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Chapter 1Introduction and Basic Con
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4-2 Energy Balance for Closed Syste
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7-2 The Increase of Entropy Princip
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Development of Gas TurbinesDeviatio
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ProblemsChapter 13Gas Mixtures13-1
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17-1 Stagnation Properties17-2 Spee
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Appendix 2Property Tables and Chart
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PREFACEBACKGROUNDThermodynamics is
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Preface | xixcoverage of oblique sh
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starts with the simplest case and a
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A CHOICE OF SI ALONE OR SI/ENGLISH
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Chapter 1INTRODUCTION AND BASIC CON
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particles to determine the pressure
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did not find universal acceptance u
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1 J 1 N # m (1-3)Chapter 1 | 7wher
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mN kgs 2andlbf 32.174 ftlbm s 2 C
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devices is best studied by selectin
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diameter) is much larger than the m
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A system is called a simple compres
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time in a periodic manner, and the
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points on a plane, these two measur
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We emphasize that the magnitudes of
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Chapter 1 | 23P gageP vacP atmP atm
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the pressure difference between poi
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Chapter 1 | 27Solution The reading
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Other Pressure Measurement DevicesA
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Chapter 1 | 31EXAMPLE 1-8Measuring
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Chapter 1 | 33Performing the integr
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Keep in mind that the solutions you
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Chapter 1 | 37which is an exact mat
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Chapter 1 | 39SUMMARYIn this chapte
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1-23C What is a steady-flow process
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60 NP atm = 95 kPam P = 4 kgChapter
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unknown density is poured into one
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1-96 The average temperature of the
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Chapter 1 | 491-112E Consider a U-t
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Chapter 2ENERGY, ENERGY TRANSFER, A
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Now if asked to name the energy tra
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Some Physical Insight to Internal E
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uranium-235 atom absorbs a neutron
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gz b E # mech m # e mech m # a P
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A process during which there is no
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Heat and work are directional quant
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Chapter 2 | 65Solution A well-insul
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EXAMPLE 2-7Power Transmission by th
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EXAMPLE 2-8Power Needs of a Car to
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erty is the total energy. Note that
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Chapter 2 | 73of a system during a
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E in E out ¢E systemChapter 2
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Chapter 2 | 777 cents per kWh, dete
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all resistance heaters is 100 perce
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the food to the energy consumed by
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converted entirely from one mechani
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Chapter 2 | 85Then the rate at whic
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usually grouped as hydrocarbons (HC
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Chapter 2 | 89a certain amount of a
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mechanical energy, and thus electri
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Chapter 2 | 93In solids, heat condu
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Chapter 2 | 95In general, both e an
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The energy flow rate associated wit
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2-23C What is the caloric theory? W
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this escalator. What would your ans
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espectively. If the pressure rise o
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700 W/m 2 and the surrounding air t
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The water flow rate through the pum
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2-141 The roof of an electrically h
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166 | ThermodynamicsThe movingbound
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168 | Thermodynamicscompression pro
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170 | ThermodynamicsEXAMPLE 4-3Isot
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172 | Thermodynamicsthe gas, and (c
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174 | ThermodynamicsGeneral Q - W =
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176 | ThermodynamicsUse actual data
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178 | ThermodynamicsVacuumP = 0W =
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180 | ThermodynamicsAIRm = 1 kg300
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182 | ThermodynamicsAIRT, Ku, kJ/kg
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184 | ThermodynamicsAIR at 300 Kc v
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186 | ThermodynamicsEXAMPLE 4-9Heat
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188 | ThermodynamicsP, kPa35023AIRF
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190 | ThermodynamicsFor solids, the
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⎫ ⎪⎬⎪⎭⎫⎪⎬⎪⎭192
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194 | ThermodynamicsA 300-Wrefriger
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196 | Thermodynamicsdays.) Although
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198 | ThermodynamicsTABLE 4-3The ra
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200 | ThermodynamicsSolution A pers
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202 | Thermodynamics4-7 A piston-cy
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204 | Thermodynamics4-30 A well-ins
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206 | Thermodynamics(Table A-2b), a
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208 | Thermodynamicsa rate of 100 b
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210 | Thermodynamicsof carbohydrate
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212 | ThermodynamicsQHePV n = const
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214 | Thermodynamicsthe entire air
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216 | Thermodynamics4-149 The speci
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218 | Thermodynamicsduring vacuum c
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220 | Thermodynamics2 kgH 216 kgO 2
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222 | Thermodynamicsm in = 50 kgWat
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224 | ThermodynamicsIt states that
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226 | Thermodynamicswhere A jet pD
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228 | ThermodynamicsThe fluid enter
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230 | ThermodynamicsFIGURE 5-17Many
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232 | ThermodynamicsCVW˙eW˙shFIGU
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234 | ThermodynamicsEXAMPLE 5-4Dece
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236 | ThermodynamicsDividing by the
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238 | ThermodynamicsAnalysis We tak
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240 | Thermodynamicsu 1 = 94.79 kJ/
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242 | Thermodynamics50°CFluid B70
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244 | ThermodynamicsR-134a. .Qw,in
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246 | ThermodynamicsSubstituting th
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248 | Thermodynamicsone of these wi
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250 | Thermodynamicssince the initi
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252 | ThermodynamicsThus,andv 2 0.
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254 | Thermodynamicsenergy per unit
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256 | Thermodynamicsunsteady-flow p
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258 | Thermodynamics5-15 Air enters
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260 | ThermodynamicsTurbines and Co
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262 | Thermodynamicsby the incoming
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264 | Thermodynamicsthe furnace. Ai
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266 | Thermodynamicsmass flow rate
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268 | Thermodynamicstank exists in
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270 | Thermodynamicsis allowed to e
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272 | Thermodynamicsfind the simple
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274 | Thermodynamicsenters the buil
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276 | Thermodynamicsopened, and air
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278 | Thermodynamics5-212 Refrigera
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280 | ThermodynamicsHOTCOFFEEHeatFI
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282 | ThermodynamicsWATERWorkFIGURE
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284 | ThermodynamicsorIt can also b
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286 | Thermodynamicsthe cycle, even
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288 | ThermodynamicsSurrounding med
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290 | ThermodynamicsFIGURE 6-23When
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292 | Thermodynamicsheat to the hou
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294 | ThermodynamicsSystem boundary
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296 | ThermodynamicsINTERACTIVETUTO
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298 | Thermodynamics20°CHeat5°C20
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300 | ThermodynamicsEnergysourceat
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302 | Thermodynamics1Irrev.HEHigh-t
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304 | Thermodynamicshave the same e
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306 | ThermodynamicsHigh-temperatur
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308 | ThermodynamicsQuantity versus
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310 | ThermodynamicsWarm environmen
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312 | ThermodynamicsTABLE 6-1Typica
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314 | ThermodynamicsCoolairWarmairR
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316 | Thermodynamicswhere W net,out
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318 | Thermodynamicsbetween the tem
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320 | Thermodynamics·120 kPax = 0.
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322 | ThermodynamicsIf the air surr
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324 | ThermodynamicsSpecial Topic:
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326 | Thermodynamics°F temperature
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328 | Thermodynamics$800 more to in
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330 | ThermodynamicsIf heat is supp
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332 | ThermodynamicsReversiblecycli
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334 | ThermodynamicsT∆S = S 2 - S
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336 | ThermodynamicsProcess 1-2(rev
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338 | ThermodynamicsSurroundings∆
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T340 | ThermodynamicsP 1 s 1 ≅ sT
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342 | ThermodynamicsEXAMPLE 7-4Entr
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344 | ThermodynamicsThe power outpu
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346 | ThermodynamicsTT HT L4A1 2W n
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348 | ThermodynamicsW shHOT BODY80
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350 | Thermodynamicsis highly irrev
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352 | ThermodynamicsEXAMPLE 7-7Effe
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354 | ThermodynamicsThen the power
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356 | ThermodynamicsandT 2 P 2s 2
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358 | ThermodynamicsIsentropic Proc
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360 | ThermodynamicsThe quantity T/
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362 | ThermodynamicsT, RT 2 = 780 R
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364 | ThermodynamicsIn gas power pl
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366 | ThermodynamicsP 1 , T 1TURBIN
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368 | ThermodynamicsPP 22Work saved
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370 | ThermodynamicsThe compressor
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372 | ThermodynamicsT,°CP 1 = 3 MP
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374 | ThermodynamicsEXAMPLE 7-15Eff
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376 | ThermodynamicsT, KP 1 = 200 k
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378 | ThermodynamicsEntropy Change
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380 | ThermodynamicsS inMassHeatSys
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382 | Thermodynamicsor, in the rate
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384 | ThermodynamicsT,°C4501Thrott
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386 | Thermodynamics(c) The entropy
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388 | ThermodynamicsSubstituting, t
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390 | Thermodynamicsat 100°C while
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392 | ThermodynamicsCompressor: 125
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394 | ThermodynamicsThen the mass f
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396 | ThermodynamicsW electricMotor
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398 | ThermodynamicsOutsideairWallA
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400 | Thermodynamicsambient in a li
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402 | ThermodynamicsPROBLEMS*Entrop
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404 | Thermodynamicsthis problem. L
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406 | Thermodynamics7-62C Starting
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408 | Thermodynamics7-91 Liquid wat
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410 | Thermodynamicstemperature of
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412 | Thermodynamics7-136E In a pro
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414 | Thermodynamicsfull load, and
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416 | Thermodynamics7-174 Consider
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418 | Thermodynamicsare 104°C and
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420 | Thermodynamicswater pipe heat
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422 | Thermodynamicsisentropic effi
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424 | ThermodynamicsAIR25°C101 kPa
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426 | Thermodynamicsm⋅⋅W max =
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428 | ThermodynamicsAtmosphericairP
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430 | ThermodynamicsIRON200°C27°C
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432 | Thermodynamicsof heat to the
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434 | ThermodynamicsFor a heat engi
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436 | Thermodynamicswhen the direct
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438 | ThermodynamicsEnergy:Exergy:e
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440 | ThermodynamicsThe properties
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442 | ThermodynamicsHeattransferEnt
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444 | ThermodynamicsThis equation c
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446 | ThermodynamicsOutersurroundin
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448 | ThermodynamicsBrick27°Cwall0
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450 | ThermodynamicsThat is, if the
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452 | Thermodynamics(b) The reversi
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454 | Thermodynamics(a) Noting that
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456 | ThermodynamicsThe useful work
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458 | ThermodynamicsWX workm ic iSu
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460 | Thermodynamicscold stream, pr
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462 | Thermodynamics(c) The second-
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464 | ThermodynamicsAssumptions 1 A
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466 | Thermodynamics“Now I’m in
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468 | ThermodynamicsI have only jus
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470 | ThermodynamicsExergytransferb
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472 | Thermodynamics8-21 How much o
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474 | Thermodynamicsactivated to st
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476 | Thermodynamics8-66E Refrigera
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478 | Thermodynamics8-87 Ambient ai
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480 | Thermodynamicsof the inner an
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482 | Thermodynamicssteam. Neglecti
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484 | Thermodynamics8-137 An adiaba
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Chapter 9GAS POWER CYCLESTwo import
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Chapter 9 | 489FIGURE 9-4An automot
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Isothermalcompressorq out43Isentrop
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oom temperature (25°C, or 77°F).
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Initially, both the intake and the
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and the specific heat ratio. This i
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Chapter 9 | 499P 3 v 3T 3 P 2v 2T 2
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We now define a new quantity, the c
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Chapter 9 | 503Process 2-3 is a con
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also by contacting some condenser m
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608 | ThermodynamicsWARMenvironment
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610 | ThermodynamicsINTERACTIVETUTO
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612 | ThermodynamicsP34Q LQ H12W in
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614 | Thermodynamicsand the turbine
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616 | ThermodynamicsAnalysis The T-
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618 | Thermodynamicshalogenated CFC
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620 | Thermodynamicsa result of thi
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622 | Thermodynamics(In practice, t
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624 | ThermodynamicsIn this system,
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626 | ThermodynamicsKitchen airTQ H
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628 | ThermodynamicsThis and other
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630 | ThermodynamicsCOLDrefrigerate
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632 | ThermodynamicsTo understand t
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634 | Thermodynamicsdecreasing sour
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636 | ThermodynamicsHeatrejectedHea
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638 | Thermodynamicsthe cycle on a
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640 | Thermodynamicsand 60°C. The
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642 | Thermodynamics6Gas Refrigerat
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644 | Thermodynamics11-79C A copper
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646 | Thermodynamics334°C·Q HCond
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648 | Thermodynamicsthen cooled to
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Chapter 12THERMODYNAMIC PROPERTY RE
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even be replaced by differences, wh
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Partial Differential RelationsNow l
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Two of the Gibbs relations were der
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volume. That is, P sat f (T sat ).
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Chapter 12 | 661to obtain saturatio
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Equating the coefficients of dT and
- Page 690 and 691:
An alternative form of this relatio
- Page 692 and 693:
Chapter 12 | 667For an ideal gas P
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temperature. This presents a proble
- Page 696 and 697:
v ZRT/P and simplifying Eq. 12-56,
- Page 698 and 699:
ors 2 s 1 1s 2 s 1 2 ideal R 1Z
- Page 700 and 701:
For liquid-vapor and solid-vapor ph
- Page 702 and 703:
General Relations for du, dh, ds, c
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12-80 Reconsider Prob. 12-79. Using
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Chapter 13GAS MIXTURESUp to this po
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Chapter 13 | 683EXAMPLE 13-1Mass an
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Dalton’s and Amagat’s laws can
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y i b ikka m a a y i a 1>2i b2andb
- Page 714 and 715:
Chapter 13 | 689This is 33 percent
- Page 716 and 717:
where P i,2 y i,2 P m,2 and P i,1
- Page 718 and 719:
dh m T m ds m v m dP m each other
- Page 720 and 721:
Chapter 13 | 695critical temperatur
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Chapter 13 | 697Discussion This res
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Chapter 13 | 699ing processes, nega
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Chapter 13 | 701gory of ideal solut
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Chapter 13 | 703It can also be expr
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Chapter 13 | 705water capacity of o
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Chapter 13 | 707(d ) The osmotic pr
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Chapter 13 | 709REFERENCES AND SUGG
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13-42E A rigid tank contains 1 lbmo
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6.50 percent water vapor, 12.20 per
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13-102 One compartment of an insula
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718 | ThermodynamicsT, °C50T,°C-1
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720 | ThermodynamicsAIR25°C,1 atmm
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722 | ThermodynamicsTT 1T dp2P v =
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724 | ThermodynamicsThus,Energy bal
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726 | Thermodynamics(c) The enthalp
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728 | ThermodynamicsFIGURE 14-17We
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730 | ThermodynamicsMost air-condit
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732 | Thermodynamics1 atm, either o
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734 | ThermodynamicsThen,Water that
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736 | Thermodynamicsh 1h 3 - h 1ω
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738 | ThermodynamicsWARMWATERCOOLWA
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740 | ThermodynamicsThe enthalpy of
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742 | ThermodynamicsDew-Point, Adia
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744 | Thermodynamics14-71 Repeat Pr
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746 | Thermodynamicsat 22°C. Deter
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748 | Thermodynamics14-123E The U.S
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750 | ThermodynamicsDesign and Essa
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752 | ThermodynamicsCRUDEOILGasolin
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754 | ThermodynamicsReactantsFIGURE
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756 | Thermodynamicsoxygen, giving
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758 | ThermodynamicsAssumptions 1 C
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760 | ThermodynamicsThus,T dp T sa
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762 | ThermodynamicsATOMMOLECULENuc
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764 | Thermodynamics1 kmol C25°C,
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766 | ThermodynamicsEnthalpy at25°
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768 | Thermodynamics1500 K, determi
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770 | Thermodynamics(b) Noting that
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772 | ThermodynamicsAssumptions 1 T
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774 | ThermodynamicsTTs(T,P)∆s =
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776 | ThermodynamicsC77°F, 1 atmO
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778 | Thermodynamics(b) Noting that
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780 | ThermodynamicsThen the total
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782 | ThermodynamicsHybrid power sy
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784 | Thermodynamics15-6C What is t
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786 | Thermodynamicstemperature of
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788 | Thermodynamicsof the surround
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790 | Thermodynamicsthis fuel mixtu
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792 | ThermodynamicsThe entropy cha
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794 | ThermodynamicsCO 2 CO 2COO 2C
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796 | ThermodynamicsH 2 → 2H0.1H
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798 | ThermodynamicsEXAMPLE 16-1Equ
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800 | ThermodynamicsT, K10002000300
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802 | ThermodynamicsAssumptions 1 T
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804 | ThermodynamicsTheny 3 x 0.
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806 | ThermodynamicsSolving Eqs. (1
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808 | ThermodynamicsFIGURE 16-17Wet
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810 | ThermodynamicsT, PNH 3 + H 2
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812 | Thermodynamicsorory A,gas sid
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814 | ThermodynamicsAirEXAMPLE 16-9
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816 | Thermodynamicswhere ∆n n C
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818 | Thermodynamics16-21 Carbon mo
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820 | Thermodynamics16-60C Using th
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822 | Thermodynamics16-102 The equi
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824 | ThermodynamicsFIGURE 17-1Airc
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826 | ThermodynamicsTemperaturerise
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828 | Thermodynamicswhich yieldsdh
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830 | ThermodynamicsAssumptions 1 C
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832 | ThermodynamicsFluidFluidThroa
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834 | ThermodynamicsMa < 1P decreas
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836 | ThermodynamicsEXAMPLE 17-4Cri
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838 | Thermodynamicscritical ratio.
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840 | ThermodynamicsThe critical-pr
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842 | ThermodynamicsFIGURE 17-26Con
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844 | Thermodynamicscrosses the nor
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846 | ThermodynamicsMa 1 > 1FlowV 1
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848 | ThermodynamicsCombining Eqs.
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850 | ThermodynamicsDifferentiating
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852 | ThermodynamicsFIGURE 17-36Sch
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854 | ThermodynamicsT 22 [2 (k 1)
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856 | ThermodynamicsFIGURE 17-43Sti
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858 | ThermodynamicsFIGURE 17-47The
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860 | ThermodynamicsSolution We are
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862 | Thermodynamicsa state functio
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864 | ThermodynamicsTMa 1T maxdT
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866 | ThermodynamicsProperty Relati
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868 | ThermodynamicsQ .EXAMPLE 17-1
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870 | ThermodynamicshWilson line (x
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872 | Thermodynamics(b) The velocit
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874 | ThermodynamicsPROBLEMS*Stagna
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876 | Thermodynamicsvelocities at t
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878 | Thermodynamics17-97C On a T-s
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880 | Thermodynamics17-135 Helium e