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Therefore steam has been extracted from LP steam level.
The MED unit is designed for integration with each steam level.
Thermodynamic and economic analyses demonstrate that utilizing steam from MP steam level has the highest rate of desalinated water production and using steam from LP steam level has the best exergy efficiency and period of return.
In addition to the simultaneous design of the utility and heat-recovery systems, the optimization variables include the steam condensate target temperature, the steam level for process heating, the energy demand for the utility system, the returning temperature of the steam condensate, and the final temperature of the boiler feed water.
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The prices of steam for each one of the steam levels are calculated.
The opportunity to use excess steam of each steam levels of steam network of utility system has been investigated.
The optimisation problem involves the selection of the steam levels with respect to their temperatures.
Because steam levels adjust according to temperature, you automatically get more for thicker clothes, which saves time.
An interesting feature of the optimal solution for the integration problem with multiple steam levels is that integration gaps arise.
The design of utility networks involves two major tasks: the selection of the steam levels, with respect to their pressure or saturation temperature, and the determination of the configuration of the operating units between the steam levels.
The proposed method gives comparable results, and the targeting method is used for optimal integration of steam levels.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com