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The operating variable was the specific gravity of the medium, feed inlet pressure and feed inlet flow rate.
There is an optimum feed inlet rate depending on the feedwell design.
The effects of feed inlet temperature, inlet benzene concentration, gas flow rate and liquid flow rate on the reactor performance are theoretically studied.
The enhancement of feed inlet velocity increased the value of TPC and VPC as well as the permeate flux in all simulated modules.
Effectiveness of hydrocyclone separations is highly dependent on their geometrical characteristics such as: chamber dimensions, aperture diameters or feed inlet geometry, for instance.
The flow field in the module and the permeate fluxes were simulated while the feed inlet velocity was varied from 0.02 m/s to 0.08 m/s.
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The fluidized bed methanation reactors of (j), on the other hand, contained two feed inlets and two in-tube heat exchanger bundles.
This contribution describes the influences of the reaction trays and feed-inlet locations of the RD column on the simulation results.
Moreover, it is shown by simulation that a lower RD reflux ratio and low required duty can be demonstrated when the feed-inlet of the reaction column is located in lower portion of the column.
Impacts of three parameters, including reactant flow rate, reaction trays, and feed-inlet location on the temperature profile and component compositions in the columns are investigated to achieve an optimum condition of the process in terms of energy demand.
The experimental set-up mainly consists of a feed-inlet pump, preheater, reactor and sample collection units.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com