下关发电厂LIFAC脱硫技术

作为电力部烟气脱硫示范工程之一的南京下关发电厂ＬＩＦＡＣ工艺烟气脱硫系统已进入施工设计阶段，本文介绍了干法ＬＩＦＡＣ烟气脱硫工艺的基本原理，系统构成及主要工艺参数，可作为类似电厂进行烟气脱硫工艺选择时的参考。     

固定床活性炭干法烟气脱硫过程的模拟研究

采用流程模拟软件对固定床活性炭干法烟气脱硫过程进行模拟,并用已公开发表的文献实验数据进行了模型验证。模型验证结果与文献值吻合较好。利用该模型对活性炭干法烟气脱硫过程进行模拟研究,探讨了脱硫过程中床层高度、进口烟气中SO_2质量浓度、吸附温度等工艺参数对SO_2脱除率的影响。模拟结果表明:随床层高度增加,SO_2脱除率提高;随进口烟气中SO_2质量浓度增加,SO_2脱除率提高;在吸附温度为100~160℃的范围内,随吸附温度升高,SO_2脱除率逐渐下降。     

臭氧氧化—钙法吸收工艺对烟气的同步脱硫脱硝

针对中国石化镇海炼化乙烯动力锅炉烟气的特点,进行烟气模拟,采用臭氧氧化—钙法吸收同时脱硫脱硝工艺处理模拟烟气。实验对比了单独脱硫和脱硝过程与同时脱硫脱硝工艺的脱硫、脱硝效果,探究了烟气在反应器中的停留时间、臭氧投加量和烟气含氧量对SO_2去除率和NO_x去除率的影响。实验结果表明:SO_2和NO的共存可促进污染物的去除;烟气停留时间延长,SO_2去除率提高,NO_x去除率先升高后降低;臭氧与NO摩尔比增加,NO_x去除率提高,SO_2去除率略有降低。综合考虑选择烟气停留时间3.4 s,烟气含氧量12%(φ),臭氧与NO摩尔比0.7,在此工艺条件下反应70 min,NO_x去除率为73.8%,SO_2去除率为74.1%。     

燃煤电厂简易烟气脱硫工艺的研究

本文提出了适合我国国情的一套燃煤电厂简易烟气脱硫工艺，并作了冷态模拟试验研究，研究结果表明，简易烟气脱硫工艺系统阻力能够达到约１０００Ｐａ的水平，脱硫效率可达到５０－８５％，值得进行更深入的研究。     

脱硫石膏液相法生产高强度α-石膏的工艺研究

脱硫石膏是火电厂烟气脱硫副产物,由于其粒径较细、颗粒分配不均,煅烧生产比天然石膏困难,而液相法工艺适合脱硫石膏生产高强度α-石膏。对脱硫石膏液相法生产高强度α-石膏的工艺参数进行了研究,通过对反应转晶剂添加量、转化温度、压力及反应时间等参数调整,得到了脱硫石膏生产的合理参数。     

湿法烟气脱硫工艺是否安装烟气换热器问题探讨

迄今为止,石灰石-石膏湿法烟气脱硫工艺已成为我国燃煤电厂烟气脱硫的首选工艺,而烟气脱硫湿法工艺是否需要进行烟气升温（即烟气脱硫是否需加装烟气换热器）的问题一直困惑着脱硫产业界.本文就安装烟气换热器（GGH）有关问题进行了阐述,提出石灰石-石膏湿法烟气脱硫工艺不宜安装烟气换热器的观点,供业内人士及有关决策部门参考.     

臭氧氧化—钙法吸收工艺对烟气的同步脱硫脱硝

针对中国石化镇海炼化乙烯动力锅炉烟气的特点,进行烟气模拟,采用臭氧氧化—钙法吸收同时脱硫脱硝工艺处理模拟烟气。实验对比了单独脱硫和脱硝过程与同时脱硫脱硝工艺的脱硫、脱硝效果,探究了烟气在反应器中的停留时间、臭氧投加量和烟气含氧量对SO₂去除率和NO_x去除率的影响。实验结果表明：SO₂和NO的共存可促进污染物的去除;烟气停留时间延长,SO₂去除率提高,NO_x去除率先升高后降低;臭氧与NO摩尔比增加,NO_x去除率提高,SO₂去除率略有降低。综合考虑选择烟气停留时间3.4 s,烟气含氧量12%（φ）,臭氧与NO摩尔比0.7,在此工艺条件下反应70 min,NO_x去除率为73.8%,SO₂去除率为74.1%。     

多炉一塔脱硫工艺取消增压风机的可行性研究

多炉一塔脱硫工艺中通常设置增压风机,但在工程实践中增压风机存在着喘振、失速、高能：耗等诸多运行问题。以某自备电厂3台220t／h燃煤锅炉烟气脱硫工程为例,针对多炉一塔湿法脱硫工艺是否设置增压风机,从性能、能耗、运行维护成本等方面对设计方案进行了经济技术比较,并利用流场模拟对烟气系统进行了优化,最终通过引风机的改造替代了增压风机的设置,为小型燃煤电厂湿法脱硫工艺的系统设计提供参考。     

海水烟气脱硫工艺在火电厂的应用

介绍了海水烟气脱硫工艺的基本原理，工艺流程，设计参数、工艺特点和实际运行效果，并提出该工艺在火电厂应用中的注意事项。     

氨法烟气脱硫技术及其进展

阐述了氨法烟气脱硫技术的原理和工艺特点.介绍了Walther氨法、AMASOX氨法、GE氨法、NADS氨-肥法、电子束氨法和流光放电氨法烟气脱硫工艺,重点介绍了新型流光放电氨法烟气脱硫技术的特点及其工程应用情况.展望了氨法烟气脱硫技术的应用前景.     

纳米晶粒TiO2多孔微球的制备及其光催化性能的研究进展

介绍了纳米晶粒TiO2多孔微球的主要制备方法、主要参量及表征、光催化性能研究进展,指出了纳米晶粒TiO2多孔微球制备过程的技术关键与基本参量的功能。针对目前存在的问题,提出了今后的主要研究方向,并展望了纳米晶粒TiO2多孔微球在水处理领域的应用前景。     

OI~2-WFGD-Ⅱ烟气脱硫技术介绍

简要介绍了江苏苏源环保工程有限公司开发的OI^2-WFGD-Ⅱ湿法烟气脱硫技术的工艺特点、设备布置、技术参数、设备国产化以及技术应用。     

锅炉大修后酸洗中的几个关键问题

电站锅炉的酸洗可以有效地清除管道内的氧化物、污垢、焊渣等,提高水汽品质和机组运行的安全性能。针对锅炉材料及酸洗中易出现的问题,提出了酸洗工作应注意清洗液选配、酸洗管路设计、酸洗关键参数控制、酸洗后废液处理及酸洗中安全事项等关键技术,可为锅炉酸洗提供技术指导,保证酸洗工作的有效性和安全性。     

CFD simulation of MSW combustion and SNCR in a commercial incinerator

A CFD scheme was presented for modeling municipal solid waste (MSW) combustion in a moving-grate incinerator, including the in-bed burning of solid wastes, the out-of-bed burnout of gaseous volatiles, and the selective non-catalytic reduction (SNCR) process between urea (CO(NH₂)₂) and NO_x. The in-bed calculations provided 2-D profiles of the gas–solid temperatures and the gas species concentrations along the bed length, which were then used as inlet conditions for the out-of-bed computations. The over-bed simulations provided the profiles of incident radiation heat flux on the top of bed. A 3-dimensional benchmark simulation was conducted with a 750 t/day commercial incinerator using the present coupling scheme incorporating with a reduced SNCR reduction mechanism. Numerical tests were performed to investigate the effects of operating parameters such as injection position, injection speed and the normalized stoichiometric ratio (NSR) on the SNCR performance. The simulation results showed that the distributions of gas velocity, temperature and NO_x concentration were highly non-uniform, which made the injection position one of the most sensitive operating parameters influencing the SNCR performance of moving grate incinerators. The simulation results also showed that multi-layer injections were needed to meet the EU2000 standard, and a NSR 1.5 was suggested as a compromise of a satisfactory NO_x reduction and reasonable NH₃ slip rates. This work provided useful guides to the design and operation of SNCR process in moving-grate incinerators.     

燃煤电站SCR烟气脱硝工程技术关键问题研究

对SCR烟气脱硝催化剂的选择、脱硝系统旁路设置与脱硝装置流场模拟这三个当前我国燃煤电站SCR烟气脱硝工程技术中的关键问题进行了分析与探讨,并提出了解决措施,为提高脱硝工程技术水平、完善当前SCR烟气脱硝技术规范提供借鉴。     

Steady-state design of horizontal systems for liquids addition at bioreactor landfills

The key parameters for designing a horizontal source (horizontal trenches, infiltration ponds, infiltration galleries or blankets) for steady state are the rate liquids can be added to the source, the lateral and vertical extents of the zone of impact of the source, and the liquids volume needed to wet the waste within the zone of impact at steady state. This paper presents charts that a designer can use to estimate these key parameters as functions of source dimensions, injection pressure, and municipal solid waste properties (porosity, hydraulic conductivity, and anisotropy) for designing a new or analyzing an existing horizontal source system for liquids addition to landfilled waste. SEEP/W was used to model liquids flow from a horizontal source in a range of conditions practically encountered for such systems. The governing equation (Richard’s equation) and the boundary conditions were analyzed to formulate dimensionless variables by normalizing the design parameters (flow rate, injection pressure, the lateral zone of impact, injection pressure, and the added liquids volume) with the waste properties and source dimensions. The simulation results were transformed to the respective dimensionless forms and presented in design charts to estimate the key design parameters as functions of the source dimensions, waste properties, and injection pressure. The presentation of the modeling results in the dimensionless form facilitates their use beyond the conditions modeled. A solved example is presented to demonstrate the use of the design charts. The approach presented in the paper should be considered as approximate and designers should use their judgement and experience when using these charts for designing a horizontal liquids addition system for a specific site.     

A/O/O工艺处理含油污水的模拟评估

利用Bio Win 5.0软件建立了某炼油厂A/O/O工艺处理含油污水的数学模型,对其工艺参数进行了评估,并提出了改进建议。经调整部分动力学参数后,模拟结果与实测值吻合度较好,相关系数在0.75~0.81之间,建立的模型可较好反映工艺的运行工况。模拟优化主要针对一级处理装置,在仅考虑NH_3-N和COD去除的情况下,目前装置的工艺参数较合理,若考虑TN,无法实现TN和NH_3-N同时达标。对一级处理装置的模型进行改进后,出水模拟值中COD轻微上升2%,但ρ(NH_3-N)和TN分别下降83%和66%,可有效减轻后续处理装置负荷。     

大豆种皮过氧化物酶在酚类废水处理中的应用

介绍了大豆种皮过氧化物酶（SBP）的特性、除酚原理及用SBP处理酚类废水的研究进展，对SBP除酚的主要技术参数进行了详细阐述，并对现存问题和解决途径进行了探讨。SBP的性质优异、酶源丰富、价格低廉。直接用大豆种皮处理废水的经济指标已基本达到实用水平，但导致废水中可溶性固形物的含量增加，解决的途径是选育酶活性高、稳定性好的大豆品种。     

基于参数化模型优化的喷氨格栅设计方法研究

从喷氨格栅工程设计要求出发,结合数值模拟分析、代理模型技术以及优化设计方法,提出了一套基于参数化模型优化的喷氨格栅设计方法和流程。该方法从工程设计要求的分析入手,根据喷氨格栅几何参数对喷氨特性的影响特点和规律,建立参数化设计数学模型,并通过优化计算最终获得喷氨格栅的最优设计。另外,通过实例计算验证了该设计方法在SCR脱硝系统喷氨格栅设计中的适用性。     

The Synthesis and FTIR, Kinetics and TG/DTG/DTA Study of Inter Penetrating Polymer Networks (IPNs) Derived from Polyurethanes of Glycerol Modified Castor Oil and Cardanol Based Dyes

Interpenetrating polymer networks from agricultural products such as glycerol modified castor oil polyurethanes and cardanol based dyes have not been extensively studied so far. Such polymers were synthesized using benzoyl peroxide as initiator and ethylene glycol dimethacrylate as cross-linker. Characterizations of these polymers were performed by Fourier Transform infra red spectra and thermal analysis techniques such as thermogravimetric analysis, derivative thermogravimetry and differential thermal analysis. The kinetic parameters such as activation energies and orders of reaction were estimated by using Freeman?CAnderson??s method. The effects of changes in polyurethane to dye monomer weight ratio and NCO/OH molar ratio of polyurethanes on the properties of such polymers were studied.