{"id":{"repo_id":"must-thes","oai_identifier":"oai:scholarsmine.mst.edu:doctoral_dissertations-1529"},"canonical_url":"https://search.dev.ndltd.org/etd/must-thes/oai:scholarsmine.mst.edu:doctoral_dissertations-1529","repository":{"repo_id":"must-thes","name":"Missouri University of Science and Technology","base_url":"https://scholarsmine.mst.edu/do/oai/"},"display":{"title":"Experimental vapor-liquid equilibria of propyne with propane, propene and propadiene","abstract":"<p>\"Vapor pressures for pure propane, pure propene, impure propadiene and pure propyne and 19 binary mixtures of propane, propene, and propadiene with propyne are reported at -20, 5, 30, 55 and 80° C. An equation of state utilizing pure component saturated vapor and liquid densities is used to correlate all the data and the effect of the propadiene impurities was theoretically removed. The data of Burcham (1981) are recorrelated using new information about the impurities, and different results are obtained. Calculated relative volatilities and saturated densities are reported for the systems propane-propyne, propene-propyne, propadiene-propyne and propane-propadiene\"-- Abstract, p. ii</p>","abstract_html":"&lt;p&gt;&quot;Vapor pressures for pure propane, pure propene, impure propadiene and pure propyne and 19 binary mixtures of propane, propene, and propadiene with propyne are reported at -20, 5, 30, 55 and 80° C. An equation of state utilizing pure component saturated vapor and liquid densities is used to correlate all the data and the effect of the propadiene impurities was theoretically removed. The data of Burcham (1981) are recorrelated using new information about the impurities, and different results are obtained. Calculated relative volatilities and saturated densities are reported for the systems propane-propyne, propene-propyne, propadiene-propyne and propane-propadiene&quot;-- Abstract, p. ii&lt;/p&gt;","abstract_has_math":false,"creators":["Kyser, Edward Allen"],"institution":"University of Missouri--Rolla","degree_name":"Ph. D. in Chemical Engineering","degree_level":null,"degree_discipline":null,"degree_department":null,"school":null,"contributors":[],"advisors":[],"committee_chairs":[],"committee_members":[],"year":2016,"date_issued":"2016-02-10T08:00:00Z","date_published":"2016-02-10T08:00:00Z","updated_at":"2026-07-24T03:18:18Z","subjects":["Chemical Engineering"],"languages":[],"rights":[],"rights_urls":[],"identifier_entries":[]},"links":{"outbound_url":"https://scholarsmine.mst.edu/doctoral_dissertations/527","outbound_label":"Repository record","outbound_source":"dc:identifier"},"metadata_groups":[{"id":"people","label":"People","entries":[{"key":"dc:creator","label":"Author","values":["Kyser, Edward Allen"]}]},{"id":"academic_context","label":"Academic Context","entries":[{"key":"dc:date.available","label":"Dc Date Available","values":["2016-02-10T08:00:00Z"]},{"key":"dc:type","label":"Dc Type","values":["Dissertation - Open Access"]},{"key":"thesis:degree_name","label":"Degree Name","values":["Ph. D. in Chemical Engineering"]},{"key":"thesis:institution_name","label":"Thesis Institution Name","values":["University of Missouri--Rolla"]}]},{"id":"subjects_keywords","label":"Subjects and Keywords","entries":[{"key":"dc:subject","label":"Dc Subject","values":["Chemical Engineering"]}]},{"id":"identifiers","label":"Identifiers","entries":[{"key":"dc:identifier","label":"Identifier","values":["https://scholarsmine.mst.edu/doctoral_dissertations/527"]}]},{"id":"additional","label":"Additional Metadata","entries":[{"key":"dc:description.abstract","label":"Abstract","values":["<p>\"Vapor pressures for pure propane, pure propene, impure propadiene and pure propyne and 19 binary mixtures of propane, propene, and propadiene with propyne are reported at -20, 5, 30, 55 and 80° C. An equation of state utilizing pure component saturated vapor and liquid densities is used to correlate all the data and the effect of the propadiene impurities was theoretically removed. The data of Burcham (1981) are recorrelated using new information about the impurities, and different results are obtained. Calculated relative volatilities and saturated densities are reported for the systems propane-propyne, propene-propyne, propadiene-propyne and propane-propadiene\"-- Abstract, p. ii</p>"]},{"key":"dc:title","label":"Title","values":["Experimental vapor-liquid equilibria of propyne with propane, propene and propadiene"]}]}],"canonical_facts":{"dc:creator":["Kyser, Edward Allen"],"dc:date.available":["2016-02-10T08:00:00Z"],"dc:description.abstract":["<p>\"Vapor pressures for pure propane, pure propene, impure propadiene and pure propyne and 19 binary mixtures of propane, propene, and propadiene with propyne are reported at -20, 5, 30, 55 and 80° C. An equation of state utilizing pure component saturated vapor and liquid densities is used to correlate all the data and the effect of the propadiene impurities was theoretically removed. The data of Burcham (1981) are recorrelated using new information about the impurities, and different results are obtained. Calculated relative volatilities and saturated densities are reported for the systems propane-propyne, propene-propyne, propadiene-propyne and propane-propadiene\"-- Abstract, p. ii</p>"],"dc:identifier":["https://scholarsmine.mst.edu/doctoral_dissertations/527"],"dc:subject":["Chemical Engineering"],"dc:title":["Experimental vapor-liquid equilibria of propyne with propane, propene and propadiene"],"dc:type":["Dissertation - Open Access"],"thesis:degree_name":["Ph. D. in Chemical Engineering"],"thesis:institution_name":["University of Missouri--Rolla"]},"updated_at":"2026-07-24T03:18:18Z"}