Contents & References of The use of combined methods with the perspective of exergy analysis in order to modify the gas turbine cycle with the simultaneous production of fresh water in the multistage distillation system and its economic feasibility.
List:
Introduction..1
Introduction..2
Chapter 2 thermodynamic design and exergy analysis of gas turbine cycle.10
2-1. Introduction..11
2-2. Cycle thermodynamic model..11
2-2-1 Compressor..12
2-2-2 gas turbine exergy analysis study.
2-4 Investigation of one stage of the evaporative desalination unit with a sudden pressure drop. 24
. 2-4-1- Mathematical modeling of the evaporative desalination process with a sudden pressure drop. 28
Chapter 3 Feasibility of fresh water production at Khaij Fars power plant. 32
3-1. Introduction..33
3-2. Determining the location of water intake in the sea..34
3-2-1. The condition of the waves..34
3-2-2 Sea and Sea..34
3-2-3 Determining the location of the site..34
3-2-4 Determining the appropriate method of water extraction from the sea.35
3-2-5 Determining the thermal balance calculations of the recovery boiler. Regenerative. 37
3-2-7 Use of electricity produced by the recuperative boiler. 38
3-2 Factors affecting production costs. 38
Chapter 4 Review of the economy of the unit of simultaneous production of electricity and fresh water. 41
4-1. Analysis of the economics of water desalination plants. 42
4-1-1 MSF method..42
4-2. Investigation of investment costs in different types of water desalination plants. 45
Chapter 5 methods of improving gas turbine cycle performance by aiming at the optimal point. 48
5-1. Absorption refrigeration system..49
5-1-1. Introduction..49
5-2-. The effects of temperature change on gas turbine performance parameters.50
5-3 advantages and disadvantages..52
5-4. Technical plan of cooling system..53
5-5. The results of the simulation in ASPEN. 56
5-6 Exergy calculations in the power and fresh water production unit. 60
5-6-1 Exergy calculations in the auxiliary combustion boiler. 67
5-7 Costs of construction and installation of the recovery boiler. 67
5-8 Functional system of a lithium-bromide absorption refrigeration unit. 68
5-9 The results of the operation of two MSF units by increasing the load capacity in one turbine unit.71
5-10 Calculation of the cooling load..78
5-11 Investigating the climatic conditions of the power plant location.82
5-12 Economic analysis..85
5-13 Thermodynamic analysis and evaluation of the turbine layer cooling process on performance Cycle. 86
5-14 Cooling process study..88
5-15 Turbine modeling..90
5-16 Internal cooling model..92
5-17 Infiltration cooling model..92
5-19 Cycle thermodynamic analysis..95
5-20 Analysis Results..98
5-21 system selection parameters for desalination units.109
5-22 comparison of reverse osmosis system with multi-stage evaporation system..109
5-23 conclusion..113
Reference and sources..114
Source:
Technical documents of Bandar Abbas power plant and 1-documents
ASPEN20062 - Process design and simulation software
[3]- Y., Cengel, M., A., Boles, "Thermodynamics: An Engineering
Approach", McGraw-Hill publication, Fourth edition, 2001.
[4]-: A. Bejan, "Advanced, Engineering Thermodynamics", John
Wiley & Sons, New York, 1988
[5]-Robert H. Perry, Don Green, "Perry's Chemical Engineering Handbook" Sixth Edition, McGraw-Hill, 1984.
[6]. Krishna, H. J., "Introduction to Desalination Technologies," University of Texas, pp. 1-7.
[7]. United Nations world water development report, "Water for people water for life", 2003
8-Technical and economic feasibility of using Bandar Abbas gas turbine in desalination units. Ramin Haghighi Khushkho. Sixth National Energy Conference
[9] Jones, J.B, and Hawkins, G.A., IZb[, "Engineering Thermodynamics", John Wiley & Sons, Inc.
[10] Spina, P.R. "Gas Turbine Performance by Using Generalized Performance Curves of Compressor and Turbine Stages", ASME Turbo Expo 2002.
[11] Cumpsty, N.A. "Compressor aerodynamics", Longman Scientific & Technical, pp15-17, 1989.
[12] Tribu, M. et. al, Thermodynamic and Economic considerations in the preparation of fresh water from sea water, VCLA Rpt, No. 56-16, 197
[13] A. Valero, MA. lozano and c.torres, "Application at the exergetic cost of theTorres, "Application of the exergetic cost to the CGAM problem", Energy vol. 99, No. 3 pp.365-381.1994
[14]Dr. Andrew K. Johns, Optimized Combustion Using Computational Modeling Combustion Unit, A.B.B
[15]-A. bejan, G. tsatsaronis, M. moran, THERMAL DESIGN AND OPTIMIZATION, john wiley &sons, INC
Increasing the capacity of gas turbines of Chabahar power plant. Mohammad Ameri. Simultaneous production of electricity and 16- Presenting a suitable method for increasing the capacity of Jabahar power plant. Mohammad Ameri unit of simultaneous production of electricity and heat. University of Water and Electricity Industry
16- Heat. University of Water and Electricity Industry.
[17]Dr. Osman Ahmed Hamed, Mohammad AK. THERMODYNAMIC ANALYSIS OF AL-JUBAIL POWER WATER CO-GENERATION CYCLES, Saline Water Conversion Corporation
[18] Al-Sofi, M. AK., (1985), MSF Chemical and Fuel Consumption in Dual Purpose Plants, Third Arab Energy Conference, Algiers, Algeria, May, 6, 205 - 240.
[19]Darwish, M. A, Yousuf, F. A. and Al-Najem, N. M., (1997), Energy Consumption and Cost with a Multi-Stage Flash (MSF) Desalting System, Desalination, 109, 285-302.
[20] Wade, N. M. and Fletcher, R. S., (1995), Energy Allocation and Other Factors Influencing Water Costs in Desalination and Dual Purpose Power / Water Plants, Proceeding, of the IDA World Congress on Desalination and Water Sciences, Abu Dhabi, UAE, November
[21] V. Dvornikov, Seawater multi-effect distillation energized by a combustion turbine, Desalination, 127 (2000) 261–269.
[22] M.A. Darwish and A. Alsairafi, Technical comparison between TVC/MEB and MSF, Desalination, 170 (2004) 223–239.