机译:CFC替代制冷剂混合物的相平衡:1,1,1,2,3,3,3-七氟丙烷(HFC-227ea)+二氟甲烷(HFC-32),+ 1,1,1,2-四氟乙烷(HFC-134a )和+ 1,1-二氟乙烷(HFC-152a)
Division of Environment and Process Technology Korea Institute of Science and Technology (KIST);
Division of Environment and Process Technology Korea Institute of Science and Technology (KIST);
Division of Environment and Process Technology Korea Institute of Science and Technology (KIST);
Division of Environment and Process Technology Korea Institute of Science and Technology (KIST);
binary mixtures; HFC-227ea; HFC-32; HFC-134a; HFC-152a; Peng–Robinson equation of state; vapor–liquid equilibria; Wong–Sandler mixing rule;
机译:CFC替代制冷剂混合物的相平衡。三氟甲烷(HFC-23)+ 1,1,1,2-四氟乙烷(HFC-134a)和三氟甲烷(HFC-23)+ 1,1,1,2,3,3,3-七氟丙烷(HFC- 227ea)在283.15和293.15 K
机译:评论“ CFC替代制冷剂混合物的相平衡:异丁烷+ 1,1,1,2-四氟乙烷,+ 1,1-二氟乙烷和加二氟甲烷的二元系统”(Lim,JS; Park,J.-Y .; Lee B.-G .; Lee Y.-W .; Kim,J.-DJChem。Eng。D
机译:CFC替代制冷剂混合物的相平衡:异丁烷+ 1,1,1,2-四氟乙烷,+ 1,1-二氟乙烷和加二氟甲烷的二元体系-答复
机译:用于制冷材料的某些替代制冷剂水合物及其混合物的相平衡
机译:“x 1,1,1,2-四氟乙烷(HFC-134a)+(1 - x)三甘醇二甲醚(TriEGDmE)混合物的高压粘度特性的勘误表:测量和建模”Fluid phase Quilibria,247(2006) )70-79