conjugate heat transfer simulations of a bypass valve for...
TRANSCRIPT
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Conjugate Heat Transfer Simulations of a Bypass Valve for the Next Generation of Highest-efficient
Power Plants
STAR GLOBAL CONFERENCE 2012
21 March 2012
Amsterdam, The Netherlands
Anis Haj Ayed, Martin Kemper, Karsten Kusterer
B&B-AGEMA GmbH, Aachen, Germany
Olaf Tebbenhoff
Welland & Tuxhorn AG, Bielefeld, Germany
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B&B−AGEMA GmbH is an independent engineering
service company providing consultancy, expertise,
design and calculation for turbo machinery and power
plants. Established in 1995 and located in Aachen
(Germany), B&B-AGEMA GmbH operates worldwide
and independently for the benefits of its customers.
Contact:
B&B-AGEMA GmbH Juelicher Strasse 338 52070 Aachen, Germany Phone: +49 (0) 241 – 56878 – 0 Fax: +49 (0) 241 – 56878 – 79 E-mail: [email protected] Web: www.bub-agema.de
B&B-AGEMA GmbH
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Contents
Background
Motivation & Task
Calculation Approach
Geometrical Model & Boundary Conditions
Results
Conclusion
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Contents
Background
Motivation & Task
Calculation Approach
Geometrical Model & Boundary Conditions
Results
Conclusion
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• Power generation for Renewables will increase significantly in the next two decades (from 600 TWh to 5200 TWh.
• In the same time the world wide total power generation will also increase significantly. • Despite the increase in renewables the power generation from coal will further increase in
absolute values. • Reduction of CO2 can only be reached if new technologies as CCS and highest efficient
technologies are applied for the steam power plants operated with coal.
Background – Future Power Generation
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Plant Efficiency [%]
Average World Average
Germany State-of-
the-art 700°C steam techn.
Spec
ific
CO
2 em
issi
ons
[g/k
Wh]
• Increased plant efficiency can contribute significantly to the CO2 reduction. • The difference in specific CO2 emissions between the World average and the investigated
700°C technology is 42%. • The theoretical potential of the specific CO2 reduction is therefore also 42%. • The Carbon Capture and Storage (CCS) technologies are only meaningful for high-efficient
power plants so that the additional efforts for the CCS are reduced.
Contribution of increased plant efficiency for reduction of CO2 emissions
Source: ALSTOM, press release 2008 on the „725°C high temperature – test track at the GKM“
Background – CO2 Reduction
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Steam turbine
Nickel-base alloys
Chromium steel
Plant efficiency
Materials steam generator:
Materials in the future high-efficient steam power plants are exposed to extreme conditions:
• High steam temperatures (>700 °C)
• Damage due to enhanced chemical
reactions
• High pressure loads (e. g. >320 bar internal pressure)
• High thermal gradients during start-up and shut-down (Thermal low cycle fatigue).
• There are only few experiences and limited knowledge in operation and design calculations for such component application (e. g. steam generator, valves, etc.) with Ni-base alloys in power plants.
Source: ALSTOM, press release 2008 on the „725°C high temperature – test track at the GKM“
Background – Material Requirements
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Contents
Background
Motivation & Task
Calculation Approach
Geometrical Model & Boundary Conditions
Results
Conclusion
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Vision: „700°C power plant“ with increased efficiency to realize the coal fired Zero Emission Plant
Idea: Erection of a test rig for innovative boiler materials in a fossil fired power plant with an adequate load profile
Participants: Utility, boiler manufacturer, manufacturer of power plant components, inspection authority, scientific research and testing institutes
Duration: 2008 – 2015 Funding: Total project costs 5.4 million EUR, 50% sponsored by German
Government, 50% industry contribution Work packages: Several work packages on planning and construction, material
technology investigations, test rig operation (e. g. cyclic bypass valve operation), concepts for damage development, etc...
*GKM: Grosskraftwerk Mannheim (Utility company for Mannheim area) (Source: VGB Workshop „Material and Quality Assurance“, May 13-15, 2009, Copenhagen, K. Metzger, Grosskraftwerk Mannheim AG)
Research Project
Research Project 725 HWT GKM: 725 °C high temperature – test track at the GKM*
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725°C Test Track at the GKM
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Research topics for the Welland&Tuxhorn bypass valve
- Valve functions check: combined stop&control with hydraulic drive - Mechanical integrity: materials and coatings at 725°C - Measurement data: pressures (in/out), temperatures, leackages - Transient thermal behaviour: automatic infrared camera measurements - Numerical analyses: Simulation of thermal transient cycles (FEM/CFD)
Welland&Tuxhorn bypass valve made of
Ni-base Alloy 617mod Infrared camera with housing
camera view angle
Numerical tasks: (B&B-AGEMA): • Transient thermal behavior (transient conjugate
heat transfer calculation of steam valve flow during open/close-cycle)
• Transient stress & strain (FEM) • Life cycle analysis
Source: Welland & Tuxhorn AG,, press release 2008 on the „725°C high temperature – test track at the GKM
Measurements & thermography analysis: (IKDG, Aachen): • Contribution of measurement data for the
validation of the numerical results
By-pass Valve Research Topics
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The Task:
Numerical simulation of cyclic thermal loading of by-pass valve
based on the conjugate heat transfer and flow simulation approach.
Current Task
The Goal:
Accurate estimation of cyclic thermal loading behaviour, which is
the basis for cyclic thermal stress calculation and service life
estimation for modern applications.
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Contents
Background
Motivation & Task
Calculation Approach
Geometrical Model & Boundary Conditions
Results
Conclusion
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Conventional procedure: Transient „Conjugate Calculation“:
Calculation Approach
Transient calculation of the temperature distribution in valve body by FEM by requirement of heat transfer coefficients
Heat transfer coefficients based on experience or on correlations with limited validity
Heat transfer coefficients given for relatively large areas not locally!
Conjugate heat transfer and flow simulation: Heat transfer is calculated directly and locally by taking into account the fluid-solid interaction explicitly
Heat transfer boundary conditions (e.g. heat transfer coefficients) are no longer needed at solid/fluid contact faces
Such transient FEM calculations are possible on modern computers with relatively low effort (Calculation time: Minutes to hours).
Significant uncertainties related to the transient thermal behavior of the valve body
Large uncertainties in the determination of thermal stresses and strains and thus inaccurate life cycles prediction
The time-dependent, three-dimensional temperature field in the solid body is a direct result of the „Conjugate Calculation“
Large calculation effort for transient calculations
Not always applicable for transient flow phenomena e.g. transient mass flow changes due to different time scales within fluid and solid simulation
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Calculation Procedure
1 • steady state conjugate calculation of closed valve condition to
get the initial temperature distribution in the solid domain
2 • steady state conjugate calculation of open valve condition with
start steam parameters to get the initial flow field in the fluid domain
3 • combine initial conditions of solid domain and fluid domain by
exchanging the region solution
4 • transient conjugate calculation of start-up process till steady
operation
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Contents
Background
Motivation & Task
Calculation Approach
Geometrical Model & Boundary Conditions
Results
Conclusion
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By-pass Valve Geometry
steam inlet
steam outlet
valve body
CAD Model polyhedral mesh
as installed
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approx. 400.000 polyhedral cells
steam outlet
steam inlet
Conjugate Calculation Model
fluid domain
solid domain
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Contents
Background
Motivation & Task
Calculation Approach
Geometrical Model & Boundary Conditions
Results
Conclusion
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steam inlet temperature
480°C
steam outlet boundary
Start Solution in Solid Domain
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valve body
steam temperature 480°C
porous region
Initial Temperature in Solid Domain
valve closed
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T 1
T 2 T 3
T 4
Validation of Initial Solution
Start Solution
Position [ - ] Measured
Values Calculated
Values
T1 [ °C ] 247 246 T2 [ °C ] 164 163 T3 [ °C ] 159 160 T4 [ °C ] 159 158
TInlet [ °C ] 480.00 480.00
measurement positions
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steam inlet temperature:
480°C
Steam outlet boundary
start solution solid domain start solution fluid domain
Initial Solution in Fluid Domain & Mapping
valve open
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Transient Calculation – Inlet Conditions
mass flow trend simplified to constant in calculation (due to large time steps)
time dependent temperature defined at inlet boundary
Inlet conditions
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Transient Thermal Load at T1
T 1
T 2 T 3
T 4
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Transient Thermal Load at T2
T 1
T 2 T 3
T 4
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Transient Thermal Load at T3
T 1
T 2 T 3
T 4
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Transient Thermal Load at T4
T 1
T 2 T 3
T 4
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steam inlet temperature:
700°C
Steam outlet boundary
porous region
valve body
Stationary Operation – Steam Flow Field
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Steam inlet: 700°C
steam outlet boundary
Stationary Operation – Solid temperatures
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valve body
steam outlet boundary
steam inlet temperature 700°C
Stationary Operation – Solid Temperatures
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Validation of Stationary Operation Solution
T 1
T 2 T 3
T 4 Stationary operation
Position [ - ] Measured
Values Calculated
Values
T1 [ °C ] 682 678 T2 [ °C ] 637 629 T3 [ °C ] 518 510 T4 [ °C ] 633 625
TInlet [ °C ] 700 700
measurement positions
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Contents
Background
Motivation & Task
Calculation Approach
Geometrical Model & Boundary Conditions
Results
Conclusion
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A new calculation approach has been applied to calculate transient temperature distribution in a valve body.
Results of steady state conjugate calculation at start condition (closed valve) show good agreement with measurement values (temperature measurement on different reference positions on valve body).
Results of transient conjugate calculation of start-up process could be compared with time dependent temperature measurements at reference positions and show qualitatively good agreement.
Design process of high temperature valves in modern power plants is improved by applying the advanced conjugate calculation approach within STAR-CCM+.
Summary & Conclusion