cogeneration with orc at elbe-stahlwerke feralpi eaf shop 2014_turboden_def.pdf · • riesa steel...
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Cogeneration with ORC at Elbe-Stahlwerke Feralpi EAF Shop
Bause T. Pelz T. Monti N.
Campana F. Filippini L. Foresti A.
2
Elbe Stahlwerke Feralpi Riesa, Germany
Founded in 1968, Feralpi group produces 5 Mtons of steel per year and employs 1,300 people in
Italy, Germany, Czech Republic, Hungary and Romania
• Long tradition of steel production in Riesa (since 1843)
• Riesa steel plant acquired by Feralpi Group in 1991
• EMAS (Eco Management and Audit Scheme) certification since 2012
ESF Elbe-Stahlwerke Feralpi GmbH produces reinforcing steel in the form of bars and coils
Steel shop for steel billets as semi-finished product (up to 1 million tons of steel billets)
Hot rolling mill (up to 0.8 million tons of reinforcing steel per year)
Elbe-Stahlwerke Feralpi, Germany: Product and Technology
Heat recovery to power means:
4
Why heat recovery system for electricity production ?
In Europe the price of energy is very high
and CO2 reduction targets have been set by the EU
Electricity costs are a significant part of the
mini mills final product costs1
Improve energy efficiency of the industrial plant
Lower specific cost of final product
Zero CO2 emissions electricity production
Environmental friendly image for the company
(1) 6 - 8 % according World Steel Dynamic data
5
Energy flow of typical EAF today
Typical energy balance for top charged scrap based EAF (Tenova)
Electricity
Fossil fuels
Metal oxidation**
Liquid steel and slag
Off gas and dust
Water cooling
Electrical losses
Other losses
361
(50%) 221
(30%) 144
(20%)
726 (100%)
455
(62%)
197
(27%)
49
(7%)
13
(2%)
12
(2%)
EAF off gas typically represents more than 25% of the total energy input
6
Heat recovery system: objective
Lower energy cost through an heat recovery system with no additional personnel
Heat to power system
Thermal user
Industrial heat recovery source
Power
Cooling system
Heat carrier loop Saturated steam
7
Task 1: Heat to power system choice
Steam Turbine
Tem
per
atu
re
Entropy
Tem
per
atu
re
Entropy
Organic Rankine Cycle (ORC)
• High enthalpy drop
• Superheating needed
• Risk of blade erosion
• Small enthalpy drop
• No need to superheat
• No risk of blade erosion
Thermodynamic
features
• Water treatment required
• High skilled personnel
• High pressures and temperatures
• Non oxidizing working fluid
• Minimum personnel
• Completely automatic
Operation and
maintenance costs
• Convenient for plants > 10 MWe
• Low flexibility
• Lower performances at partial load
• High flexibility and good
performances at partial load
• Well proven in industrial heat
recovery
Other features
8
Task 2: heat carrier choice
Thermal oil Hot water Saturated Steam
High ORC efficiency (up to 24 % due to high temperature , 600 °F)
Reliability (wide spread solution in ORC based heat
recovery systems)
Flammable
Steelshop operators usually not familiar with thermal oil
Simple technical solution (low temperature, no change of phase)
Many application in ORC (waste to energy, geothermal plants, etc.)
Lower ORC efficiency (e.g. 16% with 350 °F hot water)
Medium ORC efficiency (~20 % with 380 psig steam)
Complex system (e.g. water quality control)
Steam engineer necessary
Good experience of EAF steam heat recovery system at GMH steel shop (Tenova-Germany)
EAF
Heat Exchanger
Thermal user ORC
Drivers for ESF choice:
Need of saturated steam for nearby Goodyear Dunlop Tires plant
9
Turboden ORC references worldwide
Application Size Plant in Operation Heat carrier
MW no. MW
Wood Biomass 0.3 - 6.5 201 214 • Thermal oil
Geothermal 1.0 - 6.0 6 19 • Hot water
Combined cycle
(bottoming of gas turbines or
reciprocating engines)
0.5 - 4.5 12 13 • Thermal oil (10)
• Direct heat exchange (2)
Industrial Heat Recovery
(Cement, Glass, Steel, etc.) 0.5 - 7.0 7 16
• Thermal oil (4)
• Hot water (1)
• Saturated Steam (1)
• Direct heat exchange (1)
Waste to Energy 0.5 - 6.0 4 10 • Thermal oil (3)
• Hot water (1)
Total Turboden Plants 230 272
Last Update: April 2014
10
Start up:
December 2013
Electric Arc Furnace
(EAF)
Heat exchangers
+ steam drum
Industrial thermal user
~ 30 t/h steam
Exhaust gases
ORC 3 MWe
Electric energy
Reduce consumption
33% 67%
ESF: Waste Heat to Power scheme
Steam and condensate return pipeline
Distance between steel shop and thermal user: 0.8 miles
ESF: Waste Heat to Power layout
0
ORC Unit
Steel Shop
Evaporative Cooling System
0
Thermal user: tire plant
ESF obtained a small contribution from EU to develop a demonstrating plant for an innovative ORC application First heat recovery to power system from EAF
Further development of steam based EAF off
gas technology proven at GMH adding a Waste Heat Boiler (convective section)
First ORC in steel industry fed with saturated steam
ESF: European Union support
CO2 reduction in electric steelmaking
EAF Heat Recovery: EAF Design Data
EAF
Heat Exchanger
Thermal user ORC
Heat source EAF process off-gas
Steel production 1,000,000 metric tons per year
Heats per day (average) 32
EAF hourly production 133 metric tons per hour
Tapping weight 100 tons
Tapping temperature 1600°C (2912°F)
Charge weight 113 tons
Average off-gas temperature (core temperature ex EAF) 1100°C (2012°F)
Average off-gas flow rate 100,000 – 140,000 Nm3/h
14
EAF
Heat Exchanger
Thermal user ORC
EAF Heat Recovery: EAF Melting cycle
Melting Phase Power-On
[min] Power-Off
[min] AVG Power
[MW]
1st scrap bucket charging 2 -
Melting 10 70
2nd scrap bucket charging 3
Melting 10 70
3rd scrap bucket charging 3
Melting & refining 13 70
Tapping & repairing 7 -
Values for the fume treatment and waste heat to power system design:
• Tap-to-tap time: 48 minutes
• Longest Power-Off time: 11 minutes
• Average Power during Power-On: 70 MW
• Total Power-On time: 33 minutes
EAF Heat Recovery: Evaporative Cooling System (1/4)
EAF
Heat Exchangers
Thermal user ORC
Thermal users
Electricity
Water cooling
Electricity + Fossil Fuels
+ Metal Oxidation
Electric Arc
Furnaces
Metal Scrap Melting
Fumes
ORC
Losses
Radiation
Heat
Exchanger
Steam
Steam
accumulator
Fumes
Steam
Fumes
Baghouse
Filter
Steam
Convective
Heat
Exchanger
Stack
Steam
Evaporative Cooling System
Steam Accumulator
Feed Water Tank
Steam Drum
EAF
Heat Exchangers
Thermal user ORC
EAF Heat Recovery: Evaporative Cooling System (2/4)
EAF
Heat Exchangers
Thermal user ORC
Minimum steam data at steam drum 228°C – 27 bar(a) (442°F - 380 psig)
Nominal steam data at steam drum 247°C – 38 bar(a) (477°F – 535 psig)
Maximum design steam data at steam drum 252°C – 42 bar(a) (486°F –590 psig)
Feed water pressure at steam drum inlet 45 bar (640 psig)
Water content cooling system (pipes + tank) approx. 37 m3
Capacity of steam accumulation of cooling system 1442 kg
Steam drum glide upper limit 19 bar (260 psig)
Capacity of steam accumulator (water content) 76 m3
EAF Heat Recovery: Evaporative Cooling System (3/4)
EAF
Heat Exchangers
Thermal user ORC
Waste heat steam generator rendering and installed equipment at ESF plant, Riesa
EAF Heat Recovery: Evaporative Cooling System (4/4)
EAF
Heat Exchangers
Thermal user ORC
Heat recovery system supplier Tenova
(Comeca subcontractor for heat exchanger parts)
ORC supplier Turboden
Hot source Saturated Steam at 27 bar(a) (380 psig)
Inlet thermal power to the ORC 13,517 kW
Steam temperature In to ORC 228÷245°C (442÷473°F)
Condensate temperature Out from ORC 100°C (212°F)
Thermal power to the cooling water 10,640 kW
Cooling water temperatures (in/out ORC) 26°C / 44°C (79°F / 111°F)
Gross electric power output 2,680 kW
Net electric power output 2,560 kW
EAF Heat Recovery: ORC power unit (1/2)
EAF
Heat Exchangers
Thermal user ORC
Turboden unit installed
EAF Heat Recovery: ORC power unit (2/2)
ORC control system
Project timeline
June 2014
Expected end of
commissioning
Dec. 2011:
ORC Order
2011 2012
Feb. 2013:
ORC delivered
at ESF waiting
for EAF annual
maintenance
shutdown
2012:
ORC components
design, manufacturing
and assembly
2013
Aug. 2013:
- convection
heat exchanger
installed
- ORC cold test
Jun. 2013:
ORC cabling and
erection
completion
Nov. 2013:
radiation heat
exchanger
installed
2014
18th Dec. 2013
ORC first parallel
19th Dec. 2013
nominal power
(2.6 MW) achieved
2014:
commissioning
First start up result
100% Nominal power output achieved
225°C
2,671 kW
20 ton/h
410 m3/h
GEN POT Gross electric Power
TT100 = Steam inlet temperature
HWF =Cooling water flow
HCP = Steam flow
Commissioning being completed
Corrective actions under way to obtain uninterrupted operation at
full power recovery
Clean water cooled condenser tubes (oxide fouling)
Eliminate waste heat boiler vibrations at full power
Correct defective heat exchangers
Improve steam control loop
Conclusion
ESF experience confirm validity of EAF off gas treatment with steam
based heat recovery and ORC power unit
Revenue from heat (steam) supply important for economics in Riesa
We open the way for future development in EAF heat recovery with ORC
with a particularly challenging application
electricity
heat
Biomass
Waste-heat
Geothermal
Solar
Turboden designs and manufactures ORC turbogenerators…
Turboden designs and develops turbogenerators based on the Organic Rankine Cycle (ORC). a technology for the combined generation of heat and electrical power from various renewable sources, particularly suitable for distributed generation.
Organic Rankine Cycle turbogenerators
Sizes range: from 200 kW to 15 MW on a single turbine*
* Larger systems can be obtained trough modular design
Video
28
… applicable to renewables energy as well as energy efficiency application
Biomass Turboden ORC units for combined generation allow to produce electrical and thermal power from wooden biomass with high efficiency Typical sizes for such units are generally in the range 200 kW – 10 MW electrical output
Waste heat recovery Turboden ORC units allow to recover waste heat from processes and/or in combined cycles, in order to generate electrical power Typical sizes for such units are generally in the range 200 kW – 10 MW electrical output
Geothermal Turboden ORC and are used for electricity production from low-medium temperature (low enthalpy) geothermal sources, generally in the range 90-180 °C Typical sizes for such units are generally in the range 2 MW – 15 MW electrical output
Concentrated Solar Power An high efficiency thermodynamic cycle is used to generate electricity from thermal power captured by solar collectors Units size is normally above 1 MW
29
Prof. Mario Gaia makes experience in the field of ORC within his research group at Politecnico di Milano
1976 – First prototype of a solar thermodynamic ORC
’60-’70 1980-1999 2000-2009 2009-2013 2014…
1980 – Prof. Mario Gaia founds Turboden to design and manufacture ORC turbogenerators
Turboden develops research projects in solar. geothermal and heat recovery applications
1998 – First ORC biomass plant in Switzerland (300 kW)
Turboden installs ORC biomass plants. especially in Austria. Germany and Italy
Turboden plans to enter new markets. with focus on North America
First heat recovery applications
2009 – Turboden achieves 100 plants sold
United Technologies Corp. (UTC) acquires the majority of Turboden’s quota. PW Power Systems supports Turboden in new markets beyond Europe
UTC exits the power market forming strategic alliance with Mitsubishi Heavy Industries
PW Power Systems becomes an MHI group company
MHI acquires the majority of Turboden. Italian quotaholders stay in charge of management
Today - Over 270 ORC plants in the world, 230 in operation
Turboden has more than 30 years of experience: born in academia and evolved into an
international industrial group
Turboden – a Group Company of MHI
30
Energy Aircraft Ship & Ocean Space
Transportation Material Handling Environment Automotive
Industrial Machinery Infrastructure Living & Leisure Defense
Mitsubishi Heavy Industries is one of the world's leading
heavy machinery manufacturers. with
consolidated sales of over $31.9 billion (in fiscal 2013). MHI's products and services
encompass shipbuilding, power plants, chemical
plants, environmental equipment, steel structures,
industrial and general machinery, aircraft, space
systems and air-conditioning systems.
31
Turboden in 2010
32
Application Size Plant in Operation Under Construction Total
MW no. MW no. MW no. MW
Wood Biomass 0.3 - 6.5 201 214 40 68 241 282 Geothermal 1.0 - 6.0 6 19 2 9 8 28 HR: Reciprocating Engines 0.5 - 4.5 11 12 1 1 12 13
HR: Oil&Gas 1.0 - 3.0 1 1 2 5 3 6 HR: Cement and Refractories 1.0 - 7.0 4 12 0 0 4 12 HR: Metallurgy 0.7 - 2.7 2 3 1 2 3 5
HR: Float Glass 0.5 - 2.0 1 1 0 0 1 1
HR: Waste incineration 0.5 - 6.0 4 10 2 8 6 18
Total Turboden Plan 230 272 48 93 278 365
Country plants Country plants
Germany 82 North America 6
Italy 74 Russia 7
Austria 32 Turkey 3
Rest of Europe 68 Rest of the world 7
Turboden has currently more than 270 reference plants worldwide
A typical heat recovery plant scheme
33
ORC battery limit
Heat-Carrying Loop (1)
Cooling system or cogeneration Electric Power Output
Source of Waste Heat
(reciprocating engine and gas turbine exhaust, cement, steel, glass
production processes, etc.)
External heat exchanger (2)
Note 1) Heat-carrying loop may be filled with verse media e.g. thermal oil, saturated steam, pressurized water or it can be
replaced by a direct exchange between the exhaust and the organic fluid 2) Possibility to exploit multiple thermal sources
34
Turboden Heat Recovery Reference: Steel - Direct exchange
4th Direct exchange ORC unit in operation
Billet reheating furnace at steel rolling mill
Client: NatSteel – Tata Group
Site: Singapore
In operation since February 2013
Heat source: exhaust gas from a rolling mill
Direct exchange between exhaust gas and working fluid
ORC electric power: ~ 0.7 MW
35
Heat recovery system: objective
Lower energy cost through an heat recovery system with no additional personnel
Traditional water-steam Rankine cycle systems are typically employed in industry for plants over 10 MW and extending up to 50 MW and above. Superheated steam cycles are seldom convenient for WHTP plants below 15-20 MW. Feralpi decided to employ to Turboden ORC technology mainly for the following reasons: - Proven high reliable technology in Europe (mostly
in biomass based generation and in geothermal applications)
- Experience in other energy intensive industries (such as cement plant).
- Suitable technology to handle the discontinuous, extremely variable waste heat of the EAF exhaust gases
- Ease of operation and minimum O&M.
Simplified cogeneration ORC based waste heat recovery scheme, as applied in Riesa.
36
Task 2: Heat to power system choice
Cycle it is a thermodynamic cycle
Rankine it is theoretically given by 2 isobar and 2 adiabatic thermodynamic transformations
Organic it exploits an organic working fluid
The principle is based on a turbo-generator working as a normal steam turbine to transform thermal energy into mechanical energy and finally into electric energy through an electric generator. Instead of the water steam, the ORC system vaporizes an organic fluid, characterized by a molecular mass higher than water, which leads to a slower rotation of the turbine and lower pressure and erosion of the metallic parts and blades
Efficiency: 98% of incoming thermal power is transformed, into electric power (around 20%) and heat (78%), with extremely limited thermal leaks, only 2 % due to thermal isolation, radiance and losses in the generator; the electric efficiency obtained in non-cogeneration cases is much higher (more than 24% of the thermal input)
CONDENSER
FEED PUMP
EVAPORATOR
EXPANDER
Water / Steam
Tem
per
atu
re
Entropy
Tem
per
atu
re
Entropy
Organic fluid
Operating Data – Commissioning
Identified problems - The convective heat exchanger is the only one in operation - Fouling problems in the ORC condenser (probably due to a not appropriate cooling water treatment) - Problems on the control system (software or hardware ?)
Power output: 2,058 kW gross (nominal power 2,680 kW gross).
Conclusion
Identified problems - The convective heat exchanger is the only one in operation - Fouling problems in the ORC condenser (probably due to a not appropriate cooling water treatment) - Problems on the control system (software or hardware ?)
Power output: 1972 kW gross achieved on March 27 th (nominal power 2,680 kW gross).