hmb for preheat train

7/23/2019 HMB for Preheat Train

1/8

LEGENDS

Burlington, MA

USA

Case Name: REFINERY ON PRESSURE SPECS.HSC

Unit Set: Refinery1

Date/Time: Tue Sep 08 10:25:24 2015

Workbook: PREHEAT TRAIN (TPL1)

Material Streams Fluid Pkg: All

Name

Vapour Fraction

Temperature

Pressure

Molar Flow

Mass Flow

Std Ideal Liq Vol Flow

Heat Flow

Liquid Fraction

Light Liquid Fraction

Heavy Liquid Fraction

Vap Frac on a Mass Basis

Vap Frac on a Volume Basis

Molar Volume

Actual Volume Flow

Power

Actual Gas Flow

Actual Liquid Flow

Liq Vol Flow @Std Cond

Std Gas Flow

Molecular Weight

Mass Density

Std Ideal Liq Mass Density

Molar Density

Average Liquid Density

Liq Mass Density @Std Cond

Molar Heat CapacityMolar Enthalpy

Mass Enthalpy

Molar Entropy

Mass Entropy

Thermal Conductivity

Viscosity

Surface Tension

Specific Gravity rel Air

Watson K

Kinematic Viscosity

Cp/Cv

(C)

(psia)

(lbmole/hr)

(lb/hr)

(barrel/day)

(Btu/hr)

(ft3/lbmole)

(USGPM)

(kW)

(ACFM)

(USGPM)

(barrel/day)

(MMSCFD)

(lb/ft3)

(lb/ft3)

(lbmole/ft3)

(lbmole/ft3)

(API_60)

(Btu/lbmole-F)(Btu/lbmole)

(Btu/lb)

(Btu/lbmole-F)

(Btu/lb-F)

(Btu/hr-ft-F)

(cP)

(dyne/cm)

(rel_to_air)

(cSt)

FEED IN 6000 bpd

0.0000

45.00

49.31

489.1

6.777e+004

6000

-6.220e+007

1.000

1.000

3.471e-005

0.0000

0.0000

2.940

179.3

-1.823e+004

---

179.3

5958

4.446

138.6

47.12

48.28

0.3401

0.3485

49.79

67.07-1.272e+005

-917.7

47.95

0.3461

6.367e-002

0.9135

20.28

---

11.96

1.210

1.220

F Oil to EA-109

0.0000

232.7

19.50

33.76

1.149e+004

890.6

-8.217e+006

1.000

1.000

0.0000

0.0000

0.0000

7.501

31.58

-2408

---

31.58

897.2

0.3069

340.3

45.36

55.14

0.1333

0.1621

29.56

220.3-2.434e+005

-715.2

238.8

0.7017

5.985e-002

0.6997

16.33

---

12.03

0.9629

1.191

HSD to EA-108

0.0000

198.9

19.70

81.10

1.686e+004

1409

-1.272e+007

1.000

1.000

0.0000

0.0000

0.0000

4.884

49.39

-3727

---

49.39

1408

0.7372

207.9

42.56

51.13

0.2047

0.2460

40.77

131.0-1.568e+005

-754.2

123.2

0.5929

5.857e-002

0.3095

13.92

---

12.03

0.4540

1.167

From Con 2

1.0000

176.2

19.88

448.4

4.542e+004

3985

-4.314e+007

0.0000

0.0000

0.0000

1.0000

1.0000

421.5

2.357e+004

-1.264e+004

3150

---

3895

4.076

101.3

0.2403

48.73

2.372e-003

0.4810

45.33

53.40-9.621e+004

-949.8

76.96

0.7598

1.319e-002

9.070e-003

---

3.497

12.04

2.356

1.044

Cold KERO

0.0000

57.50*

16.88

116.3

1.627e+004

1446

-1.478e+007

1.000

0.9935

6.456e-003

0.0000

0.0000

3.033

43.99

-4331

---

43.99

1444

1.058

139.8

46.11

48.10

0.3297

0.3440

51.52

69.44-1.270e+005

-908.5

46.22

0.3306

6.470e-002

0.6209

---

---

12.04

0.8408

1.219

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* Specified by user.Licensed to: LEGENDS


2/8

LEGENDS

Burlington, MA

USA


Unit Set: Refinery1


Workbook: PREHEAT TRAIN (TPL1) (continued)

Material Streams (continued) Fluid Pkg: All

Name

Vapour Fraction

Temperature

Pressure

Molar Flow

Mass Flow


Heat Flow

Liquid Fraction





Molar Volume

Actual Volume Flow

Power

Actual Gas Flow

Actual Liquid Flow


Std Gas Flow

Molecular Weight

Mass Density


Molar Density




Mass Enthalpy

Molar Entropy

Mass Entropy


Viscosity

Surface Tension


Watson K

Kinematic Viscosity

Cp/Cv

(C)

(psia)

(lbmole/hr)

(lb/hr)

(barrel/day)

(Btu/hr)

(ft3/lbmole)

(USGPM)

(kW)

(ACFM)

(USGPM)

(barrel/day)

(MMSCFD)

(lb/ft3)

(lb/ft3)

(lbmole/ft3)

(lbmole/ft3)

(API_60)


(Btu/lb)

(Btu/lbmole-F)

(Btu/lb-F)

(Btu/hr-ft-F)

(cP)

(dyne/cm)

(rel_to_air)

(cSt)

Feed to EA-101

0.0000

42.00*

33.00

2685

4.837e+004

3319

-3.289e+008

1.000

0.0000

1.000

0.0000

0.0000

0.2902

97.15

-9.639e+004

---

97.15

3264

24.41

18.02

62.08

62.30

3.446

3.458

7.655

18.57-1.225e+005

-6799

13.86

0.7691

0.3663

0.6274

69.14

---

---

0.6309

1.157

Feed to EA-102

0.0000

56.46

47.31

489.1

6.777e+004

6000

-6.151e+007

1.000

1.000

0.0000

0.0000

0.0000

2.978

181.6

-1.803e+004

---

181.6

5958

4.446

138.6

46.53

48.28

0.3358

0.3485

49.79

68.87-1.258e+005

-907.6

50.36

0.3635

6.264e-002

0.7849

19.24

---

11.96

1.053

1.219

Feed to EA-104

0.1002

135.3

41.31

489.1

6.777e+004

6000

-5.583e+007

0.8998

0.8998

0.0000

0.0555

0.0645

21.11

1287

-1.636e+004

---

187.0

5958

4.446

138.6

6.565

48.28

4.738e-002

0.3485

49.79

80.23-1.141e+005

-823.8

67.76

0.4890

---

---

13.19

---

11.96

---

1.004

Feed to EA-105

0.1770

144.5

39.31

489.1

6.777e+004

6000

-5.477e+007

0.8230

0.8230

0.0000

0.1044

0.1185

37.16

2266

-1.605e+004

---

177.9

5958

4.446

138.6

3.729

48.28

2.691e-002

0.3485

49.79

80.78-1.120e+005

-808.1

70.70

0.5103

---

---

12.95

---

11.96

---

1.006

Cold HSD

0.0000

76.03

29.01*

81.10

1.686e+004

1409

-1.483e+007

1.000

0.9982

1.820e-003

0.0000

0.0000

4.289

43.37

-4347

---

43.37

1408

0.7372

207.9

48.47

51.13

0.2332

0.2460

40.77

104.6-1.829e+005

-879.8

87.85

0.4226

6.703e-002

1.278

---

---

12.03

1.647

1.183


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3/8

LEGENDS

Burlington, MA

USA


Unit Set: Refinery1




Name

Vapour Fraction

Temperature

Pressure

Molar Flow

Mass Flow


Heat Flow

Liquid Fraction





Molar Volume

Actual Volume Flow

Power

Actual Gas Flow

Actual Liquid Flow


Std Gas Flow

Molecular Weight

Mass Density


Molar Density




Mass Enthalpy

Molar Entropy

Mass Entropy


Viscosity

Surface Tension


Watson K

Kinematic Viscosity

Cp/Cv

(C)

(psia)

(lbmole/hr)

(lb/hr)

(barrel/day)

(Btu/hr)

(ft3/lbmole)

(USGPM)

(kW)

(ACFM)

(USGPM)

(barrel/day)

(MMSCFD)

(lb/ft3)

(lb/ft3)

(lbmole/ft3)

(lbmole/ft3)

(API_60)


(Btu/lb)

(Btu/lbmole-F)

(Btu/lb-F)

(Btu/hr-ft-F)

(cP)

(dyne/cm)

(rel_to_air)

(cSt)

11

0.0000

92.68

43.31

489.1

6.777e+004

6000

-5.923e+007

1.000

1.000

0.0000

0.0000

0.0000

3.108

189.5

-1.736e+004

---

189.5

5958

4.446

138.6

44.59

48.28

0.3218

0.3485

49.79

74.56-1.211e+005

-873.9

57.83

0.4174

5.920e-002

0.5124

16.05

---

11.96

0.7175

1.213

Feed to EA-109

0.2346

149.6

37.31

489.1

6.777e+004

6000

-5.408e+007

0.7654

0.7654

0.0000

0.1435

0.1609

51.22

3123

-1.585e+004

---

170.2

5958

4.446

138.6

2.705

48.28

1.952e-002

0.3485

49.79

80.88-1.106e+005

-798.0

72.58

0.5238

---

---

12.91

---

11.96

---

1.008

Feed to PreFlash

0.3049

155.6

35.31

489.1

6.777e+004

6000

-5.323e+007

0.6951

0.6951

0.0000

0.1939

0.2148

70.17

4279

-1.560e+004

---

160.2

5958

4.446

138.6

1.975

48.28

1.425e-002

0.3485

49.79

80.95-1.088e+005

-785.4

74.88

0.5404

---

---

12.88

---

11.96

---

1.010

22

0.0000

166.0*

17.50

33.76

1.149e+004

890.6

-9.068e+006

1.000

1.000

0.0000

0.0000

0.0000

7.038

29.63

-2658

---

29.63

897.2

0.3069

340.3

48.34

55.14

0.1421

0.1621

29.56

199.4-2.686e+005

-789.3

209.1

0.6146

6.496e-002

1.527

20.57

---

12.03

1.972

1.202

23

0.0000

166.0*

17.50*

33.76*

1.149e+004

890.6

-9.068e+006

1.000

1.000

0.0000

0.0000

0.0000

7.038

29.63

-2658

---

29.63

897.2

0.3069

340.3

48.34

55.14

0.1421

0.1621

29.56

199.4-2.686e+005

-789.3

209.1

0.6146

6.496e-002

1.527

20.57

---

12.03

1.972

1.202


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4/8

LEGENDS

Burlington, MA

USA


Unit Set: Refinery1




Name

Vapour Fraction

Temperature

Pressure

Molar Flow

Mass Flow


Heat Flow

Liquid Fraction





Molar Volume

Actual Volume Flow

Power

Actual Gas Flow

Actual Liquid Flow


Std Gas Flow

Molecular Weight

Mass Density


Molar Density




Mass Enthalpy

Molar Entropy

Mass Entropy


Viscosity

Surface Tension


Watson K

Kinematic Viscosity

Cp/Cv

(C)

(psia)

(lbmole/hr)

(lb/hr)

(barrel/day)

(Btu/hr)

(ft3/lbmole)

(USGPM)

(kW)

(ACFM)

(USGPM)

(barrel/day)

(MMSCFD)

(lb/ft3)

(lb/ft3)

(lbmole/ft3)

(lbmole/ft3)

(API_60)


(Btu/lb)

(Btu/lbmole-F)

(Btu/lb-F)

(Btu/hr-ft-F)

(cP)

(dyne/cm)

(rel_to_air)

(cSt)

HSD to EA-103

0.0000

162.0*

17.70*

81.10*

1.686e+004

1409

-1.340e+007

1.000

1.000

0.0000

0.0000

0.0000

4.680

47.32

-3927

---

47.32

1408

0.7372

207.9

44.42

51.13

0.2137

0.2460

40.77

123.2-1.652e+005

-794.9

112.9

0.5431

6.121e-002

0.4384

16.57

---

12.03

0.6162

1.172

HSD Rundown

0.0000

48.00*

27.56*

81.10

1.686e+004

1409

-1.525e+007

1.000

0.9958

4.177e-003

0.0000

0.0000

4.181

42.27

-4469

---

42.27

1408

0.7372

207.9

49.72

51.13

0.2392

0.2460

40.77

98.45-1.880e+005

-904.6

79.30

0.3815

6.865e-002

2.094

---

---

12.03

2.630

1.179

diesel minors to EA-1

0.9087

168.0*

17.88

448.4

4.542e+004

3985

-4.421e+007

9.128e-002

9.128e-002

0.0000

0.8656

0.8651

420.5

2.351e+004

-1.296e+004

---

18.62

3895

4.076

101.3

0.2409

48.73

2.378e-003

0.4810

45.33

53.89-9.859e+004

-973.2

74.19

0.7324

---

---

12.72

---

12.04

---

1.039

35

0.0000

76.00*

15.70

81.10

1.686e+004

1409

-1.483e+007

1.000

0.9982

1.820e-003

0.0000

0.0000

4.289

43.37

-4347

---

43.37

1408

0.7372

207.9

48.46

51.13

0.2331

0.2460

40.77

104.6-1.829e+005

-879.9

87.85

0.4226

6.703e-002

1.279

---

---

12.03

1.648

1.183

Feed to EA-103

0.0000

79.49

45.31

489.1

6.777e+004

6000

-6.008e+007

1.000

1.000

0.0000

0.0000

0.0000

3.058

186.5

-1.761e+004

---

186.5

5958

4.446

138.6

45.31

48.28

0.3270

0.3485

49.79

72.48-1.228e+005

-886.5

55.13

0.3979

6.049e-002

0.5934

17.20

---

11.96

0.8177

1.215


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5/8

LEGENDS

Burlington, MA

USA


Unit Set: Refinery1




Name

Vapour Fraction

Temperature

Pressure

Molar Flow

Mass Flow


Heat Flow

Liquid Fraction





Molar Volume

Actual Volume Flow

Power

Actual Gas Flow

Actual Liquid Flow


Std Gas Flow

Molecular Weight

Mass Density


Molar Density




Mass Enthalpy

Molar Entropy

Mass Entropy


Viscosity

Surface Tension


Watson K

Kinematic Viscosity

Cp/Cv

(C)

(psia)

(lbmole/hr)

(lb/hr)

(barrel/day)

(Btu/hr)

(ft3/lbmole)

(USGPM)

(kW)

(ACFM)

(USGPM)

(barrel/day)

(MMSCFD)

(lb/ft3)

(lb/ft3)

(lbmole/ft3)

(lbmole/ft3)

(API_60)


(Btu/lb)

(Btu/lbmole-F)

(Btu/lb-F)

(Btu/hr-ft-F)

(cP)

(dyne/cm)

(rel_to_air)

(cSt)

1

0.0000

98.00*

17.00*

448.4

4.542e+004

3985

-5.440e+007

1.000

0.6831

0.3169

0.0000

0.0000

2.265

126.7

-1.594e+004

---

126.7

3895

4.076

101.3

44.72

48.73

0.4414

0.4810

45.33

57.81-1.213e+005

-1198

42.77

0.4223

6.711e-002

0.4654

---

---

12.04

0.6497

1.196

4

1.0000

98.00

17.00

0.0000

0.0000

0.0000

0.0000

0.0000

0.0000

0.0000

1.0000

1.0000

416.8

0.0000

0.0000

0.0000

---

0.0000

0.0000

32.19

7.724e-002

53.75

2.399e-003

1.670

21.19

14.58-1.020e+005

-3170

47.21

1.467

1.271e-002

1.007e-002

---

1.111

12.05

8.139

1.165

5

0.0000

98.00

17.00

306.3

4.287e+004

3809

-3.727e+007

1.000

1.000

0.0000

0.0000

0.0000

3.175

121.3

-1.092e+004

---

121.3

3804

2.784

139.9

44.07

48.10

0.3149

0.3438

51.53

75.86-1.217e+005

-869.4

54.77

0.3914

6.281e-002

0.3994

17.94

---

12.04

0.5657

1.209

7

0.0000

98.00

17.00

142.1

2560

175.6

-1.714e+007

1.000

0.0000

1.000

0.0000

0.0000

0.3039

5.384

-5022

---

5.384

172.7

1.292

18.02

59.28

62.30

3.291

3.458

7.655

18.90-1.206e+005

-6694

16.91

0.9389

0.3928

0.2849

58.98

---

12.05

0.3001

1.175

Kerosene

0.0000

101.7

17.88

116.3

1.627e+004

1446

-1.409e+007

1.000

1.000

0.0000

0.0000

0.0000

3.186

46.22

-4130

---

46.22

1444

1.058

139.8

43.88

48.10

0.3138

0.3440

51.52

76.39-1.211e+005

-866.3

55.51

0.3970

6.271e-002

0.3853

17.67

---

12.04

0.5481

1.208


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6/8

LEGENDS

Burlington, MA

USA


Unit Set: Refinery1




Name

Vapour Fraction

Temperature

Pressure

Molar Flow

Mass Flow


Heat Flow

Liquid Fraction





Molar Volume

Actual Volume Flow

Power

Actual Gas Flow

Actual Liquid Flow


Std Gas Flow

Molecular Weight

Mass Density


Molar Density




Mass Enthalpy

Molar Entropy

Mass Entropy


Viscosity

Surface Tension


Watson K

Kinematic Viscosity

Cp/Cv

(C)

(psia)

(lbmole/hr)

(lb/hr)

(barrel/day)

(Btu/hr)

(ft3/lbmole)

(USGPM)

(kW)

(ACFM)

(USGPM)

(barrel/day)

(MMSCFD)

(lb/ft3)

(lb/ft3)

(lbmole/ft3)

(lbmole/ft3)

(API_60)


(Btu/lb)

(Btu/lbmole-F)

(Btu/lb-F)

(Btu/hr-ft-F)

(cP)

(dyne/cm)

(rel_to_air)

(cSt)

Naptha

0.0122

71.71

19.20

231.4

2.143e+004

2058

-1.942e+007

0.9878

0.9878

0.0000

0.0093

0.0100

6.296

181.6

-5692

---

63.86

2050

2.104

92.63

14.71

44.52

0.1588

0.4806

65.75

49.93-8.393e+004

-906.1

26.94

0.2909

---

---

14.98

---

12.12

---

1.001

3

0.0000

42.00*

17.20

231.4

2.143e+004

2058

-2.005e+007

1.000

0.9994

6.000e-004

0.0000

0.0000

2.145

61.89

-5876

---

61.89

2050

2.104

92.63

43.18

44.52

0.4662

0.4806

65.75

46.48-8.664e+004

-935.4

22.39

0.2417

6.156e-002

0.3470

---

---

12.12

0.5017

1.287

8

0.9088

168.0*

17.88*

448.4*

4.542e+004

3985

-4.421e+007

9.123e-002

9.123e-002

0.0000

0.8657

0.8652

420.5

2.351e+004

-1.296e+004

---

18.61

3895

4.076

101.3

0.2409

48.73

2.378e-003

0.4810

45.33

53.89-9.858e+004

-973.2

74.20

0.7324

---

---

12.72

---

12.04

---

1.039

Cold Fractionater Ovh

0.6017

145.0*

15.88

448.4

4.542e+004

3985

-4.760e+007

0.3983

0.3983

0.0000

0.4326

0.4277

301.6

1.686e+004

-1.395e+004

---

76.84

3895

4.076

101.3

0.3359

48.73

3.316e-003

0.4810

45.33

55.78-1.062e+005

-1048

64.59

0.6376

---

---

14.22

---

12.04

---

1.024

12

0.0000

162.0*

17.70

81.10

1.686e+004

1409

-1.340e+007

1.000

1.000

0.0000

0.0000

0.0000

4.680

47.32

-3927

---

47.32

1408

0.7372

207.9

44.42

51.13

0.2137

0.2460

40.77

123.2-1.652e+005

-794.9

112.9

0.5431

6.121e-002

0.4384

16.57

---

12.03

0.6162

1.172


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69



7/8

LEGENDS

Burlington, MA

USA


Unit Set: Refinery1




Name

Vapour Fraction

Temperature

Pressure

Molar Flow

Mass Flow


Heat Flow

Liquid Fraction





Molar Volume

Actual Volume Flow

Power

Actual Gas Flow

Actual Liquid Flow


Std Gas Flow

Molecular Weight

Mass Density


Molar Density




Mass Enthalpy

Molar Entropy

Mass Entropy


Viscosity

Surface Tension


Watson K

Kinematic Viscosity

Cp/Cv

(C)

(psia)

(lbmole/hr)

(lb/hr)

(barrel/day)

(Btu/hr)

(ft3/lbmole)

(USGPM)

(kW)

(ACFM)

(USGPM)

(barrel/day)

(MMSCFD)

(lb/ft3)

(lb/ft3)

(lbmole/ft3)

(lbmole/ft3)

(API_60)


(Btu/lb)

(Btu/lbmole-F)

(Btu/lb-F)

(Btu/hr-ft-F)

(cP)

(dyne/cm)

(rel_to_air)

(cSt)

Cold FO

0.0000

91.00*

16.50

33.76

1.149e+004

890.6

-9.921e+006

1.000

0.9997

2.651e-004

0.0000

0.0000

6.598

27.78

-2908

---

27.78

897.2

0.3069

340.3

51.57

55.14

0.1516

0.1621

29.56

174.7-2.938e+005

-863.6

174.1

0.5117

7.058e-002

5.364

---

---

12.03

6.494

1.194

2

0.0000

42.00*

16.88

116.3

1.627e+004

1446

-1.500e+007

1.000

0.9927

7.323e-003

0.0000

0.0000

2.984

43.28

-4397

---

43.28

1444

1.058

139.8

46.86

48.10

0.3351

0.3440

51.52

67.00-1.290e+005

-922.2

42.93

0.3070

6.561e-002

0.7553

---

---

12.04

1.006

1.221

Kero Water

0.0000

35.00*

35.00*

857.7

1.545e+004

1060

-1.053e+008

1.000

0.0000

1.000

0.0000

0.0000

0.2886

30.86

-3.085e+004

---

30.86

1043

7.797

18.02

62.42

62.30

3.465

3.458

7.655

18.56-1.227e+005

-6812

13.44

0.7460

0.3612

0.7185

70.36

---

---

0.7186

1.153

14

0.0000

42.78*

35.00

857.7

1.545e+004

1060

-1.050e+008

1.000

0.0000

1.000

0.0000

0.0000

0.2904

31.05

-3.078e+004

---

31.05

1043

7.797

18.02

62.05

62.30

3.444

3.458

7.655

18.57-1.225e+005

-6798

13.90

0.7717

0.3668

0.6184

69.01

---

---

0.6222

1.157

HSD Water

0.0000

35.00*

35.00*

1252

2.255e+004

1547

-1.536e+008

1.000

0.0000

1.000

0.0000

0.0000

0.2886

45.04

-4.501e+004

---

45.04

1521

11.38

18.02

62.42

62.30

3.465

3.458

7.655

18.56-1.227e+005

-6812

13.44

0.7460

0.3612

0.7185

70.36

---

---

0.7186

1.153


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8/8

LEGENDS

Burlington, MA

USA


Unit Set: Refinery1




Name

Vapour Fraction

Temperature

Pressure

Molar Flow

Mass Flow


Heat Flow

Liquid Fraction





Molar Volume

Actual Volume Flow

Power

Actual Gas Flow

Actual Liquid Flow


Std Gas Flow

Molecular Weight

Mass Density


Molar Density




Mass Enthalpy

Molar Entropy

Mass Entropy


Viscosity

Surface Tension


Watson K

Kinematic Viscosity

Cp/Cv

(C)

(psia)

(lbmole/hr)

(lb/hr)

(barrel/day)

(Btu/hr)

(ft3/lbmole)

(USGPM)

(kW)

(ACFM)

(USGPM)

(barrel/day)

(MMSCFD)

(lb/ft3)

(lb/ft3)

(lbmole/ft3)

(lbmole/ft3)

(API_60)


(Btu/lb)

(Btu/lbmole-F)

(Btu/lb-F)

(Btu/hr-ft-F)

(cP)

(dyne/cm)

(rel_to_air)

(cSt)

16

0.0000

45.00*

35.00

1252

2.255e+004

1547

-1.532e+008

1.000

0.0000

1.000

0.0000

0.0000

0.2909

45.39

-4.489e+004

---

45.39

1521

11.38

18.02

61.94

62.30

3.438

3.458

7.655

18.58-1.224e+005

-6793

14.03

0.7789

0.3684

0.5939

68.62

---

---

0.5986

1.158

Nap Water

0.0000

35.00*

35.00*

2685

4.837e+004

3319

-3.295e+008

1.000

0.0000

1.000

0.0000

0.0000

0.2886

96.63

-9.657e+004

---

96.63

3264

24.41

18.02

62.42

62.30

3.465

3.458

7.655

18.56-1.227e+005

-6812

13.44

0.7460

0.3612

0.7185

70.36

---

---

0.7186

1.153

19

0.0000

50.00*

16.50

33.76

1.149e+004

890.6

-1.034e+007

1.000

0.9952

4.803e-003

0.0000

0.0000

6.383

26.87

-3031

---

26.87

897.2

0.3069

340.3

53.30

55.14

0.1567

0.1621

29.56

160.7-3.063e+005

-900.2

154.0

0.4526

7.295e-002

11.07

---

---

12.03

12.97

1.170

FO Water

0.0000

35.00*

35.00*

1048

1.887e+004

1295

-1.286e+008

1.000

0.0000

1.000

0.0000

0.0000

0.2886

37.70

-3.768e+004

---

37.70

1273

9.523

18.02

62.42

62.30

3.465

3.458

7.655

18.56-1.227e+005

-6812

13.44

0.7460

0.3612

0.7185

70.36

---

---

0.7186

1.153

21

0.0000

47.00*

35.00

1048

1.887e+004

1295

-1.281e+008

1.000

0.0000

1.000

0.0000

0.0000

0.2913

38.05

-3.755e+004

---

38.05

1273

9.523

18.02

61.84

62.30

3.433

3.458

7.655

18.58-1.223e+005

-6790

14.15

0.7854

0.3697

0.5731

68.26

---

---

0.5786

1.159


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hmb for preheat train

Documents