混合蒸汽在活性炭上的吸附平衡

The XG equation, which is developed by us previously for describing the adsorption equilibrium of pure vapor on activated carbon, is extended to multi-component system. Verified by experimental data, the extended XG equation was found to be more successful in predicting the adsorption equilibrium of vapor mixture on activated carbon than the extended Langmuir equation, the extended BET equation and the ideal adsorbed solution theory (IAST).     

活性炭上CS2与CO2混合气体的吸附模型

利用纯气体的等温吸附数据，研究了303K下CS2与CO2混合气体在活性炭上的等温吸附行为．采用两种混合气体模型方程即扩展的Langmuir修正式和Lewis关系式模拟混合气体的等温吸附，结果显示，分别以纯气体的Langmuir方程和D-R方程为基础的Langmuir修正式和Lewis关系式均能较好地描述混合气体的等温吸附，且误差均小于士5％．混合气体中CS2的吸附量约为COz吸附量的20倍．CS2与CO2混合气体在活性炭上的等温吸附以对CS2的吸附为主．     

活性炭改性及其对SO_2的吸附动力学与吸附平衡研究

在微波改性基础上,分别用KMnO_4、K_2Cr_2O_7和H_2O_2对椰壳活性炭进行氧化改性,采用BET和FTIR分析其表面物理化学性质,进行了吸附实验和吸附模型的研究。结果表明,活性炭改性后,微孔容积减小,平均孔径增大,含氧官能团含量增加;对SO_2的吸附动力学可通过粒内扩散和Bangham动力学模型较好的描述;微波分别与KMnO_4,K_2Cr_2O_7改性样品的吸附平衡能被Freundlich等温吸附模型较好的预测,而Langmuir等温吸附模型能准确预测微波与H_2O_2改性样品的吸附平衡,各样品Freundlich拟合常数n>1,故易于吸附SO_2。实验表明,活性炭改性有助于提高其对SO_2的吸附能力。     

氯化汞水溶液在活性炭上的吸附等温线

测定了氯化汞水溶液在活性炭上的吸附平衡数据。证明氯化汞在液固两相中的平衡关系,可用Langmuir方程式拟合。 文中介绍了该方程式的两方面应用:①用微量氯化汞溶液也能制出合格的氯化汞-活性炭催化剂。②用活性炭脱除废水中氯化汞时所需活性炭的最小用量。     

吸附势理论推算混合气在载铜活性炭上的吸附平衡

本文根据吸附势理论,预测了CO/CO_2和CO/N_2两种二元混合气在载铜活性炭（C/Cu)上的吸附平衡数据,该数据与实测结果的比较表明,上述理论误差较小,并且适用于CO/CO_2这类共沸体系,从而推广了这一理论的应用范围.相应的比较结果还表明,Flory-Huggins空穴溶液模型和负荷比夫联方程均不能描述CO/CO_2的共沸行为.     

二氯乙烷在N型吸附剂上的竞争吸附及吸附平衡研究

在模拟汽油体系中研究了二氯乙烷在N型吸附剂上的竞争吸附及吸附平衡。研究结果表明,汽油中存在的烯烃和芳烃与二氯乙烷之间存在着强烈的竞争吸附,严重影响了N型吸附剂的脱氯性能;二氯乙烷在N型吸附剂上的吸附等温线适合利用Langmuir方程进行拟合,而通过对吸附热力学函数值的估算,表明二氯乙烷在N型吸附剂上的吸附过程为可自发进行的放热过程。     

含水树脂吸附剂在烃-醇二元溶液中的吸附

研究了DOO1和TS -TR树脂在非水烃 -醇溶液中的吸附 ,考察了不同水含量的两种树脂在正丁醇 -正庚烷、乙醇 -正己烷组成的二元混合溶液中的等温吸附特性 ,用NBP -a模型建立了相应的等温吸附数学模型 ,并就树脂水含量对其表面能量非均匀性的影响进行了初步研究 ,用Stieltjes变换法对树脂表面能量非均匀密度函数给出了分析解 .结果表明 ,吸附剂表面能量非均匀性及溶液非理想性是影响等温吸附的重要因素 ,极性的DOO1树脂水含量增加 ,其表面能量非均匀性增强 ,非极性TS -TR树脂水含量变化 ,其表面能量非均匀性也有明显变化 .模型拟合与实验吻合很好     

CO2/CH4在活性炭上吸附与分离的分子模拟

Monte Carlo 模拟(GCMC)研究了CO2和CH4在活性炭中的吸附情况.氢气和二氧化碳分子被模拟作Kennard-Jones球体,活性炭用一个裂缝气孔模型代替.研究了压力、温度、孔径活性炭对CO2(以CH4为基准)的选择性的影响.结果表明,低压、低温、孔径越小,选择性越大,即对分离CO2和CH4有利;233 K、孔径为2.29 nm以及低压下选择性达到10,此时分离效果较好.     

Zn2+和Cd2+在酿酒酵母上的生物吸附平衡

研究了金属离子Zn2+和Cd2+在酿酒酵母上的生物吸附平衡.吸附等温线表明,Zn2+和Cd2+在酵母上的吸附可以用Langmuir方程来描述,Zn2+的最大吸附量qmax为9.66mg/g(0.148mmol/g),Cd2+的最大吸附量qmax为15.36mg/g(0.137mmol/g).当q以mg/g为单位时,两者在酵母上的吸附量大小顺序为Cd2+＞Zn2+.与Cd2+比较,Zn2+在酵母上的吸附力更强,更容易被酵母吸附.酵母作为生物吸附剂可用于处理含Zn2+和Cd2+的废水,适合用于溶液中低浓度Zn2+和Cd2+的去除.     

基于沸石ZSM-5的CH4/N2/CO2二元体系吸附平衡

采用Rubotherm磁悬浮天平测量CH₄、N₂和CO₂在沸石ZSM-5上的单组分吸附平衡等温线,温度273～353 K,压力0～500 kPa。采用Sips模型、Toth模型和MSL模型对单组分吸附平衡实验数据进行拟合,拟合结果良好,非线性回归得到相应的模型参数。测量双组分CO₂/N₂、CO₂/CH₄和CH₄/N₂在沸石ZSM-5上的竞争吸附平衡等温线,实验温度为293 K,实验压力为0～500 kPa。采用基于Sips模型的理想吸附溶液理论和双组分MSL模型预测双组分气体在沸石ZSM-5上的竞争吸附平衡等温线,并与实验结果进行比较,预测结果良好。比较CO₂/N₂、CO₂/CH₄以及CH₄/N₂体系在沸石ZSM-5上的竞争吸附选择性系数,探究沸石ZSM-5吸附分离烟道气（CO₂/N₂体系）、垃圾填埋气（CO₂/CH₄体系）或煤层气（CH₄/N₂体系）的可行性,为将来进行工艺设计提供基础数据。     

ZL50活性炭吸附脱除二氧化硫的吸附动力学模型(英文)

A semi-empirical adsorption kinetic model was proposed with the time compensation method to describe the chemisorption of SO2 in flue gas by carbon adsorbents for flue gas purification. The change in adsorption capacity and adsorption rate with time at different water vapor concentrations and different SO2 concentrations was studied. The model was in good agreement with experimental data. The surface reaction was probably the rate controlling step in the early stage for SO2 adsorption by ZL50 activated carbon. The parameters m and n in the nth order adsorption kinetic model were related to the magnitude of the time compensation and adsorption driving force, respectively. The change of parameter n with water vapor concentrations and sulfur dioxide concentrations was studied and some physical implications were given. The sum of square errors was less than 1.0 and the average absolute percentage deviations ranged from 0.5 to 3.2. The kinetic model was compared with other models in the literature.     

Separation of He/N2/CH4 ternary mixtures by a triple-reflux pressure swing adsorption process

Conventional pressure swing adsorption (PSA) processes can only produce one high purity product in a single stage, whereas the state-of-art dual-reflux PSA (DR-PSA) can produce two high purity products simultaneously. However, multicomponent gas separation is often required in the industry, targeting at recovering several valued products at the same time. In this study, we propose a novel adsorption process, namely triple-reflux PSA (TR-PSA), to separate three components simultaneously. A middle product outlet and a middle reflux stream were introduced to the adsorption columns of a conventional DR-PSA process to separate ternary mixtures of nitrogen, methane, and helium. Nonisothermal dynamic models were built to investigate the impacts of operating parameters particularly the location of the middle reflux/product stream and the middle reflux flow rates. Results showed that the TR-PSA process successfully separated ternary mixtures obtaining three enriched products simultaneously in a single stage, yielding a separation performance comparable to that of the double-stage DR-PSA with significantly lower capital and energy cost.     

CH4, C2H6, and C2H4 Phase Equilibria on SAPO-34 Using the Vacancy Solution Theory

Adsorption data of single, binary, and ternary mixtures of methane, ethane, and ethylene on Silicoalumina-Phosphate molecular Sieve (SAPO-34) were obtained experimentally in the pressure range of 0 to 600 kPa at 303, 313, and 323 K. The adsorbed equilibrium concentration was predicted based on the vacancy solution theory (VST) using excess Gibbs energy (EGE) models of activity coefficients. EGE models were studied comparatively, i.e., the Wilson, Flory Huggins, and NRTL equations. The VSM-model results were compared with the mixture adsorption data. The results revealed higher capability of EGE models against the extended Langmuir equation in predicting adsorption behavior of the so-called gas mixture.     

CH4/C2H6/C3H8在MOF-505@5GO上吸附相平衡和选择性

应用溶剂热法合成了不同氧化石墨烯（GO）负载量的MOF-505@GO复合材料,分别采用全自动表面积吸附仪、P-XRD、SEM和Raman对材料进行了性能表征,测定了CH₄、C₂H₆和C₃H₈在MOF-505@GO上的吸附等温线,并进行Langmuir-Freundlich方程拟合,依据IAST理论模型计算了C₂H₆/CH₄和C₃H₈/CH₄二元混合气在MOF-505@5GO上的吸附选择性。研究结果表明,随着GO负载量增大,MOF-505@GO复合材料的孔容及BET比表面积先增大后减小,当GO负载量为5%（质量）时,复合材料MOF-505@5GO的孔容及BET比表面积达到最大,当GO负载量进一步增大至8%（质量）和10%（质量）时,复合材料的孔容及BET比表面积逐渐降低。在0.1 MPa和298 K条件下,MOF-505@5GO对CH₄、C₂H₆和C₃H₈的吸附容量分别为0.88、4.81和5.17 mmol·g^-1,相比MOF-505分别提高了14.9%、30.7%和13.1%。MOF-505@5GO对C₂H₆/CH₄和C₃H₈/CH₄的吸附选择性分别为40.1和3056.1,其对C₂H₆/CH₄和C₃H₈/CH₄具有极高的吸附选择性。     

Adsorption of H2, CO2, CH4, CO,N2 and H2O in Activated Carbon and Zeolite for Hydrogen Production

Abstract

The design of a layered pressure swing adsorption unit to treat a specified off-gas stream is based on the properties of the adsorbent materials. In this work we provide adsorption equilibrium and kinetics of the pure gases in a SMR off-gas: H₂O, CO₂, CH₄, CO, N₂, and H₂ on two different adsorbents: activated carbon and zeolite. Data were measured gravimetrically at 303–343 K and 0–7 bar. Water adsorption was only measured in the activated carbon at 303 K and kinetics was evaluated by measuring a breakthrough curve with high relative humidity.     

水中丙酮在活性炭上吸附平衡与动力学研究

研究了水中丙酮在活性炭上的吸附平衡与动力学曲线,对在20、30、40℃下的吸附等温线用Freundich方程拟合,得出了满意的结果。选择合适的实验条件,在消除了外膜阻力的条件下,表明颗粒内扩散中的表面扩散占主要地位,考察了初始浓度、温度、活性炭粒径等因素对丙酮吸附的影响,并用间歇搅拌槽吸附的表面扩散模型拟合出扩散时间常数。     

螯合树脂对有机胺脱硫液中Fe2+的吸附平衡

研究了4种螯合型树脂对有机胺脱硫液中Fe2+的吸附及解吸特性,发现D751型螯合树脂具有较高的吸附选择性和良好的脱附性能,采用静态吸附实验研究了D751型螯合树脂对Fe2+的吸附平衡,并用红外光谱的方法探讨了树脂吸附Fe2+的机理。结果表明,Langmuir模型和Freundlich模型均能较好地描述D751树脂对Fe2+的吸附行为;吸附自由能变G<0,熵变S>0,吸附为自发的熵增过程,升高温度有利于吸附的进行。红外光谱表明,D751树脂通过离子交换和配位双重作用与Fe2+结合。     

Dynamics adsorption of the enhanced CH4 recovery by CO2 injection

The dynamic adsorption isotherms of CO₂-EGR were measured by using an Intelligent Gravimetric Analysis system. In the initial CO₂ injecting stage, all the injected CO₂ enters into the adsorbent and the mole fraction of CH₄ in the gas phase () is maintained at 1.0. The CH₄ recovery factor () increases. The duration of this stage (t_CD) depends on the selectivity of CO₂ over CH₄ (). An adsorbent with large has long t_CD. In the second stage, the injected CO₂ competes with CH₄ for adsorption. The cumulative of the second stage is much larger than that of the initial stage. However, decreases sharply. in the whole CO₂ injection is always larger than that before CO₂ injection, suggesting that CH₄ desorption results from the displacement of CO₂ rather than from pressure depletion.