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This paper introduces a new approach for the design of water utilization networks featuring minimum freshwater usage and minimum utility consumption in process plants.
Hydrogen utility consumption minimization is one of the key strategies for reducing refinery operating costs.
To minimize hydrogen utility consumption, it is necessary to optimize the hydrogen network with purification as a whole.
The usage of complementary source pair(s) to reduce utility consumption is investigated.
Process integration is an effective way to reduce hydrogen utility consumption in refineries.
Simulation results demonstrate that the RDWD-VRHP can substantially reduce utility consumption of RDWD.
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The results show that the unified model is capable of minimizing both CO2 emissions and energy and utility consumptions.
Sizing of unit operations, chemicals and utility consumptions, and estimation of capital and operating costs with the cost breakdown analysis were acquired from the simulation.
Thus, comparison of crude palm oil (CPO) and RSO production processes have been made in term of (i) energy and utility consumptions, (ii) feedstock price and (iii) environmental impact.
Impacts of two key design variables, H2/CO ratio at the inlet of the FT unit and biomass/coal ratio of the feedstock, on the product yield and utility consumptions are investigated.
Thus, to limit utilities consumption, energy integration has to be incorporated for all process design alternatives.
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