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The aim of the present work is to design and obtain steam ejector geometry, based on pre-specified operating conditions, and to investigate the flow behavior inside the ejector by using Computational Fluid Dynamics CFD through using "ANSYS FLUENT 14.5" software.
The main objective of the control system is to obtain steam at constant temperature and pressure at the solar field outlet, so that changes in inlet water conditions and/or in solar radiation affect the amount of steam, but not its quality or the nominal plant efficiency.
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The obtained steamed graphene hydrogel (S-GH) displays three and ten times higher responses to NO2 and NH3, respectively, compared with its unmodified GH counterpart before steaming treatment.
The steam distillation rates obtained with steam superheated by 40 °C, steam superheated by 10 °C, and saturated steam were 11.158%, 10.903% and 10.423%, respectively.
While evaporation of liquids in crossflow and counterflow or co-current flow micro-channel devices is possible, it is, in many cases, not possible to obtain superheated steam due to certain boundary conditions.
To obtain saturated steam at 210°C, the pressure inside the vessel was maintained at 19 to 20 bars.
Excellent adsorption capacities of 2000 and 1111 mg g−1 were obtained for steam and chemical followed by steam-activated carbons, respectively.
Most of the steam utilized to make hot springs is obtained from steam production wells (hereafter SPWs), the depth of which are less than 500 m.
The sulfur passivated reforming (SPARG) process was developed to decrease the syngas H2/CO ratio from 2.7 obtained from steam reforming to 1.8 without changing the steam reforming facility.
Lemongrass, or sweet rush (Cymbopogon citratus), contains citral, obtained by steam distillation of the leaves.
The oil is obtained by steam distillation of the wood and is used in perfumes, soaps, candles, incense, and folk medicines.
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