printing common output file contents

8/13/2019 Printing Common Output File Contents

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Common Output File ContentsUnits

Item Description X ace X phe X ist SI US MKH Type

1 Breaker record (seventy-eight asterisks on one line) followed by theunits type in parenthesis. Values are (SI UNITS), (US UNITS), (MKHUNITS), or blank. If blank, the file is in US Customary units.

— — — —

2 Case Identification (70 columns) — — — alpha

3 Problem Description (70 columns) — — — alpha

4 Program version number — — — real

5 Number of data check informative messages — — — integer

6 Number of data check warning messages — — — integer

7 Number of data check error messages — — — integer

8 Number of data check fatal error messages — — — integer

9 Number of run time informative messages — — — integer

10 Number of run time warning messages — — — integer

11 Number of run time error messages — — — integer

12 Number of run time fatal error messages — — — integer

13 Calculation mode — — — alpha

• Rating

• Design

• Simulation

14 Flow direction 1st pass — — — alpha

• Countercurrent

• Cocurrent

15 Total shellside volume, shell-and-tube exchanger m³ ft³ m³ real

16 Total tubeside volume, shell-and-tube exchanger m³ ft³ m³ real

17 Tube type — — — alpha• X is t

Plain

Finned

• X ace

Plain

Low-finned

High-finned

Stud-finned

18 Number of cost units — — — real

19 Shell type (TEMA designation) — — — alpha

20 Number of shells in parallel — — — integer

21 Number of shells in series — — — integer

22 Number of pairs of sealing strips — — — integer

23 Percent overdesign — — — real

24 Total area m² ft² m² integer

25 Total heat transfer area (for one shell) m² ft² m² real

26 Number of tubes in window — — — real

27 Impingement protection — — — alpha

• Yes

• No



28 Bundle to shell diametral clearance mm in. mm real

29 Baffle to shell diametral clearance mm in. mm real

30 Baffle to tube diametral clearance mm in. mm real

31 Baffle cut, percent of shell diameter % % % real

32 Central baffle spacing mm in. mm real

33 Inlet baffle spacing mm in. mm real34 Outlet baffle spacing mm in. mm real

35 Angle of baffle cut to centerline nozzle deg deg deg real

36 Baffle type — — — alpha

• None

• Segmental

• Double-segmental

• Triple-segmental *

• No-tubes-in-window (NTIW) segmental

• Support plates

• Rod-ring RODbaffles *

• Plate-ring RODbaffles *

• RODbaffles

*These baffle types were available in previous HTRI programs,but are not available currently in X ist .

37 Baffle thickness mm in. mm real

38 Number of crosspasses — — — integer

39 Number of tubepasses — — — integer

40 Tube OD mm in. mm real

41 Tube ID mm in. mm real

42 Tube pattern deg deg deg real

43 Tube pi tch mm in. mm real

44 Thermal conductivity tube material W/m °C Btu/hr ft °F kcal/hr m °C real

45 Tube material code — — — integer

46 Total number of tubes (Previous HTRI programs output this value asan integer.)

— — — real

47 Low-fin tube root diameter mm in. mm real

48 Wall thickness under fins mm in. mm real

49 Number of fins per unit length 1/m 1/in. 1/m real

50 Fin height mm in. mm real

51 Fin thickness mm in. mm real

52 Tube plain at the baffles — — — alpha

• Yes

• No

53 Total tube length m ft mm real

54 Effective tube length m ft mm real

55 Shell inlet nozzle diameter mm in. mm real

56 Shell outlet nozzle diameter mm in. mm real

57 Bundle weight kb lb kg real

58 Height under shell inlet nozzle mm in. mm real

59 Height under shell outlet nozzle mm in. mm real

60 Number of tuberows in crossflow — — — real

61 Number of tuberows in crossflow in the windows — — — real

62 Number of tuberows submerged — — — real

63 Total flow shellside kg/s lb/hr 1000 kg/hr real

64 Total flow tubeside kg/s lb/hr 1000 kg/hr real



208 Maximum heat flux W/m² Btu/hr ft² kcal/hr m² real

209 Vapor generation rate kg/s lb/hr kg/hr real

210 Total vapor rate kg/s lb/hr kg/hr real

211 Maximum wet wall superheat °C °F °C real

212 Temperature difference for film boiling at onset °C °F °C real

213 Temperature difference for film boiling at completion °C °F °C real

214 Shell orientation angle (from horizontal) deg deg deg real

215 Differential resistance m² °C/W hr ft² °F/Btu hr m² °C/ kcal real

216 Total length of boiling side inlet piping mm in. mm real

217 Total length of boiling side outlet piping mm in. mm real

218 Vertical height mm in. mm real

219 Static pressure drop kPa psi kg/cm² real

220 Frictional pressure drop kPa psi kg/cm² real

221 Valve pressure drop, inlet kPa psi kg/cm² real

222 Valve pressure drop, outlet kPa psi kg/cm² real

223 Area ratio (fin/bare) — — — real

224 Fin type (high-finned tubes only) — — — alpha

225 Over-fin diameter mm in. mm real

226 Number of fans per bay — — — integer

227 Fan diameter m ft mm real

228 Fan brake horsepower (BHP) W hp W real

229 Motor power per fan W hp W real

230 Tube wall thickness mm in. mm real

231 Design pressure, shellside KPa G psig kg/cm² G real

232 Design pressure, tubeside KPa G psig kg/cm² G real

233 Design temperature, shellside °C °F °C real

234 Design temperature, tubeside °C °F °C real

235 Tubeside nozzle entrance type — — — alpha

• Axial

• Radial

236 Tube bundle diameter (OTL) mm in. mm real

237 Double tubesheet design — — — alpha

• Yes

• No

238 No-tubes-in-window — — — alpha

• Yes

• No

239 Expansion joint — — — alpha

• Yes

• No

240 U-bend orientation — — — alpha

• Horizontal

• Vertical

241 Fin efficiency — — — real

242 Fin thickness at tip — — — real

243 Fan area per face area — — — real

244 Fin tip clearance — — — real

245 Fin material code — — — real

246 Fin material thermal conductivity W/m °C — kcal/hr m °C real

247 Fluid allocation code

— — — integer

1 = Shell hot



2 = Shell cold

248 Shell ID mm — mm real

249 Number of seal rods — — — integer

250 Diameter of seal rod mm in. mm real

251 Annular distributor code — — — integer

0 = None

1 = Inlet

2 = Outlet

3 = Both

252 Inlet annular distributor radial clearance mm in. mm real

253 Inlet annular distributor length mm in. mm real

254 Inlet annular distributor slot area mm² ft² mm² real

255 Outlet annular distributor slot area mm² ft² mm² real

256 Number of vertical passlanes — — — integer

257 Number of horizontal passlanes — — — integer

258 Width of vertical passlanes mm in. mm real

259 Width of horizontal passlanes mm in. mm real260 Baffle cut, percent free area in window % % % real

261 Tuberows overlap for multi-segmental baffles (Previous HTRIprograms output this value as an integer.)

— — — real

262 Number of crosspasses in region 1 — — — integer

263 Central spacing in region 1 mm in. mm real






269 Central spacing in region 4 mm in. mm real270 Number of crosspasses in region 5 — — — integer


272 Number of support plates in each baffle space — — — integer

273 Number of shellside passes — — — integer

274 Tube axial stress (for vibration analysis) kPa psi kg/cm² real

275 Overall heat transfer coefficient required W/m² °C Btu/hr ft² °F kcal/hr m² °C real

276 Shellside fluid name — — — alpha

277 Tubeside fluid name — — — alpha

278 Requested units of output data set — — — integer

1 = US

2 = SI3 = MKH

279 Tubeside inlet nozzle diameter mm in. mm real

280 Tubeside outlet nozzle diameter mm in. mm real

281 Tubeside intermediate nozzle mm in. mm real

282 Tubeside liquid outlet nozzle diameter mm — mm real

283 Shellside liquid outlet nozzle diameter mm — mm real

284 Outlet annular distributor radial clearance mm in. mm real

285 Outlet annular distributor length mm in. mm real

286 Shell entry momentum flux kg/m s² lb/ft sec² kg/m s² real

287 Shell exit momentum flux kg/m s² lb/ft sec² kg/m s² real

288 Mole fraction inert at condensing inlet — — — real



289 Shellside inlet Reynolds number — — — real

• Liquid

• Vapor

• Two-phase

290 Tubeside inlet Reynolds number — — — real

• Liquid

• Vapor

• Two-phase

291 Shellside midpoint Reynolds number — — — real

• Liquid

• Vapor

• Two-phase

292 Tubeside midpoint Reynolds number — — — real

• Liquid

• Vapor

• Two-phase

293 Shellside outlet Reynolds number — — — real

• Liquid

• Vapor

• Two-phase

294 Tubeside outlet Reynolds number — — — real

• Liquid

• Vapor

• Two-phase

295 Area ratio, inside/outside — — — real

296 Shellside maximum velocity m/s ft/sec m/s real

297 Nominal midpoint crossflow velocity m/s ft/sec m/s real

298 Nominal midpoint window velocity m/s ft/sec m/s real

299 Integral average flow area, baffle m² ft² m² real

300 Port pressure drop, hot inlet kPa psi kg/cm² real

301 Port pressure drop, hot outlet kPa psi kg/cm² real

302 Port pressure drop, cold inlet kPa psi kg/cm² real

303 Port pressure drop, cold outlet kPa psi kg/cm² real

304 Port velocity, hot inlet m/s ft/sec m/s real

305 Port velocity, hot outlet m/s ft/sec m/s real

306 Port velocity, cold inlet m/s ft/sec m/s real

307 Port velocity, cold outlet m/s ft/sec m/s real

308 Nominal channel velocity, hot m/s ft/sec m/s real

309 Nominal channel velocity, cold m/s ft/sec m/s real

310 Heat transfer safety factor, hot — — — real311 Heat transfer safety factor, cold — — — real

312 Shear stress, hot kPa psi kg/cm² real

313 Shear stress, cold kPa psi kg/cm² real

314 Heat duty, specified W Btu/hr kcal/hr real

315 Log mean temperature difference °C °F °C real

316 F-correction factor — — — real

317 Number of plate types — — — integer

318 Number of plates, total — — — integer

319 Number of plates, effective — — — integer

320 Total number of channel types — — — integer

321 Channel width mm in. mm real



371 Chevron angle (plate type 2) deg deg deg real

372 Surface area enhancement factor (plate type 2) — — — real

373 Equivalent diameter (plate type 2) mm in. mm real

374 Plate thickness (plate type 2) mm mm mm real

375 Effective area per plate (plate type 2) m² ft² m² real

376 Plate material (plate type 2)

— — — alpha377 Plate thermal conductivity (plate type 2) W/m °C Btu/hr ft °F kcal/hr m °C real

378 Gasket material (plate type 2) — — — alpha

379 First plate number (plate group 1) — — — integer

380 Second plate number (plate group 1) — — — integer

381 Number of channels (plate group 1) — — — integer

382 Hot pass number (plate group 1) — — — integer

383 Cold pass number (plate group 1) — — — integer










































423 Cold pass number (plate group 9 — — — integer




427 Hot pass number (plate group 10 — — — integer












439 HTRI research variable 1 — — — real










449 Midpoint hot side flow regime — — — alpha

Boiling regimes output by HTRI X changer Suite components include

• Convective

• Convect

• Nucleate

• Film

• Mist

• Liquid

• Vapor

• Flow• Sub Nucleate

• Sub Nucl

• F/M Tran

• Transition

• Tran

Condensing flow regimes output by HTRI X changer Suite components

• Gravity

• Trans

• Shear

• Ann-Mist

• GC Lam

• GC Trans



486 Air-cooler number of tubes in even rows — — — integer

487 Air-cooler number of tubes in odd rows — — — integer

488 Unit type — — — integer

1 = Thermosiphon reboiler

2 = Forced flow reboiler

11 = Air-cooled heat exchanger

12 = Economizer

13 = Natural draft air-cooled heat exchanger

14 = One-increment air-cooled heat exchanger

15 = Fired heater firebox coil

16 = Fired heater heat convection bundle

489 Air-cooler number of bundles in parallel/bay — — — integer

490 Air-cooler number of bays in parallel/unit — — — integer

491 Steam coil present in air-cooler — — — alpha

• Yes

• No

492 Louvers present in air-cooler — — — alpha

•

Yes• No

493 Tube material name — — — alpha

494 Distance from centerline to cut, baffle 1 mm in. mm real



497 Full support at U-bend — — — alpha

• Yes

• No

498 Floating head support plate present — — — alpha

• Yes

• No

499 Shell inlet nozzle position (0 = top of shell) — — — real

500 Fan ring type — — — real

0 = Straight

1 = Flanged

2 = 15 degree cone

3 = 30 degree cone

4 = Bell

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