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The PRO simulation shows that both water recovery and energy production are enhanced by increasing the PRO influent volume, while the substrate concentration in the feed effluent remains stable (Fig. 3a, b).
Meanwhile, the PRO unit could produce a feed effluent containing 1,007 mg L−1 acetate, a draw effluent with 0.46 M NaCl, and 579 J of energy (Table 1; Fig. 2a).
Stable operation at the design specifications (5.5% solids, 100 mg/l SCN− feed, effluent SCN− <1 mg/l) was achieved within 50 days, including a period of adaptation.
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A key experiment showing that cats developed the characteristic disease when fed effluent water from a polluting factory was suppressed by the sponsoring company, and the detailed results became available only after a delay of 40 years (Eto et al. 2001).
Chapter 7. Feed-Effluent Heat Exchangers.
In order to further save energy, a feed-effluent heat exchanger can be added in the proposed extractive distillation system.
Simple feed-effluent heat exchanger can be added in the proposed extractive distillation system to further save energy without much complication of the process design flowsheet.
The reactor effluent enthalpy can cover feed preheating, evaporation and superheating in a sequence of three feed-effluent-heat exchanger units.
The space of the design parameters, feed-effluent heat-exchanger (FEHE) efficiency and steam-generator duty, is divided by bifurcation varieties into regions with different controllability properties.
The non-linear behaviour of the heat-integrated multibed plug flow reactor (PFR), consisting of feed-effluent heat exchanger (FEHE), furnace, multibed adiabatic tubular reactor with intermediate cooling, and steam generator is studied.
Energy consumption is reduced by employing a feed-effluent heat exchanger and employing a 3-phase distillate receiver at the top of the distillation column and refluxing only the organic phase.
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