石油化工
石油化工
석유화공
PETROCHEMICAL TECHNOLOGY
2001年
2期
121-125
,共5页
吸附分离%对二氯苯%疏水MFI沸石%无粘接剂吸附剂
吸附分離%對二氯苯%疏水MFI沸石%無粘接劑吸附劑
흡부분리%대이록분%소수MFI비석%무점접제흡부제
在无粘结剂疏水硅沸石S-Ⅰ吸附剂上研究混合二氯苯液相吸附平衡。对二氯苯对邻二氯苯的选择吸附分离系数为12.3。筛选出五种与吸附剂相匹配的脱附剂:苯、甲苯、乙苯、一氯苯、对二乙苯。二氯苯异构体与脱附剂单组份液相吸附等温线均呈典型的Langmuir吸附,并测得饱和吸附量。对混合二氯苯的液相竞争吸附行为进行了考察。S-Ⅰ吸附剂不吸附间二氯苯,对二氯苯对邻二甲苯的高选择性与吸附剂的结构特征有关。S-Ⅰ吸附剂在液相吸附分离使用中不需控制水含量,且可活化再生。
在無粘結劑疏水硅沸石S-Ⅰ吸附劑上研究混閤二氯苯液相吸附平衡。對二氯苯對鄰二氯苯的選擇吸附分離繫數為12.3。篩選齣五種與吸附劑相匹配的脫附劑:苯、甲苯、乙苯、一氯苯、對二乙苯。二氯苯異構體與脫附劑單組份液相吸附等溫線均呈典型的Langmuir吸附,併測得飽和吸附量。對混閤二氯苯的液相競爭吸附行為進行瞭攷察。S-Ⅰ吸附劑不吸附間二氯苯,對二氯苯對鄰二甲苯的高選擇性與吸附劑的結構特徵有關。S-Ⅰ吸附劑在液相吸附分離使用中不需控製水含量,且可活化再生。
재무점결제소수규비석S-Ⅰ흡부제상연구혼합이록분액상흡부평형。대이록분대린이록분적선택흡부분리계수위12.3。사선출오충여흡부제상필배적탈부제:분、갑분、을분、일록분、대이을분。이록분이구체여탈부제단조빈액상흡부등온선균정전형적Langmuir흡부,병측득포화흡부량。대혼합이록분적액상경쟁흡부행위진행료고찰。S-Ⅰ흡부제불흡부간이록분,대이록분대린이갑분적고선택성여흡부제적결구특정유관。S-Ⅰ흡부제재액상흡부분리사용중불수공제수함량,차가활화재생。
The static equilibrium of dichlorobenzene mixture in liquid phase was studied with a binder-free MFI zeolite adsorbent,which possesses perfect framework and high hydrophobicity.The selectivity factor for p-dichlorobenzene/o-dichlorobenzene is 12.3.A series of desorbents matched with the adsorbent such as benzene,toluene,ethylbenzene,mono-chlorobenzene,and p-diethylbenzene were investigated as well.The adsorbent can be regenerated and used without controlling the content of water.The isotherms of each dichlorobenzene isomer and the desorbents exhibit the adsorption characteristics of Langmuir type.The saturation adsorption capacities of the adsorbates on the adsorbent S-Ⅰ were determined.No adsorption of m-dichlorobenzene was found.The competitive adsorption curves of multicomponent feed were also explored.The high shape-selectivity of separation is related to the perfect structure of the adsorbent.