旋流板塔煤浆法烟气脱硫研究

煤浆法烟气脱硫是以煤浆洗涤含二氧化硫的烟气,二氧化硫溶于浆液形成亚硫酸,煤中黄铁矿与亚硫酸、氧气发生反应,亚硫酸被氧化为硫酸,从而实现烟气脱硫.反应过程中,煤中的黄铁矿硫也被转化为硫酸而浸出,反应产生的Fe3＋/Fe2＋又对脱硫反应起到了催化剂的作用.以旋流板塔为吸收设备,研究了煤浆法烟气脱硫过程中浆液温度、液气比、空塔气速及浆液固液比等操作参数对脱硫率的影响规律.试验表明,在其他条件不变的情况下,适当提高液气比、空塔气速及浆液固液比均有利于提高脱硫效果.随着烟气脱硫过程的进行,脱硫浆液中的总铁含量不断增加,说明煤中黄铁矿被不断浸出,故此法在脱除烟气中的二氧化硫的同时也降低了煤中黄铁矿硫含量.     

离心式杂质泵蜗壳内部流场数值模拟

利用计算流体动力学分析软件,对离心式杂质泵的内部流场进行了数值模拟.计算了颗粒直径为0.076mm,固相体积分数为10%的两相流工况下的三维湍流流场,得到了蜗壳内的速度、压力和固相体积分数分布等流动信息.计算结果表明：自进口至最大半径处蜗壳内的速度不断减小,压力逐渐增大,颗粒体积分数随半径增大而增大.     

Al2O3陶瓷粉料的喷雾干燥工艺要点

本文阐述了喷雾造粒过程中的相关制备工艺 ,并通过实验总结出一套合理的工艺控制参数     

水煤浆加压气化有关堵塞问题的探讨

通过对水煤浆加压气化装置中堵塞问题的原因分析 ,提出了具体的技术改造措施 ,并从操作方法上加以改进和调整     

Reducing N losses (NH3, N2o, N2) and immobilization from slurry through optimized application techniques

In model, pot and field trials the effect of C reduced slurries and different application techniques on N losses and N immobilization were investigated. The C reduced slurries were produced by mechanical separation. Ammonia losses from surface-applied and injected cattle slurry were measured under field conditions using a wind tunnel system. Injection of slurry was the most efficient way to reduce volatilization of ammonia. After 6 days the total loss from the injected slurry was only 9% of that from surface band application. Furthermore, additional losses of N may occur through denitrification, specially after injection of slurry which may create an anaerobic environment abundant in readily oxidizable C. Therefore denitrification measurements by the acetylene inhibition technique were conducted. Until 100 days after application the loss from the injected slurry was 7.3 kg compared to 4.5 kg N ha^–1 from surface band applied slurry. After injection, denitrification was only 4.1 kg N ha^–1 for C reduced compared to 6.5 kg N ha^–1 for normal slurry. In pot trials the ammonium-¹⁵N of normal slurry and C-reduced slurry was utilized by oats between 52 and 60%, the ammonium sulfate by 67%. The increased biomass C confirmed a greater immobilization of the NH₄-N of the normal slurry resulting in a lower initial efficiency.Dedicated to Prof. Dr. A. Amberger on his 75th birthday     

6.5MPa水煤浆气化炉工艺分析

对引进的６．５ＭＰａ德士古水煤浆气化炉设计与生产数据进行了工艺分析，对气化炉操作条件的选择进行了探讨。     

A pre-heating vaporization technology of coal-water-slurry for the gasification process

A pre-heating vaporization technology of coal water slurry, CWS, was developed to increase the efficiency of coal gasification with the reduction of oxygen consumption. A CWS pre-heating experimental unit having a capacity of 2.0 tons-coal/day was manufactured. After the CWS was heated to 573 K at about 10 MPa, water in CWS was continuously vaporized in a tube of which the diameter increased gradually (2–10 mm I.D.), and dry coal particles with steam were atomized and fed to a vessel. No aggregation of coal particles was observed in the atomized samples. The temperature and the pressure distributions of the fluid were calculated with empirical heat transfer and pressure drop correlations. The calculated results well corresponded to the experimental data measured in some test points. Using the calculation model, a large scale apparatus of 100 tons-coal/day was designed using KNO₃ + NaNO₂ + NaNO₃ molten salt as a heating medium.     

工业木质素的改性及其作为精细化工产品的研究进展

随着社会的发展,人类正面临着资源消耗过度、环境污染加剧的困境。积极寻找可再生资源,采用绿色化学工艺、减少环境污染是人类社会可持续发展的必然选择。木质素是自然界第二丰富的生物质可再生资源,工业木质素是制浆造纸的副产品,目前回收利用率不高,大部分随废水排放,既污染环境,又浪费资源。工业木质素的资源化利用具有重大的经济、社会与环境效益。实现工业木质素的资源生态化利用,必须考虑市场对产品的需求、产品的性能价格比、生产工艺的绿色化及发挥工业木质素本身的特性等四方面的因素。技术创新是保证实现工业木质素资源生态化利用最重要的条件。工业木质素通过改性后作为混凝土减水剂、水处理剂、水煤浆分散剂等方面的研究与应用已取得良好进展,是工业木质素资源生态化利用的成功例子。     

煤间接液化技术及其发展状况

介绍了煤间接液化技术的特点,从其原理、工艺路线、关键技术及发展现状等方面对间接液化技术进行了详细的阐述,指出发展煤间接液化是解决我国油品短缺的根本途径。     

Investigations of fluid dynamics in mechanically stirred aerated slurry reactors

The fluid dynamics of stirred aerated slurry reactors with A-310® propeller, 4-blade 45° pitch turbine and 6-blade Rushton disc turbine were studied over a wide range of gas flow rates. With respect to power consumption, gas hold-up, and fluid dynamically limiting cases, viz., suspension and flooding, the Rushton disc turbine was found to be the best in stirred aerated slurry reactors. The influence of particle density, shape and mass fraction and of liquid properties on gassed critical stirrer speed, N_jsg, and of gassed power input per unit volume, P_jsg, on particle suspension and gas dispersion, were investigated. Empircal correlations in combination with that of Zwietering were established for scale-up design in three-phase slurry reactors.