2016
DOI: 10.1007/s10450-016-9846-1
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Equilibrium and kinetics of adsorption of high molecular weight n-paraffins on a calcium LTA molecular sieve

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Cited by 11 publications
(3 citation statements)
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“…These trends were opposing, thus indicating the possibility of obtaining different products depending on the process arrangement. Similar observations were made later on different type X and Y zeolites [223] and on 5A zeolite [224]. The effects of material polarity (Si/Al ratio) and pore size on adsorption have been studied as well on a range of materials [52,225].…”
Section: Linear From Branched Hydrocarbonssupporting
confidence: 65%
“…These trends were opposing, thus indicating the possibility of obtaining different products depending on the process arrangement. Similar observations were made later on different type X and Y zeolites [223] and on 5A zeolite [224]. The effects of material polarity (Si/Al ratio) and pore size on adsorption have been studied as well on a range of materials [52,225].…”
Section: Linear From Branched Hydrocarbonssupporting
confidence: 65%
“…Due to equilibrium limitations, low temperatures are needed in order to minimize hydrocracking. ,, A strategy which prevents hydrocracking from taking place and thus increases the yield and productivity of the unit includes separation of the branched products from the effluent and recycling of the linear and monobranched hydrocarbons to the head of the unit. , The separation of linear from branched isomers is done by adsorption using zeolite 5A as the adsorbent. This zeolite has been implemented in liquid- (SMB) and vapor-phase (VSA/TSA) hydrocarbon separation processes since the 1960s. ,,,− In fact, molecular sieving separations of linear and branched paraffins were one of the first major industrial successes of zeolites. ,,, Other zeolites, such as X, Y, and ZSM-5, have been commercialized for this purpose, as well.…”
Section: Chemical Separations By Zeolitesmentioning
confidence: 99%
“…Alkandary et al reported that for a liquid mixture of linear paraffins with isooctane (iC8), the adsorption equilibrium of C12–C20 n -alkanes in the 5A zeolite at room temperature (RT) is established after several dozen hours. In another work, Águeda et al studied the adsorption equilibrium and kinetics of n C5, n C10, n C14, and n C18 mixed with iC8 in Ca-LTA, reporting the highest sorption capacity for n C10 and the highest affinity for n C14. Silva and Rodriguez , obtained type I adsorption isotherms of n C5 and n C6 in pellets of zeolite 5A at a temperature of 373 K or higher.…”
Section: Introductionmentioning
confidence: 99%