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INTEGRATION OF SOLID OXIDE FUEL CEL
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Abstract It is investigated whether
- Page 9: Preface This report is documentatio
- Page 12 and 13: CONTENTS Preface . . . . . . . . .
- Page 14 and 15: CONTENTS 4.2.3 SOFC stack . . . . .
- Page 16 and 17: CONTENTS A.4 DG appendix . . . . .
- Page 18 and 19: LIST OF FIGURES 4.3 Diagram of sing
- Page 21 and 22: NOMENCLATURE Acronyms Acronym ABS A
- Page 23 and 24: Greek (and other) Symbols Greek (an
- Page 25: Subscripts Subscripts Subscript 2P
- Page 28 and 29: 1. INTRODUCTION Chapter 4, System d
- Page 30 and 31: 1. INTRODUCTION the electricity and
- Page 32 and 33: 1. INTRODUCTION 1.4 SOFC The fuel c
- Page 34 and 35: 1. INTRODUCTION 1.5 Heat driven coo
- Page 36 and 37: 1. INTRODUCTION Cycle description.
- Page 38 and 39: 1. INTRODUCTION Ammonia-water The C
- Page 40 and 41: 1. INTRODUCTION 1.5.3 Platen Munter
- Page 42 and 43: 1. INTRODUCTION Open loop In an ope
- Page 44 and 45: 1. INTRODUCTION 1.7 Problem stateme
- Page 46 and 47: 2. MARKET INVESTIGATION appendix A.
- Page 48 and 49: 2. MARKET INVESTIGATION 2.2.2 Ship
- Page 50 and 51: 2. MARKET INVESTIGATION Pay Back Ti
- Page 52 and 53: 2. MARKET INVESTIGATION 2.3.2 Micro
- Page 54 and 55: 2. MARKET INVESTIGATION Sensitivity
- Page 56 and 57: 2. MARKET INVESTIGATION • ECH pri
- Page 58 and 59: 2. MARKET INVESTIGATION 2.4.3 Resul
- Page 62 and 63: 2. MARKET INVESTIGATION Annuity pri
- Page 64 and 65: 2. MARKET INVESTIGATION 2.4.4 Concl
- Page 67 and 68: C H A P T E R 3 COMPONENT DESCRIPTI
- Page 69 and 70: 3.1. Introduction The seven stream
- Page 71 and 72: 3.2. Absorber - ABSO 3.2 Absorber -
- Page 73 and 74: 3.2. Absorber - ABSO implicitly thr
- Page 75 and 76: 3.4. Burner - BURN 3.4 Burner - BUR
- Page 77 and 78: 3.5. Condenser - COND T [° C ] ΔT
- Page 79 and 80: 3.6. Desorber - DES 3.6 Desorber -
- Page 81 and 82: 3.7. Evaporator - EVAP 3.7 Evaporat
- Page 83 and 84: 3.8. Heat Exchanger - HEX 3.8 Heat
- Page 85 and 86: 3.8. Heat Exchanger - HEX The press
- Page 87 and 88: 3.10. Pre Reformer - PR 3.10 Pre Re
- Page 89 and 90: 3.11. Pump - PUMP 3.11 Pump - PUMP
- Page 91 and 92: 3.12. Solid Oxide Fuel Cell - SOFC
- Page 93 and 94: 3.12. Solid Oxide Fuel Cell - SOFC
- Page 95 and 96: 3.12. Solid Oxide Fuel Cell - SOFC
- Page 97 and 98: 3.14 Cooling Tower - TOWER 3.14. Co
- Page 99 and 100: 3.14. Cooling Tower - TOWER tower d
- Page 101 and 102: 3.14. Cooling Tower - TOWER The air
- Page 103: 3.15. Expansion valve - VA/VB possi
- Page 106 and 107: 4. SYSTEM DESCRIPTION 8 SPG 10 20 1
- Page 108 and 109: 4. SYSTEM DESCRIPTION Pre reformer
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4. SYSTEM DESCRIPTION which increas
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4. SYSTEM DESCRIPTION 4.3 Absorptio
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4. SYSTEM DESCRIPTION 4.3.3 Pumping
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4. SYSTEM DESCRIPTION The temperatu
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4. SYSTEM DESCRIPTION 4.5 Absorptio
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4. SYSTEM DESCRIPTION 4.6 Cooling T
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4. SYSTEM DESCRIPTION (below 100
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4. SYSTEM DESCRIPTION as: Ẇ AC =
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4. SYSTEM DESCRIPTION 4.8 Verificat
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4. SYSTEM DESCRIPTION SOFC net effi
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C H A P T E R 5 SIMULATION AND RESU
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5.1. Basic absorption cooling Figur
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5.1. Basic absorption cooling geous
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5.1.3 Changing evaporator temperatu
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5.1. Basic absorption cooling as de
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5.2. System configurations Red repr
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5.2. System configurations Dual Hea
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5.2. System configurations in a hot
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5.3. Partial optimization of standa
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5.3. Partial optimization of standa
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5.3. Partial optimization of standa
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5.3. Partial optimization of standa
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Anode recycling (α SPG1 ) 5.3. Par
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5.3. Partial optimization of standa
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5.3. Partial optimization of standa
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5.3. Partial optimization of standa
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5.3. Partial optimization of standa
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5.3. Partial optimization of standa
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5.3. Partial optimization of standa
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5.4. Sensitivity Analysis ηsys,el,
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5.4. Sensitivity Analysis the press
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5.4. Sensitivity Analysis 1. The x-
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5.5 Total optimization of system 5.
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5.5. Total optimization of system i
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5.5. Total optimization of system e
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C H A P T E R 6 CASES AND ECONOMICS
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6.2. High humidity climate BBC Home
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6.2. High humidity climate Figure 6
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6.3. Low humidity climate Figure 6.
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6.4. Economics 6.4 Economics When t
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C H A P T E R 7 DISCUSSION In this
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7.1.1 Accuracy and sensitivity 7.1.
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7.2. Economical considerations Furt
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7.2.3 Distributed Generation (DG) D
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7.2. Economical considerations to 6
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7.2. Economical considerations As m
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C H A P T E R 8 CONCLUSION System c
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For the APU segment a SOFC-ABS syst
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C H A P T E R 9 FURTHER WORK Some i
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BIBLIOGRAPHY [1] Acfshop.dk: http:/
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Bibliography [24] Nordea invest: ht
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Appendices 187
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A. MARKET INVESTIGATION A.1 Market
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A. MARKET INVESTIGATION No cost for
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Absorpton unit (free waste heat) Pr
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A. MARKET INVESTIGATION A.3 CHP app
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Absorption Refrigerator RGE 400 fro
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Sensitivity analysis The effect on
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A. MARKET INVESTIGATION A.4 DG appe
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From the "CHP in the Hotel and Casi
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Hotel with 230 rooms and 18000 m^2
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SOFC + Water Heating (no ABS), Cool
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16000 Pay Back Time: Entire System
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SOFC + Water Heating (no ABS), Cool
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Hot climate SOFC + ABS + HW vs pure
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Assumptions SOFC price = 2650kr/kW
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Hot climate Increase (Delta NPV_10)
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Prices of absorption cooling units
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1'000'000 900'000 800'000 143'600 7
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A. MARKET INVESTIGATION A.6 Gas and
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Retail electricity prices Exchange
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B. DIAGRAMS AND PLOTS B.1 GAX diagr
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B. DIAGRAMS AND PLOTS B.3 Closed ad
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B. DIAGRAMS AND PLOTS B.4.2 p-T dia
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C. EES Efficiencies SOFC η inver t
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C. EES ∆ p;GGHE X 1;c = −1 [kPa
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C. EES ˙Q loss;Bur n = 0 [kW ] ˙Q
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C. EES SOFC ∆ T ;SOFC ;av = 30 [C
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C. EES C.2 Results - Standard param
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C. EES 244 DES2 h;o = 42 DES2 i = 7
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C. EES SOFC ano;i = 5 SOFC ano;o =
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C. EES Point T i p i ṁ i qu i h i
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C. EES C.3 Results - Optimized para
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C. EES ∆ T ;min;W GHE X 3;w;i = 1
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C. EES ˙Q tr ans;W GHE X 3 = 2,752
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C. EES Point T i p i ṁ i qu i h i
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C. EES C.4 Results - Uncertainty pr
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C. EES ∆T ;min;W GHE X 3;w;i = 15
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C. EES ∆p;TOW ER1;air ;dr y = 0,1
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C. EES ∆p;GGHE X 1;c = −1 ±
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C. EES C.4.4 ∆p for absorption su
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C. EES C.4.5 ˙Qloss for absorption
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A P P E N D I X D OTHER D.1 Explana
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D.3. Water consumption Hence it is
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A P P E N D I X E OPTIMIZATION GRAP
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E.1. Simulations and Results E.1.2
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E.1. Simulations and Results Figure
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E.1. Simulations and Results Figure
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E.2. Cases E.2 Cases E.2.1 Extreme
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SEG Scandinavian Energy Group Aps.
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SEG Scandinavian Energy Group Aps.
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SEG Scandinavian Energy Group Aps.
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SEG Scandinavian Energy Group Aps.
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8 SPG 1 10 1-α GGHEX1 9 α 7 GGHEX
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1 8 GGHEX1 CH4, in Air, in 21 2 11