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The combined extracts were dried on anhydrous sodium sulfate to remove moisture content and evaporated using a rotary evaporator on a water bath at 40 °C.
An aluminum (Al) electrode was deposited by the evaporator on the sample.
The OHP was tested vertically, i.e., the evaporator on the bottom and the condenser on the top.
Open image in new window Figure 9 Relationship length of evaporator on heat flux of THMCLOHP/CV.
The OHP was tested vertically, i.e., the evaporator on the bottom heated by a uniform electrical flat heater.
The effect of NTU of evaporator on heat transfer rate, network output, system thermal efficiency and investment payback years were studied.
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However, either high-cost metal nanoparticles solved in water were used as nanofluids or these heat pipes were operated only in a horizontal or limited tilt arrangement, rather than the vertical arrangement, in which their thermal performance deteriorates because nanoparticles always accumulate on the evaporator of heat pipes with evaporation converting water to vapor.
Based on the thermodynamic mathematical models, the effects of key design parameters, including that of turbine inlet pressures, mass flow rates of working fluids and outlet steam fractions of evaporators on the system performance are investigated from the view of both thermodynamics and economics with CPP (cost per net power output) as the objective function.
The hexane was evaporated on rotary evaporator.
After completion of reaction, DMC layer was washed with distilled water, dried over sodium sulphate and evaporated on rotary evaporator to yield the intermediates (3a-o).
Combined ethyl acetate layer was washed with brine water, dried over sodium sulphate and evaporated on rotary evaporator to afford the final compounds 5a-o.
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