Thermic Fluid HX

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Output Summary Page 1Released to the following HTRI Member Company: Johnson Controls Johnson Controls

Xhpe Ver. 6.00 3/16/2015 16:12 SN: 1500214208 SI Units

Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesSee Data Check Messages Report for Warning Messages.See Runtime Message Report for Warning Messages.

Process Conditions Cold Shellside Hot TubesideFluid name Oil Flue Gas Flow rate (kg/s) 1.2172 0.7724Inlet/Outlet Y (Wt. frac vap.) 0.000 0.000 1.000 1.000Inlet/Outlet T (Deg C) 80.00 110.00 250.00 150.00Inlet P/Avg (kPa) 140.002 139.282 400.006 395.957dP/Allow. (kPa) 1.440 0.000 8.097 0.000Fouling (m2-K/W) 0.000350 0.000999

Exchanger PerformanceShell h (W/m2-K) 170.04 Actual U (W/m2-K) 75.04Tube h (W/m2-K) 194.44 Required U (W/m2-K) 64.14Hot regime (--) Sens. Gas Duty (MegaWatts) 0.0800Cold regime (--) Sens. Liquid Area (m2) 12.349EMTD (Deg C) 101.0 Overdesign (%) 17.00

Shell Geometry Baffle GeometryType (--) Hairpin Baffle type (--) Single-Seg.Shell ID (mm) 250.000 Baffle cut (Pct Dia.) 31.53Series (--) 1 Baffle orientation (--) Perpend.Parallel (--) 1 Central spacing (mm) 300.000Orientation (deg) 0.00 Crosspasses (--) 11

Tube Geometry NozzlesTube type (--) Plain Shell inlet (mm) 52.502Tube OD (mm) 25.400 Shell outlet (mm) 52.502Nominal length (m) 2.000 Inlet height (mm) 43.559Pitch ratio (--) 1.2500 Outlet height (mm) 16.063Layout (deg) 30 Tube inlet (mm) 102.261Tubecount (--) 34 Tube outlet (mm) 102.261

Thermal Resistance, % Velocities, m/s Flow FractionsShell 44.13 Shellside 8.012e-2 A 0.005Tube 44.36 Tubeside 31.17 B 0.693Fouling 11.25 Crossflow 6.080e-2 C 0.204Metal 0.26 Window 0.13 E 0.098

F 0.000


Run Log Page 2Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesBeginning Run Running Xhpe Unit 1, 100Run Completed. Solution Reached in 00:02.


Data Check Messages Page 3Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesUnit ID 100 - WARNING MESSAGES (CALCULATIONS CONTINUE)

Fouling resistance based on area of side (hot): is high, but no layer thickness has been specified. The actual pressure drop may be higher if a layer is present.

Reference pressure (hot): should bracket the operating pressure to avoid unnecessaryextrapolation.


Runtime Messages Page 4Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesUnit ID 100 - WARNING MESSAGES (CALCULATIONS CONTINUE)

WARNING - The number of tubes removed to meet the TEMA entrance requirement is not the sameon each side of the bundle. For single segmental baffles with perpendicular baffle cut, thiscondition results in unequal window flow areas. If possible, redesign the exchanger such that thewindow flow areas are equal. The program used an average window flow area.

The physical properties of the cold fluid have been extrapolated beyond the valid temperature range. Check calculated values.

A high fouling resistance was specified on the tube side, but no fouling layer was specified. Use thecalculated pressure drop with caution.


Final Results Page 5Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesProcess Data Cold Shellside Hot Tubeside

Fluid name Oil Flue Gas Fluid condition Sens. Liquid Sens. GasTotal flow rate (kg/s) 1.2172 0.7724Weight fraction vapor, In/Out (--) 0.000 0.000 1.000 1.000Temperature, In/Out (Deg C) 80.00 110.00 250.00 150.00Temperature, Average/Skin (Deg C) 95.00 137.14 200.00 148.32Wall temperature, Min/Max (Deg C) 112.64 175.49 112.82 175.80Pressure, In/Average (kPa) 140.002 139.282 400.006 395.957Pressure drop, Total/Allowed (kPa) 1.440 8.097Velocity, Mid/Max allow (m/s) 8.012e-2 31.17Mole fraction inert (--) 0.0000Average film coef. (W/m2-K) 170.04 194.44Heat transfer safety factor (--) 1.000 1.000Fouling resistance (m2-K/W) 0.000350 0.000999

Overall Performance DataOverall coef., Reqd/Clean/Actual (W/m2-K) 64.14 / 84.56 / 75.04Heat duty, Calculated/Specified (MegaWatts) 0.0800 / 0.0800Effective overall temperature difference (Deg C) 101.0EMTD = (MTD) * (DELTA) * (F/G/H) (Deg C) 101.23 * 0.9978 * 1.0000

See Runtime Messages Report for warnings.

Exchanger Fluid VolumesApproximate shellside (L) 145.1Approximate tubeside (L) 97.7

Shell Construction InformationType Hairpin Shell ID (mm) 250.000Shells Series 1 Parallel 1 Total area (m2) 12.487Passes Shell 1 Tube 1 Eff. area (m2/shell) 12.349Shell orientation angle (deg) 0.00 Ctr-Ctr (mm) 383.698

Pairs seal strips 1

Weight estimation Wet/Dry/Bundle 892.63 / 650.07 / 170.98 (kg/shell)Baffle Information

Type Perpend. Single-Seg. Baffle cut (% dia) 31.53Crosspasses/shellpass 11 No. (Pct Area) (mm) to C.LCentral spacing (mm) 300.000 1 31.05 46.185Inlet spacing (mm) 690.191 2 0.00 0.000Outlet spacing (mm) 558.968Baffle thickness (mm) 3.175

Tube InformationTube type Plain Tubecount per shell 34Nominal length (m) 2.000 Pct tubes removed (none)Effective length (m) 4.552 Outside diameter (mm) 25.400Total tubesheet (mm) 50.800 Wall thickness (mm) 1.651Area ratio (out/in) 1.1494 Pitch (mm) 31.7500 Ratio 1.2500Tube metal Carbon steel Tube pattern (deg) 30

2

m

383.7

mm


Final Results Page 6Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesShellside Performance

Nom vel, X-flow/window 6.080e-2 / 0.13

Flow fractions for heat transfer 0.783 A=0.0050 B=0.6932 C=0.2039 E=0.0979 F=0.0000

Shellside Heat Transfer CorrectionsTotal Beta Gamma End Fin

0.573 0.920 0.623 0.939 1.000Pressure Drops (Percent of Total)

Cross Window Ends Nozzle Shell Tube30.00 24.70 4.64 Inlet 16.14 22.28

MOMENTUM 0.00 Outlet 24.53 10.96Two-Phase Parameters

Method Inlet Center Outlet Mix F

H. T. Parameters Shell TubeOverall wall correction 1.162 1.000Midpoint Prandtl no. 683.37 0.66Midpoint Reynolds no. 47 57115Bundle inlet Reynolds no. 15 52569Bundle outlet Reynolds no. 39 60826Fouling layer (mm)

Thermal ResistanceShell Tube Fouling Metal Over Des

44.13 44.36 11.25 0.26 17.00Total fouling resistance 0.00150Differential resistance 0.00227

Shell NozzlesInlet Outlet

Diameter (mm) 52.502 52.502Velocity (m/s) 0.58 0.60Pressure drop (kPa) 0.232 0.353Height under nozzle (mm) 43.559 16.063Nozzle R-V-SQ (kg/m-s2) 328.17 334.85Shell ent. (kg/m-s2) 0.00 0.00

Inlet OutletTube Nozzle

Diameter (mm) 102.261 102.261Velocity (m/s) 55.32 45.31Pressure drop (kPa) 1.804 0.887Nozzle R-V-SQ (kg/m-s2) 5202.72 4261.13

Diametral Clearances (mm)Baffle-to-shell Bundle-to-shell Tube-to-baffle

3.1750 32.1253 0.7938


Supplementary Results Page 7Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesExternally Enhanced Tube Geometry Internally Enhanced Tube Geometry

Type Plain Type NoneFin density (fin/meter) Thickness (mm)Fin height (mm) Pitch (L/D)Fin thickness (mm)Root diameter (mm)Area/length (m2/m)

Mean Metal TemperaturesMean shell temperature 92.95 (C)

Mean tube metal temperature, (C)Inside Outside Radial139.81 139.56 139.68


Shellside Incremental Monitor Page 8Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesShellside Flow Region 1 1.2172 kg/sPoint number (--) 1 2 3 4 5Shell pass (--) 1 1 1 1 1Length from tube inlet (mm) 3949.16 3604.06 3108.97 2808.97 2508.97Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) 80.00 81.84 84.61 86.54 88.56Skin temperature (C) 115.26 118.05 121.94 126.05MTD (C) 74.0 80.6 85.0 89.8Delta MTD correction (--) 1.000 0.999 0.999 0.998Pressure (kPa) 140.002 139.865 139.790 139.684 139.583Pressure drop (kPa) 0.232 0.041 0.109 0.103 0.098Friction loss (kPa) 0.041 0.109 0.103 0.098Static head loss (kPa) 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000Shear stress at tube wall Crossflow (Pa) 0.00 4.84 4.54 4.24 Longitudinal flow (Pa) 1.85 1.71 1.63 1.54Area (m2) 1.873 0.814 0.814 0.814Cumulative area (m2) 1.873 2.686 3.500 4.314Duty (MegaWatts) 0.0096 0.0049 0.0052 0.0055Cumulative duty (MegaWatts) 0.0096 0.0146 0.0198 0.0253Heat flux (W/m2) 5152.11 6076.51 6420.57 6783.34Calculated heat flux (W/m2) 5243.07 6188.34 6538.82 6909.03Critical heat flux (W/m2) 0.00 0.00 0.00 0.00Overall U (W/m2-K) 69.68 75.91 76.11 76.33Shellside h (W/m2-K) 150.78 179.89 179.80 179.70Sensible liquid h (W/m2-K) 150.78 179.89 179.80 179.70Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00Local Reynolds (--) 15 22 37 40 42Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 15 22 37 40 42Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 941.15 903.30 838.95 798.80 758.55Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq




Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesShellside Flow Region 1Point number (--) 6 7 8 9 10Shell pass (--) 1 1 1 1 1Length from tube inlet (mm) 2208.97 1908.97 1608.97 1308.97 1008.97Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) 90.70 92.95 95.32 97.80 100.43Skin temperature (C) 130.41 135.02 139.90 145.06 150.51MTD (C) 94.8 100.0 105.6 111.5 117.7Delta MTD correction (--) 0.998 0.998 0.997 0.997 0.997Pressure (kPa) 139.488 139.399 139.314 139.235 139.161Pressure drop (kPa) 0.092 0.087 0.082 0.077 0.072Friction loss (kPa) 0.092 0.087 0.082 0.077 0.072Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Shear stress at tube wall Crossflow (Pa) 3.96 3.70 3.44 3.19 2.95 Longitudinal flow (Pa) 1.45 1.37 1.29 1.22 1.14Area (m2) 0.814 0.814 0.814 0.814 0.814Cumulative area (m2) 5.128 5.942 6.756 7.570 8.384Duty (MegaWatts) 0.0058 0.0062 0.0065 0.0069 0.0073Cumulative duty (MegaWatts) 0.0312 0.0373 0.0438 0.0507 0.0580Heat flux (W/m2) 7166.00 7569.40 7995.10 8442.67 8911.02Calculated heat flux (W/m2) 7300.35 7713.65 8150.77 8611.36 9094.30Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 76.55 76.77 77.01 77.25 77.50Shellside h (W/m2-K) 179.60 179.49 179.38 179.27 179.15Sensible liquid h (W/m2-K) 179.60 179.49 179.38 179.27 179.15Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 44 47 50 53 57Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 44 47 50 53 57Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 719.58 683.37 647.39 611.56 576.00Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq




Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesShellside Flow Region 1Point number (--) 11 12 13Shell pass (--) 1 1 1Length from tube inlet (mm) 708.968 279.484 0.000Mass fraction vapor (--) 0.0000 0.0000 0.0000Bulk temperature (C) 103.21 107.32 110.00Skin temperature (C) 156.27 168.85MTD (C) 124.2 133.6Delta MTD correction (--) 0.997 0.997Pressure (kPa) 139.091 139.044 138.562Pressure drop (kPa) 0.067 0.026 0.353Friction loss (kPa) 0.067 0.026Static head loss (kPa) 0.000 0.000Momentum loss (kPa) 0.000 0.000Shear stress at tube wall Crossflow (Pa) 2.71 0.00 Longitudinal flow (Pa) 1.06 0.96Area (m2) 0.814 1.517Cumulative area (m2) 9.198 10.714Duty (MegaWatts) 0.0077 0.0144Cumulative duty (MegaWatts) 0.0656 0.0800Heat flux (W/m2) 9399.22 9484.78Calculated heat flux (W/m2) 9598.66 9694.01Critical heat flux (W/m2) 0.00 0.00Overall U (W/m2-K) 77.75 73.17Shellside h (W/m2-K) 179.01 155.37Sensible liquid h (W/m2-K) 179.01 155.37Sensible vapor h (W/m2-K) 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00Local Reynolds (--) 61 47 39Vapor Reynolds (--) 0 0 0Liquid Reynolds (--) 61 47 39Vapor Prandtl (--) 0.00 0.00 0.00Liquid Prandtl (--) 540.53 493.79 460.55Flow regime param. (--) 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq


Tubeside Incremental Monitor Page 11Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesPoint number (--) 1 2 3 4 5Tube Pass (--) 1 1 1 1 1Length from tube inlet (mm) 0.000 279.484 708.968 1008.97 1308.97Mass fraction vapor (--) 1.0000 1.0000 1.0000 1.0000 1.0000Bulk temperature (C) 250.00 241.15 227.51 218.23 209.40Skin temperature (C) 183.32 170.79 164.23 158.01MTD (C) 133.6 124.2 117.7 111.5Pressure (kPa) 400.006 397.033 396.710 396.393 396.083Pressure drop (kPa) 2.320 0.653 0.323 0.316 0.310Enhanced pressure drop mult (--)Friction loss (kPa) 0.689 0.342 0.334 0.327Static head loss (kPa) 0.000 0.000 0.000 0.000Momentum loss (kPa) -0.035 -0.019 -0.018 -0.017Maximum velocity (m/s) 34.56 33.55 32.91 32.31Average velocity (m/s) 34.54 33.48 32.86 32.26Shear stress at tube wall (Pa) 6.51 6.30 6.16 6.03Area (m2) 1.517 0.814 0.814 0.814Cumulative area (m2) 1.517 2.330 3.144 3.958Duty (MegaWatts) 0.0144 0.0077 0.0073 0.0069Cumulative duty (MegaWatts) 0.0144 0.0220 0.0293 0.0362Heat flux (W/m2) 9484.78 9399.22 8911.02 8442.67Calculated heat flux (W/m2) 9726.83 9632.00 9123.52 8636.72Critical heat flux (W/m2)Overall U (W/m2-K) 73.17 77.75 77.50 77.25Tubeside h (W/m2-K) 203.25 200.20 198.62 197.08Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 0.00 0.00 0.00 0.00Sensible vapor h (W/m2-K) 203.25 200.20 198.62 197.08Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00Local Reynolds (--) 52569 52591 53912 54733 55541Vapor Reynolds (--) 52209 52591 53912 54733 55541Liquid Reynolds (--) 0 0 0 0 0Vapor Prandtl (--) 0.66 0.66 0.66 0.66 0.66Liquid Prandtl (--) 0.00 0.00 0.00 0.00 0.00Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000Condensate regime (--) Sens Gas Sens Gas Sens Gas Sens GasBoiling regime (--)Boiling mechanism (--)




Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesPoint number (--) 6 7 8 9 10Tube Pass (--) 1 1 1 1 1Length from tube inlet (mm) 1608.97 1908.97 2208.97 2508.97 2808.97Mass fraction vapor (--) 1.0000 1.0000 1.0000 1.0000 1.0000Bulk temperature (C) 200.99 193.03 185.50 178.37 171.62Skin temperature (C) 152.12 146.56 141.31 136.35 131.66MTD (C) 105.6 100.0 94.8 89.8 85.0Pressure (kPa) 395.778 395.478 395.183 394.892 394.605Pressure drop (kPa) 0.304 0.300 0.295 0.291 0.287Enhanced pressure drop mult (--)Friction loss (kPa) 0.321 0.314 0.309 0.304 0.299Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) -0.016 -0.015 -0.013 -0.012 -0.011Maximum velocity (m/s) 31.74 31.20 30.72 30.27 29.86Average velocity (m/s) 31.69 31.17 30.69 30.24 29.84Shear stress at tube wall (Pa) 5.91 5.79 5.69 5.59 5.50Area (m2) 0.814 0.814 0.814 0.814 0.814Cumulative area (m2) 4.772 5.586 6.400 7.214 8.028Duty (MegaWatts) 0.0065 0.0062 0.0058 0.0055 0.0052Cumulative duty (MegaWatts) 0.0427 0.0488 0.0547 0.0602 0.0654Heat flux (W/m2) 7995.10 7569.40 7166.00 6783.34 6420.57Calculated heat flux (W/m2) 8172.61 7732.14 7315.62 6921.27 6548.16Critical heat flux (W/m2)Overall U (W/m2-K) 77.01 76.77 76.55 76.33 76.11Tubeside h (W/m2-K) 195.60 194.16 192.79 191.48 190.23Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Sensible vapor h (W/m2-K) 195.60 194.16 192.79 191.48 190.23Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 56338 57115 57870 58604 59316Vapor Reynolds (--) 56338 57115 57870 58604 59316Liquid Reynolds (--) 0 0 0 0 0Vapor Prandtl (--) 0.66 0.66 0.66 0.66 0.66Liquid Prandtl (--) 0.00 0.00 0.00 0.00 0.00Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--) Sens Gas Sens Gas Sens Gas Sens Gas Sens GasBoiling regime (--)Boiling mechanism (--)




Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesPoint number (--) 11 12 13Tube Pass (--) 1 1 1Length from tube inlet (mm) 3108.97 3604.06 4551.56Mass fraction vapor (--) 1.0000 1.0000 1.0000Bulk temperature (C) 165.23 156.06 150.00Skin temperature (C) 127.24 122.83MTD (C) 80.6 74.0Pressure (kPa) 394.321 393.649 391.909Pressure drop (kPa) 0.284 0.672 1.741Enhanced pressure drop mult (--)Friction loss (kPa) 0.294 0.692Static head loss (kPa) 0.000 0.000Momentum loss (kPa) -0.011 -0.020Maximum velocity (m/s) 29.48 29.05Average velocity (m/s) 29.46 29.03Shear stress at tube wall (Pa) 5.42 5.34Area (m2) 0.814 1.873Cumulative area (m2) 8.842 10.714Duty (MegaWatts) 0.0049 0.0096Cumulative duty (MegaWatts) 0.0704 0.0800Heat flux (W/m2) 6076.51 5152.11Calculated heat flux (W/m2) 6194.93 5245.50Critical heat flux (W/m2)Overall U (W/m2-K) 75.91 69.68Tubeside h (W/m2-K) 189.04 188.03Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 0.00 0.00Sensible vapor h (W/m2-K) 189.04 188.03Condensate film h (W/m2-K) 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00Local Reynolds (--) 60006 60851 60826Vapor Reynolds (--) 60006 60851 61168Liquid Reynolds (--) 0 0 0Vapor Prandtl (--) 0.66 0.66 0.66Liquid Prandtl (--) 0.00 0.00 0.00Flow regime param. (--) 0.0000 0.0000Condensate regime (--) Sens Gas Sens GasBoiling regime (--)Boiling mechanism (--)


HEAT EXCHANGER RATING DATA SHEET Page 14 SI Units

Service of Unit Item No. Type Hairpin Orientation Horizontal Connected In 1 Parallel 1 SeriesSurf/Unit (Gross/Eff) 12.49 / 12.35 m2 Shell/Unit 1 Surf/Shell (Gross/Eff) 12.49 / 12.35 m2

PERFORMANCE OF ONE UNITFluid Allocation Shell Side Tube SideFluid Name Oil Flue Gas Fluid Quantity, Total kg/s 1.2172 0.7724 Vapor (In/Out) wt% 0.0 0.0 100.0 100.0 Liquid wt% 100.0 100.0 0.0 0.0Temperature (In/Out) C 80.00 110.00 250.00 150.00Density kg/m3 963.20 944.00 1.7001 2.0757Viscosity mN-s/m2 64.788 29.302 0.0251 0.0212Specific Heat kJ/kg-C 2.1520 2.2530 1.0544 1.0015Thermal Conductivity W/m-C 0.1482 0.1434 0.0400 0.0320Critical Pressure kPaInlet Pressure kPa 140.002 400.006Velocity m/s 8.012e-2 31.17Pressure Drop, Allow/Calc kPa 1.440 8.097Average Film Coefficient W/m2-K 170.04 194.44Fouling Resistance (min) m2-K/W 0.000350 0.000999Heat Exchanged 0.0800 MegaWatts MTD (Corrected) 101.0 C Overdesign 17.00 %Transfer Rate, Service 64.14 W/m2-K Calculated 75.04 W/m2-K Clean 84.56 W/m2-K

CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)Shell Side Tube Side

Design Pressure kPaG 1034.21 1034.21Design Temperature C 250.00 250.00No Passes per Shell 1 1Flow Direction Downward

Connections In mm 1 @ 52.502 1 @ 102.261Size & Out mm 1 @ 52.502 1 @ 102.261Rating Liq. Out mm @ @

Tube No. 34 OD 25.400 mm Thk(Avg) 1.651 mm Length 4.602 m Pitch 31.750 mm Layout 30Tube Type Plain Material CARBON STEEL Pairs seal strips 1Shell ID 250.000 mm Kettle ID mm Passlane Seal Rod No.0Cross Baffle Type PERPEND. SINGLE-SEG. %Cut (Diam) 31.53 Impingement Plate NoneSpacing(c/c) 300.000 mm Inlet 690.191 mm No. of Crosspasses 11Rho-V2-Inlet Nozzle 328.17 kg/m-s2 Shell Entrance 0.00 Shell Exit 0.00 kg/m-s2

Bundle Entrance 0.00 Bundle Exit 0.00 kg/m-s2Weight/Shell 650.07 Filled with Water 892.63 Bundle 170.98 kgNotes: Thermal Resistance, % Velocities, m/s Flow Fractions

Shell 44.13 Shellside 8.012e-2 A 0.005Tube 44.36 Tubeside 31.17 B 0.693Fouling 11.25 Crossflow 6.080e-2 C 0.204Metal 0.26 Window 0.13 E 0.098

F 0.000

2

m

383.7

mm


HEAT EXCHANGER SPECIFICATION SHEET Page 15 SI Units

Job No.Customer Reference No.Address Proposal No.Plant Location Date 3/16/2015 Rev Service of Unit Item No.Size 250.000 x 4602.35 mm Type Hairpin Horz. Connected In 1 Parallel 1 SeriesSurf/Unit (Gross/Eff) 12.49 / 12.35 m2 Shell/Unit 1 Surf/Shell (Gross/Eff) 12.49 / 12.35 m2

PERFORMANCE OF ONE UNITFluid Allocation Shell Side Tube SideFluid Name Oil Flue Gas Fluid Quantity, Total kg/hr 4381.83 2780.76 Vapor (In/Out) 2780.76 2780.76 Liquid 4381.83 4381.83 Steam Water NoncondensablesTemperature (In/Out) C 80.00 110.00 250.00 150.00Specific Gravity 0.9636 0.9444Viscosity mN-s/m2 64.788 29.302 0.0251 0.0212Molecular Weight, VaporMolecular Weight, NoncondensablesSpecific Heat kJ/kg-C 2.1520 2.2530 1.0544 1.0015Thermal Conductivity W/m-C 0.1482 0.1434 0.0400 0.0320Latent Heat kJ/kgInlet Pressure kPa 140.002 400.006Velocity m/s 8.012e-2 31.17Pressure Drop, Allow/Calc kPa 1.440 8.097Fouling Resistance (min) m2-K/W 0.000350 0.000999Heat Exchanged W 79999.9 MTD (Corrected) 101.0 CTransfer Rate, Service 64.14 W/m2-K Clean 84.56 W/m2-K Actual 75.04 W/m2-K

CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)Shell Side Tube Side

Design/Test Pressure kPaG 1034.21 / 1034.21 /Design Temperature C 250.00 250.00No Passes per Shell 1 1Corrosion Allowance mm

Connections In mm 1 @ 52.502 1 @ 102.261Size & Out mm 1 @ 52.502 1 @ 102.261Rating Intermediate @ @

Tube No. 34 OD 25.400 mm Thk(Avg) 1.651 mm Length 4.602 m Pitch 31.750 mm Layout 30Tube Type Plain Material CARBON STEELShell ID 250.000 mm OD mm Shell CoverChannel or Bonnet Channel CoverTubesheet-Stationary Tubesheet-FloatingFloating Head Cover Impingement Plate NoneBaffles-Cross Type SINGLE-SEG. %Cut (Diam) 31.53 Spacing(c/c) 300.000 Inlet 690.191 mmBaffles-Long Seal Type Supports-Tube U-Bend Type Bypass Seal Arrangement Tube-Tubesheet JointExpansion Joint Type Rho-V2-Inlet Nozzle 328.17 kg/m-s2 Bundle Entrance 0.00 Bundle Exit 0.00 kg/m-s2Gaskets-Shell Side Tube Side -Floating Head Code Requirements TEMA ClassWeight/Shell 650.07 Filled with Water 892.63 Bundle 170.98 kgRemarks:

Reprinted with Permission (v6 )

2

m

383.7

mm


Properties Profile Monitor Page 16Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesPhysical Properties Profile: Hot Tubeside (Flue Gas) Reference pressure, (kPa) (P1= 100.001) (P2= 109.093) (P3= 118.184) (P4= 127.275) (P5= 136.366) (P6= 145.457)

(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 1 2 3 4 5 6 7 8 9 10

Temperature, (C) 1 500.00 490.21 480.39 470.53 460.65 450.73 440.77 430.78 420.76 410.692 500.00 490.21 480.39 470.53 460.65 450.73 440.77 430.78 420.76 410.693 500.00 490.21 480.39 470.53 460.65 450.73 440.77 430.78 420.75 410.694 500.00 490.21 480.39 470.53 460.64 450.72 440.77 430.78 420.75 410.695 500.00 490.21 480.39 470.53 460.64 450.72 440.77 430.78 420.75 410.696 500.00 490.21 480.39 470.53 460.64 450.72 440.77 430.77 420.75 410.687 500.00 490.21 480.39 470.53 460.64 450.72 440.76 430.77 420.75 410.688 500.00 490.21 480.38 470.53 460.64 450.72 440.76 430.77 420.74 410.689 500.00 490.21 480.38 470.53 460.64 450.72 440.76 430.77 420.74 410.68

10 500.00 490.21 480.38 470.53 460.64 450.72 440.76 430.77 420.74 410.6811 500.00 490.21 480.38 470.53 460.64 450.71 440.76 430.77 420.74 410.6712 500.00 490.21 480.38 470.53 460.64 450.71 440.76 430.76 420.74 410.67

Heat duty/flow rate, (kJ/kg) 1 0.0000 11.3760 22.7520 34.1270 45.5030 56.8790 68.2540 79.6300 91.0060 102.3822 0.0060 11.3819 22.7589 34.1350 45.5109 56.8880 68.2640 79.6400 91.0170 102.3933 0.0110 11.3880 22.7649 34.1430 45.5200 56.8970 68.2740 79.6510 91.0279 102.4054 0.0170 11.3949 22.7719 34.1500 45.5280 56.9060 68.2830 79.6610 91.0390 102.4175 0.0219 11.4010 22.7790 34.1580 45.5360 56.9149 68.2930 79.6710 91.0500 102.4286 0.0280 11.4070 22.7860 34.1649 45.5440 56.9240 68.3030 79.6820 91.0610 102.4407 0.0340 11.4129 22.7929 34.1730 45.5530 56.9330 68.3120 79.6919 91.0719 102.4528 0.0390 11.4200 22.8000 34.1810 45.5610 56.9419 68.3219 79.7019 91.0830 102.4639 0.0449 11.4259 22.8070 34.1880 45.5689 56.9500 68.3319 79.7130 91.0940 102.475

10 0.0500 11.4320 22.8140 34.1960 45.5780 56.9590 68.3410 79.7229 91.1050 102.48711 0.0559 11.4380 22.8210 34.2030 45.5860 56.9680 68.3510 79.7329 91.1159 102.49812 0.0610 11.4450 22.8280 34.2110 45.5940 56.9770 68.3610 79.7440 91.1270 102.510

Weight fraction vapor 1 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.00002 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.00003 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.00004 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.00005 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.00006 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.00007 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.00008 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.00009 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000

10 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.000011 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.000012 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000





(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 11 12 13 14 15 16 17 18 19 20

Temperature, (C) 1 400.59 390.45 380.28 370.06 359.79 349.49 339.14 328.75 318.30 307.822 400.59 390.45 380.27 370.05 359.79 349.49 339.14 328.74 318.30 307.813 400.59 390.45 380.27 370.05 359.79 349.48 339.13 328.74 318.30 307.814 400.59 390.45 380.27 370.05 359.78 349.48 339.13 328.74 318.30 307.815 400.58 390.44 380.27 370.04 359.78 349.48 339.13 328.73 318.29 307.816 400.58 390.44 380.26 370.04 359.78 349.47 339.13 328.73 318.29 307.807 400.58 390.44 380.26 370.04 359.78 349.47 339.12 328.73 318.29 307.808 400.58 390.44 380.26 370.04 359.77 349.47 339.12 328.72 318.28 307.809 400.58 390.43 380.25 370.03 359.77 349.47 339.12 328.72 318.28 307.79

10 400.57 390.43 380.25 370.03 359.77 349.46 339.11 328.72 318.28 307.7911 400.57 390.43 380.25 370.03 359.77 349.46 339.11 328.72 318.28 307.7912 400.57 390.43 380.25 370.03 359.76 349.46 339.11 328.71 318.27 307.78


10 113.869 125.250 136.632 148.014 159.396 170.778 182.160 193.541 204.923 216.30511 113.881 125.263 136.646 148.028 159.411 170.794 182.176 193.559 204.941 216.32412 113.893 125.276 136.660 148.043 159.426 170.809 182.192 193.576 204.959 216.342


10 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.000011 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.000012 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000





(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 21 22 23 24 25 26 27 28 29 30

Temperature, (C) 1 297.28 286.69 276.05 265.36 254.61 243.81 232.95 222.03 211.05 200.002 297.28 286.69 276.05 265.36 254.61 243.81 232.95 222.03 211.05 200.003 297.27 286.69 276.05 265.36 254.61 243.81 232.95 222.03 211.05 200.004 297.27 286.68 276.05 265.35 254.61 243.80 232.94 222.03 211.04 200.005 297.27 286.68 276.04 265.35 254.60 243.80 232.94 222.02 211.04 200.006 297.27 286.68 276.04 265.35 254.60 243.80 232.94 222.02 211.04 200.007 297.26 286.68 276.04 265.35 254.60 243.80 232.94 222.02 211.04 200.008 297.26 286.67 276.03 265.34 254.60 243.80 232.94 222.02 211.04 200.009 297.26 286.67 276.03 265.34 254.60 243.80 232.94 222.02 211.04 200.00

10 297.25 286.67 276.03 265.34 254.59 243.79 232.94 222.02 211.04 200.0011 297.25 286.66 276.03 265.34 254.59 243.79 232.93 222.02 211.04 200.0012 297.25 286.66 276.02 265.33 254.59 243.79 232.93 222.02 211.04 200.00


10 227.687 239.069 250.451 261.832 273.214 284.596 295.978 307.360 318.742 330.12311 227.706 239.089 250.471 261.854 273.236 284.619 296.001 307.384 318.766 330.14912 227.725 239.108 250.492 261.875 273.258 284.641 296.024 307.408 318.791 330.174


10 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.000011 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.000012 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000





(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 1 2 3 4 5 6 7 8 9 10

Vapor PropertiesDensity, (kg/m3) 1 0.5749 0.5822 0.5898 0.5976 0.6057 0.6140 0.6226 0.6314 0.6405 0.6500

2 0.6271 0.6351 0.6434 0.6520 0.6607 0.6698 0.6792 0.6888 0.6988 0.70903 0.6793 0.6881 0.6970 0.7063 0.7158 0.7256 0.7357 0.7462 0.7570 0.76814 0.7316 0.7410 0.7506 0.7606 0.7708 0.7814 0.7923 0.8036 0.8152 0.82725 0.7838 0.7939 0.8042 0.8149 0.8259 0.8372 0.8489 0.8610 0.8734 0.88636 0.8361 0.8468 0.8578 0.8692 0.8809 0.8930 0.9055 0.9183 0.9316 0.94547 0.8883 0.8997 0.9114 0.9235 0.9360 0.9488 0.9621 0.9757 0.9898 1.00448 0.9405 0.9526 0.9650 0.9778 0.9910 1.0046 1.0186 1.0331 1.0481 1.06359 0.9928 1.0055 1.0186 1.0321 1.0461 1.0604 1.0752 1.0905 1.1063 1.1226

10 1.0450 1.0584 1.0722 1.0864 1.1011 1.1162 1.1318 1.1479 1.1645 1.181611 1.0972 1.1113 1.1258 1.1408 1.1561 1.1720 1.1884 1.2053 1.2227 1.240712 1.1495 1.1642 1.1794 1.1951 1.2112 1.2278 1.2449 1.2626 1.2809 1.2998

Viscosity, (mN-s/m2) 1 0.0340 0.0336 0.0333 0.0330 0.0326 0.0323 0.0320 0.0316 0.0313 0.03092 0.0340 0.0336 0.0333 0.0330 0.0326 0.0323 0.0320 0.0316 0.0313 0.03093 0.0340 0.0336 0.0333 0.0330 0.0326 0.0323 0.0320 0.0316 0.0313 0.03094 0.0340 0.0336 0.0333 0.0330 0.0326 0.0323 0.0320 0.0316 0.0313 0.03095 0.0340 0.0336 0.0333 0.0330 0.0326 0.0323 0.0320 0.0316 0.0313 0.03096 0.0340 0.0336 0.0333 0.0330 0.0326 0.0323 0.0320 0.0316 0.0313 0.03097 0.0340 0.0336 0.0333 0.0330 0.0327 0.0323 0.0320 0.0316 0.0313 0.03098 0.0340 0.0336 0.0333 0.0330 0.0327 0.0323 0.0320 0.0316 0.0313 0.03099 0.0340 0.0336 0.0333 0.0330 0.0327 0.0323 0.0320 0.0316 0.0313 0.0309

10 0.0340 0.0336 0.0333 0.0330 0.0327 0.0323 0.0320 0.0316 0.0313 0.030911 0.0340 0.0336 0.0333 0.0330 0.0327 0.0323 0.0320 0.0316 0.0313 0.030912 0.0340 0.0336 0.0333 0.0330 0.0327 0.0323 0.0320 0.0316 0.0313 0.0309

Thermal conductivity, (W/m-C) 1 0.0583 0.0577 0.0570 0.0563 0.0556 0.0549 0.0542 0.0535 0.0528 0.05212 0.0583 0.0577 0.0570 0.0563 0.0556 0.0549 0.0542 0.0535 0.0528 0.05213 0.0583 0.0577 0.0570 0.0563 0.0556 0.0549 0.0542 0.0535 0.0528 0.05214 0.0583 0.0577 0.0570 0.0563 0.0556 0.0550 0.0543 0.0535 0.0528 0.05215 0.0584 0.0577 0.0570 0.0563 0.0556 0.0550 0.0543 0.0535 0.0528 0.05216 0.0584 0.0577 0.0570 0.0563 0.0556 0.0550 0.0543 0.0535 0.0528 0.05217 0.0584 0.0577 0.0570 0.0563 0.0557 0.0550 0.0543 0.0536 0.0528 0.05218 0.0584 0.0577 0.0570 0.0563 0.0557 0.0550 0.0543 0.0536 0.0528 0.05219 0.0584 0.0577 0.0570 0.0563 0.0557 0.0550 0.0543 0.0536 0.0528 0.0521

10 0.0584 0.0577 0.0570 0.0563 0.0557 0.0550 0.0543 0.0536 0.0528 0.052111 0.0584 0.0577 0.0570 0.0563 0.0557 0.0550 0.0543 0.0536 0.0528 0.052112 0.0584 0.0577 0.0570 0.0563 0.0557 0.0550 0.0543 0.0536 0.0528 0.0521





(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 11 12 13 14 15 16 17 18 19 20


2 0.7197 0.7307 0.7421 0.7539 0.7661 0.7788 0.7920 0.8057 0.8199 0.83473 0.7796 0.7916 0.8039 0.8167 0.8300 0.8437 0.8580 0.8728 0.8883 0.90434 0.8396 0.8525 0.8657 0.8795 0.8938 0.9086 0.9240 0.9400 0.9566 0.97395 0.8996 0.9133 0.9276 0.9423 0.9576 0.9735 0.9900 1.0071 1.0249 1.04346 0.9595 0.9742 0.9894 1.0052 1.0215 1.0384 1.0560 1.0742 1.0932 1.11307 1.0195 1.0351 1.0512 1.0680 1.0853 1.1033 1.1220 1.1414 1.1616 1.18268 1.0795 1.0960 1.1131 1.1308 1.1491 1.1682 1.1880 1.2085 1.2299 1.25229 1.1394 1.1569 1.1749 1.1936 1.2130 1.2331 1.2540 1.2757 1.2982 1.3217

10 1.1994 1.2177 1.2367 1.2564 1.2768 1.2980 1.3200 1.3428 1.3666 1.391311 1.2593 1.2786 1.2986 1.3192 1.3407 1.3629 1.3860 1.4100 1.4349 1.460912 1.3193 1.3395 1.3604 1.3820 1.4045 1.4278 1.4520 1.4771 1.5032 1.5305

Viscosity, (mN-s/m2) 1 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.02722 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.02723 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.02724 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.02725 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.02726 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.02727 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.02728 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.02729 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.0272

10 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.027211 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.027212 0.0306 0.0302 0.0299 0.0295 0.0291 0.0288 0.0284 0.0280 0.0276 0.0272


10 0.0514 0.0507 0.0499 0.0492 0.0484 0.0476 0.0469 0.0461 0.0453 0.044511 0.0514 0.0507 0.0499 0.0492 0.0484 0.0476 0.0469 0.0461 0.0453 0.044512 0.0514 0.0507 0.0499 0.0492 0.0484 0.0476 0.0469 0.0461 0.0453 0.0445





(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 21 22 23 24 25 26 27 28 29 30


2 0.8502 0.8663 0.8831 0.9007 0.9190 0.9383 0.9585 0.9797 1.0019 1.02543 0.9210 0.9385 0.9567 0.9757 0.9956 1.0165 1.0384 1.0613 1.0855 1.11094 0.9919 1.0107 1.0303 1.0508 1.0723 1.0947 1.1183 1.1430 1.1690 1.19645 1.0628 1.0829 1.1039 1.1259 1.1489 1.1729 1.1982 1.2247 1.2525 1.28196 1.1336 1.1551 1.1775 1.2010 1.2255 1.2512 1.2781 1.3064 1.3361 1.36747 1.2045 1.2273 1.2511 1.2760 1.3021 1.3294 1.3580 1.3880 1.4196 1.45298 1.2753 1.2995 1.3248 1.3511 1.3787 1.4076 1.4379 1.4697 1.5032 1.53849 1.3462 1.3717 1.3984 1.4262 1.4553 1.4858 1.5178 1.5514 1.5867 1.6239

10 1.4171 1.4439 1.4720 1.5013 1.5320 1.5641 1.5978 1.6331 1.6703 1.709511 1.4879 1.5161 1.5456 1.5764 1.6086 1.6423 1.6777 1.7148 1.7539 1.795012 1.5588 1.5884 1.6192 1.6515 1.6852 1.7206 1.7576 1.7965 1.8375 1.8806

Viscosity, (mN-s/m2) 1 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.02312 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.02313 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.02314 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.02315 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.02316 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.02317 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.02318 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.02319 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.0231

10 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.023111 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.023112 0.0268 0.0265 0.0261 0.0256 0.0252 0.0248 0.0244 0.0240 0.0236 0.0231


10 0.0437 0.0429 0.0420 0.0412 0.0404 0.0395 0.0386 0.0378 0.0369 0.036011 0.0437 0.0429 0.0420 0.0412 0.0404 0.0395 0.0387 0.0378 0.0369 0.036012 0.0437 0.0429 0.0421 0.0412 0.0404 0.0395 0.0387 0.0378 0.0369 0.0360





(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 1 2 3 4 5 6 7 8 9 10

Enthalpy, (kJ/kg) 1 0.0000 -11.383 -22.766 -34.149 -45.532 -56.915 -68.298 -79.681 -91.064 -102.452 0.0000 -11.384 -22.767 -34.151 -45.534 -56.919 -68.302 -79.686 -91.070 -102.453 0.0000 -11.384 -22.769 -34.153 -45.537 -56.922 -68.306 -79.691 -91.075 -102.464 0.0000 -11.386 -22.770 -34.155 -45.541 -56.926 -68.310 -79.695 -91.081 -102.475 0.0000 -11.386 -22.772 -34.157 -45.543 -56.929 -68.314 -79.700 -91.086 -102.476 0.0000 -11.386 -22.772 -34.160 -45.546 -56.932 -68.318 -79.705 -91.092 -102.487 0.0000 -11.387 -22.774 -34.162 -45.548 -56.935 -68.322 -79.710 -91.097 -102.488 0.0000 -11.388 -22.776 -34.163 -45.551 -56.939 -68.327 -79.714 -91.103 -102.499 0.0000 -11.389 -22.777 -34.165 -45.554 -56.942 -68.330 -79.719 -91.107 -102.50

10 0.0000 -11.389 -22.779 -34.167 -45.557 -56.945 -68.335 -79.724 -91.112 -102.5011 0.0000 -11.390 -22.779 -34.170 -45.559 -56.949 -68.339 -79.729 -91.118 -102.5112 0.0000 -11.391 -22.781 -34.172 -45.562 -56.952 -68.343 -79.733 -91.123 -102.51

Specific heat, (kJ/kg-C) 1 1.1637 1.1601 1.1563 1.1526 1.1487 1.1448 1.1408 1.1367 1.1326 1.12842 1.1638 1.1601 1.1564 1.1526 1.1487 1.1448 1.1408 1.1368 1.1326 1.12843 1.1638 1.1601 1.1564 1.1526 1.1488 1.1449 1.1409 1.1368 1.1327 1.12854 1.1638 1.1602 1.1565 1.1527 1.1488 1.1449 1.1409 1.1369 1.1327 1.12855 1.1639 1.1602 1.1565 1.1527 1.1489 1.1449 1.1410 1.1369 1.1328 1.12866 1.1639 1.1603 1.1565 1.1527 1.1489 1.1450 1.1410 1.1369 1.1328 1.12867 1.1640 1.1603 1.1566 1.1528 1.1489 1.1450 1.1410 1.1370 1.1329 1.12878 1.1640 1.1603 1.1566 1.1528 1.1490 1.1451 1.1411 1.1370 1.1329 1.12879 1.1640 1.1604 1.1566 1.1529 1.1490 1.1451 1.1411 1.1371 1.1330 1.1288

10 1.1641 1.1604 1.1567 1.1529 1.1491 1.1451 1.1412 1.1371 1.1330 1.128811 1.1641 1.1604 1.1567 1.1529 1.1491 1.1452 1.1412 1.1372 1.1331 1.128912 1.1641 1.1605 1.1568 1.1530 1.1491 1.1452 1.1413 1.1372 1.1331 1.1289





(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 11 12 13 14 15 16 17 18 19 20

Enthalpy, (kJ/kg) 1 -113.83 -125.21 -136.60 -147.98 -159.36 -170.75 -182.13 -193.51 -204.89 -216.282 -113.84 -125.22 -136.60 -147.99 -159.37 -170.76 -182.14 -193.52 -204.91 -216.293 -113.84 -125.23 -136.61 -148.00 -159.38 -170.77 -182.15 -193.53 -204.92 -216.304 -113.85 -125.24 -136.62 -148.01 -159.39 -170.78 -182.16 -193.55 -204.93 -216.325 -113.86 -125.24 -136.63 -148.01 -159.40 -170.79 -182.17 -193.56 -204.94 -216.336 -113.86 -125.25 -136.64 -148.02 -159.41 -170.80 -182.18 -193.57 -204.95 -216.347 -113.87 -125.26 -136.65 -148.03 -159.42 -170.81 -182.19 -193.58 -204.97 -216.358 -113.88 -125.27 -136.65 -148.04 -159.43 -170.82 -182.20 -193.59 -204.98 -216.379 -113.88 -125.27 -136.66 -148.05 -159.44 -170.83 -182.21 -193.60 -204.99 -216.38

10 -113.89 -125.28 -136.67 -148.06 -159.45 -170.84 -182.23 -193.62 -205.00 -216.3911 -113.90 -125.29 -136.68 -148.07 -159.46 -170.85 -182.24 -193.63 -205.02 -216.4112 -113.91 -125.30 -136.69 -148.08 -159.47 -170.86 -182.25 -193.64 -205.03 -216.42


10 1.1246 1.1202 1.1158 1.1113 1.1068 1.1021 1.0974 1.0926 1.0877 1.082811 1.1246 1.1203 1.1159 1.1114 1.1068 1.1022 1.0975 1.0927 1.0878 1.082812 1.1247 1.1203 1.1159 1.1114 1.1069 1.1023 1.0975 1.0927 1.0879 1.0829





(P7= 154.547) (P8= 163.638) (P9= 172.730) (P10= 181.821) (P11= 190.912) (P12= 200.003) (P) 21 22 23 24 25 26 27 28 29 30

Enthalpy, (kJ/kg) 1 -227.66 -239.04 -250.43 -261.81 -273.19 -284.57 -295.96 -307.34 -318.72 -330.112 -227.67 -239.06 -250.44 -261.82 -273.21 -284.59 -295.98 -307.36 -318.74 -330.133 -227.69 -239.07 -250.46 -261.84 -273.22 -284.61 -295.99 -307.38 -318.76 -330.154 -227.70 -239.09 -250.47 -261.86 -273.24 -284.63 -296.01 -307.40 -318.78 -330.175 -227.71 -239.10 -250.49 -261.87 -273.26 -284.64 -296.03 -307.41 -318.80 -330.196 -227.73 -239.11 -250.50 -261.89 -273.27 -284.66 -296.05 -307.43 -318.82 -330.217 -227.74 -239.13 -250.52 -261.90 -273.29 -284.68 -296.06 -307.45 -318.84 -330.238 -227.76 -239.14 -250.53 -261.92 -273.31 -284.69 -296.08 -307.47 -318.86 -330.259 -227.77 -239.16 -250.55 -261.93 -273.32 -284.71 -296.10 -307.49 -318.88 -330.26

10 -227.78 -239.17 -250.56 -261.95 -273.34 -284.73 -296.12 -307.51 -318.90 -330.2811 -227.80 -239.19 -250.58 -261.97 -273.35 -284.75 -296.13 -307.52 -318.91 -330.3012 -227.81 -239.20 -250.59 -261.98 -273.37 -284.76 -296.15 -307.54 -318.93 -330.32


10 1.0777 1.0726 1.0673 1.0620 1.0566 1.0511 1.0455 1.0397 1.0339 1.028011 1.0778 1.0726 1.0674 1.0621 1.0567 1.0512 1.0456 1.0399 1.0340 1.028112 1.0779 1.0727 1.0675 1.0622 1.0568 1.0513 1.0457 1.0400 1.0342 1.0283




Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesPhysical Properties Profile: Cold Shellside (Oil) Reference pressure, (kPa) (P1= 140.002)

(P) 1 2 3 4 5 6 7Temperature, (C) 1 100.00 90.00 80.00 70.00 60.00 50.00 40.00Heat duty/flow rate, (kJ/kg) 1 127.147 105.113 83.4137 62.0500 41.0264 20.3431 0.0000Weight fraction vapor 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Liquid PropertiesDensity, (kg/m3) 1 950.400 956.800 963.200 969.700 976.200 982.900 989.700Viscosity, (mN-s/m2) 1 37.8436 48.8753 64.7881 88.3003 124.356 181.811 277.901Thermal conductivity, (W/m-C) 1 0.1450 0.1466 0.1482 0.1498 0.1513 0.1529 0.1545Enthalpy, (kJ/kg) 1 0.0000 -22.034 -43.733 -65.097 -86.121 -106.80 -127.15Specific heat, (kJ/kg-C) 1 2.2190 2.1850 2.1520 2.1180 2.0840 2.0500 2.0160Surface tension, (mN/m) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Critical pressure, (kPa) 1 0.000 0.000 0.000 0.000 0.000 0.000 0.000Latent heat, (kJ/kg) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000


Stream Properties Page 26Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesHot Tubeside Fluid Inlet OutletFluid name Flue GasTemperature (C) 250.00 150.00Pressure (kPa) 400.006 391.909Weight fraction vapor (--) 1.0000 1.0000

Vapor PropertiesDensity (kg/m3) 1.7001 2.0757Viscosity (mN-s/m2) 0.0251 0.0212Conductivity (W/m-C) 0.0400 0.0320Heat capacity (kJ/kg-C) 1.0544 1.0015Molecular weight (--) 0 0

Liquid PropertiesDensity (kg/m3) -- --Viscosity (mN-s/m2) -- --Conductivity (W/m-C) -- --Heat capacity (kJ/kg-C) -- --Molecular weight (--) -- --Latent heat (kJ/kg) -- --Surface tension (mN/m) -- --

Molar Composition Vapor Liquid K-Value Vapor Liquid K-Value


Stream Properties Page 27Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesCold Shellside Fluid Inlet OutletFluid name OilTemperature (C) 80.00 110.00Pressure (kPa) 140.002 138.562Weight fraction vapor (--) 0.0000 0.0000

Vapor PropertiesDensity (kg/m3) -- --Viscosity (mN-s/m2) -- --Conductivity (W/m-C) -- --Heat capacity (kJ/kg-C) -- --Molecular weight (--) -- --

Liquid PropertiesDensity (kg/m3) 963.200 944.000Viscosity (mN-s/m2) 64.7881 29.3019Conductivity (W/m-C) 0.1482 0.1434Heat capacity (kJ/kg-C) 2.1520 2.2530Molecular weight (--) 0 0Latent heat (kJ/kg) -- --Surface tension (mN/m) 0.0000 0.0000

Molar Composition Vapor Liquid K-Value Vapor Liquid K-Value


Input Reprint Page 28Released to the following HTRI Member Company: Johnson Controls Johnson Controls


Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesShell DataService type Generic Shell and TubeTEMA type HairpinRun mode RatingHot fluid location TubesideNumber of shells in series 1Number of shells in parallel 1Shell inside diameter 250.000 mmFlow in 1st tubepass CountercurrentTrain flow direction Countercurrent

Reboiler DataReboiler type No piping specifiedInlet pressure location Inlet nozzle

Tube DataTube type PlainTube outside diameter 25.400 mmTube wall thickness 1.651 mmTube pitch 31.750 mmTube pitch ratio 1.250Tubepasses per shell 1Tube pattern 30 degreesTube count method RigorousTube material Carbon steel

Tubepass Arrangement DataForce symmetric layout NoForce cleaning lanes NoTubes to remove for tie rods None

Baffle DataBaffle type Single segmentalBaffle orientation Program setsCentral baffle spacing 300.000 mmVariable baffle spacing NoWindow cut from baffles No

Clearance DataNumber of seal strip pairs CalculatedBaffle clearance type TEMABlock A stream NoBlock E stream NoBlock F stream NoNumber of passlane seal rods Calculated




Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesNozzle DataShellside inlet ID 52.502 mmNumber of shellside inlet nozzles 1Shellside outlet ID 52.502 mmNumber of shellside outlet nozzles 1Tubeside inlet ID 102.261 mmNumber of tubeside inlet nozzles 1Tubeside outlet ID 102.261 mmNumber of tubeside outlet nozzles 1Radial position on shell inlet nozzle TopLongitudinal position on shell of inlet nozzle At rear headRadial position on shell outlet nozzle Opposite sideTubeside entry type AxialTubeside inlet position Front headTubeside exit type Same as inletFront head location Left

Impingement DataImpingement device present If required by TEMAImpingement type Circular plate

Optional Geometry DataSmall exchanger NoTubesheet type SingleShell expansion joint NoFloating head support type NoneInsulated longitudinal baffle No

Process Conditions Data Hot Fluid Cold FluidPhase condition Sensible gas Sensible liquidInlet vapor fraction 1 0Outlet vapor fraction 1 0Inlet temperature 250.00 80.00 COutlet temperature 150.00 110.00 CInlet pressure 400.000 140.000 kPaExchanger duty 0.0800 MegaWattsDuty multiplier 1

Process Fouling Data Hot Fluid Cold FluidFouling resistance 0.00100 3.500e-4 m2-K/W

Hot Fluid Property DataFluid name Flue GasPhysical property method Bulk properties via gridHeat release method User specified via TP gridFlash type IntegralQuantity units MolesTemperature interpolation option ProgramHeat release type Specific enthalpy




Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesHot Fluid Physical Property DataPressure Set, 200.000 kPa

Vapor Vapor Vapor VaporMass Vapor Dynamic Thermal Heat

Temp. Enthalpy Fraction Density Viscosity Cond. CapacityC kJ/kg kg/m3 mN-s/m2 W/m-C kJ/kg-C

500.00 741.010 1 1.1495 0.0340 0.0584 1.1641490.21 729.626 1 1.1642 0.0336 0.0577 1.1605480.38 718.243 1 1.1794 0.0333 0.0570 1.1567470.52 706.860 1 1.1951 0.0330 0.0563 1.1530460.63 695.477 1 1.2112 0.0327 0.0556 1.1491450.71 684.094 1 1.2278 0.0323 0.0550 1.1452440.75 672.711 1 1.2449 0.0320 0.0543 1.1412430.76 661.327 1 1.2626 0.0316 0.0535 1.1372420.73 649.944 1 1.2809 0.0313 0.0528 1.1331410.67 638.561 1 1.2998 0.0309 0.0521 1.1289400.57 627.178 1 1.3193 0.0306 0.0514 1.1246390.43 615.794 1 1.3395 0.0302 0.0507 1.1203380.25 604.411 1 1.3604 0.0299 0.0499 1.1159370.02 593.028 1 1.3821 0.0295 0.0492 1.1114359.76 581.645 1 1.4045 0.0291 0.0484 1.1069349.46 570.262 1 1.4278 0.0288 0.0476 1.1022339.11 558.879 1 1.4520 0.0284 0.0469 1.0975328.71 547.495 1 1.4771 0.0280 0.0461 1.0927318.27 536.112 1 1.5033 0.0276 0.0453 1.0879307.78 524.729 1 1.5305 0.0272 0.0445 1.0829297.25 513.346 1 1.5588 0.0268 0.0437 1.0778286.66 501.963 1 1.5884 0.0265 0.0429 1.0727276.02 490.579 1 1.6192 0.0261 0.0420 1.0675265.33 479.196 1 1.6515 0.0256 0.0412 1.0622254.59 467.813 1 1.6852 0.0252 0.0404 1.0567243.79 456.430 1 1.7206 0.0248 0.0395 1.0512232.93 445.047 1 1.7576 0.0244 0.0386 1.0456222.02 433.663 1 1.7966 0.0240 0.0378 1.0399211.04 422.280 1 1.8375 0.0236 0.0369 1.0341200.00 410.897 1 1.8806 0.0231 0.0360 1.0282

Pressure Set, 190.909 kPaVapor Vapor Vapor VaporMass Vapor Dynamic Thermal Heat


500.00 741.015 1 1.0972 0.0340 0.0583 1.1641490.21 729.633 1 1.1113 0.0336 0.0577 1.1604480.38 718.250 1 1.1258 0.0333 0.0570 1.1567470.53 706.868 1 1.1408 0.0330 0.0563 1.1529460.64 695.485 1 1.1561 0.0327 0.0556 1.1491450.71 684.103 1 1.1720 0.0323 0.0550 1.1452440.76 672.720 1 1.1884 0.0320 0.0543 1.1412







430.76 661.338 1 1.2053 0.0316 0.0535 1.1371420.74 649.955 1 1.2227 0.0313 0.0528 1.1330410.67 638.573 1 1.2407 0.0309 0.0521 1.1288400.57 627.190 1 1.2593 0.0306 0.0514 1.1246390.43 615.808 1 1.2786 0.0302 0.0507 1.1203380.25 604.425 1 1.2986 0.0299 0.0499 1.1159370.03 593.043 1 1.3192 0.0295 0.0492 1.1114359.76 581.660 1 1.3407 0.0291 0.0484 1.1068349.46 570.278 1 1.3629 0.0288 0.0476 1.1022339.11 558.895 1 1.3860 0.0284 0.0469 1.0975328.71 547.513 1 1.4100 0.0280 0.0461 1.0927318.27 536.130 1 1.4349 0.0276 0.0453 1.0878307.79 524.747 1 1.4609 0.0272 0.0445 1.0828297.25 513.365 1 1.4879 0.0268 0.0437 1.0778286.66 501.982 1 1.5162 0.0265 0.0429 1.0726276.03 490.600 1 1.5456 0.0261 0.0420 1.0674265.34 479.217 1 1.5764 0.0256 0.0412 1.0621254.59 467.835 1 1.6086 0.0252 0.0404 1.0567243.79 456.452 1 1.6423 0.0248 0.0395 1.0511232.93 445.070 1 1.6777 0.0244 0.0386 1.0455222.02 433.687 1 1.7148 0.0240 0.0378 1.0398211.04 422.305 1 1.7539 0.0236 0.0369 1.0340200.00 410.922 1 1.7950 0.0231 0.0360 1.0281



500.00 741.021 1 1.0450 0.0340 0.0583 1.1640490.21 729.639 1 1.0584 0.0336 0.0577 1.1604480.38 718.257 1 1.0722 0.0333 0.0570 1.1567470.53 706.875 1 1.0865 0.0330 0.0563 1.1529460.64 695.493 1 1.1011 0.0327 0.0556 1.1490450.71 684.112 1 1.1162 0.0323 0.0550 1.1451440.76 672.730 1 1.1318 0.0320 0.0543 1.1411430.77 661.348 1 1.1479 0.0316 0.0535 1.1371420.74 649.966 1 1.1645 0.0313 0.0528 1.1330410.67 638.584 1 1.1816 0.0309 0.0521 1.1288400.57 627.202 1 1.1994 0.0306 0.0514 1.1245390.43 615.821 1 1.2177 0.0302 0.0506 1.1202380.25 604.439 1 1.2367 0.0299 0.0499 1.1158370.03 593.057 1 1.2564 0.0295 0.0492 1.1113







359.77 581.675 1 1.2768 0.0291 0.0484 1.1068349.46 570.293 1 1.2980 0.0288 0.0476 1.1021339.11 558.911 1 1.3200 0.0284 0.0469 1.0974328.72 547.530 1 1.3428 0.0280 0.0461 1.0926318.28 536.148 1 1.3666 0.0276 0.0453 1.0877307.79 524.766 1 1.3913 0.0272 0.0445 1.0827297.25 513.384 1 1.4171 0.0268 0.0437 1.0777286.67 502.002 1 1.4439 0.0265 0.0429 1.0725276.03 490.620 1 1.4720 0.0261 0.0420 1.0673265.34 479.239 1 1.5013 0.0256 0.0412 1.0620254.59 467.857 1 1.5320 0.0252 0.0404 1.0566243.79 456.475 1 1.5641 0.0248 0.0395 1.0511232.93 445.093 1 1.5978 0.0244 0.0386 1.0454222.02 433.711 1 1.6331 0.0240 0.0378 1.0397211.04 422.329 1 1.6703 0.0236 0.0369 1.0339200.00 410.948 1 1.7095 0.0231 0.0360 1.0280



500.00 741.026 1 0.9928 0.0340 0.0583 1.1640490.21 729.645 1 1.0055 0.0336 0.0577 1.1603480.38 718.264 1 1.0186 0.0333 0.0570 1.1566470.53 706.883 1 1.0321 0.0330 0.0563 1.1528460.64 695.502 1 1.0461 0.0327 0.0556 1.1490450.72 684.120 1 1.0604 0.0323 0.0549 1.1451440.76 672.739 1 1.0752 0.0320 0.0542 1.1411430.77 661.358 1 1.0905 0.0316 0.0535 1.1371420.74 649.977 1 1.1063 0.0313 0.0528 1.1329410.68 638.596 1 1.1226 0.0309 0.0521 1.1287400.57 627.215 1 1.1394 0.0306 0.0514 1.1245390.43 615.834 1 1.1569 0.0302 0.0506 1.1202380.25 604.452 1 1.1749 0.0299 0.0499 1.1157370.03 593.071 1 1.1936 0.0295 0.0492 1.1113359.77 581.690 1 1.2130 0.0291 0.0484 1.1067349.46 570.309 1 1.2331 0.0288 0.0476 1.1021339.11 558.928 1 1.2540 0.0284 0.0469 1.0973328.72 547.547 1 1.2757 0.0280 0.0461 1.0925318.28 536.166 1 1.2982 0.0276 0.0453 1.0876307.79 524.784 1 1.3217 0.0272 0.0445 1.0827297.26 513.403 1 1.3462 0.0268 0.0437 1.0776







286.67 502.022 1 1.3717 0.0265 0.0429 1.0725276.03 490.641 1 1.3984 0.0261 0.0420 1.0672265.34 479.260 1 1.4262 0.0256 0.0412 1.0619254.59 467.879 1 1.4553 0.0252 0.0404 1.0565243.79 456.498 1 1.4858 0.0248 0.0395 1.0510232.94 445.116 1 1.5178 0.0244 0.0386 1.0453222.02 433.735 1 1.5514 0.0240 0.0378 1.0396211.04 422.354 1 1.5868 0.0236 0.0369 1.0338200.00 410.973 1 1.6239 0.0231 0.0360 1.0279



500.00 741.032 1 0.9405 0.0340 0.0583 1.1640490.21 729.651 1 0.9526 0.0336 0.0577 1.1603480.38 718.271 1 0.9650 0.0333 0.0570 1.1566470.53 706.890 1 0.9778 0.0330 0.0563 1.1528460.64 695.510 1 0.9910 0.0327 0.0556 1.1490450.72 684.130 1 1.0046 0.0323 0.0549 1.1450440.76 672.749 1 1.0186 0.0320 0.0542 1.1411430.77 661.369 1 1.0331 0.0316 0.0535 1.1370420.74 649.988 1 1.0481 0.0313 0.0528 1.1329410.68 638.608 1 1.0635 0.0309 0.0521 1.1287400.58 627.227 1 1.0795 0.0306 0.0514 1.1244390.44 615.847 1 1.0960 0.0302 0.0506 1.1201380.26 604.466 1 1.1131 0.0299 0.0499 1.1157370.03 593.086 1 1.1308 0.0295 0.0491 1.1112359.77 581.705 1 1.1492 0.0291 0.0484 1.1066349.47 570.325 1 1.1682 0.0288 0.0476 1.1020339.12 558.944 1 1.1880 0.0284 0.0469 1.0973328.72 547.564 1 1.2085 0.0280 0.0461 1.0925318.28 536.183 1 1.2299 0.0276 0.0453 1.0876307.79 524.803 1 1.2522 0.0272 0.0445 1.0826297.26 513.422 1 1.2753 0.0268 0.0437 1.0775286.67 502.042 1 1.2995 0.0265 0.0429 1.0724276.03 490.661 1 1.3248 0.0261 0.0420 1.0672265.34 479.281 1 1.3511 0.0256 0.0412 1.0618254.60 467.901 1 1.3787 0.0252 0.0403 1.0564243.80 456.520 1 1.4076 0.0248 0.0395 1.0509232.94 445.140 1 1.4379 0.0244 0.0386 1.0452222.02 433.759 1 1.4697 0.0240 0.0378 1.0395







211.04 422.379 1 1.5032 0.0236 0.0369 1.0337200.00 410.998 1 1.5384 0.0231 0.0360 1.0278



500.00 741.037 1 0.8883 0.0340 0.0583 1.1639490.21 729.658 1 0.8997 0.0336 0.0577 1.1603480.38 718.278 1 0.9114 0.0333 0.0570 1.1565470.53 706.898 1 0.9235 0.0330 0.0563 1.1528460.64 695.518 1 0.9360 0.0326 0.0556 1.1489450.72 684.139 1 0.9488 0.0323 0.0549 1.1450440.76 672.759 1 0.9621 0.0320 0.0542 1.1410430.77 661.379 1 0.9757 0.0316 0.0535 1.1370420.74 649.999 1 0.9898 0.0313 0.0528 1.1328410.68 638.619 1 1.0044 0.0309 0.0521 1.1287400.58 627.240 1 1.0195 0.0306 0.0514 1.1244390.44 615.860 1 1.0351 0.0302 0.0506 1.1200380.26 604.480 1 1.0512 0.0299 0.0499 1.1156370.04 593.100 1 1.0680 0.0295 0.0491 1.1111359.78 581.720 1 1.0853 0.0291 0.0484 1.1066349.47 570.341 1 1.1033 0.0288 0.0476 1.1019339.12 558.961 1 1.1220 0.0284 0.0468 1.0972328.73 547.581 1 1.1414 0.0280 0.0461 1.0924318.29 536.201 1 1.1616 0.0276 0.0453 1.0875307.80 524.821 1 1.1826 0.0272 0.0445 1.0825297.26 513.442 1 1.2045 0.0268 0.0437 1.0775286.67 502.062 1 1.2273 0.0265 0.0429 1.0723276.04 490.682 1 1.2511 0.0261 0.0420 1.0671265.34 479.302 1 1.2760 0.0256 0.0412 1.0617254.60 467.923 1 1.3021 0.0252 0.0403 1.0563243.80 456.543 1 1.3294 0.0248 0.0395 1.0508232.94 445.163 1 1.3580 0.0244 0.0386 1.0451222.02 433.783 1 1.3880 0.0240 0.0378 1.0394211.04 422.403 1 1.4196 0.0236 0.0369 1.0336200.00 411.024 1 1.4529 0.0231 0.0360 1.0277







500.00 741.043 1 0.8361 0.0340 0.0583 1.1639490.21 729.664 1 0.8468 0.0336 0.0577 1.1602480.38 718.285 1 0.8578 0.0333 0.0570 1.1565470.53 706.906 1 0.8692 0.0330 0.0563 1.1527460.64 695.527 1 0.8809 0.0326 0.0556 1.1489450.72 684.147 1 0.8930 0.0323 0.0549 1.1450440.76 672.768 1 0.9055 0.0320 0.0542 1.1410430.77 661.389 1 0.9183 0.0316 0.0535 1.1369420.75 650.010 1 0.9316 0.0313 0.0528 1.1328410.68 638.631 1 0.9454 0.0309 0.0521 1.1286400.58 627.252 1 0.9595 0.0306 0.0514 1.1243390.44 615.873 1 0.9742 0.0302 0.0506 1.1200380.26 604.494 1 0.9894 0.0299 0.0499 1.1156370.04 593.115 1 1.0052 0.0295 0.0491 1.1111359.78 581.735 1 1.0215 0.0291 0.0484 1.1065349.47 570.356 1 1.0384 0.0288 0.0476 1.1019339.12 558.977 1 1.0560 0.0284 0.0468 1.0972328.73 547.598 1 1.0743 0.0280 0.0461 1.0923318.29 536.219 1 1.0932 0.0276 0.0453 1.0874307.80 524.840 1 1.1130 0.0272 0.0445 1.0825297.26 513.461 1 1.1336 0.0268 0.0437 1.0774286.68 502.082 1 1.1551 0.0265 0.0428 1.0722276.04 490.703 1 1.1775 0.0261 0.0420 1.0670265.35 479.324 1 1.2010 0.0256 0.0412 1.0616254.60 467.944 1 1.2255 0.0252 0.0403 1.0562243.80 456.565 1 1.2512 0.0248 0.0395 1.0507232.94 445.186 1 1.2781 0.0244 0.0386 1.0450222.02 433.807 1 1.3064 0.0240 0.0378 1.0393211.04 422.428 1 1.3361 0.0236 0.0369 1.0335200.00 411.049 1 1.3674 0.0231 0.0360 1.0275



500.00 741.048 1 0.7838 0.0340 0.0583 1.1639490.21 729.670 1 0.7939 0.0336 0.0577 1.1602480.39 718.292 1 0.8042 0.0333 0.0570 1.1565470.53 706.913 1 0.8149 0.0330 0.0563 1.1527460.64 695.535 1 0.8259 0.0326 0.0556 1.1488450.72 684.156 1 0.8372 0.0323 0.0549 1.1449440.77 672.778 1 0.8489 0.0320 0.0542 1.1409







430.77 661.399 1 0.8610 0.0316 0.0535 1.1369420.75 650.021 1 0.8734 0.0313 0.0528 1.1328410.68 638.643 1 0.8863 0.0309 0.0521 1.1286400.58 627.264 1 0.8996 0.0306 0.0514 1.1243390.44 615.886 1 0.9133 0.0302 0.0506 1.1199380.26 604.507 1 0.9276 0.0299 0.0499 1.1155370.04 593.129 1 0.9423 0.0295 0.0491 1.1110359.78 581.750 1 0.9576 0.0291 0.0484 1.1065349.48 570.372 1 0.9735 0.0288 0.0476 1.1018339.13 558.994 1 0.9900 0.0284 0.0468 1.0971328.73 547.615 1 1.0071 0.0280 0.0461 1.0923318.29 536.237 1 1.0249 0.0276 0.0453 1.0874307.80 524.858 1 1.0435 0.0272 0.0445 1.0824297.27 513.480 1 1.0628 0.0268 0.0437 1.0773286.68 502.102 1 1.0829 0.0265 0.0428 1.0722276.04 490.723 1 1.1039 0.0261 0.0420 1.0669265.35 479.345 1 1.1259 0.0256 0.0412 1.0616254.60 467.966 1 1.1489 0.0252 0.0403 1.0561243.80 456.588 1 1.1729 0.0248 0.0395 1.0506232.94 445.209 1 1.1982 0.0244 0.0386 1.0449222.02 433.831 1 1.2247 0.0240 0.0377 1.0392211.04 422.453 1 1.2525 0.0236 0.0369 1.0334200.00 411.074 1 1.2819 0.0231 0.0360 1.0274



500.00 741.054 1 0.7316 0.0340 0.0583 1.1638490.21 729.676 1 0.7410 0.0336 0.0577 1.1602480.39 718.299 1 0.7506 0.0333 0.0570 1.1564470.53 706.921 1 0.7606 0.0330 0.0563 1.1526460.64 695.543 1 0.7708 0.0326 0.0556 1.1488450.72 684.165 1 0.7814 0.0323 0.0549 1.1449440.77 672.788 1 0.7923 0.0320 0.0542 1.1409430.78 661.410 1 0.8036 0.0316 0.0535 1.1368420.75 650.032 1 0.8152 0.0313 0.0528 1.1327410.69 638.654 1 0.8272 0.0309 0.0521 1.1285400.59 627.277 1 0.8396 0.0306 0.0514 1.1242390.45 615.899 1 0.8525 0.0302 0.0506 1.1199380.27 604.521 1 0.8657 0.0299 0.0499 1.1155370.05 593.143 1 0.8795 0.0295 0.0491 1.1110







359.78 581.766 1 0.8938 0.0291 0.0484 1.1064349.48 570.388 1 0.9086 0.0288 0.0476 1.1018339.13 559.010 1 0.9240 0.0284 0.0468 1.0970328.74 547.632 1 0.9400 0.0280 0.0461 1.0922318.29 536.255 1 0.9566 0.0276 0.0453 1.0873307.81 524.877 1 0.9739 0.0272 0.0445 1.0823297.27 513.499 1 0.9919 0.0268 0.0437 1.0772286.68 502.121 1 1.0107 0.0265 0.0428 1.0721276.04 490.744 1 1.0303 0.0261 0.0420 1.0668265.35 479.366 1 1.0508 0.0256 0.0412 1.0615254.61 467.988 1 1.0723 0.0252 0.0403 1.0560243.80 456.610 1 1.0947 0.0248 0.0395 1.0505232.94 445.233 1 1.1183 0.0244 0.0386 1.0448222.02 433.855 1 1.1430 0.0240 0.0377 1.0391211.04 422.477 1 1.1690 0.0236 0.0369 1.0333200.00 411.099 1 1.1964 0.0231 0.0360 1.0273



500.00 741.060 1 0.6793 0.0340 0.0583 1.1638490.21 729.683 1 0.6881 0.0336 0.0577 1.1601480.39 718.306 1 0.6970 0.0333 0.0570 1.1564470.53 706.928 1 0.7063 0.0330 0.0563 1.1526460.64 695.551 1 0.7158 0.0326 0.0556 1.1488450.72 684.174 1 0.7256 0.0323 0.0549 1.1448440.77 672.797 1 0.7357 0.0320 0.0542 1.1408430.78 661.420 1 0.7462 0.0316 0.0535 1.1368420.75 650.043 1 0.7570 0.0313 0.0528 1.1327410.69 638.666 1 0.7681 0.0309 0.0521 1.1285400.59 627.289 1 0.7796 0.0306 0.0514 1.1242390.45 615.912 1 0.7916 0.0302 0.0506 1.1198380.27 604.535 1 0.8039 0.0299 0.0499 1.1154370.05 593.158 1 0.8167 0.0295 0.0491 1.1109359.79 581.781 1 0.8300 0.0291 0.0484 1.1064349.48 570.404 1 0.8437 0.0288 0.0476 1.1017339.13 559.027 1 0.8580 0.0284 0.0468 1.0970328.74 547.649 1 0.8728 0.0280 0.0461 1.0921318.30 536.273 1 0.8883 0.0276 0.0453 1.0872307.81 524.895 1 0.9043 0.0272 0.0445 1.0823297.27 513.518 1 0.9210 0.0268 0.0437 1.0772







286.69 502.141 1 0.9385 0.0265 0.0428 1.0720276.05 490.764 1 0.9567 0.0261 0.0420 1.0667265.35 479.387 1 0.9757 0.0256 0.0412 1.0614254.61 468.010 1 0.9956 0.0252 0.0403 1.0559243.80 456.633 1 1.0165 0.0248 0.0395 1.0504232.94 445.256 1 1.0384 0.0244 0.0386 1.0447222.02 433.879 1 1.0613 0.0240 0.0377 1.0390211.04 422.502 1 1.0855 0.0236 0.0369 1.0331200.00 411.125 1 1.1109 0.0231 0.0360 1.0272



500.00 741.065 1 0.6271 0.0340 0.0583 1.1638490.21 729.689 1 0.6351 0.0336 0.0577 1.1601480.39 718.312 1 0.6434 0.0333 0.0570 1.1564470.53 706.936 1 0.6520 0.0330 0.0563 1.1526460.65 695.560 1 0.6607 0.0326 0.0556 1.1487450.73 684.183 1 0.6698 0.0323 0.0549 1.1448440.77 672.807 1 0.6792 0.0320 0.0542 1.1408430.78 661.431 1 0.6888 0.0316 0.0535 1.1367420.75 650.054 1 0.6988 0.0313 0.0528 1.1326410.69 638.678 1 0.7090 0.0309 0.0521 1.1284400.59 627.301 1 0.7197 0.0306 0.0514 1.1241390.45 615.925 1 0.7307 0.0302 0.0506 1.1198380.27 604.549 1 0.7421 0.0299 0.0499 1.1154370.05 593.172 1 0.7539 0.0295 0.0491 1.1109359.79 581.796 1 0.7661 0.0291 0.0484 1.1063349.48 570.419 1 0.7788 0.0288 0.0476 1.1016339.14 559.043 1 0.7920 0.0284 0.0468 1.0969328.74 547.667 1 0.8057 0.0280 0.0461 1.0921318.30 536.290 1 0.8199 0.0276 0.0453 1.0872307.81 524.914 1 0.8347 0.0272 0.0445 1.0822297.28 513.538 1 0.8502 0.0268 0.0437 1.0771286.69 502.161 1 0.8663 0.0265 0.0428 1.0719276.05 490.785 1 0.8831 0.0261 0.0420 1.0667265.36 479.408 1 0.9007 0.0256 0.0412 1.0613254.61 468.032 1 0.9190 0.0252 0.0403 1.0559243.81 456.656 1 0.9383 0.0248 0.0395 1.0503232.95 445.279 1 0.9585 0.0244 0.0386 1.0446222.03 433.903 1 0.9797 0.0240 0.0377 1.0389







211.04 422.527 1 1.0019 0.0236 0.0369 1.0330200.00 411.150 1 1.0254 0.0231 0.0360 1.0271



500.00 741.071 1 0.5749 0.0340 0.0583 1.1637490.21 729.695 1 0.5822 0.0336 0.0577 1.1601480.39 718.319 1 0.5898 0.0333 0.0570 1.1563470.53 706.944 1 0.5976 0.0330 0.0563 1.1525460.65 695.568 1 0.6057 0.0326 0.0556 1.1487450.73 684.192 1 0.6140 0.0323 0.0549 1.1447440.77 672.817 1 0.6226 0.0320 0.0542 1.1408430.78 661.441 1 0.6314 0.0316 0.0535 1.1367420.76 650.065 1 0.6405 0.0313 0.0528 1.1326410.69 638.689 1 0.6500 0.0309 0.0521 1.1284400.59 627.314 1 0.6597 0.0306 0.0514 1.1241390.45 615.938 1 0.6698 0.0302 0.0506 1.1197380.27 604.562 1 0.6802 0.0299 0.0499 1.1153370.05 593.187 1 0.6911 0.0295 0.0491 1.1108359.79 581.811 1 0.7023 0.0291 0.0484 1.1062349.49 570.435 1 0.7139 0.0288 0.0476 1.1016339.14 559.059 1 0.7260 0.0284 0.0468 1.0968328.74 547.684 1 0.7385 0.0280 0.0460 1.0920318.30 536.308 1 0.7516 0.0276 0.0453 1.0871307.82 524.932 1 0.7652 0.0272 0.0445 1.0821297.28 513.557 1 0.7793 0.0268 0.0437 1.0770286.69 502.181 1 0.7941 0.0265 0.0428 1.0719276.05 490.805 1 0.8095 0.0261 0.0420 1.0666265.36 479.430 1 0.8256 0.0256 0.0412 1.0612254.61 468.054 1 0.8424 0.0252 0.0403 1.0558243.81 456.678 1 0.8601 0.0248 0.0395 1.0502232.95 445.303 1 0.8786 0.0244 0.0386 1.0445222.03 433.927 1 0.8980 0.0240 0.0377 1.0388211.04 422.551 1 0.9184 0.0236 0.0368 1.0329200.00 411.175 1 0.9399 0.0231 0.0360 1.0269




Rating - Horizontal Countercurrent Flow Hairpin With Single-Segmental BafflesCold Fluid Property DataFluid name OilPhysical property method Bulk properties via gridHeat release method User specified via TP gridFlash type IntegralQuantity units MolesTemperature interpolation option ProgramHeat release type Specific enthalpy

Cold Fluid Physical Property DataPressure Set - 1

Vapor Liquid Liquid LiquidMass Liquid Dynamic Thermal Heat

Temp. Fraction Density Viscosity Cond. CapacityC kg/m3 mN-s/m2 W/m-C kJ/kg-C40.00 0 989.700 277.901 0.1545 2.016050.00 0 982.900 181.811 0.1529 2.050060.00 0 976.200 124.356 0.1513 2.084070.00 0 969.700 88.3003 0.1498 2.118080.00 0 963.200 64.7881 0.1482 2.152090.00 0 956.800 48.8753 0.1466 2.1850

100.00 0 950.400 37.8436 0.1450 2.2190

Control Methods DataShellside friction factor method CommercialTubeside friction factor method CommercialPure longitudinal flow NoPure component condensation NoCondensing correlation HTRI ProrationMole fraction inerts 0Momentum exclusion 0 %Pure component boiling NoCheck film boiling YesNucleate boiling method Physical property/theoretical boiling rangeComponent boiling method Nucleate and convective

Control Safety DataCold fluid/shellside film coefficient multiplier 1Hot fluid/tubeside film coefficient multiplier 1

Control User-Defined Methods DataAdd non-nucleate boiling Yes

Documents

Thermic Fluid HX