Chapter 1 Gas Properties |
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1 | (1) |
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2 | (1) |
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1.3 Density, Specific Weight, and Specific Volume |
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3 | (1) |
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3 | (1) |
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4 | (5) |
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9 | (5) |
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14 | (2) |
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16 | (3) |
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1.9 Pseudo-Critical Properties from Gas Gravity |
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19 | (1) |
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1.10 Impact of Sour Gas and Non-Hydrocarbon Components |
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20 | (1) |
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1.11 Compressibility Factor |
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21 | (6) |
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1.11.1 Standing-Katz Method |
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22 | (1) |
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1.11.2 Dranchuk, Purvis, and Robinson Method |
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23 | (1) |
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1.11.3 American Gas Association (AGA) Method |
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23 | (1) |
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1.11.4 California Natural Gas Association (CNGA) Method |
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24 | (3) |
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27 | (1) |
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27 | (1) |
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28 | (1) |
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29 | (2) |
Chapter 2 Pressure Drop Due to Friction |
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31 | (1) |
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32 | (1) |
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2.3 General Flow Equation |
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33 | (2) |
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2.4 Effect of Pipe Elevations |
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35 | (2) |
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2.5 Average Pipe Segment Pressure |
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37 | (1) |
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2.6 Velocity of Gas in a Pipeline |
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37 | (3) |
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40 | (3) |
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2.8 Reynolds Number of Flow |
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43 | (2) |
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45 | (2) |
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2.10 Colebrook-White Equation |
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47 | (3) |
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50 | (4) |
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2.12 Modified Colebrook-White Equation |
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54 | (3) |
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2.13 American Gas Association (AGA) Equation |
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57 | (4) |
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61 | (3) |
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2.15 Panhandle A Equation |
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64 | (4) |
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2.16 Panhandle B Equation |
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68 | (2) |
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2.17 Institute of Gas Technology (IGT) Equation |
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70 | (4) |
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74 | (2) |
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76 | (1) |
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77 | (1) |
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2.21 Effect of Pipe Roughness |
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78 | (2) |
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2.22 Comparison of Flow Equations |
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80 | (1) |
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81 | (1) |
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82 | (1) |
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83 | (2) |
Chapter 3 Pressure Required to Transport |
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3.1 Total Pressure Drop Required |
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85 | (1) |
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86 | (1) |
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3.3 Effect of Pipeline Elevation |
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86 | (4) |
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3.4 Effect of Changing Pipe Delivery Pressure |
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90 | (3) |
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3.5 Pipeline with Intermediate Injections and Deliveries |
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93 | (11) |
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104 | (7) |
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111 | (10) |
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121 | (2) |
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3.9 Hydraulic Pressure Gradient |
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123 | (3) |
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3.10 Pressure Regulators and Relief Valves |
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126 | (3) |
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3.11 Temperature Variation and Gas Pipeline Modeling |
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129 | (3) |
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132 | (3) |
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135 | (1) |
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136 | (1) |
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137 | (2) |
Chapter 4 Compressor Stations |
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4.1 Compressor Station Locations |
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139 | (7) |
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146 | (1) |
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4.3 Isothermal Compression |
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146 | (2) |
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4.4 Adiabatic Compression |
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148 | (3) |
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4.5 Polytropic Compression |
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151 | (1) |
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4.6 Discharge Temperature of Compressed Gas |
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152 | (1) |
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153 | (4) |
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4.8 Optimum Compressor Locations |
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157 | (6) |
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4.9 Compressors in Series and Parallel |
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163 | (3) |
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4.10 Types of Compressors-Centrifugal and Positive Displacement |
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166 | (2) |
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4.11 Compressor Performance Curves |
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168 | (3) |
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4.12 Compressor Station Piping Losses |
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171 | (1) |
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4.13 Compressor Station Schematic |
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172 | (1) |
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173 | (1) |
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174 | (1) |
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175 | (2) |
Chapter 5 Pipe Loops versus Compression |
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5.1 Purpose of a Pipe Loop |
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177 | (1) |
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5.2 Purpose of Compression |
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178 | (1) |
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5.3 Increasing Pipeline Capacity |
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179 | (10) |
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5.4 Reducing Power Requirements |
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189 | (3) |
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5.5 Looping in Distribution Piping |
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192 | (6) |
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198 | (1) |
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198 | (1) |
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199 | (2) |
Chapter 6 Pipe Analysis |
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201 | (1) |
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202 | (1) |
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203 | (2) |
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6.4 Derivation of Barlow's Equation |
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205 | (2) |
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6.5 Pipe Material and Grade |
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207 | (1) |
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6.6 Internal Design Pressure Equation |
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207 | (2) |
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209 | (1) |
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210 | (1) |
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6.9 Hydrostatic Test Pressure |
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211 | (31) |
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6.10 Blowdown Calculations |
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242 | (1) |
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6.11 Determining Pipe Tonnage |
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243 | (3) |
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246 | (1) |
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246 | (1) |
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247 | (2) |
Chapter 7 Thermal Hydraulics |
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7.1 Isothermal versus Thermal Hydraulics |
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249 | (2) |
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7.2 Temperature Variation and Gas Pipeline Modeling |
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251 | (2) |
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7.3 Review of Simulation Model Reports |
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253 | (20) |
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273 | (1) |
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274 | (1) |
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274 | (1) |
Chapter 8 Transient Analysis and Case Studies |
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275 | (4) |
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8.1.1 Transient Due to Mainline Valve Closure |
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276 | (1) |
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8.1.2 Transient Due to Compressor Shutdown |
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277 | (2) |
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279 | (17) |
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8.2.1 Offshore Pipeline Case |
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279 | (17) |
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296 | (1) |
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296 | (1) |
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297 | (2) |
Chapter 9 Valves and Flow Measurements |
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299 | (1) |
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300 | (2) |
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9.3 Material of Construction |
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302 | (1) |
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9.4 Codes for Design and Construction |
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302 | (1) |
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303 | (2) |
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305 | (1) |
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305 | (1) |
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305 | (1) |
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306 | (1) |
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307 | (1) |
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9.11 Pressure Control Valve |
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308 | (1) |
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309 | (1) |
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9.13 Pressure Relief Valve |
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309 | (1) |
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310 | (1) |
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310 | (11) |
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310 | (20) |
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313 | (1) |
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9.15.1.2 Expansion Factor |
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314 | (7) |
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321 | (2) |
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323 | (2) |
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325 | (1) |
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325 | (1) |
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325 | (3) |
Chapter 10 Pipeline Economics |
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328 | (2) |
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330 | (6) |
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330 | (2) |
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10.2.2 Compressor Stations |
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332 | (1) |
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10.2.3 Mainline Valve Stations |
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333 | (1) |
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10.2.4 Meter Stations and Regulators |
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333 | (1) |
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10.2.5 SCADA and Telecommunication System |
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333 | (1) |
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10.2.6 Environmental and Permitting |
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334 | (1) |
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10.2.7 Right of Way Acquisitions |
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334 | (1) |
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10.2.8 Engineering and Construction Management |
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335 | (1) |
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10.2.9 Other Project Costs |
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335 | (1) |
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336 | (3) |
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10.4 Determining Economic Pipe Size |
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339 | (14) |
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353 | (1) |
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353 | (1) |
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354 | (1) |
Appendix A Units and Conversions |
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355 | (4) |
Appendix B Physical Properties of Various Gases |
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359 | (4) |
Appendix C Pipe Properties-U.S. Customary System of Units |
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363 | (10) |
Appendix D GASMOD Output Report |
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373 | (6) |
Appendix E Summary of Formulas |
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379 | (22) |
Index |
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401 | |