Evaluation of the column components size on the vapour enrichment and system performance in small power NH3-H2O absorption refrigeration machines

被引:14
作者
Sieres, Jaime [1 ]
Fernandez-Seara, Joes [1 ]
机构
[1] Univ Vigo, Escuela Tecn Super Ingn Ind, Area Maquinas & Motores Term, Vigo 36200, Spain
来源
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID | 2006年 / 29卷 / 04期
关键词
absorption system; ammonia-water; survey; component; distillation; performance; concentration; vapour;
D O I
10.1016/j.ijrefrig.2005.10.004
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper presents an analysis of the influence of the distillation column components size on the vapour enrichment and system performance in small power NH3-H2O absorption machines with partial condensation. It is known that ammonia enrichment is required in this type of systems; otherwise water accumulates in the evaporator and strongly deteriorates the system performance and efficiency. The distillation column analysed consists of a stripping adiabatic section below the column feed point and an adiabatic rectifying packed section over it. The partial condensation of the vapour is produced at the top of the column by means of a heat integrated rectifier with the strong solution as coolant and a water cooled rectifier. Differential mathematical models based on mass and energy balances and heat and mass transfer equations have been developed for each one of the column sections and rectifiers, which allow defining their real dimensions. Results are shown for a given practical application. Specific geometric dimensions of the column components are considered. Different distillation column configurations are analysed by selecting and discarding the use of the possible components of the column and by changing their dimensions. The analysis and comparison of the different column arrangements has been based on the system COP and on the column dimensions. (c) 2005 Elsevier Ltd and IIR. All rights reserved.
引用
收藏
页码:579 / 588
页数:10
相关论文
共 22 条
[1]  
[Anonymous], INT J REFRIG
[2]  
[Anonymous], AMMONIA ABSORPTION R
[3]   Mass transfer (absorption) coefficients - Prediction from data on great transfer and fluid friction [J].
Chilton, TH ;
Colburn, AP .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1934, 26 :1183-1187
[4]  
COLBURN AP, 1937, AICHE T, P33
[5]   DESIGN OF ADIABATIC PACKED TOWERS FOR GAS ABSORPTION AND STRIPPING [J].
FEINTUCH, HM ;
TREYBAL, RE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :505-513
[6]   Heat and mass transfer analysis of a helical coil rectifier in an ammonia-water absorption system [J].
Fernández-Seara, J ;
Sieres, J ;
Vázquez, M .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2003, 42 (08) :783-794
[7]   Distillation column configurations in ammonia-water absorption refrigeration systems [J].
Fernández-Seara, J ;
Sieres, J ;
Vázquez, M .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2003, 26 (01) :28-34
[8]   Simultaneous heat and mass transfer of a packed distillation column for ammonia-water absorption refrigeration systems [J].
Fernández-Seara, J ;
Sieres, J ;
Vázquez, M .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2002, 41 (10) :927-935
[9]  
FERNANDEZSEARA J, 2002, C ESP CIENC TECN FRI
[10]  
FERNANDEZSEARA J, 2003, 2 INT C HEAT TRANSF