半干法钙基烟气脱硫技术

阐述了半干法脱硫机理和影响因素以及容易出现的问题及其解决方法。针对半干法脱硫剂利用率低、Ca／S高的问题，提出了几种提高脱硫剂利用率的技术。     

钙基脱硫剂孔隙中SO2气体非线性扩散的研究

以动态生成的CaO孔隙网络为骨架,按照不退行随机行走模型（NRRW）,模拟气体分子在CaO孔隙中的扩散过程,计算了SO2分子的扩散系数和行走维数,并在SO2非线性扩散反应方程基础上,分析了CaO颗粒孔隙中SO2浓度的分布特性。     

用于干式脱污的CaO蒸汽活化实验研究

利用小型活化转炉实验台对以CaO为主要成分的钙基脱污剂在300～650℃的温度范围内进行蒸汽活化处理,结合X射线衍射和压汞仪的分析结果,初步探讨了蒸汽活化的机理.研究表明,蒸汽活化温度在600℃以上时,脱污剂孔隙结构有显著的改善,比孔容积和比表面积有着显著的增加,微孔(＜100nm)的数量大量增加,而低温下蒸汽活化的效果不是十分明显;研究还发现高温下延长活化时间有利于改善脱污剂的孔隙结构.     

分级燃烧工况下高岭土对煤中微量元素排放的影响研究

通过在一维煤粉燃烧炉上进行肥煤、无烟煤添加高岭土吸附剂的燃烧实验 ,研究了肥煤、无烟煤及其燃烧产物中 18种微量元素的含量和分布 ;计算了高岭土在分级燃烧工况条件下对每种微量元素的吸附率 .结果表明 :高岭土对中、低挥发性微量元素具有不同的吸附作用 ,吸附效率与煤种、元素种类、燃烧温度等因素有关 ,无烟煤燃烧比肥煤燃烧吸附效果更好 .     

钙基CO2吸收剂循环特性影响因素分析

利用小型固定床反应器研究了循环煅烧/碳酸化过程中,煅烧温度、煅烧气氛、碳酸化温度、压力等对钙基CO2吸收剂循环特性的影响,确定了影响钙基CO2吸收剂循环特性的主要因素。结果表明:随循环次数的增加,吸收剂的转化率明显下降,循环10次后,其基本都下降到20%左右;煅烧温度是影响吸收剂循环特性最重要的因素;煅烧气氛中存在CO2对吸收剂活性保持不利;吸收压力和温度也对吸收剂的循环特性有一定影响,较高的吸收压力和吸收温度有利于吸收剂转化。     

流化床O2/CO2气氛燃煤痕量元素的排放特性及控制

通过平顶山烟煤在小型流化床中的燃烧实验,采用X-射线荧光光谱仪(XRF)对低压撞击器(LPI)收集到的细颗粒物元素组成进行定量测定,研究了O2/CO2气氛下硅藻土对煤粉燃烧痕量元素的排放控制.结果表明,Zn、Mn和Ni的含量随粒径呈双峰分布,峰值分别在0.1μm和2μm附近,Hg和Co的含量在0.1μm附近有一峰值;Hg和Zn在亚微米颗粒上有一定程度的富集,Mn、Ni和Co在亚微米和超微米颗粒上的含量基本相当;当颗粒物粒径一定时,随着硅藻土含量的增加,5种元素的富集因子呈减小的趋势;随着添加剂粒径的减小,颗粒物中Hg、Mn、Zn、Ni和Co的含量呈减少的趋势;当颗粒物粒径一定时,5种元素含量顺序为MnZnNiCoHg.     

PHBV表面疏水改性用作吸油材料的研究

利用多种表面改性剂对生物可降解材料PHBV进行了表面改性实验研究，测定了不同改性剂改性后PHBV的吸油率以及温度对其吸油效果的影响，并探讨了改性机理，研究结果表明：不同改性剂对PHBV的改性效果有所差异，从疏水和吸油的共同效果来看，最佳疏水改性剂为添加量5％时的硅油，温度对未改性PHBV和改性PHBV的吸油率及吸油速度均有影响。     

新型氨化菌丝体吸附剂的制备及吸附典型内分泌干扰物的研究

以产黄青霉(Penicillium chrysogenum)菌丝体为原料,通过2步化学反应将含有大量氨基的聚乙烯亚胺(PEI)嫁接到菌丝体表面,优化反应条件,得到最佳的氨化菌丝体吸附剂.该氨化吸附剂的等电点为pH 10.2,是一种表面带正电荷的菌丝体吸附剂,能有效吸附水中的阴离子内分泌干扰物五氯酚钠(PCP)、2,4二氯苯氧乙酸(2,4-D)和全氟辛烷磺酸钾(PFOS).3种污染物的吸附等温线符合Langmuir方程,15℃时最大吸附量分别为342.9、234.1、1725.6 mg/g.热力学计算表明,3种污染物的吸附均是自发发生的,2,4-D和PFOS的吸附是吸热反应,而PCP是放热反应.     

Reaction mechanism of arsenic capture by a calcium-based sorbent during the combustion of arsenic-contaminated biomass: A pilot-scale experience

Pilot-scale combustion is required to treat arsenic-enriched biomass in China. CaO addition to arsenic-enriched biomass reduces arsenic emission. CaO captures arsenic via chemical adsorption to form Ca₃(AsO₄)₂. Large quantities of contaminated biomass due to phytoremediation were disposed through combustion in low-income rural regions of China. This process provided a solution to reduce waste volume and disposal cost. Pilot-scale combustion trials were conducted for in site disposal at phytoremediation sites. The reaction mechanism of arsenic capture during pilot-scale combustion should be determined to control the arsenic emission in flue gas. This study investigated three Pteris vittata L. biomass with a disposal capacity of 600 kg/d and different arsenic concentrations from three sites in China. The arsenic concentration in flue gas was greater than that of the national standard in the trial with no emission control, and the arsenic concentration in biomass was 486 mg/kg. CaO addition notably reduced arsenic emission in flue gas, and absorption was efficient when CaO was mixed with biomass at 10% of the total weight. For the trial with 10% CaO addition, arsenic recovery from ash reached 76%, which is an ~8-fold increase compared with the control. Synchrotron radiation analysis confirmed that calcium arsenate is the dominant reaction product.     

Effect of steam hydration on performance of lime sorbent for CO2 capture

Lime is considered a feasible sorbent for the capture of CO₂ from large stationary sources. The positive attributes of a natural source material, low cost and lack of harmful by-products are offset by rapid deterioration in performance and high regeneration temperature. Performance can be improved by hydrating the lime using steam. We investigate a steam hydration process wherein lime is hydrated for 5 min at 300 °C and atmospheric pressure in a mixture of steam and CO₂. The experiments consisted of 10 capture cycles with 60% of the lime active at the end. Extrapolation using a decay model suggests a residual carbonation level of 48%, significantly higher than the 8% achieved by dry lime cycles. The cost of replacement sorbent under these conditions is less than $1/t of CO₂ captured. The hydrated lime process also reduces the thermal load, for heating and cooling, by half as well as the inventory, and therefore solids handling, by a factor 5 over dry lime. The introduction of the hydration reaction provides another exothermic reaction for heat management.