THE REACTIVITY AND DURABILITY OF ZINC FERRITE HIGH TEMPERATURE DESULFURIZATION SORBENTS

Cylindrical pellets of zinc ferrite high temperature desulfurization sorbent have been prepared using a number of formulation recipes and induration conditions. Physical and structural properties of the resultant sorbents were measured, and reactivity and durability screening tests were carried out using a single pellet electrobalance reactor. The formulation variables studied were ZnO to Fe₂O₃ ratio, Fe₂O₃ source, and the addition of inorganic (bentonite) and organic (methocel) binders to the sorbents. Pellet induration conditions ranged from 0.25 hours at 815^°C to 4.0 hours at 1038°C. Stronger pellets having greater attrition resistance resulted when 5% bentonite was added to the formulation recipe and when the pellets were indurated at high temperature for extended times. In contrast, bentonite content was not a significant factor in determining sorbent reactivity and durability, both of which were improved by mild induration conditions. Sorbent regeneration temperature was found to be an important factor in improving reaction durability, as was the addition of 0.5% methocel to the formulation recipe. Pellets containing catalyst-grade Fe₂O₃ were more reactive than those containing pigment-grade Fe₂O₃. This effect, however, was less important than the effect of induration conditions.     

Desulfurization of commercial fuels by π-complexation: Monolayer CuCl/γ-Al2O3

Monolayer CuCl/γ-Al₂O₃ sorbent was studied for desulfurization of a commercial jet fuel (364.3 ppmw S) and a commercial diesel (140 ppmw S). The sorbent was prepared by means of spontaneous monolayer dispersion methods. Deep desulfurization (sulfur levels of <1 ppmw) was accomplished with this sorbent using a fixed-bed adsorber. The CuCl/γ-Al₂O₃ sorbent was capable of removing 6.4 and 11.2 mg of sulfur per gram for jet fuel at breakthrough (at <1 ppmw S) and saturation, respectively. The same sorbent was capable of removing 0.94 and 1.8 mg of sulfur per gram for BP diesel at breakthrough and saturation, respectively. The difference in sulfur capacities for jet fuel and diesel was apparently caused by the difference in concentrations of strongly binding compounds, such as nitrogen heterocycles, heavy (polynuclear) aromatics and fuel additives. In comparison with CuCl/γ-Al₂O₃, Cu(I)Y zeolite has higher sulfur capacities but is less stable and can be easily oxidized to Cu(II)Y by fuel additives (such as oxygenates) and moisture and consequently loses π-complexation ability. However, all these cuprous π-complexation sorbents selectively adsorb thiophenic compounds over aromatics and olefins (as predicted by the high separation factors), which resulted in the observed desulfurization capability. A feasibility study is shown for efficient regeneration of CuCl/γ-Al₂O₃ using ultrasound at ambient temperature. Possible problems associated with desulfurization using π-complexation sorbents for commercial fuels are discussed.     

Desulfurization in a plate-type gas-lift photobioreactor using light emitting diodes

Hydrogen sulfide gas was removed in a 2-dimensional gas-lift reactor by the photosynthetic microorganismChlorobium thiosulfatophilum using light emitting diodes (LEDs) as a light source. LEDs saved light energy by 99% compared with the incandescent light source. The plate-type gas-lift reactor removed hydrogen sulfide five times better per unit mg of protein, and performed two times better in the maximum performance per unit luminous flux, compared with cylindrical fermentors.     

国华惠电脱硫及灰渣与主机系统一体化控制研究

本文主要针对神华国华惠州电厂脱硫及灰渣控制系统存在的主要问题,同时结合国家发展改革委和环境保护部提出的＂脱硫脱硝除尘DCS主要参数应逐步设置于同一集控室内＂的具体要求,避免主机集控室与灰硫控制室运行人员在机组异常情况下沟通不及时,造成环保参数超标发生环保事件,给集团公司造成恶劣的影响。重点介绍了在双机不同时停运的情况下,以机组运行安全为第一,逐步实现脱硫及灰渣控制系统单元制改造的过程,同时与主机控制系统联网,达到脱硫及灰渣控制系统与主机控制系统一体化控制的目的,给火力发电厂实现控制系统一体化改造工程一定的借鉴意义。     

煤气化过程中单颗粒吸收剂脱硫反应模型概述

对煤气化过程中吸收剂脱硫反应的气固反应模型进行了概述.气固反应模型大致可分为未反应缩核模型,晶粒模型、孔模型及逾渗模型等几种基本型式.未反应缩核模型结构比较简单,可以作为其它模型的基础和组成部分,晶粒模型应用较为广泛且已经得到了充分的发展和改进,孔模型侧重于颗粒内部孔隙特性对反应影响的分析,逾渗模型则基于孔模型将逾渗理论引入来描述脱硫反应过程.     

煤炭复合型助燃固硫剂的开发与研究

通过对不同粒径煤样的全硫量及黄铁矿硫量的测试分析,以及在燃烧过程中生成酸性气体,从而选用复合型碱性固硫剂来进行固硫试验。通过对这几种试验方案的优选比较分析,确定按煤90%∶CaO 9%∶NaCl 1%的配方脱硫率高且成本低廉,可适合工业化生产使用。同时,用高精度微机全自动量热仪做上述配方的煤燃烧热效率实验,结果表明,煤热效率有明显的提高。这说明复合型碱性添加剂不但可促进煤炭的燃烧,同时在燃烧的过程中取到固硫的作用。     

氨水脱硫液质量对H2S吸收的影响

研究了H2S吸收液中酸性杂质对吸收平衡的影响，研究表明，H2S在脱硫液中的溶解量随着活性氨的增加而提高，随杂质含量的增加而减少，对于酸性物较多的吸收液，应相应提高总氨量，以提高脱硫液中的活性氨含量。     

钢水钙基脱硫剂的应用探讨

在钢铁市场面临激烈竞争的形势下,用户对产品质量,品种的要求不断提高。深脱硫已经成为提高钢质量、扩大品种和开拓钢材市场的重要手段。针对钢水钙基脱硫剂的文献研究中,并对其学者的文献和观点进行归纳和总结,找出提高钢水快速脱硫的途径。     

B2O3-CaO、CaF2-CaO对LATS钢包渣的调质处理实验

为减少LATS合金化精炼浸渍罩粘渣,分别采用B2O3-CaO和CaF2-CaO作调质剂对钢包渣进行调质处理实验.调质后熔渣物性研究结果表明:两种调质剂都有效地降低了钢包渣的熔点和粘度.硫在渣-金属间分配平衡实验表明,调质后的钢包渣不会引起钢液回硫,而且可使钢中的硫含量进一步降低.     

马钢2500m~3高炉炉渣的冶金性能

在目前的原燃料条件下,为保证马钢2500m3高炉炉渣具有良好的流动性和较高的脱硫能力,炉渣的CaO／SiO2应控制在1．05至1．15之间,炉渣温度不低于1450℃．