title: Ð§Ð¸ÑÐ»ÐµÐ½Ð½Ð¾Ðµ Ð¼Ð¾Ð´ÐµÐ»Ð¸ÑÐ¾Ð²Ð°Ð½Ð¸Ðµ Ð¸ ÑÐµÑ Ð½Ð¸ÐºÐ¾-ÑÐºÐ¾Ð½Ð¾Ð¼Ð¸ÑÐµÑÐºÐ°Ñ Ð¾ÑÐµÐ½ÐºÐ° Ð¼Ð½Ð¾Ð³Ð¾ÐºÐ¾Ð»Ð¾Ð½Ð½Ð¾Ð¹ Ð´Ð¸ÑÑÐ¸Ð»Ð»ÑÑÐ¸Ð¸ Ð´Ð»Ñ ÑÐ¸ÑÑÐµÐ¼ Ð¾Ð¿ÑÐµÑÐ½ÐµÐ½Ð¸Ñ Ð¼Ð¾ÑÑÐºÐ¾Ð¹ Ð²Ð¾Ð´Ñ Ñ Ð¸ÑÐ¿Ð¾Ð»ÑÐ·Ð¾Ð²Ð°Ð½Ð¸ÐµÐ¼ MEDMPS
title: Ð²ÑÐ¿ÑÑÐºÐ½Ð°Ñ ÐºÐ²Ð°Ð»Ð¸ÑÐ¸ÐºÐ°ÑÐ¸Ð¾Ð½Ð½Ð°Ñ ÑÐ°Ð±Ð¾ÑÐ° Ð¼Ð°Ð³Ð¸ÑÑÑÐ°
titleType: Subtitle
title: Numerical simulation, technical and economic evaluation of multi-effect desalination systems using MEDMPS
Creators: name: ÐÑÐ»Ð´ÑÐ·, ÐÑÐ¸Ñ
Publisher: name: Ð¡Ð°Ð½ÐºÑ-ÐÐµÑÐµÑÐ±ÑÑÐ³ÑÐºÐ¸Ð¹ Ð¿Ð¾Ð»Ð¸ÑÐµÑÐ½Ð¸ÑÐµÑÐºÐ¸Ð¹ ÑÐ½Ð¸Ð²ÐµÑÑÐ¸ÑÐµÑ ÐÐµÑÑÐ° ÐÐµÐ»Ð¸ÐºÐ¾Ð³Ð¾
Year: 2023
Subjects: ÐÐ¾ÑÑÐºÐ°Ñ Ð²Ð¾Ð´Ð°
ÐÐ°ÑÐµÐ¼Ð°ÑÐ¸ÑÐµÑÐºÐ¾Ðµ Ð¼Ð¾Ð´ÐµÐ»Ð¸ÑÐ¾Ð²Ð°Ð½Ð¸Ðµ
Ð¾ÑÐ½Ð¾ÑÐµÐ½Ð¸Ðµ ÐºÐ¾ÑÑÑÐ¸ÑÐ¸ÐµÐ½ÑÐ° ÑÑÐ¸Ð»ÐµÐ½Ð¸Ñ Ðº ÐºÐ¾ÑÑÑÐ¸ÑÐ¸ÐµÐ½ÑÑ Ð²ÑÑ Ð¾Ð´Ð°
Ð¼Ð½Ð¾Ð³Ð¾ÑÐµÐ»ÐµÐ²Ð¾Ðµ Ð¼Ð¾Ð´ÐµÐ»Ð¸ÑÐ¾Ð²Ð°Ð½Ð¸Ðµ
ÑÑÑÐ¾Ð¹ÑÐ¸Ð²Ð¾Ðµ ÑÐ¾ÑÑÐ¾ÑÐ½Ð¸Ðµ ÑÐ¸ÑÑÐµÐ¼ med
ÐºÐ¾ÑÑÑÐ¸ÑÐ¸ÐµÐ½Ñ Ð²Ð¾ÑÑÑÐ°Ð½Ð¾Ð²Ð»ÐµÐ½Ð¸Ñ
gain to output ratio
multi-objective modeling
steady state med systems
recovery factor

description: Ð¦ÐµÐ»Ñ Ð´Ð°Ð½Ð½Ð¾Ð³Ð¾ Ð¸ÑÑÐ»ÐµÐ´Ð¾Ð²Ð°Ð½Ð¸Ñ - Ð¿ÑÐ¾Ð²ÐµÑÑÐ¸ ÐºÐ¾Ð¼Ð¿Ð»ÐµÐºÑÐ½ÑÐ¹ ÑÐ¸ÑÐ»ÐµÐ½Ð½ÑÐ¹, ÑÐºÐ¾Ð½Ð¾Ð¼Ð¸ÑÐµÑÐºÐ¸Ð¹ Ð¸ ÑÐµÑÐ¼Ð¾Ð´Ð¸Ð½Ð°Ð¼Ð¸ÑÐµÑÐºÐ¸Ð¹ Ð°Ð½Ð°Ð»Ð¸Ð· ÑÐµÐ¾ÑÐµÑÐ¸ÑÐµÑÐºÐ¾Ð¹ Ð¼Ð½Ð¾Ð³Ð¾ÑÑÑÐµÐºÑÐ¸Ð²Ð½Ð¾Ð¹ Ð¾Ð¿ÑÐµÑÐ½Ð¸ÑÐµÐ»ÑÐ½Ð¾Ð¹ ÑÑÑÐ°Ð½Ð¾Ð²ÐºÐ¸ Ð¸ Ð¿Ð¾ÐºÐ°Ð·Ð°ÑÑ Ð·Ð°Ð²Ð¸ÑÐ¸Ð¼Ð¾ÑÑÑ ÐºÐ¾ÑÑÑÐ¸ÑÐ¸ÐµÐ½ÑÐ° Ð¿Ð¾Ð»ÐµÐ·Ð½Ð¾Ð³Ð¾ Ð´ÐµÐ¹ÑÑÐ²Ð¸Ñ (GOR) Ð¾Ñ ÑÐ°Ð·Ð»Ð¸ÑÐ½ÑÑ Ð¼Ð¾ÑÐ½Ð¾ÑÑÐµÐ¹ Ð¸ Ð¿Ð°ÑÐ°Ð¼ÐµÑÑÐ¾Ð² ÑÑÑÐ°Ð½Ð¾Ð²ÐºÐ¸, Ð¸ÑÐ¿Ð¾Ð»ÑÐ·ÑÑ ÑÐ°Ð·ÑÐ°Ð±Ð¾ÑÐ°Ð½Ð½ÑÐ¹ Ð½Ð° Ð·Ð°ÐºÐ°Ð· Ð¿Ð°ÐºÐµÑ Ð¿ÑÐ¸ÐºÐ»Ð°Ð´Ð½ÑÑ Ð¿ÑÐ¾Ð³ÑÐ°Ð¼Ð¼ MATLAB (MEDMPS). ÐÑÐ»Ð° ÑÐ°Ð·ÑÐ°Ð±Ð¾ÑÐ°Ð½Ð° ÑÐ¿ÐµÑÐ¸Ð°Ð»ÑÐ½Ð°Ñ Ð¿ÑÐ¾Ð³ÑÐ°Ð¼Ð¼Ð° Ð¼Ð¾Ð´ÐµÐ»Ð¸ÑÐ¾Ð²Ð°Ð½Ð¸Ñ ÑÐ¸ÑÑÐµÐ¼ MED (MEDMPS), ÐºÐ¾ÑÐ¾ÑÐ°Ñ Ð¼Ð¾Ð¶ÐµÑ Ð°Ð½Ð°Ð»Ð¸Ð·Ð¸ÑÐ¾Ð²Ð°ÑÑ Ð»ÑÐ±ÑÑ ÐºÐ¾Ð½ÑÐ¸Ð³ÑÑÐ°ÑÐ¸Ñ Ð¼Ð½Ð¾Ð³Ð¾ÑÑÑÐµÐºÑÐ¸Ð²Ð½Ð¾Ð¹ Ð¾Ð¿ÑÐµÑÐ½Ð¸ÑÐµÐ»ÑÐ½Ð¾Ð¹ ÑÐ¸ÑÑÐµÐ¼Ñ, Ð¸ Ð¿ÑÐ¾Ð²ÐµÐ´ÐµÐ½Ð° Ð¿ÑÐ¾Ð²ÐµÑÐºÐ° ÐµÐµ ÑÐµÐ·ÑÐ»ÑÑÐ°ÑÐ¾Ð² Ñ Ð¸ÑÐ¿Ð¾Ð»ÑÐ·Ð¾Ð²Ð°Ð½Ð¸ÐµÐ¼ Ð´Ð°Ð½Ð½ÑÑ ÑÐµÐ°Ð»ÑÐ½Ð¾Ð¹ ÑÐ°Ð±Ð¾ÑÐµÐ¹ Ð¾Ð¿ÑÐµÑÐ½Ð¸ÑÐµÐ»ÑÐ½Ð¾Ð¹ ÑÑÑÐ°Ð½Ð¾Ð²ÐºÐ¸. Ð£ÑÐ¿ÐµÑÐ½Ð°Ñ Ð²Ð°Ð»Ð¸Ð´Ð°ÑÐ¸Ñ Ð¿ÑÐ¾Ð³ÑÐ°Ð¼Ð¼Ñ MEDMPS Ð±ÑÐ»Ð° Ð¿ÑÐ¾Ð²ÐµÐ´ÐµÐ½Ð° ÑÐ¾ ÑÑÐµÐ´Ð½Ð¸Ð¼ Ð¿ÑÐ¾ÑÐµÐ½ÑÐ¾Ð¼ Ð¾ÑÐ¸Ð±Ð¾Ðº Ð² %5, Ð¿ÑÐ¸ ÑÑÐ¾Ð¼ Ð±ÑÐ»Ð¸ ÑÐ¼Ð¾Ð´ÐµÐ»Ð¸ÑÐ¾Ð²Ð°Ð½Ñ ÑÑÐµÐ½Ð°ÑÐ¸Ð¸ Ð¸ÑÐ¿Ð¾Ð»ÑÐ·Ð¾Ð²Ð°Ð½Ð¸Ñ ÑÐ°Ð·Ð»Ð¸ÑÐ½ÑÑ ÑÐµÐ¾ÑÐµÑÐ¸ÑÐµÑÐºÐ¸Ñ ÑÐ¸ÑÑÐµÐ¼ ÑÑÑÐ°Ð½Ð¾Ð²Ð¾Ðº MED. ÐÐ±ÑÑÐ¶Ð´Ð°Ð»Ð¸ÑÑ Ð¾Ð³ÑÐ°Ð½Ð¸ÑÐµÐ½Ð¸Ñ Ð¿ÑÐ¾Ð³ÑÐ°Ð¼Ð¼Ñ Ð¸ ÑÐ¼Ð¾Ð´ÐµÐ»Ð¸ÑÐ¾Ð²Ð°Ð½Ð½ÑÑ ÑÐ¸ÑÑÐµÐ¼ ÑÑÑÐ°Ð½Ð¾Ð²Ð¾Ðº MED. Ð ÐµÐ·ÑÐ»ÑÑÐ°ÑÑ ÑÐ¸ÑÐ»ÐµÐ½Ð½Ð¾Ð³Ð¾ Ð¼Ð¾Ð´ÐµÐ»Ð¸ÑÐ¾Ð²Ð°Ð½Ð¸Ñ Ð¸ ÑÐ¸ÑÑÐ½ÐºÐ¸ Ð¿Ð¾Ð´ÑÐ²ÐµÑÐ¶Ð´Ð°ÑÑ Ð²Ð°Ð¶Ð½ÑÐµ ÑÐ°ÐºÑÐ¾ÑÑ ÑÐ¸ÑÑÐµÐ¼ MED. ÐÐ±ÑÑÐ¶Ð´Ð°ÑÑÑÑ ÑÑÑÐµÐºÑÑ Ð¸Ð·Ð¼ÐµÐ½ÐµÐ½Ð¸Ñ ÐºÐ¾Ð»Ð¸ÑÐµÑÑÐ²Ð° ÑÑÐµÐµÐº, Ð´Ð²Ð¸Ð¶ÑÑÐµÐ³Ð¾ Ð¿Ð°ÑÐ°, Ð¼Ð°ÑÑÐ¾Ð²Ð¾Ð³Ð¾ ÑÐ°ÑÑÐ¾Ð´Ð° Ð¼Ð¾ÑÑÐºÐ¾Ð¹ Ð²Ð¾Ð´Ñ Ð¸ ÑÐ¾Ð¾ÑÐ½Ð¾ÑÐµÐ½Ð¸Ñ ÑÐ°ÑÑÐ¾Ð»Ð°, GOR, ÐºÐ¾ÑÑÑÐ¸ÑÐ¸ÐµÐ½ÑÐ° Ð¸Ð·Ð²Ð»ÐµÑÐµÐ½Ð¸Ñ Ð¸ Ñ.Ð´., Ð° ÑÐ°ÐºÐ¶Ðµ Ð½Ð°Ð±Ð»ÑÐ´Ð°ÑÑÑÑ Ð¸ Ð¾Ð±ÑÑÐ¶Ð´Ð°ÑÑÑÑ Ð¾Ð³ÑÐ°Ð½Ð¸ÑÐµÐ½Ð¸Ñ Ð¿Ð¾ Ð²ÑÑÑÑÐ°Ð½Ð¸Ñ. Ð Ð´Ð°Ð»ÑÐ½ÐµÐ¹ÑÐµÐ¹ ÑÐ°Ð±Ð¾ÑÐµ MEDMPS Ð¼Ð¾Ð¶ÐµÑ Ð±ÑÑÑ Ð´Ð¾ÑÐ°Ð±Ð¾ÑÐ°Ð½ Ð´Ð»Ñ Ð²ÐºÐ»ÑÑÐµÐ½Ð¸Ñ ÑÐ°Ð·Ð»Ð¸ÑÐ½ÑÑ ÑÐµÑÐ½Ð¾Ð»Ð¾Ð³Ð¸Ð¹ Ð¾Ð¿ÑÐµÑÐ½ÐµÐ½Ð¸Ñ Ð¸ ÑÐ°Ð±Ð¾ÑÑ Ñ Ð¿ÐµÑÐµÑÐ¾Ð´Ð½ÑÐ¼ ÑÐ¾ÑÑÐ¾ÑÐ½Ð¸ÐµÐ¼, Ð·Ð°Ð²Ð¸ÑÑÑÐ¸Ð¼ Ð¾Ñ Ð²ÑÐµÐ¼ÐµÐ½Ð¸.
description: This study aims to provide a comprehensive numerical, economical, and thermodynamic analysis of a theoretical multi-effect desalination plant and show the relation of Gain-to-Output Ratio (GOR) to different plant capacities and parameters, using custom developed MATLAB application package (MEDMPS). A custom MED systems simulation program (MEDMPS) that can analyze any configuration of multi-effect desalination system was developed and the validation of its results was done using a real-life working desalination plant data. The successful validation of MEDMPS was carried out with an average error percentage of %5 and use case scenarios for different theoretical MED plant systems were simulated. Limitations of the program and the simulated MED plant systems were discussed. The important factors of MED systems were reiterated with numerical simulation results and figures. The effects of change in cell number, motive steam, seawater mass flow rate to the brine ratio, GOR, recovery rate, etc. are discussed and the dry out limitations were observed and discussed. For future work, MEDMPS can be developed further to include different desalination technologies and operate on time dependent transient state.