Multistage flash desalination combined with thermal vapor compression

A novel system is proposed to increase the performance of the multistage fl ash desalination process (MSF) by combination with thermal vapor compressio n (TVC). The proposed system integrates the vapor compression unit within t he conventional MSF brine circulation configuration without variations in t he process layout. Two schemes are evaluated, which includes vapor entrainm ent and compression from the heat recovery or rejection sections. These sch emes may call for use of one or two jet ejectors depending on the required compression range. Performance evaluation for the proposed schemes is made as a function of the top brine temperature and location of vapor entrainmen t. Results show that the increase in thermal performance ratio of the propo sed system over the conventional MSF varies between 6 and 16%. Additional p ower savings are realized as a result of 62-74% reduction in the specific f low rate of cooling water to the system. Use of high pressure steam results in 60% size reduction in the diameter of the steam piping system. Use of t he steam jet ejector, eliminates the control loops and process units for th rottling and desuperheating, which are found in conventional MSF. Vapor ent rainment and compression from the stages of the heat recovery section gives higher thermal performance ratio and lower specific heat transfer area tha n for vapor entrainment from the heat rejection stages. However, the main a dvantage for vapor entrainment and compression from the heat rejection stag es is that the specific flow rate of cooling water is lower by 40%. Gains a nd features of the proposed vapor compression modes would reduce the unit p roduct cost as a result of reduction in the capital and operating costs of the process. (C) 2000 Elsevier Science S.A. All rights reserved.