A phase model for the gas–liquid equilibria in the ammonia–carbon dioxide–water–urea system in chemical equilibrium at urea synthesis conditions. II. Experimental verification
{"title":"A phase model for the gas–liquid equilibria in the ammonia–carbon dioxide–water–urea system in chemical equilibrium at urea synthesis conditions. II. Experimental verification","authors":"S. Lemkowitz, Eric Vet, P. Berg","doi":"10.1002/JBT.2570270149","DOIUrl":null,"url":null,"abstract":"Bubble- and critical-points in the ammonia–carbon dioxide plane and ammonia–urea system are presented as well as bubble-points in the carbon dioxide–urea system. In order to confirm the form of a previously presented phase model a large number of bubble- and dew-points were measured at various ammonia–carbon dioxide–water–urea compositions (including those most important to the urea industry) in the range of 140 ⩽ T ⩽ 200°C and 15 < P < 400 atm. All of the measurements were carried out under conditions of complete chemical equilibrium. The results are in agreement with the ternary phase model presented in a previous article.","PeriodicalId":15255,"journal":{"name":"Journal of biochemical toxicology","volume":"82 1","pages":"335-348"},"PeriodicalIF":0.0000,"publicationDate":"2007-05-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"4","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of biochemical toxicology","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1002/JBT.2570270149","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 4
Abstract
Bubble- and critical-points in the ammonia–carbon dioxide plane and ammonia–urea system are presented as well as bubble-points in the carbon dioxide–urea system. In order to confirm the form of a previously presented phase model a large number of bubble- and dew-points were measured at various ammonia–carbon dioxide–water–urea compositions (including those most important to the urea industry) in the range of 140 ⩽ T ⩽ 200°C and 15 < P < 400 atm. All of the measurements were carried out under conditions of complete chemical equilibrium. The results are in agreement with the ternary phase model presented in a previous article.