摘要
为综合利用黄磷尾气中的CO,通过钢瓶配气模拟和气相色谱GC-14C测定的方法,研究了酸碱改性碳吸附净化PH3和H2S的相关问题。结果表明:H2S在碱改性碳上平均吸附活化能为23.77 kJ/mol,为负一级吸附反应,PH3在酸改性碳上平均吸附活化能为61.3 kJ/mol,为负二级吸附反应,吸附时以先物理吸附后化学吸附的顺序进行;TG/DTA和孔径分布初步证明吸附质主要为硫和硫氧化物或磷和磷氧化物,酸碱改性碳孔径<1.5 nm的微孔对H2S和PH3的吸附贡献较大,吸附质质量损失主要发生在0—100℃阶段;由机理推导的吸附模型具有很好的可行性。
For the comprehensive utilization of CO in off-gas of yellow phosphorus, chromatography GC-14C and gas stimulation through steel-vase container were used to research adsorbing removal of H:S and PH3 by activated carbon (AC) modified through acid and alkali. The results showed that it was minus first order and 23.77 kJ/mol of average adsorbing activation energy for adsorbing reaction of HES on alkali modified carbon, and minus second order and 61.3 kJ/mol of average adsorbing activation energy for adsorbing reaction of PH3 on acid modified carbon with the order of first physisorption and then chemisorption ; TG/DTA and pore size distribution indicated that main adsorbates were sulfur and sulfur oxides or phosphorus and phosphorus oxides; micropore with radius 〈 1.5 nm made primary contribution for adsorbing removal of H2S and PH3 ; and mass loss of adsorbates occurred mainly in the stage of 0-100℃. A well feasible math model was induced according to mechanism of adsorbing reaction to forecast breakthrough curve.
出处
《化学工程》
EI
CAS
CSCD
北大核心
2007年第7期7-10,18,共5页
Chemical Engineering(China)
基金
'八六三'国家高技术研究发展计划资助项目(2004AA649010)
关键词
改性活性碳
吸附脱除
黄磷尾气
吸附活化能
吸附模型
modified activated carbon
adsorbing removal
off-gas of yellow phosphorus
adsorbing activation energy
adsorbing model