Analysis of a Triple-Effect Low Temperature Distillation Desalination Process

Article Preview

Abstract:

A new process of low temperature triple-effect distillation desalination is designed. Firstly, the appropriate effect number is determined. The total heat transfer coefficients and the heat loads of each evaporator are calculated. When the pressure differences between near effects are equal to △P, the freshwater outputs and the heat transfer coefficients of every effect would be increased as △P improved; if △P is too low, the seawater un-evaporated in the last evaporator would be difficult to flow into the next one. By analysis, the appropriate value of △P is 0.005 MPa. If the seawater flowing into the first effect is preheated by the heat source flow outpouring the unit, the total heat utilization rate and the freshwater output would be enhanced.

You might also be interested in these eBooks

Info:

Periodical:

Advanced Materials Research (Volumes 204-210)

Pages:

2001-2006

Citation:

Online since:

February 2011

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2011 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] Hongfei Zheng, Kaiyan He, Ziqian Chen. Solar Desalinization Technology, Beijing: Beijing   Institute Of Technology Press. (2005), 179-184.

Google Scholar

[2] Dario Breschi. Seawater Distillation from Low-temperature Streams: A case history. Desalination, V122 . (1999), 247-254.

DOI: 10.1016/s0011-9164(99)00045-4

Google Scholar

[3] Jianhua Yin, Qingchun Lv, Guoling Ruan. Low Temperature Multiple-Effect Distillation for Seawater Desalination, Sea technology, Vol. 21, No. 4. (2002), 23-25.

Google Scholar

[4] Shammiri M, Safar M. Multi-effect Distillation Plants: state of the art[J]. Desalination, Vol. 126. (1999), 45-59.

DOI: 10.1016/s0011-9164(99)00154-x

Google Scholar

[5] Congjie Gao, Guohua Chen. Desalinization Technology, Beijing: Chemistry Industry Press. (2004), 91-106.

Google Scholar

[6] Shichang Wang. Project of Desalinization, Beijing: Chemistry Industry Press. (2003), 30-52.

Google Scholar

[7] Kailu Yu, Qingchun Lv, Guoling Ruan. Progress in Engineering and Technology of Low-temperature Multiple Effect Distillation for Seawater Desalination. CHINA WATER& WASTEWATER. Vol. 24, No. 22. (2008), 82-85.

Google Scholar

[8] R Phi1ip Hammond, David M Eissenberg,Dieter K Emmerman. et a1. Large-scale Seawater Distillation for Southern California [J]. Desalination. (1992), 69-83.

DOI: 10.1016/0011-9164(92)80134-u

Google Scholar

[9] Guoling Ruan, Houjun Feng. Technical Progress in Seawater Desalination Technology at Home and Abroad. CHINA WATER & WASTEWATER. Vol. 24, No. 20. (2008), 86-90.

Google Scholar

[10] Jun Zhuang, Hong Zhang. Heat Pipe Technology and Its Engineering Application. Beijing: Chemical Industry Press. (2006), 1-8.

Google Scholar

[11] [USA] S.W. Ji. Heat Pipe Theory and Application. Beijing: Science Press, (1981).

Google Scholar

[12] Li Xu, Shichang Wang, Yuxin Wang, etc. Heat-transfer Film Coefficients Outside Tube of Falling Film Horizontal-tube evaporator. Journal of Chemical Industry and Engineering. (2004), 19-24.

DOI: 10.1016/j.desal.2004.06.077

Google Scholar

[13] Shiming Yang, Wenquan Tao, Heat Transferring, Higher Education Press. (1980), 321-339.

Google Scholar

[14] Eulalia, Heat Exchanger Design Handbook, Hydrocarbon Processing Press. (1987), chapter 1.

Google Scholar