OPTIMIZATION OF THE TUBE SIZE AND THE ARRANGEMENT OF EVAPORATOR TUBE BUNDLE TO IMPROVE THE PERFORMANCE OF MED-TVC SYSTEMS
|
|
- Ethel Park
- 6 years ago
- Views:
Transcription
1 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt 359 OPTIMIZATION OF THE TUBE SIZE AND THE ARRANGEMENT OF EVAPORATOR TUBE BUNDLE TO IMPROVE THE PERFORMANCE OF MED-TVC SYSTEMS Ramin K. Kamali and S. Mohebbinia Fan Niroo Company, Tehran, Iran s: ABSTRACT The present work summarizes parametric optimization technique for the tube size and arrangement of tube bundle inside MED-TVC system (Multi Effect Desalination with Thermal Vapor Compression) to increase GOR (Gain Output Ratio) value. For this purpose, a simulation model of MED-TVC system is presented. This program provides engineers a cost effective tools for thermodynamics and thermo hydraulic designing, developing and optimizing the thermal desalination plants. It is the objectives of this article to develop a mathematical model which predicts the influence of all factors on total capacity, performance ratio, temperature difference between effects and pressure on each effect to select the optimum size and arrangement of the tubes for various capacities of the MED units. The pressure drop across the system should be minimized in order to decrease the overall energy consumption of the system and therefore to improve the gain output ratio of the plant. The simulation package is applied for a specified capacity in order to achieve the best size and arrangement for tube bundles of the system. A comparison of GOR values between two actual systems with different size and arrangement in their evaporators shows that a system which has designed according to results of simulation package, has higher amount of GOR value. The comparison between the simulation results, with experimental data well proves optimization method s validity. INTRODUCTION The need for high quality water significantly increased during the second half of the last century. It has been a complex task to develop an effective thermo hydraulic design without actual testing which usually requires costly test procedures. The desalination industry is the life live for several countries and zones around the world, especially the countries around the Persian Gulf such as IRAN. Expansion in desalination industry is associated with reduction in the power consumption and increase GOR value. For this reason, a general computer code for MED type of desalination has been developed and is currently used by the only MED-TVC Manufacturer Company in IRAN (Fan-Niroo Co.)[1]. Uche [2], Kafi [3], Hisham [4,5], Jernqvist [6] and Hisham [7] developed a simulation code for MED system with
2 360 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt shell and tube evaporators. Vertical channels instead of horizontal tubes were considered by Mitrovic and Raach [8] in 2005 but there is no corrugation on the plates in their investigation. The present work deals with both shell and tube and plate type evaporators with horizontal corrugation and in addition, thermo-compressor and ejectors are designed as well. TVC systems are affecting on increasing GOR value in MED systems [9].In this paper, it is shown that parametric study as one of the optimization method on thermo hydraulic data, strongly help to increase GOR value inside MED-TVC systems. Some of the energy losses in the system take place due to pressure drop in the evaporators. By decreasing the overall pressure drop of the system, the energy losses decreased and the performance of the system will increase consequently. Steam pressure drop in the system is a function of tube length, tube internal diameter and the arrangement of the tube bundle. The purpose of this work is the investigation of the effect of tube length and tube arrangement in the evaporators. THERMO HYDRAULIC MODELING A schematic of MED-TVC system is shown in Figure (1). The system is consisting of some evaporators, a condenser, and thermo-compressor. In each effect, two phase flow inside the evaporators is modeled by conservation equations to account pressure drop and flow specifications [10], [11], [12], [13]. Figure 1. Schematic of MED-TVC system. In mathematical modeling, mass and energy balance equations have been developed for the system and then heat exchangers, thermo-compressor and ejectors are designed based on the results of mass and energy balance.
3 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt 361 Evaporators and Condenser Design Evaporators are the main part of desalination units. Therefore, it is very important to design them more cost effective and more efficient. Two types of configuration would be applied to desalination plants are conventional shell and tube and plate type evaporators. Plate type evaporators are a new technology to have a compact and portable system. Shell and Tube Evaporators To design a shell and tube evaporators, there are some parameters should be calculated such as tube size (diameter and length), number of pass and number of tubes. Figure (2) illustrates the design algorithm which was used to determine these parameters and finalize evaporators design. Figure 2. Shell and tube evaporators design algorithm.
4 362 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt Figure (3) illustrates a schematic view of the MED-TVC design cod. Plate Type Evaporators For being compact, easy to clean, efficient and more flexible, the gasket plate type heat exchangers are employed in desalination process. To design a plate type heat exchanger, there are some parameters which have to be calculated such as number of plates, plate size, chevron type, the length of gap between plates and so on. The design algorithm for plate type evaporator is illustrated in Figure (4).
5 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt 363 Figure 4. Plate type evaporators design algorithm Shell and Tube Condenser A part of vapor generated in the last effect is passed through condenser and condensed by seawater intake to the system. Condenser is usually shell and tube type in MED system which has the same design algorithm as shell and tube evaporators. Thermo-Compressor and Ejectors Thermal desalination systems operate at pressures lower than atmosphere pressure. Therefore, using vacuum devices in these systems are unavoidable. Ejectors and thermo compressors are common thermal devices can provide vacuum requirement for these systems. It should be noted that thermo compressor is one kind of an ejector. The ejector is a pumping device which uses jet action of a high pressure and temperature primary
6 364 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt motive steam to entrain and accelerate a slower secondary steam (load). Due to the simplicity of design and absence of motive parts, ejectors are very reliable; require practically no maintenance and have a relatively low installation cost [14]. The ejectors are powered by heat, which is low-grade energy and it is obviously less expensive to run than electrical or mechanical-related power. The steam required for the jet ejector is commonly drawn from boilers. These devices used in vapor compression desalination systems as a heat pump. A thermo vapor compression desalination unit mainly comprises a steam jet ejector, a single or multi effect evaporator, and a condenser. The thermo compressor is used to compress the vapor from pressure P s [which is the vapor pressure leaving the last effect or condenser depends on the system design] to P 1 [which is the vapor pressure entering the first effect] by using an external source of steam at a pressure P e greater than the vapor pressure. Two types of ejectors are usually used in the systems. They are hogging ejector and NCG ejector. First one provides the initial vacuum of the system and the other one discharge non-condensable gases (NCG) from system. The ejector design can be classified into two categories which is known "Constantarea mixing ejector" and "Constant-pressure mixing ejector". In this case, the ejectors and thermo compressor have been designed based on "Constant-pressure mixing ejector" [14], [15]. Thermo compressor and ejectors design flowchart is shown in Figure (5). Simulation Algorithm Finally, the simulation algorithm of thermo hydraulic design of MED-TVC system can be considered as Figure (6). The program is modular in structure and includes a number of modules for evaporators, condensers, thermo-compressor, steam jet ejectors and etc. Each module has its own mathematical model. The program also includes a comprehensive database for the physical properties of seawater. There is a library containing correlations for heat transfer coefficient of different heat transfer surfaces and flow regime. [16], [17], [18].
7 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt 365 Inputs: m, P P p, η, T p, P s, T s, m s P Calculate nozzle throat and nozzle outlet diameters. Determine number of required nozzles. Set Mach number of the nozzle outlet equal to 3.5 and calculate the nozzle outlet diameters, then determine the number of required nozzle (usually 3) Set the Mach number of secondary flow at the inlet of mixing section equal to 1 and calculate the pressure and temperature of both of streams, and determine the diameter of constant area section. By assuming "constant pressure mixes ", calculate the flow condition before shock (Pressure, Mach number...) Calculate flow condition after Mach number, and its condition at the outlet of ejector, By means of diameter of constant area, determine the lengths of mixing section, constant area section and diffuser section Figure 5. Thermo-compressor and ejectors design algorithm. Figure 6. Thermo hydraulic design algorithm.
8 366 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt PARAMETRIC STUDY As GOR value is depend on temperature difference between effects, so it is important to investigate the influence of temperature difference between effects on GOR value. For a four effects system with high pressure steam inlet, this effect is observed on Figure (7). It can be seen that, if the temperature difference between effects decrease, the amount of GOR value will increase. In order to decrease the temperature difference between effects, the pressure drop between effects should be decreased. Therefore it is very important to optimize evaporator s thermo hydraulic design inside MED-TVC systems to minimize pressure drop between effects GO R Temperature Difference between Effects [ o C] Figure 7. Variation of GOR value with temperature difference between effects. In MED-TVC systems with shell and tube evaporators, thermo hydraulic design depends on definition of some parameters such as tube lengths, pitches and diameters. In addition, tube bundle arrangement between tube sheets can affect on heat transfer coefficient and required heat transfer surface area. To fix Thermohydraulic design condition, it is necessary to define the best values for tube lengths, pitches and diameters in order to minimize pressure drop between effects. As the vapor generated in each effect is passed through tube bundles and demisters and enter inside tubes in the next effect, so the pressure drop between effects is approximately equal to summation of pressure drop around the tubes and pressure drop inside the tubes in the next effect. So, it is necessary to find optimum points for thermo hydraulic data because some of them affect against each other. For example, to minimize the pressure drop around the tube bundles, it is better to select tubes with higher length but to minimize the pressure drop inside the tube bundles, it is better to select shorter tubes. Therefore, parametric study should be done to find optimum points and minimize pressure drop between effects.
9 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt 367 EXPERIMENTAL SETUP A sample system with 2400 cubic meter fresh water per day capacity is selected and an experimental test was performed on this system to prove the validity of parametric study. Figure (8), shows a schematic of the experimental unit. Figure 8. A schematic of experimental Unit. The desalination package is controlled by a Unit Control Panel (UCP) as shown in Figure (9). Table (1) shows the list of controllable parameters and their tag numbers in the package. The desalination unit is automatically controlled from the Unit Control Panel but is interfaced for monitoring purpose. Figure (10) shows a schematic of monitoring instruments in the control room. These monitoring instruments can show the general faults, status of the operation and the entire amount of temperature and pressure gauges in the system. Figure 9. A schematic of unit control panel.
10 368 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt Table 1. List of control valves and their nominal value in the package Main Number Code Description 1 PT01 Inlet Steam Pressure 2 PT02 Pressure in Effect#1 3 PT03 Pressure in Condenser 4 LT01 Product Level in Condenser 5 LT02 Brine Level in Effect#5 6 CT01 Product Conductivity 7 CT02 Condensate conductivity 8 FT14 Condense water Flow 9 FT01 Product Flow 10 FT02 Total Feed Flow 11 FT03 Effect #1 Flow Water 12 FT04 Sea Water Flow 13 TE01 Sea Water Temperature 14 TE02 Feed Water Temperature 15 TE03 Effect #1 Temperature 16 TE04 Condensate Water Temperature 17 TE05 Condenser Temperature Figure 10: A schematic of monitoring instruments in the control room. To investigate the effect of optimized thermo hydraulic data, a new system was installed according to new thermo hydraulic data in order to compare the results. All of the mentioned parameters in Table (1) are extracted in order to do parametric study on the sensitive parameters. It should be noted that, there was no difference between
11 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt 369 process condition, mechanical parameters and materials between optimized and nonoptimized system. In addition, all of the experimental results were obtained according to summer condition. RESULT AND DISCUSSION Steam produced from seawater evaporation in each effect, while passes across the tube bundle and condenses through the tubes of the next effect has pressure drop. Decreasing the pressure drop of the MED system signifies lowering the load of the thermo-compressor which has to endure. It means that by decreasing the P, the amount of thermo-compressor steam consumption will decrease. In other words, by decreasing the overall pressure drop of the system, the energy losses decreased and the performance of the system will increase consequently. Steam pressure drop in the system is a function of tube length, tube internal diameter and the arrangement of the tube bundle. Increasing the tube length leads to increase in pressure drop; whereas increasing the tube length itself leads to decreased number of tubes and consequently increases pressure drop. Pressure drop in these two zones of the system changes differently, so that in a specific interval of the tube length its amount will be minimum. By comparison of the obtained results from actual system and simulation data, it will be understood that the systems in which the length of the tubes are comparable with the length obtained from simulation, result higher efficiencies than the others. Increasing the tube pitch decreases the pressure drop in tube side and as a result leads to higher efficiency of the unit; but on the other hand it increases the shell diameter and extra capital costs. Finding the optimum value for this parameter depends on the importance of operating costs versus capital costs. As mentioned, thermo hydraulic performance of a sample system with 2400 cubic meter per day capacity with shell and tube evaporators has been evaluated. Figure (11) shows that the optimum length for the evaporator s tubes with 1 inch diameter to achieve the minimum pressure drop between effects is 3.8 meters. Pressure drop (bar) Length of Tubes [m] Figure 11. Variation of pressure drop with length of tubes.
12 370 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt Figure (12) shows that the optimum length for the evaporator s tubes to achieve the minimum pressure drop between effects is varied by amount of tube pitch. For a tube bundles with a higher tube pitch, the amount of pressure drop and the optimum length for tube bundle decreases Pressure Drop [bar] Length of tube bundle [m] Tube Pitch=1.36 in Tube Pitch=1.31 in Figure 12. Variation of pressure drop with length of evaporators tubes. Figure (13) shows that the pressure drop inside condenser tube bundles decreases if the length of tube bundle increases to a higher value Pressure Drop [bar] Length of tube bundle [m] Figure 13. Variation of pressure drop with length of condenser tubes. For mentioned system with shell and tube heat exchangers, parametric study on thermo hydraulic data has been done. Table (2) shows the comparison between optimized and non-optimized system. Unfortunately, there was not any available
13 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt 371 system in order to verify the results of optimized plate type evaporators, but it is interesting to note here that a new system is going to be built based on optimized plate type MED-TVC design data. According to this Table, it is obviously clear that, a system with optimized thermo hydraulic data has lower required heat transfer surface area. Therefore, GOR value in optimized system for a same heat transfer surface area is more than GOR value for a non-optimized system. Table 1. Optimized and non-optimized design data for MED-TVC system with shell and tube evaporators Parameter Unit Design Optimized Deviation Data Data (%) Total distillated product Ton/day Seawater temperature o C Motive steam Ton/day First Effect steam temperature o C Feed water temperature o C Number of effects Number of tubes in each effect Effects Tube length m Effects Tube diameter cm Number of condenser tubes Condenser Tube length m Condenser Tube outer diameter cm Steam Pressure barg GOR Shell depth m Shell length m CONCLUSIONS The method of parametric study is an appropriate tool to estimate the optimum thermo hydraulic parameters. By comparison of the obtained results from actual system and simulation data, it will be understood that the systems in which the length of the tubes are comparable with the length obtained from simulation, result higher efficiencies than the others. Decreasing the pressure drop of the MED system signifies lowering the load of the thermo-compressor which has to endure. It means that by decreasing the P, the amount of thermo-compressor steam consumption will decrease. In other words, by decreasing the overall pressure drop of the system, the energy losses decreased and the performance of the system will increase consequently. Another conclusion is that the optimum length of tubes inside the evaporators is strongly depending on the capacity of the system. Parametric study on thermo hydraulic data is one of the best methods to arise amount of GOR value of the system.
14 372 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt NOMENCLATURE B D D r R F M c T S m P Brine blow down mass flow rate, ton/hr Distillate product mass flow rate, ton/hr Entrained steam mass flow rate, ton/hr Rejected water mass flow rate, ton/hr Seawater feed to effects flow rate, ton/hr Seawater mass flow rate, ton/hr Temperature of effect, o C Motive steam mass flow rate, ton/hr Mass flow rate Steam pressure SUBSCRIPTS i Index B Brine F Feed f Condenser product n Number of effects p Primary steam s Motive steam sw Seawater η Nozzle Efficiency P REFERENCES 1. R.K. Kamali, A. Abbassi, and S.A. Sadough, A simulation model and parametric study of MED-TVC process, EDS international conference, EuroMed (2006). 2. Javier Uche, Javier Artal, and Luis Serra, Comparison of heat transfer coefficient correlations for thermal desalination units, Journal of Desalination 152 (2002) F. Kafi, V. Renaudin, D. Alonso, and J.M. Hornut, New MED plate desalination process: Thermal performances, Journal of Desalination 166 (2004) Hisham M. Ettouney, and Hisham El-Dessouky, A simulator for thermal desalination process, Desalination 125 (1999) Hisham T. El-Dessouky, H.M. Ettouney, Multiple effect evaporation desalination systems: thermal analysis, Desalination 125 (1999) Jernqvist, M. Jernqvist, and G. Aly, Simulation of thermal desalination process, Desalination 134 (2001) Hisham Ettouney, Visual basic computer package for thermal and membrane desalination processes, Desalination 165 (2004)
15 Eleventh International Water Technology Conference, IWTC Sharm El-Sheikh, Egypt Henning Raach, and Jovan Mitrovic, Simulation of heat and mass transfer in a multi effect distillation plant for seawater desalination", EDS International conference, EuroMed (2006). 9. Najem M. Al-Najem, M.A. Darwish, and F.A. Youssef, Thermo vapor Compression Desalters: Energy and Availability Analysis of Single and Multi- Effect Systems, Desalination J., 110 (1997) Ould Didi, M.B., N. Kattan, and J.R. Thome, Prediction of two-phase pressure gradients of refrigerants in horizontal tubes, International Journal of Refrigeration 25 (2002) Yu, W., D.M. France, M.W. Wambsganss, and J.R. Hull, Two-phase pressure drop, boiling heat transfer, and critical heat flux to water in a small-diameter horizontal tube, International Journal of Multiphase Flow 28 (2002) Saunders, E.A.D., Heat Exchangers, John Wiley & Sons, Inc, Kakac, S., A.E. Bergles, F. Mayinger, Heat Exchanger, Thermal-Hydraulic Fundamentals and Design, Hemisphere Publication, Mc Graw-Hill Book Company Hisham El-Dessouky, Hisham Ettouney, Evaluation of steam jet ejectors, Chemical Engineering and processing 41 (2002) B.J. Huang, J.M. Chang, C.P. Wang, and V.A. Petrenko, A 1-D analysis of ejector performance, International Journal of Refrigeration 22 (1999) Parken, W.H., L.S. Fletcher, V. Sernas, and J.C. Han, Heat transfer through falling film evaporation and boiling on horizontal tubes, Heat transfer J. Transaction of the ASME Vol. 112, August Cavallini, A., G. Censi, D. Del Col, L. Doretti, G.A. Longo, L. Rossetto, and C. Zilio, Review Condensation inside and outside smooth and enhanced tubes a review of recent research, International Journal of Refrigeration 26 (2003) P. Fiorini, E. Sciubba, and C. Sommariva, A new formulation for the nonequilibrium allowance in MSF processes, Desalination J., 136 (2001)
Chapter-2 LITERATURE REVIEW. A brief review of previous and ongoing research investigations on thermal
Chapter-2 LITERATURE REVIEW A brief review of previous and ongoing research investigations on thermal desalination processes is presented in this chapter. The chapter begins with the introduction of the
More informationTHERMOECONOMIC ANALYSIS OF MULTI STAGE FLASH- THERMAL VAPOR COMPRESSSION (MSF-TVC) DESALINATION PROCESS
Tenth International Water Technology Conference, IWTC0 2006, Alexandria, Egypt 89 THERMOECONOMIC ANALYSIS OF MULTI STAGE FLASH- THERMAL VAPOR COMPRESSSION (MSF-TVC) DESALINATION PROCESS A S Nafey, H E
More informationMulti Stage Flash Desalination with Direct Mixing Condensation
Multi Stage Flash Desalination with Direct Mixing Condensation Andrea Cipollina*, Giorgio Micale, Salvatore Noto, Alberto Brucato Dipartimento di Ingegneria Chimica Gestionale Informatica Meccanica, Università
More informationDeveloping a Design and Simulation Tool for Coupling Thermal Desalination Plants with Nuclear Reactors by using APROS Simulator
Developing a Design and Simulation Tool for Coupling Thermal Desalination Plants with Nuclear Reactors by using APROS Simulator Khairy Agha,, Khalid Al Fared, Ali Rashed, and Salem Ghurbal Simulation Group,
More informationChapter 2 Conventional Thermal Processes
Chapter 2 Conventional Thermal Processes Hisham Ettouney Abstract Thermal desalination processes account for about 50% of the entire desalination market. The remaining market share is dominated by the
More informationCFD ANALYSIS OF STEAM EJECTOR WITH DIFFERENT NOZZLE DIAMETER
CFD ANALYSIS OF STEAM EJECTOR WITH DIFFERENT NOZZLE DIAMETER G.Saidulu 1, A.Purender reddy 2, Shreenivas 3 1 Student,Mech Dept,Sphoorthy Engineering College, Hyderabad,(India) 2 Assistant professor,mech
More informationWater Desalination Through MED-TVC
Water Desalination Through MED-TVC IMPROVEMENT OF MULTI-EFFECT DESALINATION SYSTEMS: LOCATION OF VAPOR COMPRESSOR Mohammed Antar Professor Mechanical Engineering Department KFUPM antar@kfupm.edu.sa 2 Outlines
More informationThermodynamic Losses in Multi-effect Distillation Process
IOP Conference Series: Materials Science and Engineering PAPER OPEN ACCESS Thermodynamic Losses in Multi-effect Distillation Process To cite this article: S Shen 2015 IOP Conf. Ser.: Mater. Sci. Eng. 88
More informationINTEGRATION OF TVC DESALINATION SYSTEM WITH COGENERATION PLANT: PARAMETRIC STUDY
Fourteenth International Water echnology Conerence, IWC 4 2, Cairo, Egypt 7 INEGRAION OF VC DESALINAION SYSEM WIH COGENERAION PLAN: PARAMERIC SUDY Fuad N. Alasour * and Hadyan F. Alajmi ** * Kuwait University,
More informationParallel Feed MED-MVC System Improved Performance. Saddam El-Tayib (M.Sc) Mohammed A. Antar (PhD) ME Department - KFUPM
Parallel Feed MED-MVC System Improved Performance Saddam El-Tayib (M.Sc) Mohammed A. Antar (PhD) ME Department - KFUPM Introduction Water shortage is related to enormous rise in population and the vastly
More informationThe design of a small-scale multi-stage desalination plant driven by the exhaust of diesel generators
Computational Methods and Experimental Measurements XVII 19 The design of a small-scale multi-stage desalination plant driven by the exhaust of diesel generators R. Jammoul 1 & O. A. El-Samni 1 Mechanical
More informationMethodology of Modeling and Comparing the Use of Direct Air-Cooling for a Supercritical Carbon Dioxide Brayton Cycle and a Steam Rankine Cycle
The 5 th International Symposium Supercritical CO2 Power Cycles March 28-31, 2016, San Antonio, Texas Methodology of Modeling and Comparing the Use of Direct Air-Cooling for a Supercritical Carbon Dioxide
More informationEnergy-Saving Study of a System for Ammonium Sulfate Recovery from Wastewater with Mechanical Vapor Compression (MVC)
Research Journal of Applied Sciences, Engineering and Technology 3(11): 1227-1232, 2011 ISSN: 2040-7467 Maxwell Scientific Organization, 2011 Submitted: July 20, 2011 Accepted: September 07, 2011 Published:
More informationCFD ANALYSIS OF STEAM EJECTOR WITH DIFFERENT NOZZLE DIAMETER
CFD ANALYSIS OF STEAM EJECTOR WITH DIFFERENT NOZZLE DIAMETER 1 B. Sampath 2 Dr.A.Raveendra 1 M.Tech, Thermal Engineering student, Department of Mechanical Engineering, Malla Reddy Engineering College (Autonomous),
More informationThermodynamic Simulation of an Advanced Hybrid Solar-Gas Seawater Desalination System
SolarPACES 24 Oaxaca, Mexico 12th International Symposium on October 6-8, 24 Solar Power and Chemical Energy Systems Thermodynamic Simulation of an Advanced Hybrid Solar-Gas Seawater Desalination System
More informationEXERGY AND THERMOECONOMICS EVALUATION OF MSF DESALINATION PLANTS USING A NEW VISUAL PACKAGE
Ninth International Water Technology Conference, IWTC9 2005, Sharm El-Sheikh, Egypt 157 EXERGY AND THERMOECONOMICS EVALUATION OF MSF DESALINATION PLANTS USING A NEW VISUAL PACKAGE A S Nafey *, H E S Fath,
More informationCFD analysis of flow phenomena inside thermo vapor compressor influenced by operating conditions and converging duct angles
Journal of Mechanical Science and Technology 23 (2009) 2366~2375 Journal of Mechanical Science and Technology www.springerlink.com/content/1738-494x DOI 10.1007/s12206-009-0626-7 CFD analysis of flow phenomena
More informationTHE EFFECT OF FOULING ON PERFORMANCE AND DESIGN ASPECTS OF MULTIPLE EFFECTS DESALINATION SYSTEMS. Furqan Tahir Maimoon Atif Mohammed A.
THE EFFECT OF FOULING ON PERFORMANCE AND DESIGN ASPECTS OF MULTIPLE EFFECTS DESALINATION SYSTEMS Furqan Tahir Maimoon Atif Mohammed A. Antar CONTENTS Introduction Problem Definition & Objectives Methodology
More informationA discussion of"heat pumps as a source of heat energy for desalination of seawater"
DESALINATION ELSEVIER Desalination 169 (004) 161-165 www.elsevier.com/locate/desal A discussion of"heat pumps as a source of heat energy for desalination of seawater" Jinzeng Chen, Suyi Huang* Energy and
More informationEnhancement of CO2 Refrigeration Cycle Using an Ejector: 1D Analysis
Purdue University Purdue e-pubs International Refrigeration and Air Conditioning Conference School of Mechanical Engineering 2006 Enhancement of CO2 Refrigeration Cycle Using an Ejector: 1D Analysis Elias
More informationMathematical Modeling of Perfect Decoupled Control System and Its Application: A Reverse Osmosis Desalination Industrial-Scale Unit
Automated Methods & Management in Chemistry, 2005 (2005), no. 2, 50 54 c 2005 Mathematical Modeling of Perfect Decoupled Control System and Its Application: A Reverse Osmosis Desalination Industrial-Scale
More informationParametric Study of a Vapor Compression Refrigeration Cycle Using a Two-Phase Constant Area Ejector
Vol:7, No:, 01 Parametric Study of a Vapor Compression Refrigeration Cycle Using a Two-Phase Constant Area Ejector E. Elgendy International Science Index, Mechanical and Mechatronics Engineering Vol:7,
More informationModelling and Simulation of MSF Desalination Plant: The Effect of Venting System Design for Non-Condensable Gases
1615 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 39, 2014 Guest Editors: Petar Sabev Varbanov, Jiří Jaromír Klemeš, Peng Yen Liew, Jun Yow Yong Copyright 2014, AIDIC Servizi S.r.l., ISBN 978-88-95608-30-3;
More informationSustainability and Innovation in Desalination. Corrado Sommariva
International Desalination Association Desalination: The Vision of Today and the Future Sustainability and Innovation in Desalination Corrado Sommariva Managing Director generation ILF Middle east 4 March
More informationTOWARDS SUSTAINABLE ENERGY IN SEAWATER DESALTING IN THE GULF AREA
Tenth International Water Technology Conference, IWTC10 2006, Alexandria, Egypt 655 TOWARDS SUSTAINABLE ENERGY IN SEAWATER DESALTING IN THE GULF AREA M. A. Darwish a, N. Al-Najem a, and N. Lior b Mechanical
More informationExperimental investigation of solar-driven double ejector refrigeration system
Experimental investigation of solar-driven double ejector refrigeration system Jedsada Visedmanee a *, Anan Pongtornkulpanich a, Sakda Somkun a and Ananchai U-kaew b a Thermal Energy Research Unit, School
More informationWe are IntechOpen, the world s leading publisher of Open Access books Built by scientists, for scientists. International authors and editors
We are IntechOpen, the world s leading publisher of Open Access books Built by scientists, for scientists 3,800 6,000 20M Open access books available International authors and editors Downloads Our authors
More informationEVALUATION OF A SOLAR POWERED DISTILLATION UNIT AS A MITIGATION TO WATER SCARCITY AND CLIMATE CHANGE
EVALUATION OF A SOLAR POWERED DISTILLATION UNIT AS A MITIGATION TO WATER SCARCITY AND CLIMATE CHANGE Marios C. Georgiou PhD Student / Research Assistant Outline Introduction Water situation in Cyprus Seawater
More informationWater zeolite adsorption heat pump combined with single effect evaporation desalination process
Renewable Energy 24 (2001) 91 111 www.elsevier.nl/locate/renene Water zeolite adsorption heat pump combined with single effect evaporation desalination process Ahmad Al-Ansari a, Hisham Ettouney b,*, Hisham
More informationANALYSIS OF STEAM EJECTOR BY USING COMPUTATIONAL FLUID DYNAMICS
, pp.41~51 Thomson Reuters ID: L-5236-2015 ANALYSIS OF STEAM EJECTOR BY USING COMPUTATIONAL FLUID DYNAMICS Dr.I Satyanarayana 1 Pricipal &Professor of Mechanical Engineering,Sri Indu Institute of Engineering
More informationEffect of Generator, Condenser and Evaporator Temperature on the Performance of Ejector Refrigeration System (ERS)
Journal of Basic and Applied Engineering Research pp. 4-9 Krishi Sanskriti Publications http://www.krishisanskriti.org/jbaer.html Effect of Generator, Condenser and Evaporator Temperature on the Performance
More informationFRESH WATER GENERATORS ONBOARD A FLOATING PLATFORM
FRESH WATER GENERATORS ONBOARD A FLOATING PLATFORM P.K. TEWARI, R.K. VERMA, B.M. MISRA, H.K. SADHULKAN Desalination Division (Chemical Engineering Group), Bhabha Atomic Research Centre, Bombay, India Abstract
More informationNuclear Power Plants Authority, 4 El-Nasr Avenue, Nasr City, P.O. Box 8191, Nasr City 11371, Cairo, Egypt
International Nuclear Energy, Article ID 569658, 6 pages http://dx.doi.org/10.1155/2014/569658 Research Article A Parametric Study of the Impact of the Cooling Water Site Specific Conditions on the Efficiency
More informationEnergy and Buildings
Energy and Buildings 41 (009) 175 181 Contents lists available at ScienceDirect Energy and Buildings journal homepage: www.elsevier.com/locate/enbuild Modeling solar-driven ejector refrigeration system
More informationGEOTHERMAL POWER PLANTS FOR MEDIUM AND HIGH TEMPERATURE STEAM AND AN OVERVIEW OF WELLHEAD POWER PLANTS
Presented at SDG Short Course II on Exploration and Development of Geothermal Resources, organized by UNU-GTP, GDC and KenGen, at Lake Bogoria and Lake Naivasha, Kenya, Nov. 9-29, 2017. Kenya Electricity
More informationENHANCING THE PART LOAD OPERATIONAL PERFORMANCE OF MSF DESALINATION PLANTS
Thirteenth International Water Technology Conference, IWTC 13 2009, Hurghada, Egypt ENHANCING THE PART LOAD OPERATIONAL PERFORMANCE OF MSF DESALINATION PLANTS Hassan E. S. Fath* and Mohamed A. Ismail**
More informationHigh-Efficiency Joule-Thomson Cryocoolers Incorporating an Ejector
1 High-Efficiency Joule-Thomson Cryocoolers Incorporating an Ejector H.S. Cao 1, S. Vanapalli 1, H.J. Holland 1, C.H. Vermeer 2, T. Tirolien 3, H.J.M. ter Brake 1 1 University of Twente, 7500 AE, Enschede,
More informationDE-TOP User s Manual. Version 2.0 Beta
DE-TOP User s Manual Version 2.0 Beta CONTENTS 1. INTRODUCTION... 1 1.1. DE-TOP Overview... 1 1.2. Background information... 2 2. DE-TOP OPERATION... 3 2.1. Graphical interface... 3 2.2. Power plant model...
More informationWritten Presentation Power and Desalination Integrated Systems : Today s Trends
Written Presentation Power and Desalination Integrated Systems : Today s Trends Abstract Jacques Andrianne Tractebel Energy Engineering 7 avenue Ariane, B-1200 Brussels, Belgium Due to the fuel cost increase
More informationHorizontal Falling Film Brine Concentrator
Horizontal Falling Film Brine Concentrator The 3rd International Sede Boqer Conference on Water Technologies, 2012: Advanced Technologies in Water Management Tuesday 16 October 2012 Dr. Yony Weiss, VP,
More informationAN INTRUSIVE METHOD FOR FILM THICKNESS MEASUREMENT ON SMOOTH HORIZONTAL TUBES FOR SUBCOOLED WATER
HEFAT2014 10 th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics 6 9 July 2014 Orlando, Florida AN INTRUSIVE METHOD FOR FILM THICKNESS MEASUREMENT ON SMOOTH HORIZONTAL TUBES
More informationAdvanced Multi-Effect Solar Desalination Technology: The PSA Experience
Advanced Multi-Effect Solar Desalination Technology: The PSA Experience Julián Blanco *, Eduardo Zarza, Diego Alarcón, Sixto Malato, Javier León CIEMAT - PSA, P.O. Box 22, 04200 Tabernas (Almería), Abstract
More informationEffect of Desalination Plant Performance on Water Cost in Dual-Purpose Plant for Production of Water and Electricity
Effect of Desalination Plant Performance on Water Cost in Dual-Purpose Plant for Production of Water and Electricity NARMINE H. ALY *, HOREYA A. ARAFA ** * Desalination Lab., Nuclear research center **Engineering
More informationJJMIE Jordan Journal of Mechanical and Industrial Engineering
JJMIE Jordan Journal of Mechanical and Industrial Engineering Volume 4, Number 3, June, 2010 ISSN 1995-6665 Pages 394-403 Dynamic Modeling and Simulation of MSF Desalination Plants Awad S. Bodalal *, Sayed
More informationThermo-Economic Analysis of a Desalination Device from the Second law of Thermodynamics Point of View and Parameter Investigation
International Journal of Scientific & Engineering Research, Volume 3, Issue 6, June-2012 1 Thermo-Economic Analysis of a Desalination Device from the Second law of Thermodynamics Point of View and Parameter
More informationCOMPARATIVE ANALYSES OF TWO IMPROVED CO 2 COMBINED COOLING, HEATING, AND POWER SYSTEMS DRIVEN BY SOLAR ENERGY
S93 Introduction COMPARATIVE ANALYSES OF TWO IMPROVED CO 2 COMBINED COOLING, HEATING, AND POWER SYSTEMS DRIVEN BY SOLAR ENERGY by Wanjin BAI a* and Xiaoxiao XU b a School of Mechanical and Vehicle Engineering,
More informationSolar-powered Membrane Distillation System: Review and Application to Performance Enhancement
Solar-powered Membrane Distillation System: Review and Application to Performance Enhancement Prof. Dr. Abd Elnaby Kabeel Faculty of Engineering Tanta University Egypt Presentation Contents 1. Introduction
More informationInnovative Process for Comprehensive Treatment of Liquid Radioactive Waste
Innovative Process for Comprehensive Treatment of Liquid Radioactive Waste - 12551 R.A. Penzin, G.A. Sarychev All-Russia Scientific Research Institute of Chemical Technology (VNIIKHT), Moscow, Russia,
More informationComparison of Technical and Economic Performance of the Main Desalination Processes with and without Renewable Energy Coupling
Comparison of Technical and Economic Performance of the Main Desalination Processes with and without Renewable Energy Coupling Ali Al-Qaraghuli and L.L. Kazmerski National Renewable Energy Laboratory,
More informationWaste to energy for seawater desalination plant
Waste to energy for seawater desalination plant Ing. Edmond Zeneli, Prof.Ing.František Jirouš Dr.Sc Abstract The solid waste management is, in different contexts, a very critical issue. The use of landfills
More informationResearch Article Analysis of Thermal Properties on Backward Feed Multieffect Distillation Dealing with High-Salinity Wastewater
Nanotechnology Volume 2015, Article ID 518015, 7 pages http://dx.doi.org/10.1155/2015/518015 Research Article Analysis of Thermal Properties on Backward Feed Multieffect Distillation Dealing with High-Salinity
More informationDEVELOPMENT OF A HYBRID AIR-CONDITIONING SYSTEM DRIVEN BY LOW TEMPERATURE WASTE HEAT
DEVELOPMENT OF A HYBRID AIR-CONDITIONING SYSTEM DRIVEN BY LOW TEMPERATURE WASTE HEAT Hirofumi Sasaki, Hiroyuki Tsuda, Technology Development Dept., Tokyo Gas Co., Ltd., Tokyo, Japan ABSTRACT Waste water
More informationNumerical Investigation of the Flow Dynamics of a Supersonic Fluid Ejector
Proceedings of the International Conference on Heat Transfer and Fluid Flow Prague, Czech Republic, August 11-12, 2014 Paper No. 171 Numerical Investigation of the Flow Dynamics of a Supersonic Fluid Ejector
More informationSIMPACK - MODEL DEVELOPMENT PACKAGE FOR POWER PLANTS
SIMPACK - MODEL DEVELOPMENT PACKAGE FOR POWER PLANTS 1.0 OVERVIEW SIMPACK is a totally integrated set of simulation software development modules for power plants. It is template based modeling tool and
More informationAdvanced Solar Desalination: A Feasible Technology to the Mediterranean Area
Advanced Solar Desalination: A Feasible Technology to the Mediterranean Area J. Blanco, D. Alarcón, E. Zarza, S. Malato, J. León CIEMAT-PSA, P.O. Box 22, 04200 Tabernas (Almería), Spain Tel.: +34 950387900,
More informationAnalysis of water production costs of a nuclear desalination plant with a nuclear heating reactor coupled with MED processes
Desalination 190 (2006) 287 294 Analysis of water production costs of a nuclear desalination plant with a nuclear heating reactor coupled with MED processes Shaorong Wu Institute of Nuclear Energy Technology,
More informationCOEFFICIENT OF PERFORMANCE OF TWO PHASE CONDENSING EJECTOR REFRIGERATION SYSTEM WITH R-22
INTERNATIONAL JOURNAL OF RESEARCH IN COMPUTER APPLICATIONS AND ROBOTICS ISSN 2320-7345 COEFFICIENT OF PERFORMANCE OF TWO PHASE CONDENSING EJECTOR REFRIGERATION SYSTEM WITH R-22 Kuldip Kumar 1, Anjani Kumar
More informationA Simulation Model of Spray Flash Desalination System
Proceedings of the 17th World Congress The International Federation of Automatic Control A Simulation Model of Spray Flash Desalination System Satoru Goto Yuji Yamamoto Takenao Sugi Takeshi Yasunaga Yasuyuki
More informationEjector Expansion Refrigeration Systems
Research Inventy: International Journal Of Engineering And Science Vol.5, Issue 2 (February 2015), PP 25-29 Issn (e): 2278-4721, Issn (p):2319-6483, www.researchinventy.com Ejector Expansion Refrigeration
More informationHORIZONTAL SHELL SIDE FLUIDIZED BED HEAT EXCHANGER, DESIGN CONSIDERATIONS AND EXPERIENCES FROM A PILOT UNIT
HORIZONTAL SHELL SIDE FLUIDIZED BED HEAT EXCHANGER, DESIGN CONSIDERATIONS AND EXPERIENCES FROM A PILOT UNIT M.C. van Beek 1, M. Cancela Vallespin 1, 1 Klaren International, Hanzeweg 35N, 3771 NG, Barneveld,
More informationDavid J. Kukulka a, *, Rick Smith b, Wei Li c VOL. 45, Introduction
799 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 45, 2015 Guest Editors: Petar Sabev Varbanov, Jiří Jaromír Klemeš, Sharifah Rafidah Wan Alwi, Jun Yow Yong, Xia Liu Copyright 2015, AIDIC Servizi
More informationAvailable online at ScienceDirect. Energy Procedia 69 (2015 )
Available online at www.sciencedirect.com ScienceDirect Energy Procedia 69 (2015 ) 1928 1937 International Conference on Concentrating Solar Power and Chemical Energy Systems, SolarPACES 2014 Thermal analysis
More informationDevelopment of an ejector cooling system with thermal pumping effect
International Journal of Refrigeration 29 (2006) 476 484 www.elsevier.com/locate/ijrefrig Development of an ejector cooling system with thermal pumping effect B.J. Huang*, S.S. Hu, S.H. Lee Department
More informationMODELING, DYNAMICS AND CONTROL OF HORIZONTAL TUBE FALLING FILM MULTIEFFECT DESALINATION PLANTS
MODELING, DYNAMICS AND CONTROL OF HORIZONTAL TUBE FALLING FILM MULTIEFFECT DESALINATION PLANTS J. Hackenberg, A. Helbig and W. Marquardt Lehrstulhl für Prozesstechnik RWTH Aachen University of Technology,
More informationEnhancement of LNG Propane Cycle through Waste Heat Powered Absorption Cooling
Enhancement of LNG Propane Cycle through Waste Heat Powered Absorption Cooling A. Mortazavi 1, P. Rodgers 2, S. Al-Hashimi 2, Y. Hwang 1 and R. Radermacher 1 1 Department of Mechanical Engineering, University
More information20/06/2011 Seminar on Geothermal Exploitation Santiago de Chile
Contents Power Plants Steam Power plants Binary Power plants Geothermal Power Plants Single flash systems Binary systems 1 Equipment Well head Gathering piping system Steam separators and moisture separators
More informationRevue des Energies Renouvelables Spécial ICT3-MENA Bou Ismail (2015) Numerical study of a single effect ejector-absorption cooling system
Revue des Energies Renouvelables Spécial ICT3-MENA Bou Ismail (2015) 71-77 Numerical study of a single effect ejector-absorption cooling system D. Sioud 1*, M. Bourouis 2 et A. Bellagi 1 1 Unité de Recherche
More informationProcess control and optimization of wastewater treatment plants using simulation softwares: a review
Review Article International Journal of Advanced Technology and Engineering Exploration, Vol 3(22) ISSN (Print): 2394-5443 ISSN (Online): 2394-7454 http://dx.doi.org/10.19101/ijatee.2016.322006 Process
More informationKeywords: - Waste heat Recovery, Desalination, Turbo spin heat exchanger, Heat transfer, Diesel engine exhaust
EXPERIMENTAL STUDY ON WASTE HEAT RECOVERY FROM EXHAUST OF DIESEL ENGINE USING HEAT EXCHANGER Kavin Suthar 1, Vinaykumar 2 1 ME Thermal Engineering Student, MIT, Piludara 2 Assistant Professor in Mechanical
More informationValidation of Deration of Heat Transfer Coefficient with Brine Usage
International Journal of Engineering Research and Development e-issn: 2278-067X, p-issn: 2278-800X, www.ijerd.com Volume 12, Issue 3 (March 2016), PP.20-27 Validation of Deration of Heat Transfer Coefficient
More informationDesign of a Solar-Driven Ejector Cooling System
Design of a Solar-Driven Ejector Cooling System S. du Clou and M.J. Brooks University of KwaZulu-Natal, Durban, 44, South Africa Centre for Renewable and Sustainable Energy Studies Abstract The Pulse Refrigeration
More informationRMIT University. Presentation at IIT Madras
RMIT University RMIT is a global university of technology and design and Australia's largest tertiary institution. The University enjoys an international reputation for excellence in practical education
More informationUniversity of Bradford ethesis
University of Bradford ethesis This thesis is hosted in Bradford Scholars The University of Bradford Open Access repository. Visit the repository for full metadata or to contact the repository team University
More informationEfficiency improvement of steam power plants in Kuwait
Energy and Sustainability V 173 Efficiency improvement of steam power plants in Kuwait H. Hussain, M. Sebzali & B. Ameer Energy and Building Research Center, Kuwait Institute for Scientific Research, Kuwait
More informationPerformance Analysis of Thermal Vapour Compression Desalination System Coupled to Cogeneration Nuclear Power Plant
Research Journal of Applied Sciences Engineering and Technology 4(8): 941-948, 2012 ISSN: 2040-7467 Maxwell Scientific Organization, 2012 Submitted: October 23, 2011 Accepted: December 08, 2011 Published:
More informationSultan Qaboos University
ACHIEVING THE ZLD TARGET USING INTEGRATED MEMBRANE SYSTEM FOR SEAWATER DESALINATION Sulaiman AL-OBAIDANI Mechanical and Industrial Engineering Department Sultan Qaboos University CONTENTS 1 OVERVIEW OF
More informationFluid Mechanics, Heat Transfer, Thermodynamics. Design Project. Production of Ammonia
Fluid Mechanics, Heat Transfer, Thermodynamics Design Project Production of Ammonia Your assignment is to continue evaluating the details of a process to produce 50,000 tonne/y of ammonia from a syngas
More informationSolar Distillation System Based on Multiple-Effect Diffusion Type Still
Solar Distillation System Based on Multiple-Effect Diffusion Type Still Bin-Juine Huang *1, Tze-Ling Chong 1, Hsien-Shun Chang 1, Po-Hsien Wu 1, Yeong-Chuan Kao 2 1 Department of Mechanical Engineering
More informationGreen FSRU for the future
Green FSRU for the future Presentation at GREEN4SEA Athens April 6 th 2016 Dr. John Kokarakis Vice President Technology & Business Development, Africa, S. Europe Hellenic, Black Sea & Middle East Zone
More informationUsing Simulation Model to Reduce System Design Time and Cost
Purdue University Purdue e-pubs International Refrigeration and Air Conditioning Conference School of Mechanical Engineering 2014 Using Simulation Model to Reduce System Design Time and Cost Vijay Bahel
More informationThe Benefit of Variable-Speed Turbine Operation for Low Temperature Thermal Energy Power Recovery
Purdue University Purdue e-pubs International Compressor Engineering Conference School of Mechanical Engineering 2014 The Benefit of Variable-Speed Turbine Operation for Low Temperature Thermal Energy
More informationParametric Study of a Double Effect Absorption Refrigeration System
Parametric Study of a Double Effect Absorption Refrigeration System 1 Abbas Alpaslan KOCER, 2 Murat OZTURK 1 Uluborlu Selahattin Karasoy Vocational School, Suleyman Demirel University, 32260, Isparta Turkey,
More informationOptimal Design and Thermodynamic Analysis of Gas Turbine and Carbon Dioxide Combined Cycles
The 6th International Supercritical CO 2 Power Cycles Symposium March 27-29, 2018, Pittsburgh, Pennsylvania Optimal Design and Thermodynamic Analysis of Gas Turbine and Carbon Dioxide Combined Cycles Yue
More informationFrance Marie M. Orden and Menandro S. Berana. Proceedings of the World Congress on Engineering 2017 Vol II WCE 2017, July 5-7, 2017, London, U.K.
, July 5-7, 2017, London, U.K. Design and Analysis of Incorporating Two Ejectors for Compression Recovery in the Inlet and Outlet Points of the Compressor in a Vapor Compression System France Marie M.
More informationDevelopment of a basic design tool for Multi-Effect Distillation plant evaporators. H Bogaards BEng
Faculty Engineering i Development of a basic design tool for Multi-Effect Distillation plant evaporators H Bogaards BEng Dissertation submitted in partial fulfilment of the requirements for the degree
More informationIJARI. Nomenclature. 1. Introduction. Volume 2, Issue 2 (2014) ISSN International Journal of Advance Research and Innovation
Thermodynamic Analysis of Alternative Regeneration Gas Turbine Cycle with Twin Shaft System P. V. Ram Kumar *, a, S. S. Kachhwaha b a Department of Mechanical Engineering, Delhi College of Engineering,
More informationDewvaporation Carrier-Gas Enhanced Atmospheric Pressure Desalination. Noah Abbas and Kehinde Adesoye
Dewvaporation Carrier-Gas Enhanced Atmospheric Pressure Desalination Noah Abbas and Kehinde Adesoye Outline Existing Technologies Reverse Osmosis Thermal Processes Dewvaporation Explanation Mathematical
More informationSolar Absorption Aqua-Ammonia Absorption system simulation base on Climate of Malaysia
Solar Absorption Aqua-Ammonia Absorption system simulation base on Climate of Malaysia POORYA OOSHAKSARAEI 1, SOHIF MAT 1, M. YAHYA 1, AHMAD MAHIR RAZALI 1, AZAMI ZAHARIM 2, K. SOPIAN 3 1 Solar Energy
More informationFluid Mechanics, Heat Transfer, and Thermodynamics Fall Design Project. Production of Dimethyl Ether
Fluid Mechanics, Heat Transfer, and Thermodynamics Fall 2001 Design Project Production of Dimethyl Ether We are investigating the feasibility of constructing a new, grass-roots, 50,000 tonne/y, (1 tonne
More informationSMR INTEGRATION OF NUSCALE SMR WITH DESALINATION TECHNOLOGIES
Proceedings of the ASME 2014 Small Modular Reactors Symposium SMR2014 April 15-17, 2014, Washington, D.C., USA SMR2014-3392 INTEGRATION OF NUSCALE SMR WITH DESALINATION TECHNOLOGIES D. T. Ingersoll NuScale
More informationNovel coupling of NPP with MED-RO Hybrid
Novel coupling of NPP with MED-RO Hybrid Leon Awerbuch, Dean of IDA Desalination Academy, President International Desalination Consultancy Assoctiates LLC IAEA s Technical Meeting on User/Vendor Interface
More informationComputational Analysis Of Ejector With Oscillating Nozzle
Purdue University Purdue e-pubs International Refrigeration and Air Conditioning Conference School of Mechanical Engineering 2018 Computational Analysis Of Ejector With Oscillating Nozzle Arun Kodamkayath
More informationFluid Mechanics, Heat Transfer, Fluid Mechanics Design Project. Production of Ethanol
Fluid Mechanics, Heat Transfer, Fluid Mechanics Design Project Production of Ethanol Your assignment is to continue evaluating the details of a process to produce 30,000 tonne/y of ethanol from ethylene.
More informationA review on Present development in refrigeration jet ejector system
Volume: 03 Issue: 0 May-201 wwwirjetnet p-issn: 239-0072 A review on Present development in refrigeration jet ejector system Abstract: This paper focuses and gives idea on the development of ejector cooling
More informationDESALINATION OF SEAWATER USING A HIGH- EFFICIENCY JET EJECTOR
DESALINATION OF SEAWATER USING A HIGH- EFFICIENCY JET EJECTOR A Thesis by MANOHAR D. VISHWANATHAPPA Submitted to the Office of Graduate Studies of Texas A&M University in partial fulfillment of the requirements
More informationSJT Steam Jet Thermocompressor
SJT Steam Jet Thermocompressor Description Jet Compressors can be utilized in a number of applications for steam circulation and increasing lower pressures to be functional. Jet Compressors are generally
More informationThermal Performances Of Three Types Of Ground Heat Exchangers In Short-Time Period Of Operation
Purdue University Purdue e-pubs International Refrigeration and Air Conditioning Conference School of Mechanical Engineering 2010 Thermal Performances Of Three Types Of Ground Heat Exchangers In Short-Time
More informationSolar membrane distillation: theoretical assessment of multi-stage concept
Desalination and Water Treatment www.deswater.com 1944-3994 / 1944-3986 2010 Desalination Publications. All rights reserved. doi: 10.5004/dwt.2010.1363 18 (2010) 133 138 June Solar membrane distillation:
More informationCONDENSATION IMPLOSION EVENT IN STRATIFIED WATER- STEAM SYSTEM
V Minsk International Seminar Heat Pipes, Heat Pumps, Refrigerators Minsk, Belarus, September 8-11, 2003 CONDENSATION IMPLOSION EVENT IN STRATIFIED WATER- STEAM SYSTEM Marijus Seporaitis, Kazys Almenas,
More informationConference Paper Evaluation of a Multiple-Effect Distillation Unit under Partial Load Operating Conditions
Conference Papers in Energy, Article ID 482743, 9 pages http://dxdoiorg/55/23/482743 Conference Paper Evaluation of a Multiple-Effect Distillation Unit under Partial Load Operating Conditions Marios C
More information