{"id":{"repo_id":"uoit","oai_identifier":"oai:ontariotechu.scholaris.ca:10155/925"},"canonical_url":"https://search.dev.ndltd.org/etd/uoit/oai:ontariotechu.scholaris.ca:10155/925","repository":{"repo_id":"uoit","name":"Ontario Institute of Technology","base_url":"https://ontariotechu.scholaris.ca/server/oai/request"},"display":{"title":"Thermal management of the thermochemical Cu-Cl cycle linked with industrial processes for hydrogen production","abstract":"This thesis study develops, analyzes and evaluates three integrated systems using process heats available in industrial applications for hydrogen production via copper-chlorine (Cu-Cl) cycle. The first system consists of single- and multi-stage reheat Rankine cycles, a four-step thermochemical Cu-Cl cycle, and a hydrogen compression system. Systems 2 consists of a thermochemical four-step hydrogen production Cu-Cl cycle, a hydrogen compression system and a multi-stage reheat Rankine cycle. System 3 contains single- and multi-stage reheat Rankine cycles, a thermochemical hydrogen production Cu-Cl cycle, a hydrogen compression system and a reverse osmosis desalination unit. Both Aspen Plus and Engineering Equation Solver software packages are employed for system analysis, modeling and performance assessment. The overall system energy and exergy efficiencies are found to be 39.8% and 40.5% for the first system, 32.7% and 32% for the second system, and 48.6% and 40.2% for the third system.","abstract_html":"This thesis study develops, analyzes and evaluates three integrated systems using process heats available in industrial applications for hydrogen production via copper-chlorine (Cu-Cl) cycle. The first system consists of single- and multi-stage reheat Rankine cycles, a four-step thermochemical Cu-Cl cycle, and a hydrogen compression system. Systems 2 consists of a thermochemical four-step hydrogen production Cu-Cl cycle, a hydrogen compression system and a multi-stage reheat Rankine cycle. System 3 contains single- and multi-stage reheat Rankine cycles, a thermochemical hydrogen production Cu-Cl cycle, a hydrogen compression system and a reverse osmosis desalination unit. Both Aspen Plus and Engineering Equation Solver software packages are employed for system analysis, modeling and performance assessment. The overall system energy and exergy efficiencies are found to be 39.8% and 40.5% for the first system, 32.7% and 32% for the second system, and 48.6% and 40.2% for the third system.","abstract_has_math":false,"creators":["Ishaq, Haris"],"institution":"University of Ontario Institute of Technology","degree_name":"Master of Applied Science (MASc)","degree_level":null,"degree_discipline":"Mechanical Engineering","degree_department":null,"school":null,"contributors":[],"advisors":["Dincer, Ibrahim"],"committee_chairs":[],"committee_members":[],"year":2018,"date_issued":"2018-04-01","date_published":"2018-04-01","updated_at":"2026-07-24T05:35:41Z","subjects":["Hydrogen production","Thermal management","Energy conversion","Cu-Cl cycle","Heat recovery"],"languages":["en"],"rights":[],"rights_urls":[],"identifier_entries":[]},"links":{"outbound_url":"https://hdl.handle.net/10155/925","outbound_label":"Handle","outbound_source":"dc:identifier.uri"},"metadata_groups":[{"id":"people","label":"People","entries":[{"key":"dc:contributor.advisor","label":"Advisor","values":["Dincer, Ibrahim"]},{"key":"dc:creator","label":"Author","values":["Ishaq, Haris"]}]},{"id":"academic_context","label":"Academic Context","entries":[{"key":"dc:date.accessioned","label":"Dc Date Accessioned","values":["2018-07-16T14:12:12Z","2022-03-29T16:48:58Z"]},{"key":"dc:date.available","label":"Dc Date Available","values":["2018-07-16T14:12:12Z","2022-03-29T16:48:58Z"]},{"key":"dc:date.issued","label":"Date","values":["2018-04-01"]},{"key":"dc:type","label":"Dc Type","values":["Thesis"]},{"key":"thesis:degree_discipline","label":"Discipline","values":["Mechanical Engineering"]},{"key":"thesis:degree_name","label":"Degree Name","values":["Master of Applied Science (MASc)"]},{"key":"thesis:institution_name","label":"Thesis Institution Name","values":["University of Ontario Institute of Technology"]}]},{"id":"subjects_keywords","label":"Subjects and Keywords","entries":[{"key":"dc:subject","label":"Dc Subject","values":["Hydrogen production","Thermal management","Energy conversion","Cu-Cl cycle","Heat recovery"]}]},{"id":"language_rights","label":"Language and Rights","entries":[{"key":"dc:language.iso","label":"Language (ISO)","values":["en"]}]},{"id":"identifiers","label":"Identifiers","entries":[{"key":"dc:identifier.uri","label":"Identifier URI","values":["https://hdl.handle.net/10155/925"]}]},{"id":"additional","label":"Additional Metadata","entries":[{"key":"dc:description.abstract","label":"Abstract","values":["This thesis study develops, analyzes and evaluates three integrated systems using process heats available in industrial applications for hydrogen production via copper-chlorine (Cu-Cl) cycle. The first system consists of single- and multi-stage reheat Rankine cycles, a four-step thermochemical Cu-Cl cycle, and a hydrogen compression system. Systems 2 consists of a thermochemical four-step hydrogen production Cu-Cl cycle, a hydrogen compression system and a multi-stage reheat Rankine cycle. System 3 contains single- and multi-stage reheat Rankine cycles, a thermochemical hydrogen production Cu-Cl cycle, a hydrogen compression system and a reverse osmosis desalination unit. Both Aspen Plus and Engineering Equation Solver software packages are employed for system analysis, modeling and performance assessment. The overall system energy and exergy efficiencies are found to be 39.8% and 40.5% for the first system, 32.7% and 32% for the second system, and 48.6% and 40.2% for the third system."]},{"key":"dc:title","label":"Title","values":["Thermal management of the thermochemical Cu-Cl cycle linked with industrial processes for hydrogen production"]}]}],"canonical_facts":{"dc:contributor.advisor":["Dincer, Ibrahim"],"dc:creator":["Ishaq, Haris"],"dc:date.accessioned":["2018-07-16T14:12:12Z","2022-03-29T16:48:58Z"],"dc:date.available":["2018-07-16T14:12:12Z","2022-03-29T16:48:58Z"],"dc:date.issued":["2018-04-01"],"dc:description.abstract":["This thesis study develops, analyzes and evaluates three integrated systems using process heats available in industrial applications for hydrogen production via copper-chlorine (Cu-Cl) cycle. The first system consists of single- and multi-stage reheat Rankine cycles, a four-step thermochemical Cu-Cl cycle, and a hydrogen compression system. Systems 2 consists of a thermochemical four-step hydrogen production Cu-Cl cycle, a hydrogen compression system and a multi-stage reheat Rankine cycle. System 3 contains single- and multi-stage reheat Rankine cycles, a thermochemical hydrogen production Cu-Cl cycle, a hydrogen compression system and a reverse osmosis desalination unit. Both Aspen Plus and Engineering Equation Solver software packages are employed for system analysis, modeling and performance assessment. The overall system energy and exergy efficiencies are found to be 39.8% and 40.5% for the first system, 32.7% and 32% for the second system, and 48.6% and 40.2% for the third system."],"dc:identifier.uri":["https://hdl.handle.net/10155/925"],"dc:language.iso":["en"],"dc:subject":["Hydrogen production","Thermal management","Energy conversion","Cu-Cl cycle","Heat recovery"],"dc:title":["Thermal management of the thermochemical Cu-Cl cycle linked with industrial processes for hydrogen production"],"dc:type":["Thesis"],"thesis:degree_discipline":["Mechanical Engineering"],"thesis:degree_name":["Master of Applied Science (MASc)"],"thesis:institution_name":["University of Ontario Institute of Technology"]},"updated_at":"2026-07-24T05:35:41Z"}