Studies on the Degradation of Desiccants in Temperature Swing Adsorption Processes and the Adsorptive Separation of Sulfur Compounds from Industrial Fluids

dc.contributor.advisorMarriott, Robert A.
dc.contributor.authorJacobs, John Henry
dc.contributor.committeememberShimizu, George Kisa Hayashi
dc.contributor.committeememberThurbide, Kevin B.
dc.contributor.committeememberDolgos, Michelle Renee
dc.contributor.committeememberEic, Mladen
dc.date2023-06
dc.date.accessioned2023-04-14T19:17:51Z
dc.date.available2023-04-14T19:17:51Z
dc.date.issued2023-04-13
dc.description.abstractAdsorptive technologies are essential to the natural gas industry and environmental protection. In natural gas systems, adsorbents remove water, carbon dioxide (CO2), and hydrogen sulfide (H2S) from natural gas through dehydration and sweetening processes. Adsorptive separation also can remove CO2 and sulfur dioxide (SO2) from industrial flue gases. The dehydration of natural gas by adsorption is a standard technology used worldwide. For natural gas wells in remote locations or offshore, adsorptive dehydration is the technology of choice. When the natural gas is to be liquified, dehydration technologies, such as glycol absorption, cannot reduce the water concentrations sufficiently, and adsorptive dehydration must be used. The dehydration units used industrially must operate continuously for several years. The study on desiccant degradation is an essential addition to the field. Nevertheless, little research is available investigating what factors influence desiccant degradation. The most common technology for removing H2S and CO2 from industrial fluids is aqueous alkanolamine absorption. This process is often expensive as the regeneration is energy intensive. Thus, alternative technologies are sought after, such as adsorbents. One of the most promising adsorbents is activated carbon for removing CO2, H2S, and SO2. A custom-built rapid cycling adsorption apparatus was used to test zeolites 4A and 13X, and three different pore-size silica gels to elucidate what factors of industrial dehydration systems would promote or mitigate desiccant degradation. Pure component H2O, methane (CH4), CO2, and H2S adsorption were measured on silica gels and activated carbon. The results from the silica gel adsorption demonstrated that the adsorption of H2O and H2S increased when the concentration of surface silanol groups increased. The adsorption of multi component CH4/CO2/H2S, N2/CO2/SO2, and N2/CO2/SO2/H2O mixtures on activated carbons derived from petroleum coke were collected. It was concluded that the selectivity of H2S/CH4 increased when the surface area decreased, and the H2S/CO2 selectivity increased with the oxygen fraction of the activated carbons. The SO2 adsorption experiments demonstrated a high affinity for SO2 on all of the tested carbons, and the adsorption capacity did not change after wet SO2 exposure for any of the carbons.
dc.identifier.citationJacobs, J. H. (2023). Studies on the degradation of desiccants in temperature swing adsorption processes and the adsorptive separation of sulfur compounds from industrial fluids (Doctoral thesis, University of Calgary, Calgary, Canada). Retrieved from https://prism.ucalgary.ca.
dc.identifier.urihttps://prism.ucalgary.ca/handle/1880/116069
dc.identifier.urihttps://dx.doi.org/10.11575/PRISM/dspace/40915
dc.language.isoen
dc.publisher.facultyGraduate Studies
dc.publisher.institutionUniversity of Calgary
dc.rightsUniversity of Calgary graduate students retain copyright ownership and moral rights for their thesis. You may use this material in any way that is permitted by the Copyright Act or through licensing that has been assigned to the document. For uses that are not allowable under copyright legislation or licensing, you are required to seek permission.
dc.subjectAdsorption
dc.subjectZeolites
dc.subjectSilica gel
dc.subjectActivated carbon
dc.subjectSour gas
dc.subject.classificationChemistry--Physical
dc.titleStudies on the Degradation of Desiccants in Temperature Swing Adsorption Processes and the Adsorptive Separation of Sulfur Compounds from Industrial Fluids
dc.typedoctoral thesis
thesis.degree.disciplineChemistry
thesis.degree.grantorUniversity of Calgary
thesis.degree.nameDoctor of Philosophy (PhD)
ucalgary.thesis.accesssetbystudentI do not require a thesis withhold – my thesis will have open access and can be viewed and downloaded publicly as soon as possible.
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