Sentence examples for flash stage from inspiring English sources

An experimental system with a transparent flash evaporation chamber was set up in this work to simulate the single-phase seawater flow in the flash stage in the multi-stage flash (MSF) desalination process.

In this study, the effect of various design as well as operating conditions on the performance ratio (PR), brine temperature and salinity as it leaves the last flash stage are investigated in a once-through system.

A number of potentially significant improvements to the OFC are possible though which includes using a secondary flash stage or replacing the throttling valve with a two-phase expander.

There is wide agreement that hormone treatment for a few years, until a woman gets past the hot flash stage, is advantageous, as is hormone replacement for a limited time for women who have had their ovaries removed before natural menopause.

You can change the size of the Flash stage to 853 by 480 and make a wide screen video.

The results are compared against phase equilibria calculations and two flash stages are shown to reduce THF concentrations by over 95%, and bring the residual solvent concentration within acceptable limits for drug applications.

Optimization problem is formulated to optimize the total number of flash stages and operating parameters such as recycle brine and seawater make up while minimizing the total monthly cost (including capital cost and operating cost) of the process for each month of the year.

The results also reveal the possibility of designing stand-alone flash stages which would offer flexible scheduling in terms of the connection of various units (to build up the process) and efficient maintenance of the units throughout the year as the weather condition changes.

For different process configurations (design) in term of number of flash stages, the operation parameters such as make-up and brine recycle flow rates are optimized at discrete time intervals (based on the storage tank level which is monitored dynamically and maintained within a limit) while the total operating cost is minimised.

The live steam used in the first evaporator is superheated to 144°C at 2.5 bar, and the five flash stages are performed at a pressure allowing a change in temperature of at least of 12°C over each evaporator.

The focus of this study is to develop a number of design correlations of the MSF flashing stage.