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CSP Technology Selection
Kuno Schallenberg
Kuno.Schallenberg@de.lahmeyer.com
+49 6101 55 1886
26 August 2013
Lahmeyer International GmbH
Engineering and Consulting Services
Energy Division; Business Unit Renewables and Economics
Lahmeyer
LahmeyerInternational
International2013
2013
Company Data
Lahmeyer Group:
Foundation:
Headquarter:
Employees (2012):
Turnover (2012):
Sites:
Projects:
Activity:
Fields (Group):
12 Affiliated Consolidated Companies
1966
Bad Vilbel, Germany
1560 (Group)
157 million Euro (Group)
Company Sites and Subsidiaries in 21 Countries
In 165 Countries
Technical and economic planning and consulting services
Energy
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Hydropower
& Water
Resources
Water
Supply &
Sanitation
Building &
Transportation
2
Key Data Business Unit Renewables and Economics (BU2)
Lahmeyer History
in Renewables:
Scope BU2:
Employees (2012):
Turnover (2012):
Projects:
Activity:
working in hydropower business since 50 years, in new and renewable energy
business since 25 years
all non-traditional renewable energies: solar, wind, biomass&waste, geothermal
energy
59
12 million Euro
In more than 90 Countries
Technical and economic planning and consulting services
Solar
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Wind
Biomass &
Waste
Geothermal
Energy
3
Range of Services
Project Management and Quality Assurance
Market Analyses, Energy Economic
Studies
Contract Management
Operation and
Maintenance Management
Planning, Tendering and Purchasing
Feasibility Studies
Detailed Design
Defects Liability Management
Design Review
Due Diligence
Construction and Erection
Supervision
Commissioning
Conceptual Planning
Rehabilitation
Training for Design, Project Management and Operation
Pre-Investment Phase
Option: Contract Award EPC
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Implementation Phase
Betriebsphase
Operation Phase
Start of Operation
4
General Process Diagram CSP Plant
Fuel
Solar Field
Concentrated
Reflector Solar Radiation
Absorber
Thermal
Energy
Storage
Thermal
Energy
Auxiliary
Input
Emissions
Thermodynamic
Process
Kinetic
Energy
Generator
Fuel Inputs
Power Block
Thermal Energy Storage
Solar Field Technologies
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Parabolic
Trough (PT)
Tower (T)
Fresnel (F)
Dish (D)
5
Possibilities for CSP Integration in Conventional Plants
Selective Catalytic
Reduction
Economizer
Secondary
Air
Steam Gen.
Desulphurisation
Superheater
HPT
LPT
G
Reheater
Feedwater
Heater
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Deaerator
Feedwater
Heater
6
Annual solar to electric efficiency vs. Technical maturity
Annual Solar to Electric
Efficiency [%]
30
Air Combined Cycle
25
20
Helium
Supercritical
15
Superheated Steam
Molten Salt
Brayton Cycle
Superheated Steam
Molten Salt
Air Rankine Cycle
Oil
Saturated
Steam
10
Superheated Steam
Saturated Steam
Demonstration
Industrial
5
0
Concept
Laboratory
Field R&D
Maturity
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7
Site Sensitive Conditions
Parabolic Trough
(PT)
Tower (T)
Fresnel (F)
Dish (D)
Site Shape/Slope
-
+
+
+
Wind Speed
-
-
+
-
Modularity
-
-
+
+
Water Consumption
-
-
-
+
Financing
+
+/-
-
-
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8
High Risk Components/Characteristics
Parabolic Trough (PT)
•
•
•
End hoses and
ball joints
Steam generator
Limited cost
reduction
possibilities
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Tower (T)
•
•
Receiver
functionality and
longevity
Heliostat Control
System
Fresnel (F)
•
•
Limited storage
options
Steam control
during transient
conditions
Dish (D)
•
•
•
Leakage of
working fluid
from Sterling
Engine
Optics
Limited and
unproven storage
options
9
Potential Risk Categories (Examples)
• Solar Collectors/Field
• Solar Absorbers/Receiver/Engine
• Steam Generator
• Steam Turbine and Generator
• Thermal Energy Storage
• Plant Control Systems
• Performance Simulation/Model
• Construction
• Geotechnical
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10
Technology Risks (Examples)
Risk
Causes
Mitigation
Reduced availability
•
multiple technical failures
•
performance guarantees
Component failures
•
•
adverse environmental
conditions
poor maintenance
•
•
•
•
•
•
accredited suppliers
sufficient warranties on key components
regular maintenance
process monitoring
spare part management
supplier audits
Interruptions
•
component breakdown
•
business interruption insurance
Weak O&M quality
•
inexperienced contractors
•
verify availability and experience of O&M
contractor
assign experienced contractors
conclude guarantees
care for acceptance
trial runs
insure operational risks
•
•
•
•
•
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11
LCOE Estimations
• Parabolic Trough – 200-330 USD/MWh
• Tower – 160-270 USD/MWh
Source (Trough)
IEA 2010a
Fichtner 2010
India
Morocco
Kutscher 2010
Hinkley 2011
AT Kearney 2010
(Tower)
Fichtner 2010
India
Morocco
Kolb 2010
Hinkley 2011
AT Kearney 2010
2011 [USD/MWh]
Low
High
200
295
220
240
330
360
220
230
220
210
230
320
185
270
220
160
210
230
202
280
220
170
320
1: dr = Discount Rate
Source: IEA-ETSAP and IRENA Technology Brief E10 – January 2013
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2020 [USD/MWh]
Low
High
100
140
100
130
130
80
160
130
110
Notes
10% dr1
S. Africa, 8% dr
wet/dry cooling
wet/dry cooling
United States
Australia, 7% dr
160
60
S. Africa, 8% dr
wet/dry cooling
wet/dry cooling
United States
Australia, 7% dr
160
12
Cost Uncertainty Level
Source: World Bank, ESMAP, Cost Drivers Overview, 2010
Parabolic Trough (PT)
Tower (T)
Fresnel (F)
Dish (D)
15%
20%
>30%
>30%
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13
Cost Comparison
• Cost is a sensitive issue, and an important one
• Influencing factors on cost of CSP plants
– Competitive situation of component suppliers (e.g. oligopoly)
– Competitive situation of markets (e.g. generous Spanish CSP-tariffs)
– Risk evaluation (e.g. new technologies, countries, companies’ infrastructure)
– Irradiation influences energy yield and hence LEC
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14
Bankability
HIGH
Parabolic Trough
Solar Tower
Perceived Risk
Linear Fresnel
Dish Sterling
LOW
LOW
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Bankability
HIGH
15
Market Status of CSP Technologies
Source: CSP Today
3,000
Capacity [MW]
2,500
2,000
Parabolic Trough
1,500
Tower
Fresnel
1,000
Dish
500
0
Operation
Construction
Development
Planning
Project Phase
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Thank you for your Attention
Questions?
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2013
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