共查询到19条相似文献,搜索用时 125 毫秒
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低挥发性有机物脱附活化能估算模型 总被引:1,自引:0,他引:1
提出了一种新的低挥发性有机物程序升温脱附(TPD)活化能估算模型.与经典 TPD 模型相比,所提出的新的 TPD理论模型不仅考虑了脱附过程中存在的吸附质分子再吸附现象的影响,而且还考虑了脱附分子在吸附剂孔内扩散的影响.通过 TPD 实验,运用所建立的活化能估算模型,技术测定了二苯并呋喃在 Norit RB1、Monolith 和 Chemviron三种活性炭上的脱附活化能.结果表明经典TPD 模型所估算出来的二苯并呋喃的活化能要比非线性 TPD 模型估算结果偏高约8.2%~9.6%,这表明脱附过程中存在吸附质分子再吸附现象和内扩散过程对脱附活化能有一定的影响. 相似文献
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《化工学报》2017,(8)
对3种常见有序介孔碳(OMCs)吸附脱除典型气相多环芳烃——萘进行了研究。分别采用吸附等温线模型(Langmuir、Freundlich、Sips)和恒定浓度波动力学模型对吸附等温线和穿透曲进行拟合分析。采用程序升温脱附法通过失重曲线分析了吸附剂的再生性能。结果表明:Langmuir模型和Sips模型能很好地描述低浓度气相萘在OMCs上的静态吸附行为(R~299%),吸附量呈CMK-5CMK-3FDU-15排列。恒定浓度波动力学模型具有较高的拟合度,介孔促使3种吸附剂对萘分子具有较高的吸附扩散系数。具有微通孔结构的CMK-5和FDU-15表现出更好的再生性能。综合吸脱附动力学分析,CMK-5在3种吸附剂中表现出更好的应用潜能。 相似文献
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对3种常见有序介孔碳(OMCs)吸附脱除典型气相多环芳烃--萘进行了研究。分别采用吸附等温线模型(Langmuir、Freundlich、Sips)和恒定浓度波动力学模型对吸附等温线和穿透曲进行拟合分析。采用程序升温脱附法通过失重曲线分析了吸附剂的再生性能。结果表明:Langmuir模型和Sips模型能很好地描述低浓度气相萘在OMCs上的静态吸附行为(R2 > 99%),吸附量呈CMK-5 > CMK-3 > FDU-15排列。恒定浓度波动力学模型具有较高的拟合度,介孔促使3种吸附剂对萘分子具有较高的吸附扩散系数。具有微通孔结构的CMK-5和FDU-15表现出更好的再生性能。综合吸脱附动力学分析,CMK-5在3种吸附剂中表现出更好的应用潜能。 相似文献
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采用磁性树脂和活性炭混合吸附剂对腐殖酸(HA)进行吸附,研究不同质量比混合吸附剂对HA的吸附,利用吸附动力学、吸附等温线和动态吸附脱附实验对树脂吸附、脱附过程进行分析。结果表明,当磁性树脂和活性炭的质量比为9:1时,混合吸附剂对HA的吸附容量最高,吸附过程符合准2级动力学模型。混合吸附剂对HA的吸附等温线更适合Langmuir模型,25℃时拟合饱和吸附量可达135.1 mg/g。动态吸附过程中,混合填柱固定床对HA的吸附要优于分层填柱,体积比1:1质量分数10%的NaOH、质量分数10%的NaCl对2种吸附固定床能快速脱附。 相似文献
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以吸附过程本征动力学模型为基础,提出了一种新的TPD非线性活化能估算模型.与经典TPD模型相比,这种新的TPD理论模型考虑了脱附过程中存在的吸附质分子再吸附现象的影响,更接近实际的脱附过程.采用TPD实验技术测定了二苯并呋喃在Norit RB1、Monolith和Chemviron 3种活性炭上、不同升温速率下的程序升温脱附图谱.以这些TPD图谱为基础,分别采用经典TPD模型和TPD非线性模型计算了二苯并呋喃在3种活性炭上的脱附活化能.结果表明,经典TPD模型所估算出来的二苯并呋喃的活化能要偏高TPD非线性模型估算结果约8%~12%,脱附过程中存在吸附质分子再吸附现象对脱附活化能有较大的影响. 相似文献
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主要研究应用微波辐射再生高聚物吸附树脂.论述了微波加热的优点和微波脱附的原理,以乙醇为吸附质研究了吸附和微波辐射再生吸附剂过程.进行了正流微波辐射脱附和逆流微波辐射脱附实验,测定了微波脱附流出曲线和床层的温升曲线,并与传统的热脱附流出曲线和在不同加热速率下得到的床层温升曲线进行比较.实验结果表明:微波脱附比热脱附脱附速度更快,效率更高;高聚物吸附树脂类吸附剂对微波是半透明的,它对微波的吸收能力随着温度的升高而下降,因此,在微波辐射下,吸附剂床层吸收微波的能力也随着床层温度的升高和吸附质的脱附而减弱,床层最终温度不超过84℃,可使吸附剂的结构和性能不会被破坏和受影响,这有利于吸附剂的循环使用.微波在脱附和吸附剂再生中有很好的应用前景. 相似文献
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Spencer D. Miller Vladimir V. Pushkarev Andrew J. Gellman John R. Kitchin 《Topics in Catalysis》2014,57(1-4):106-117
The dissociative adsorption energy of oxygen on Pt(111) is known to be coverage dependent. Simple Redhead analysis of temperature programmed desorption (TPD) experiments that assumes a coverage independent desorption barrier can lead to errors in estimated properties such as desorption barriers and adsorption energies. A simple correction is to assume a linear coverage dependence of the desorption barrier, but there is usually no formal justification given for that functional form. More advanced TPD analysis methods that are suitable for determining coverage dependent adsorption parameters are limited by their need for large amounts of high quality, low noise data. We present a method to estimate the functional form of the coverage dependent desorption barrier from density functional theory calculations for use in analysis of TPD spectra. Density functional theory was employed to calculate the coverage dependence of the adsorption energy. Simulated TPD spectra were then produced by empirically scaling the DFT based adsorption energies utilizing the Brønstead–Evans–Polyani relationship between adsorption energies and desorption barriers. The resulting simulated spectra show better agreement with the experimental spectra than spectra predicted using barriers that are either coverage-independent or simply linearly dependent on coverage. The empirically derived scaling of the desorption barriers for Pt(111) is shown to be useful in predicting the low coverage desorption barriers for oxygen desorption from other metal surfaces, which showed reasonable agreement with the reported experimental values for those other metals. 相似文献
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Ali Izadbakhsh Fatholah Farhadi Farhad Khorasheh Zi-Feng Yan 《Journal of Porous Materials》2009,16(5):599-603
Comparison of the traditional linear heating method of TPD with an original stepwise heating scheme was reported for the first time. Stepwise heating TPD was carried out by keeping the temperature constant as soon as ammonia desorption signal rises until the signal returns to the baseline. More ammonia desorption peaks on a SAPO-34 catalyst were identified using TPD with stepwise heating. The effect of temperature ramp on desorption peak broadening in TPD curve was also addressed. The more distinct ammonia desorption peaks in stepwise TPD indicates that ammonia adsorbs in about five or six different ways on SAPO-34, and attribution of different adsorptions may be explained considering some known features of SAPO’s acidity; including adsorption on the bridge hydroxyl groups Brønsted acid sites with different acid strength resulting from different silicon environment of SAPO molecular sieves, adsorption on terminal hydroxyl groups Brønsted acid sites, and by multiple adsorption of ammonia on acid sites. 相似文献
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abstract The heterogeneity of adsorption sites and adsorption kinetics of n-hexane on a chromium terephthalate-based metal-organic framework MIL-101(Cr) were studied by gravimetric method and temperatu... 相似文献
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TPD studies of n-hexane and n-heptane from NaX, Y and ZSM-5 (Na+ or H+ exchanged) in the experimental system with a TCD detector were performed, using pure He or He/n-alkane mixture as a carrier gas. The TPD profiles with one desorption peak for Y and two peaks for ZSM-5, measured using
He/hydrocarbon mixture, were similar to the previously reported equilibrated thermodesorption results. TPD profiles were accurately
fitted with a model based on the equilibrium control of the desorption and the adsorption functions derived from the Langmuir
or dual site Langmuir isotherms. 相似文献
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YU Moxin LI Zhong XI Hongxia XIA Qibin WANG Shuwen 《Frontiers of Chemical Science and Engineering》2008,2(3):269
In this work, the effect of the textural property of activated carbons on desorption activation energy and adsorption capacity for benzothiophene (BT) was investigated. BET surface areas and the textural parameters of three kinds of the activated carbons, namely SY-6, SY-13 and SY-19, were measured with an ASAP 2010 instrument. The desorption activation energies of BT on the activated carbons were determined by temperature-programmed desorption (TPD). Static adsorption experiments were carried out to determine the isotherms of BT on the activated carbons. The influence of the textural property of the activated carbons on desorption activation energy and the adsorption capacity for BT was discussed. Results showed that the BET surface areas of the activated carbons, SY-6, SY-13 and SY-19 were 1106, 1070 and 689 m2g-1, respectively, and their average pore diameters were 1.96, 2.58 and 2.16 nm, respectively. The TPD results indicated that the desorption activation energy of BT on the activated carbons, SY-6, SY-19 and SY-13 were 58.84, 53.02 and 42.57 KJ/mol, respectively. The isotherms showed that the amount of BT adsorbed on the activated carbons followed the order of SY-6 > SY-19 > SY-13. The smaller the average pore diameter of the activated carbon, the stronger its adsorption for BT and the higher the activation energy required for BT desorption on its surface. The Freundlich adsorption isotherm model can be properly used to formulate the adsorption behavior of BT on the activated carbons. 相似文献
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M. Huuhtanen T. Määttä K. Rahkamaa-Tolonen T. Maunula R.L. Keiski 《Topics in Catalysis》2004,(1):359-363
Adsorption and desorption of NO and propene on pure and platinum-loaded ZSM-5, Beta, Y and Ferrierite zeolites have been studied by FTIR and temperature programmed desorption (TPD). Platinum-loaded ZSM-5 and Beta are found to have a good adsorption capacity for hydrocarbons and NO at low temperatures. HC-SCR on Pt-zeolites is a promising NO abatement method. 相似文献
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《Catalysis Today》1994,20(3):367-380
The water-gas shift reaction has been investigated by the temperature-programmed desorption (TPD) of reaction components over a commercial low-temperature catalyst. It has been found that the oxidation state (and consequently the activity) of the catalyst is strongly influenced by the composition of the gaseous mixture. The adsorption capacity of catalysts decreases in the order: H2O CO2CO; hydrogen does not adsorb. The existence of two types of sites for carbon oxides adsorption has been found experimentally. A further type of storage (inactive) sites for water exists. On the basis of experimental results, model equations for TPD of H2O, CO2 and CO were derived. Models best fitting the experimental data were based on the assumption of a non-uniform heterogeneous surface of the catalyst. 相似文献