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The optimal power generation of hydro-thermal systems to minimize total operating costs is one of the most important targets in short-term hydro-thermal scheduling (STHS) and its evaluation is complicated by several complex and interconnected equality and inequality constraints.
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Accordingly, their total operating costs are $98968 and $100018 respectively.
As a consequence, G2 and G3 are committed less in HWP, and the total operating costs are substantially different between base case 2 (BS2) at $83782 and HWP at $79985.
It integrates otherwise mutually exclusive secondary route networks for their respective services so that the total operating cost is minimized while meeting the service time and operations restrictions.
For a more general discussion, two optimal designs that differ on how the total operating cost is computed are discussed.
For different process configurations (design) in term of number of flash stages, the operation parameters such as make-up and brine recycle flow rates are optimized at discrete time intervals (based on the storage tank level which is monitored dynamically and maintained within a limit) while the total operating cost is minimised.
The total operating cost was 2.8 CNY/t.
The total capital and operating costs were estimated to be US$8,110,6000 and US$ 0.022 per m3, respectively.
To accomplish this aim, a pyrolysis plant with a 50 t/d capacity was designed, and the total capital investment and operating costs were estimated.
The basic objective of operators is to produce wells using the least amount of total costs of which operating costs are crucial because of the ever-increasing cost of power.
Food made up the largest component (48.7% of total cost), and transport operating costs were the second largest item (23.5%).
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com