Welcome! [] Webinars/Webinar 1 - Asse… · Overall HRSG Thermodynamic Data 1. HRSG Summary HRSG efficiency 81,58 % Heat recovered 66040 kW Heat loss 495,3 kW Heat available in exhaust

Welcome!

Webinar #1: ASSEMBLIES in THERMOFLEX 13 JUNE 2017

Agenda:

* Introduction

* HRSG Assembly

* Boiler Assembly

* Steam Turbine Assembly

* Plant Assembly

* Q & A Session

Presenter: IGNACIO MARTIN (SPAIN)Support: Meritt Elmasri (U.S. HQ)

- Welcome and purpose of the FAW. TF Education options

- Thermoflow Background

- Programs: Application Specific vs Fully Flexible Approach

- Assemblies in THERMOFLEX/PEACE: Why

1. Introduction

©Thermoflow Inc. 2017 – Webinar: Assemblies in THERMOFLEX, June 13, 2017 by IGNACIO MARTIN 2

Thermoflow Training and Support

- Standard Training

- On-site Training course

- Advanced Workshop

- Webinars when new Version is released

- Help, Tutorials, PPT, Videos

- Technical Support

Feature Awareness Webinars


Thermoflow Background

Consulting company 1981-1987 while founder was professor at MIT.

Since 1987, full-time focus on power plant modeling software. First copy of GT PRO sold in

1988.

Thermoflow provides the world’s most complete and mature heat balance software product line,

with over 330,000 man-hours of advanced talent invested during 28 years of steady evolution.

We believe that the Thermoflow heat balance software suite is the most widely used in the world.

Developed and maintained by a stable group of experienced mechanical engineers, mostly top

MIT graduates and Ph.D.’s, no ‘programmers’ or external subcontractors ever used.

Thermoflow has always been independent, stable, profitable and conservative. Ample financial

resources for stability, derived from excellence of its products, not from sponsors.


Thermoflow Programs

ProgramYear First Copy

Licensed

Aprx Total Licenses/Seats

Sold (end 2015)

GT PRO 1988 2400

GT MASTER 1988 1840

STEAM PRO 1990 1020

STEAM MASTER 1991 850

RE-MASTER 1992 400

THERMOFLEX 1995 1370

PDE 1995 800

PEACE 1998 1640


System

Subsystem SubsystemSubsystem

Details DetailsDetails Details Details Details Details Details Details System


Details DetailsDetails Details Details Details Details Details Details

Application-Specific

ProgramFully-Flexible

Program

...built from the outside in ...built from the inside out


System


Details DetailsDetails Details Details Details Details Details Details

Subsystem

Details

Details

Details

Application-Specific + Fully-Flexible

...you can even get the best of both worlds


GT PRO-Design of Gas Turbine Combined Cycle

and Cogeneration Systems

GT Template- User-Defined GT

Plant Design Expert (PDE)- Executive level of GT PRO

GT MASTER- Simulation

- OFF-Design

PEACE*-Preliminary Engineering

-Cost Estimation

-Detailed Hardware Specifications

* Plant Engineering and Construction Estimator

Elink

DRS

TOPS


STEAM PRO- Design of conventional steam power plants

STEAM MASTER- Simulation

- OFF-Design

RE-MASTER- Design and Simulation of conventional

Steam power plants with gas turbines

Elink

DRS

TOPS

PEACE*-Preliminary Engineering

-Cost Estimation

-Detailed Hardware Specifications

* Plant Engineering and Construction Estimator


THERMOFLEX-Modular program with graphical interface

-More than 100 components

-All types of power plants

-Thermal power systems and networks

PEACE

Load

File:

GT PRO

STEAM PRO

GT MASTER

Elink

DRS

TOPS

User def. Component-External *.exe file

or EXCEL workbook

-Your developments

-Own database

Link

File:

GT PRO

GT MASTER

STEAM MASTER


- HRSG Design in TFX. TD and ED

- HRSG Assembly Definition and Requisites

- HRSG Assembly Outputs

- Managing the HRSG Assembly

- HRSG Assembly in OD Mode

- HRSG Assembly in files imported from GTP-GTM

2. HRSG Assembly


2. HRSG Assembly: Definition and Requisites


2. HRSG Assembly: Definition and Requisites


0 15000 30000 45000 60000 750000

150

300

450

600

750

HRSGAssembly[1]Heat Transfer [kW]

Tem

peratu

re [

C]

HRSGAssembly[1] TQ Diagram

E[4]LTE4028

E[5]LPE9680

B[7]IPB

3034

E[13]HPE13647

S[6]IPS261

E[15]HPE24239

B[17]HPB

28912

S[14]HPS17543

S[18]HPS25190

THERMOFLEX Version 26.1 Revision: June 2, 2017 Unregistered User Ignacio Martin Gonzalez

1305 06-12-2017 15:44:18 file= C:\Users\imart\Documents\Thermoflow 26\IMG\FAW1_Assemblies\IMG_CC2P_ED_HRSG Ass.tfx

FOR QUALITATIVE INDICATION ONLY

A A

B B

C C

D D

E E

F F

1

1

2

2

3

3

4

4

5

5

6

6

7

7

8

8

Thermoflow, Inc.

Date: 06/12/17

Company : Ignacio Martin Gonzalez

User: Unregistered User

HRSGAssembly [1]Drawing No:

HEAT RECOVERY STEAM GENERATOR

PLAN VIEW

A C D E

F

A B C D E F G H I J

TOTAL BOILER LENGTH = 21,7 m

4,95 m - 6,93 m 6,108 m 2,172 m 3,686 m 3,124 m - - -

G




A A

B B

C C

D D

E E

F F

1

1

2

2

3

3

4

4

5

5

6

6

7

7

8

8

Thermoflow, Inc.

Date: 06/12/17



HRSGAssembly [1]Drawing No:

HEAT RECOVERY STEAM GENERATOR

ELEVATION VIEW

A C D E

F

G

H

A B C D E F G H I J

TOTAL BOILER LENGTH = 21,7 m

4,95 m - 6,93 m 6,108 m 2,172 m 17,18 m 11,82 m 2,64 m - -



2. HRSG Assembly: Outputs


2. HRSG Assembly: Outputs


2. HRSG Assembly: OutputsHRSGAssembly[1]

Estimated HRSG Data

1. HRSG System Summary

Size

Overall Length (horizontal) 21,72 m

Overall Width 3,686 m

Overall Height (HRSG) 11,82 m

Overall Height (Main stack height) 17,18 m

Weight

Overall Weight (dry) 220.400 kg

Round to Square 7.400 kg

Transition Duct 25.150 kg

Main HRSG Section 187.850 kg

Overall Weight (wet) 234.650 kg

Heat Transfer Surface Area

Overall surface area 20309 m^2

Economiser 11542 m^2

Evaporator 7051 m^2

Superheater 1716 m^2

Miscellaneous

Total number of tubes 1948

Equipment

Overall HRSG Unit Cost - including: 5.352.000 €

Main Stack 257.450 €

Mechanical

Mechanical Labor 12.280 hours

Mechanical Labor Cost 453.150 €

Transportation & Rigging

On-site Transportation & Rigging 239.000 €

Civil

Foundation Concrete Volume 272 m^3

Civil Labor 5.200 hours

Civil Labor Cost 168.600 €

Total Civil Cost 365.400 €

Total Cost

Total Reference Installed Cost 6.410.000 €

Total Installed Cost Adjustment Factor 1

Total Adjusted Reference Installed Cost 6.410.000 €

Total Estimated Installed Cost 6.855.000 €

2. GT-to-Ductwork Transition

Length 4,95 m

Height 2,64 m

HRSGAssembly[1]

Overall HRSG Thermodynamic Data

1. HRSG Summary

HRSG efficiency 81,58 %

Heat recovered 66040 kW

Heat loss 495,3 kW

Heat available in exhaust gas (cooled to ambient) 80954 kW

HRSG gas inlet temperature 610,9 C

Stack gas exit temperature 120,1 C

HRSG gas inlet mass flow 443 t/h

Stack gas exit mass flow 443 t/h

HRSG gas inlet pressure 1,035 bar

Stack gas exit pressure 1,011 bar

Ambient pressure 1,013 bar

HRSG total gas-side pressure drop to top of stack 24,52 millibar

HRSG total gas-side pressure drop to ambient 21,96 millibar

2. Water/Steam Paths

Path 1

Total heat transfer 49162 kW

Steam/water exit

Pressure 80,72 bar

Temperature 500 C

Mass flow 70,81 t/h

Steam/water inlet

Pressure 81,97 bar

Temperature 210,8 C

Mass flow 71,52 t/h

Path 2


Steam/water exit

Pressure 20,57 bar

Temperature 275 C

Mass flow 5,686 t/h

Steam/water inlet

Pressure 20,86 bar

Temperature 105,7 C

Mass flow 77,26 t/h

Path 3


Steam/water exit

Pressure 1,209 bar

Temperature 90 C

Mass flow 77,26 t/h

Steam/water inlet

Pressure 1,344 bar

Temperature 45,53 C

Mass flow 77,26 t/h


2. HRSG Assembly: Managing


2. HRSG Assembly: Managing


- Boiler Design in TFX. TD and ED

- Boiler Assembly Definition and Requisites

- Boiler Assembly Outputs

- Managing the Boiler Assembly

- Boiler Assembly in OD Mode

- Boiler Assembly in files imported from STP

3. Boiler Assembly


3. Boiler Assembly Definition


3. Boiler Assembly Definition



3. Boiler Assembly Arrangement


3. Boiler Assembly


3. Boiler Assembly


3. Boiler Assembly, Outputs



B

A B C D E F G H I J

- 14,79 m - - - - - - - -


A A

B B

C C

D D

E E

F F

1

1

2

2

3

3

4

4

5

5

6

6

7

7

8

8

Thermoflow, Inc.

Date: 06/13/17

Company: Ignacio Martin Gonzalez


Boiler Assembly[1]Drawing No:

Boiler Assembly[1]

Plan View


1305 06-13-2017 14:14:12 file= C:\Users\imart\Documents\Thermoflow 26\IMG\a_FAW1_Assemblies\Boiler\STPRO_No Ass_ED_Ass.TFX

To pulverizers

AB

C

D

E

F

J


A A

B B

C C

D D

E E

F F

1

1

2

2

3

3

4

4

5

5

6

6

7

7

8

8

Thermoflow, Inc.

Date: 06/13/17

Company: Ignacio Martin Gonzalez


Boiler Assembly[1]Drawing No:

Boiler Assembly[1]

Elevation View

A B C D E F G H I J

51,46 m 14,79 m 7,393 m 8,872 m 66,3 m 76,66 m - - - 12,53 m



0 200000 400000 600000 800000 10000000

500

1000

1500

2000

2500

Boiler Assembly[1] Heat Transfer [kW]

Tem

per

atu

re [

C]

Boiler Assembly - Boiler Assembly[1] T-Q Diagram

AH(11)87394

E(7)85013

S(6)60272

S(5)60243

S(4)60269

S(3)84050

FRN(1)405612





- ST Design in TFX

- ST Assembly Definition and Requisites

- ST Assembly Outputs

- Differences ST Assembly / No Assembly

- Managing the ST Assembly

- Leakage Flows to a TFX Source

- ST Assembly in OD Mode

- ST Assembly in files imported from GTP-GTM-STP

4. Steam Turbine Assembly




4. Steam Turbine Assembly Definition





No Assembly

Assembly

4. Steam Turbine Assembly Outputs


STAssembly[1]

p[bar], T[C], h[kJ/kg], M[t/h]

Valve Stem leak 1 To

LP section inlet

0,1478 M

Valve Stem leak 2 To

SSR

0,0883 M

HPT

HPT HP leak 1 To

LP section inlet

1,798 M

HPT HP leak 2 To

SSR

0,863 M

SSR1,241 p

148,9 T

1,171 m

Leak in 0,9512 M Make-up steam (from HPT inlet) 0 M

Desup water

0,2197 M

Excess steam to LPT exhaust

0,8761 M

LPT SS to LPT exhaust

0,1814 M

LPT SS packing exhaust discharged

0,1134 M


1305 06-13-2017 08:42:05 file= C:\Users\imart\Documents\Thermoflow 26\IMG\FAW1_Assemblies\ST\IMG_CC2P_ED_ST Ass.tfx

5,5 6,0 6,5 7,0 7,5 8,02000

2200

2400

2600

2800

3000

3200

3400

3600

Entropy [kJ/kg-C]

En

tha

lpy

[k

J/k

g]

STAssembly[1]: Steam Turbine Expansion Path

0,95

0,9

0,85

Wilson 0,97

200 C

300 C

400 C

500 C

80 bar

20 bar

0,1 bar




A A

B B

C C

D D

E E

F F

1

1

2

2

3

3

4

4

5

5

6

6

7

7

8

8

Thermoflow, Inc.

Date: 06/13/17



STAssembly [1]Drawing No:

STEAM TURBINE PACKAGE

ELEV

MS

I

A

D

B

C

E

A B C D E F G H I J

SHAPE, DIMENSIONS & SCALE ARE APPROXIMATE

4,9 m 6,916 m 13,41 m 2,36 m 2,061 m - - - - -




A A

B B

C C

D D

E E

F F

1

1

2

2

3

3

4

4

5

5

6

6

7

7

8

8

Thermoflow, Inc.

Date: 06/13/17



STAssembly [1]Drawing No:

STEAM TURBINE PACKAGE

PLAN

A B

C

F D E

A B C D E F G H I J

SHAPE, DIMENSIONS & SCALE ARE APPROXIMATE

4,9 m 6,916 m 13,41 m 3,322 m 2,723 m 3,987 m - - - -




4. Steam Turbine Assembly Outputs

4. ST Assembly, Efficiency Definition



4. ST Assembly: Leakage to TFX Source



4. ST Assembly: Exhaust End


4. ST Assembly: Miscellaneous

4. Steam Turbine Assembly at Off Design


- PEACE Cost Estimation Difference:App. SP.: Total Plant CostTFX-PCE: Sum of cost of Equipment (included Ass.)

- Plant Assembly Definition (GT Plants)Main Components, configurationMiscellaneousEconomic Assumptions

- Plant Assembly Outputs

- Plant Assembly in files imported from GTP-GTM

5. Plant Assembly


5. Plant Assembly: Definition and Inputs



5. Plant Assembly: Definition and Inputs

5. Plant Assembly, Non-Flowsheet Equipment


5. Plant Assembly, Economics


5. Plant Assembly, Regional Costs


5. Plant Assembly: Outputs






