串并联综合型双气头甲醇电力联产系统集成研究

多产品联产和多能源互补，已成为能源动力系统可持续发展的主要趋势与特征。文章基于联产概念和双气头互补思路，提出PSA法预分离氢气与利用合成煤气高温显热作为重整热的低能耗焦炉煤气重整、和双气头混合手段实现低能耗调整CO／H2组分的机制与方法，并采取甲烷适度重整和甲醇合成适度循环的优化整合原则，构建了一类串并联综合型双气头整...     

焦炉煤气二氧化碳重整制合成气中La0.6Sr0.4NixCo1-xO3钙钛矿催化剂的合成、表征和催化性能研究

采用溶胶凝胶法制备了La0.6Sr0.4NixCo1-xO3钙钛矿催化剂,并测试了该催化剂在焦炉煤气CO2重整反应中的性能.通过X射线衍射、N2吸附脱附、程序升温还原、扫描电镜、透射电镜和热重-微分扫描量热等方法对催化剂进行了表征.结果表明,溶胶凝胶法合成的La0.6Sr0.4NixCo1-xO3催化剂形成了钙钛矿结构的固溶体.着重考察了钙钛矿催化剂焙烧温度和A位Ni的掺杂含量对其催化性能和反应后积碳的影响.结果表明： La0.6Sr0.4NixCo1-xO3钙钛矿催化剂在反应中生成了活性金属Ni, Co颗粒和La2O2CO3,这些组分对催化剂的活性和稳定性起关键性的作用,并且能够抑制积碳的形成;焦炉煤气中的富氢气体具有抑制甲烷裂解反应发生的作用,从而减少催化剂的积碳.     

Hydrogen production from simulated hot coke oven gas by catalytic reforming over Ni/Mg（Al）O catalysts

Hydrogen production by catalytic reforming of simulated hot coke oven gas (HCOG) with toluene as a model tar compound was investigated in a fixed bed reactor over Ni/Mg(Al)O catalysts. The catalysts were prepared by a homogeneous precipitation method using urea hydrolysis and characterized by ICP, BET, XRD, TPR, TEM and TG. XRD showed that the hydrotalcite type precursor after calcination formed (Ni, Mg)Al₂O₄ spinel and Ni-Mg-O solid solution structure. TPR results suggested that the increase in Ni/Mg molar ratio gave rise to the decrease in the reduction temperature of Ni²⁺ to Ni⁰ on Ni/Mg(Al)O catalysts. The reaction results indicated that toluene and CH₄ could completely be converted to H₂ and CO in the catalytic reforming of the simulated HCOG under atmospheric pressure and the amount of H₂ in the reaction effluent gas was about 4 times more than that in original HCOG. The catalysts with lower Ni/Mg molar ratio showed better catalytic activity and resistance to coking, which may become promising catalysts in the catalytic reforming of HCOG.     

炼焦过程氧化铅高温焦炉煤气均相脱硫的研究

考察了焦煤中少量氧化铅添加剂对炼焦过程高温焦炉煤气硫化氢浓度以及对焦炭质量的影响。实验表明，煤中添加少量的氧化铅，可以达到焦炉粗煤气脱硫的目的，并且对焦炭的质量影响很小。针对实验所用的煤种，相当于焦煤质量的0.6％的氧化铅添加量在炼焦前期具有最佳的抑制硫释放的效果。炼焦后期，半焦中的硫化铅分解或铅转变为气态铅。气态铅和硫化氢在离开炼焦室时，由于煤气降低温度，又生成硫化铅。从而实现均相脱硫。焦炭中超过一半的铅可以挥发出去。在炼焦收缩阶段，半焦中过多的铅的存在不利于硫化铅的分解。