下降 ,塔的运行稳定性有所下降 ,结垢有所增加。因此 ,在将麻石水膜除尘器改造成旋流板塔脱硫除尘系统的过程中 ,增大叶片仰角的同时一定要考虑脱硫率的下降问题。     

氧化镁FGD脱硫过程的建模及其应用

氧化镁烟气脱硫是以氧化镁为脱硫反应剂的一种湿法烟气脱硫技术,目前国内外应用甚少,但开发前景广阔。以实验室小试为基础,从气液传质入手,利用双膜理论建立脱硫过程的数学模型,从而对中试脱硫效率进行预测并进行参数敏感性分析。结果表明,模型预测的脱硫效率与实际脱硫效率有很高的吻合度,其计算参数能反映出实际运行参数对脱硫效率的影响,对实际工况中操作条件的变更以及运行参数的调试有很高的指导意义。     

循环流化床烟气脱硫塔入口结构改进的数值模拟

采用商用Fluent软件提供的k-ε湍流模型对循环流化床脱硫塔内部流场进行了数值模拟,重点考察入口结构对脱硫塔内气相速度分布均匀性的影响,并用速度不均匀度定量描述了流场的均匀性。结果表明,当前使用90°弯管进气结构的脱硫塔内部流场存在明显的不均匀性,主要是入口处气流90°转向造成的。为此采用组合弯管进气结构代替90°弯管进气结构,以改善脱硫塔内流场不均匀性。入口结构改为组合弯管进气结构后,脱硫塔内流场不均匀性得到很大改善,速度分布的不均匀度明显减小,因此组合弯管进气结构有利于烟气与脱硫剂的充分混合反应,提高脱硫效率。     

一株脱硫菌的分离及脱硫动力学

从污水处理厂二沉池分离获得一株硫酸盐还原菌厌氧菌株,依据生理生化分析和16S rDNA基因序列测定该菌株被鉴定为脱硫脱硫弧菌(Desulfovibrio desulfuricans)。在气体吸收的双膜理论和液相中微生物转化的米门方程基础上,建立了搅拌式生物吸收反应器中脱硫脱硫弧菌净化二氧化硫气体的动力学模型,并求解出相应的动力学参数基质转化最大速度Vmax和米氏常数Km,实验结果所得到的线性方程相关性较好,线性相关系数可以达到0.998,而且脱硫脱硫弧菌吸收液具有较高转化二氧化硫的能力。     

旋流塔板叶片仰角对湿钙法烟气脱硫过程的影响

实验研究了旋流塔板叶片仰角对钙基湿法烟气脱硫工艺的影响。结果表明，一般情况下，叶片仰角增大，脱硫率有所下降，塔的运行稳定性有所下降，结垢有所增加。因此，在将麻石水膜除尘器改造成旋流板塔脱硫除尘系统的过程中，增大叶片仰角的同时一定要考虑脱硫率的下降问题。     

氧化镁FGD脱硫过程的建模及其应用

氧化镁烟气脱硫是以氧化镁为脱硫反应剂的一种湿法烟气脱硫技术，目前国内外应用甚少，但开发前景广阔。以实验室小试为基础，从气液传质入手，利用双膜理论建立脱硫过程的数学模型，从而对中试脱硫效率进行预测并进行参数敏感性分析。结果表明，模型预测的脱硫效率与实际脱硫效率有很高的吻合度，其计算参数能反映出实际运行参数对脱硫效率的影响，对实际工况中操作条件的变更以及运行参数的调试有很高的指导意义。     

飞灰/水菱镁石新型复合脱硫剂的性能研究

采用飞灰和水菱镁石水合搅拌制备飞灰/水菱镁石新型复合脱硫剂,模拟湿法烟气脱硫过程,采用正交实验分析法探讨了液固比(质量比)、反应温度、搅拌速度以及鼓泡深度4个因素对脱硫效率的影响。结果发现:复合脱硫剂的比表面积增大,这有利于该复合脱硫剂与气相SO2的接触和反应,因而提高了脱硫效率。复合脱硫剂的最佳反应组合:液固比为15.0∶1.0、反应温度为常温(20℃)、搅拌速度为150r/min、鼓泡深度为2.0cm,该条件下脱硫效率为98.58%。     

石灰石湿法脱硫过程中SO2吸收数学模型

为揭示石灰石湿法脱硫体系中喷淋塔内SO2的浓度和脱硫效率的变化情况,针对喷淋塔内石灰石在气膜控制、气液膜控制和固体溶解控制的3个不同阶段,以双膜理论为基础,以单个石灰石颗粒为研究对象,通过石灰石在不同阶段的转化率和粒径变化,得到SO2在不同阶段脱硫效率随时间的变化规律,建立SO2吸收的数学模型.模型计算结果表明,在烟气行程上,脱硫效率受SO2气膜传质阻力和石灰石溶解速率限制.在吸收塔底部和上端SO2吸收速率较低,在SO2和石灰石摩尔比在适宜条件下,有效吸收段高度为2 m左右.理论模型揭示的规律对喷淋塔的设计和运行参数选取有一定借鉴意义.     

活性炭吸附有机蒸气过程中的初始浓度测定

以PTA生产尾气为实验体系，讨论了在活性炭对有机气体动态吸附过程中，有机气体初始浓度的三种测定方法，即气相色谱法、吸附称量法和气体方程计算法。结果得出，吸附称量法误差最小，其次是气体方程计算法，误差最大的是气相色谱法。     

生物膜填料塔净化低浓度苯乙烯废气的实验研究

研究了进口气体中苯乙烯浓度、气体流量和液体流量等3个因素对生物膜填料塔净化苯乙烯废气的影响.研究结果表明,当进口气体中苯乙烯浓度为1000 mg/m3以下、气体流量为200L/h、循环液流量为10L/h的操作条件下,废气中苯乙烯的去除率可达90%以上.     

生物膜填料塔净化低浓度苯乙烯废气的实验研究

研究了进口气体中苯乙烯浓度、气体流量和液体流量等3个因素对生物膜填料塔净化苯乙烯废气的影响。研究结果表明，当进口气体中苯乙烯浓度为1000mg／m^3以下、气体流量为200L／h、循环液流量为10L／h的操作条件下，废气中苯乙烯的去除率可达90％以上。     

The Gas Supply Situation in the United States

The body of information presented in this paper is directed to those individuals who require information on the present natural gas supply and demand relationship and the prospects for future changes, including individuals concerned with air quality control and the use of natural gas for combating air pollution.

If natural gas could continue to capture large shares of the energy market, as in the past when supply was not a growth inhibiting factor, annual demand for gas is projected to increase to 34.5 and 46.4 trillion cubic feet in 1980 and 1990, respectively. Annual production levels which could be supported by presently proven reserves and anticipated future reserve additions are estimated to peak in the mid-1970’s and decline to about 18 trillion cubic feet in 1990.

When viewed from the perspective of anticipated indigenous supply deficiencies, the acquisition of supplemental sources of gas becomes of paramount importance. Pipeline imports, the only substantive supplemental source presently available, could almost double by 1980 and be about 2 trillion cubic feet annually in 1990.

Available volumes of gas from Alaska could be 0.7 trillion cubic feet in 1980 and could increase to 2.3 trillion cubic feet annually by 1990. Actual initial deliveries of gas are inextricably related to construction of an oil pipeline from Prudhoe Bay. Construction delays postpone initial delivery dates for gas as well as oil.

Advancements in cryogenic transportation and storage technologies have made the heretofore largely untapped supplies of gas from several countries with limited internal markets available to the United States as LNG. Annual LNG imports could be about 0.3 trillion cubic feet in 1975 and perhaps 2 and 4 trillion cubic feet by 1980 and 1990, respectively.

Pipeline quality gas from coal presents the prospect for a supplemental source of gaseous fuel independent of foreign sources and free from balance of payments problems. The first pipeline quality gas from coal may be expected by 1976, and by 1980 perhaps 0.3 trillion cubic feet could be provided annually from this source; in 1990, 3.3 trillion cubic feet might be available. An additional, but presently unqualified, source of synthetic gas will be the conversion of liquid hydrocarbons.

In the aggregate, supplemental gas supplies are anticipated to total about 4.6 and 11.5 trillion cubic feet annually by 1980 and 1990, respectively. While demand for gas is anticipated to increase, domestic conventional gas production is projected to peak in the mid-1970’s and decrease somewhat thereafter. As a consequence, a continuing gas supply-demand imbalance is anticipated.     

The impact of methanogenesis on flow and transport in coarse sand

The effects of biofilm growth and methane gas generation on water flow in porous media were investigated in an anaerobic two-dimensional sand-filled cell. Inoculation of the lower portion of the cell with a methanogenic culture and addition of methanol to the bottom of the cell led to biomass growth and formation of a gas phase. Biomass distributions in the water and on the sand in the cell were measured by protein analysis. The biofilm distribution on sand was observed by confocal laser scanning microscopy. The formation, migration, distribution and saturation of gases in the cell were visualized by the charge-coupled device (CCD) camera. The effects of biofilm and gas generation on water flow were separated by performing one tracer test in the presence of both biofilm and a gas phase and a second tracer test after removal of the gas phase through water flushing. The results of tracer tests demonstrated that flow and transport in the two-dimensional cell were significantly affected by both gas generation and biofilm growth. Gas generated at the bottom of the cell in the biologically active zone moved upwards in discrete fingers, so that gas phase saturations (gas-filled fraction of void space) in the biologically active zone at the bottom of the cell did not exceed 40-50%, while gas accumulation at the top of the cell produced gas phase saturations as high as 80%. The greatest reductions in water phase permeability, based on measurements of reductions in water phase saturations, occurred near the top of the box as a result of the gas accumulation. In contrast the greatest reductions in permeability due to biofilm growth, based on measurements of biofilm thickness, occurred in the most biologically active zone at the bottom of the cell, where gas phase saturations were approximately 40-50%, but permeability reductions due to biofilm growth were estimated to be 80-95%.     

Oxidation of elemental mercury using atmospheric pressure non-thermal plasma

The oxidation of gas phase elemental mercury (Hg0) by atmospheric pressure non-thermal plasma has been investigated at room temperature, employing both dielectric barrier discharge (DBD) of the gas mixture of Hg0 and injection of ozone (O3) into the gas mixture of Hg0. Results have shown that the oxidative efficiencies of Hg0 by DBD and the injection of O3 are 59% and 93%, respectively, with energy consumption of 23.7 J L(-1). This combined approach has indicated that O3 plays a decisive role in the oxidation of gas phase Hg0. Also the oxidation of Hg0 by injecting O3 into the gas mixture of Hg0 proceeds with better efficiency than DBD of the gas mixture of Hg0. These results have been explained by the incorporation of the competitive reaction pathways between the formation of HgO by O3 and the decomposition of HgO back to Hg0 in the plasma environment.     

燃煤手烧炉烟尘生成特征及其控制

使用烟气净化测试系统,对燃煤手烧炉燃烧过程烟尘浓度变化进行了在线测定,对水浴净化前后烟气中的颗粒分散度进行了测定分析,并对SW型烟气净化装置的除尘效率进行了测定计算。实验表明,燃煤手烧炉的烟尘生成过程,与其加煤方式直接相关,且受燃烧温度的一定影响。在正常工作条件下,SW型燃煤炉窑烟气净化装置的平均除尘效率可达96 4%。     

Gas phase transport in gravity sewers--A methodology for determination of horizontal gas transport and ventilation.

A method was developed for determination of horizontal gas transport and ventilation in gravity sewers. This was achieved by changing the composition of the sewer atmosphere by pulse injection of oxygen gas and subsequently measuring the oxygen concentration in a downstream manhole. Conventional tracer techniques may require sampling and may also affect the environment. The method developed is simple, based on direct monitoring and without environmental or toxic effects. The method was developed based on measurements in an intercepting gravity sewer. The horizontal gas transport processes were quantified by measuring the velocity and dispersion of the gas in the sewer atmosphere. Based on 54 measurements, the gas velocity was found to vary between 0.05 and 0.22 m/s. The coefficients of dispersion were calculated to be in the range 0.05 to 1.1 m2/s. Climatic conditions did not significantly influence the gas phase transport.     

Gas-phase mercury reduction to measure total mercury in the flue gas of a coal-fired boiler

Gaseous elemental and total (elemental + oxidized) mercury (Hg) in the flue gas from a coal-fired boiler was measured by a modified ultraviolet (UV) spectrometer. Challenges to Hg measurement were the spectral interferences from other flue gas components and that UV measures only elemental Hg. To eliminate interference from flue gas components, a cartridge filled with gold-coated sand removed elemental Hg from a flue gas sample. The Hg-free flue gas was the reference gas, eliminating the spectral interferences. To measure total Hg by UV, oxidized Hg underwent a gas-phase, thermal-reduction in a quartz cell heated to 750 degrees C. Simultaneously, hydrogen was added to flash react with the oxygen present forming water vapor and preventing Hg re-oxidation as it exits the cell. Hg concentration results are in parts per billion by volume Hg at the flue gas oxygen concentration. The modified Hg analyzer and the Ontario Hydro method concurrently measured Hg at a field test site. Measurements were made at a 700-MW steam turbine plant with scrubber units and selective catalytic reduction. The flue gas sampled downstream of the selective catalytic reduction contained 2100 ppm SO2 and 75 ppm NOx. Total Hg measured by the Hg analyzer was within 20% of the Ontario Hydro results.     

非规范生活垃圾填埋场填埋气横向迁移规律及控制

我国城市中尚有大量非规范生活垃圾填埋场存在,对其进行污染整治消除填埋气导致的环境安全隐患刻不容缓.以重庆某垃圾填埋场为例,研究重庆市主城区的非规范生活垃圾填埋场填埋气的横向迁移问题,在垃圾场周边区域布设36个监测井,对监测井中的填埋气进行分析监测,以填埋气特征组分CH4气体的体积浓度变化研究填埋气的横向迁移规律.结果表明,监测井到填埋场边界的距离为监测井中CH4气体浓度的主要影响因素;垃圾场周边距离填埋场场界50 m以外的区域,填埋气的横向迁移已经相当微弱;但是距离填埋场边界50 m以内区域的填埋气的横向迁移明显,需要在距离填埋场边界50 m范围内采取措施与场内填埋气的导排措施配合,进行填埋气的污染控制.