Indian Port Sector By Hans Ole Madsen – CEO, South Asia for A.P. Moller-Maersk
Ole Hedegaard Madsen - International Solid Waste … · Ole Hedegaard Madsen ... The CFD simulation...
Transcript of Ole Hedegaard Madsen - International Solid Waste … · Ole Hedegaard Madsen ... The CFD simulation...
New furnace concept improving the electrical efficiency
Ole Hedegaard Madsen
Director Technology, Sales & Marketing
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .2
Agenda
Introduction
What determine the limits for electrical efficiency?
The basic principle and concept - SteamBOOST™
The measurements and results - Alkali/Chloride release during
waste combustion
The numerical laboratory - CFD
Control the combustion process
What is on the horizon
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .3
Rankine and other steam power processes
TH
TL
1
2 3
4
Steam Process with super heating
QH
QL
Wturbine
P
Co
Wpump
Boiler
t = (Wturbine – Wpump) / QH
T
s
p2
p1
1
2
3
4
C = 1 – TL / TH
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .4
The boundaries for electrical efficiency Fuel = Waste
TH
TL
1
2 3
4
QH
QL
Wturbine
P
Co
Wpump
Boiler
t = (Wturbine – Wpump) / QH
High temperature TH:
Corrosion
• Steam temperature SH
• Flue gas temperature
Particle impact
High velocity
Low temperature TL:
Operating conditions condenser
• District heating system
• Air cooled +
• Water cooled ++
C = 1 – TL / TH
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .5
Process
Parameters Unit Guarantee 300-
Hour
Test Waste flow T/h 20 21.72 Heating value lower MJ/kg 12 11.28 Steam production Kg/s 22.42 22.55 Steam temperature ˚C/F 425/797 423/796 Steam pressure bar 50 48.6 Heat input MW 66.66 67.69 Electrical output MW 17.918 18.232 Thermal efficiency % 85.56 87.1 Electrical efficiency % 26.88 26.93 TOC bottom ash % < 2.0 < 0.23 Temperature < SH ˚C/F 620/1148 530/986 Temperature boiler
out ˚C/F 180/356 181/356
Waste Fired Power Plant: Reno Nord, Denmark 2006
Waste Fired Power Plants
High Energy Efficiency
el = 27 %
Th = 97 %
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .6
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .7
Reduce corrosion by:
Ceramic tiles
New materials
• Inconel
Co-flow super
heaters
CFD modeling
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .8
Solid Fuel Combustion on a Grate
The processes in a burning
refuse bed include:
Drying
Ignition
Pyrolysis
Gasification
Solid-phase combustion
Gas-phase combustion
The process is mainly controlled
by mass and heat transfer
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .9
Hypothesis
Cl and other corrosive elements are released during the pyrolysis.
Cl is a precursor for release of other elements with influence on
corrosion fx. Na, K, Pb, og Zn.
Char combustion releases enough energy to super heat the steam.
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .10
Steam
Super heater
+ 50 °C
Basic Principle for SteamBoost™
Improved electrical efficiency by using fraction of the
flue gas for passing through an extra super heater
Controlling flow by Nozzle design:
Create a double
rotating flow
Uniform flue gas
temperature
• Even in the corners
Good burnout in the
gas phase
• No carbon mono-
oxide
VoluMix SYSTEM™
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .11
Rankine and other steam power processes
TH
TL
1
2
3
4
Steam Process with SteamBoost™
QH
QL
Wturbine
P
Co
Wpump
Boiler
t = (Wturbine – Wpump) / (QH + QG)
T
s
p1
1
2
3
4
3’
427˚C ~ 800F
477˚C ~ 890F 3’
Furnace SH
QG
p2
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .12
Test at VF5 - WFPP
750 ton/day
Data acquisition
Gas temperature
O2, CO, and CO2
Na, K, Cl, S, Pb, Zn, and Ca in rawgas
SRO data
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .13
Data collected
Absolute gas temperature measurements with suction
pyrometer (on-line collection of data)
O2, CO, and CO2 measurements (on-line collection of
data)
Na, K, Cl, S, Pb, Zn, and Ca flue gas concentrations
(collected batch sample sent to laboratory for analysis)
Various data from the plant control system (used to
confirm stability of the unit)
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .14
Gas concentrations of O2/CO/CO2
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .15
Absolute gas temperatures at ports L2-L6
Proprietary and Confidential
S release - average Cl release - average
Concentration profiles along grate
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .17
Concentration profiles along grate
Proprietary and Confidential
Numerical Laboratory = CFD modeling CFD Design:
Heat transfer to Super
Heater
Flow pattern
Uniform flue gas
temperature
SA nozzle design
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .19
FASAN WFPP
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .20
CFD – analysis of SteamBoostTM
Furnace volume with corrosive gas
Super heater
Furnace volume with non-corrosive gas
Wall
Fasan line 4:
Steam production = 30 ton/h
Temperature = 405 °C
Pressure = 54 Bar
Retention time > 2 sec.
+ 50 °C Super heater needs to transfer
1 MW.
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .21
Velocity [m/s] vector plot, in a plane with jets,
close to the centre of the furnace
Modify direction
Re-circulation in super heater is avoided by
moving nozzles
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .22
Gas temperature distributions in the furnace
The CFD simulation indicates that it will be possible to extract at least 1 to
1 MW in the final super heater SteamBoost™ and still meet the demand
for sufficient residence time.
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .23
Shorter passage through furnace causes unburned
particles in outlet from furnace
Small leakage between the two volumes
CFD – analysis of SteamBoostTM
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .24
CO concentrations in the centre of the
furnace - note that scales are logarithmic
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .25
Control and adjustment of the position of the main combustion zone:
Ensure correct spilt of flue gases – “corrosive/clean”
Optimize energy flux to the final
super heater
Meet variations in the waste heating value and composition
• Hn, MSW fuel composition
Control speed or primary air
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .26
WaVeGRATE™
The Dynamic Movement of
Combustion
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .27
Summery
Increased steam data by final super heater in the furnace – new patent
technology - SteamBoost™
Release profile indicates volatile corrosive species to be released early
on the grate – verified by full scale experiments
A high heat flue gas flow is present with low content of corrosive species
• CFD Study indicate that the temperature increase > 50°C
A new flame front control system is develop to optimize the process
The next steps in the research program
• Development of new furnace concept including SA system
• Final development of automatic flame front control
• Full scale test
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .28
The Technology – R&D Targets
Ensure B&W Vølund’s position as a
Leading technology supplier in our business
The best research & development
• Power efficiency
• Fuel flexibility
Most advanced design tools
• CFD
• Thermoflex
• 3D - PDMS
The Waste Fired Power plant FASAN, Denmark, 2006
Proprietary and Confidential © 2008 Babcock & Wilcox Vølund A/S. All rights reserved. .29