ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2025 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received October 29, 2010
Accepted August 1, 2011
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

Exergy analysis of two-stage steam-water jet injector

1College of Power Engineering, Chongqing University, Chongqing 400044, China 2Key Laboratory of Low-grade Energy Utilization Technologies and Systems, Ministry of Education, Chongqing University, Chongqing 400044, China
caiqincqu@163.com
Korean Journal of Chemical Engineering, April 2012, 29(4), 513-518(6), 10.1007/s11814-011-0197-z
downloadDownload PDF

Abstract

Exergy analysis is used as a tool to evaluate exergy losses in the steam-water jet injector so as to improve its overall performance. What this article addresses here is mainly about a parametric study on the injector under various operating conditions, such as different inlet water temperature, inlet steam pressure, pressure ratio, entrainment ratio and flowrate ratio. In addition, the irreversible losses in the component parts of the two-stage injector were analyzed in detail. The results show that the operating parameters have great effects on exergy efficiency of the injector. The average exergy efficiency of the two-stage injector is 21% more than that of the single-stage one. Moreover, calculations based on experimental data indicate that the highest exergy losses due to irreversibility occur in the first-stage mixing chamber. In light of this comparison, the exergy losses occurring in the system are proportional to the exergy efficiency obtained by applying the system.

References

El-Dessouky H, Ettouney H, Alatiqi I, Al-Nuwaibit G, Chem. Eng. Process., 41(6), 551 (2002)
Kim DS, Lee Y, Lee DH, Korean J. Chem. Eng., 26(1), 288 (2009)
Nabil Beithou, Aybar HS, Int. J. Multiphase Flow., 26, 1609 (2000)
Balamurugan S, Lad MD, Gaikar VG, Patwardhan AW, Chem. Eng. J., 131(1-3), 83 (2007)
Kim MI, Kim OS, Lee DH, Kim SD, Chem. Eng. Sci., 62(24), 7133 (2007)
Yari M, Int. J. Therm. Sci., 48, 1997 (2009)
Grazzini G, Rocchetti A, Int. J. Refrigeration., 25, 621 (2002)
Trela M, Kwidzinski R, Butrymowicz D, Karwacki J, Appl. Therm. Eng., 30, 340 (2010)
Dai Y, Wang J, Gao L, Appl. Therm. Eng., 29, 1983 (2009)
Bejan A, Tsatsaronis G, Moran M, Thermal Design and Optimization, Inc., New York, NY (1996)
Yan H, Chong D, Wu X, Appl. Therm. Eng., 30, 623 (2010)
Kim JJ, Park MH, Kim C, Korean J. Chem. Eng., 18(1), 94 (2001)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
TEL. No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로