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.     

无烟煤熔融盐催化气化反应特性研究

根据煤催化气化原理及熔融盐特性,设计了一套小型熔融盐催化煤气化实验装置。针对无烟煤燃烧特性差的特点,在实验中研究了温度和二氧化碳流量对气化结果的影响,并对影响机理进行分析。     

CO2 gasification of wood charcoals derived from vacuum and atmospheric pyrolysis

The gasification of biomass derived char obtained via vacuum and atmospheric pyrolysis of Populus tremuloides has been studied in the ranges of 725–960°C and 0.1 to 6 MPa. CO₂ was used as the oxidizing gas. The results show that char reactivity is influenced by the preheating rates and that pressure effects are significant between 850°C and 950°C. A correlation based on the expression: df/dt = k₀{exp(-E/RT)}(1 - f)^af^βP^yCO₂ was used to fit the experimental data. In general, vacuum pyrolysis derived char showed a higher reactivity than atmospheric pyrolysis chars. An explanation based on a higher oxygen content of the vacuum pyrolysis char is suggested.     

Manipulation of gasification coal feed in order to increase the ash fusion temperature of the coal enabling the gasifiers to operate at higher temperatures

Coal is a crucial feedstock for South Africa’s unique synfuels and petrochemicals industry and used by Sasol as a feedstock to produce synthesis gas via the Sasol-Lurgi Fixed Bed Dry Bottom (FBDB) gasification process. The ash fusion temperature (AFT) gives detail information on the suitability of a coal source for gasification purposes, and specifically to which extent ash agglomeration or clinkering is likely to occur within the gasifier. Ash clinkering inside the gasifier can cause channel burning and unstable operation.Sasol-Lurgi FBDB gasifiers are currently operated with the philosophy of adding an excess of steam to the process to control the H₂/CO ratio of the syngas produced, but indirectly also to control the maximum gasifier temperature below the AFT of the coal. An opportunity exists to increase the AFT of the coal fed to the gasifiers by adding AFT increasing minerals to the coal blend before it is fed into the gasification process. For the aim of this study a South African coal source was investigated, as being used by the gasification operations in Secunda.With the specific aim of this study, to increase the AFT, the determination of the AFT of the coal blends where acidic components such as silica (SiO₂), alumina (Al₂O₃) and titania (TiO₂) were added was conducted. The Al₂O₃ had the biggest and most significant effect on the AFT with the least addition to the coal blend. The effect of SiO₂ and TiO₂ were very similar, but the effect was much smaller and further Al₂O₃ was needed to increase the AFT to a similar AFT level in comparison to the SiO₂ used. Kaolinite, roof and floor components (containing mainly Al₂O₃ and SiO₂) were also added, also showing an increase in the AFT with up to 4 mass% addition. Another observation was that the AFT was non-additive (not a linear weighted calculated average) and not the weighted average AFT as was expected for the other coal properties such as the ash content, for example. The ash slagging characteristics is a non-additive property of individual coal sources in the blend and therefore difficult to predict.In general it can be concluded that the unique opportunity exists to increase the AFT, was tested, proven and mechanistically outlined in this study on the coal source fed to the Sasol-Lurgi FBDB gasifiers. The AFT can be increased to >1350 °C by adding AFT increasing minerals or species to the coal blend before it is fed into the gasification process. By increasing the AFT, the direct effect will be that steam consumption can be decreased, which in turn will improve carbon utilization.     

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。     

双原料化一室二段气流床气化炉工艺及应用

在介绍甲烷转化工艺和煤气化工艺制取合成气生产技术的基础上,着重介绍了以煤炭和煤层气中的甲烷为原料的双原料化合成气制造工艺。论述了该工艺流程的特点,对其关键设备———一室二段气流床气化炉从设备结构和应用效果方面进行了介绍。结果表明,在富产煤层气的地区,以双原料化工艺制取的合成气生产甲醇和二甲醚,生产效率比传统方法高10%~16%,并可减轻煤炭利用对环境的影响。     

壳牌煤气化配套硫回收工艺方案的选择

对壳牌煤气化合成气处理技术进行了分析，总结了从粗煤气中脱除的酸性气的特点。对硫回收技术的8种工艺方案从H2S浓度要求、生产能力、环保、投资和运行费用方面进行了对比，指出了壳牌煤气化硫回收工艺方案的选择要领。     

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.     

联醇工艺中影响醇氨比调整的关键因素探讨

介绍了联醇工艺的发展概况和最新进展;阐述了目前最先进的两级联醇 甲烷化或烃化新工艺的特点;对影响醇氨比调整的关键因素——造气、变换、精脱硫、甲醇合成、脱碳等工序的生产操作提出了相关调整控制措施。     

2.25CrMo钢在还原性含氯气氛中的高温腐蚀行为

采用热重法及SEM／EDX，XRD研究了2．25CrMo钢在500和600℃下含氯还原性气氛中的腐蚀行为．结果表明，实验材料在两种温度下均发生了加速腐蚀，并且在外氧化膜／基体界面检测到了氯的存在．合金腐蚀动力学从500℃时的近似抛物线向600℃时的直线转变与氯化物在该温度下的蒸汽压有关．讨论了材料发生加速腐蚀的机制．