| Full text | |
| Author(s): |
Total Authors: 4
|
| Affiliation: | [1] Univ Sao Paulo, Polytech Sch, Dept Chem Engn, BR-05508900 Sao Paulo - Brazil
[2] Polytech Univ, Othmer Jacobs Dept Chem & Biol Engn, Brooklyn, NY 11201 - USA
Total Affiliations: 2
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| Document type: | Journal article |
| Source: | ENERGY CONVERSION AND MANAGEMENT; v. 50, n. 9, p. 2200-2209, SEP 2009. |
| Web of Science Citations: | 36 |
| Abstract | |
The thermal performance of a cooling tower and its cooling water system is critical for industrial plants, and small deviations from the design conditions may cause severe instability in the operation and economics of the process. External disturbances such as variation in the thermal demand of the process or oscillations in atmospheric conditions may be suppressed in multiple ways. Nevertheless, such alternatives are hardly ever implemented in the industrial operation due to the poor coordination between the utility and process sectors. The complexity of the operation increases because of the strong interaction among the process variables. In the present work, an integrated model for the minimization of the operating costs of a cooling water system is developed. The system is composed of a cooling tower as well as a network of heat exchangers. After the model is verified, several cases are studied with the objective of determining the optimal operation. It is observed that the most important operational resources to mitigate disturbances in the thermal demand of the process are, in this order: the increase in recycle water flow rate, the increase in air flow rate and finally the forced removal of a portion of the water flow rate that enters the cooling tower with the corresponding make-up flow rate. (C) 2009 Elsevier Ltd. All rights reserved. (AU) | |