A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶...

30
7. November 2013 Prof. Dr.-Ing. S. Lecheler 1 A Program for first Estimation of Power Output, Costs and Profit of Geothermal Heat and Power Plants Prof. Dr.-Ing. Stefan Lecheler Thermodynamics Mechanical Engineering Bundeswehr University München

Transcript of A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶...

Page 1: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 1

A Program for first Estimation of

Power Output, Costs and Profit of

Geothermal Heat and Power Plants

Prof. Dr.-Ing. Stefan Lecheler

Thermodynamics

Mechanical Engineering

Bundeswehr University München

Page 2: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 2

• Motivation

• Program Overview

– Input Data

– Thermodynamics

– Investment Costs

– Earnings and Amortisation Time

• Sensitivity Studies

• Conclusions and Acknowledgement

Table of Content

Page 3: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 3

• About 100 Geothermal heat and

power projects are planned in

Germany within the next years

• Investors and communities need

a first estimation, if a new project

will be profitable

• A program was developed, which gives a first

estimation of profit with only a few, generally

known input parameters

Motivation

Page 4: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 4

• Definition of simple input parameters

• Calculation of thermodynamic quantities

• Estimation of costs

• Estimation of earnings

• Calculation of amortization time

Program Overview

Page 5: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 5

• Should be easily availabe for new locations

• Only a few values

– Thermal water

o Mass flow

o Inlet and outlet temperatures

– District Heating

o Number of inhabitants of community

o Length of waste water grid of community

o Area and length/width ratio of community

– Power plant

o Some standard values for component efficiencies and cooling

Input Data (1)

Page 6: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 6

Input Data (2) Thermalwasser Massenstrom m_B 150 kg/s

Förderbohrung Temperatur T_B1 150 °C

Geschätzter Betriebsdruck =1,2*ps(T_B1) p_B 5,7 bar

Spez. Enthalpie h_B1 632 kJ/kg

Dichte rho_B1 917,1 kg/m3

Volumenstrom V_B1 164 l/s

Injektionsbohrung Temperatur T_B3 60 °C

Spez. Enthalpie h_B3 252 kJ/kg

Zur Verfügung stehender Wärmestrom Q_B 57.104 kW

Heizwerk Einwohner Kommune EW 20.000 Personen

Anschlußgrad AG 50 %

Gleichzeitigkeitsfaktor GF 50 %

Wärmemenge pro Person und Jahr Q_P 34 MWh/a/Pers

Wärmestrom maximal Q_HWm 76.484 kW

Benötigter Wärmestrom für Nahwärmenetz Q_HW 19.121 kW

länge Abwassernetz berichtigt 62.000 m

Verhältnis Länge/Breite 1,18

Fläche der Gemeinde 24.590.000 m2

Kraftwerk Wärmestrom ins Kraftwerk Q_KW 37.983 kW

Isentroper Wirkungsgrad Pumpe etas_P 80 %

Isentroper Wirkungsgrad Turbine etas_T 80 %

Min. Temperaturdifferenz Wärmezufuhr DTmin_zu 5 °C

Min. Temperaturdifferenz Wärmeabfuhr DTmin_ab 7 °C

Kühlwasser Betriebsdruck p_K 2,0 bar

Temperatur Kühlwassereintritt T_K1 15 °C

Spez. Enthalpie Kühlwassereintritt h_K1 63 kJ/kg

Temperatur Kühlwasseraustritt T_K3 20 °C

Spez. Enthalpie Kühlwasseraustritt h_K3 84 kJ/kg

Reihenschaltung Spez. Enthalpie Thermalwasser Austritt KW h_KW 379 kJ/kg

Temperatur Thermalwasser Austritt KW T_KW 90 °C

Parallelschaltung Massenstrom Thermalwasser KW m_KW 100 kg/s

Massenstrom Thermalwasser HW m_HW 50 kg/s

• Example of

input data

Sorry, but

program

description

and figures

currently only

available

in German

Page 7: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 7

Thermodynamics (1)

• Calculation of heat transfer rates

– Available heat from thermal water

– Needed heat for district heating

– Available heat for power

generation

𝑄 𝐵 = 𝑚 𝐵 ∙ ℎ𝐵1 − ℎ𝐵3

𝑄 𝐻𝑊 = 𝐴𝐺 ∗ 𝐺𝐹 ∗ 𝐸𝑊 ∗ 𝑄 𝑃

𝑄 𝐾𝑊 = 𝑄 𝐵 − 𝑄 𝐻𝑊

Page 8: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 8

• Calculation of power cycles

– Organic Rankine cycle with various organic fluids

– Kalina cycle

Thermodynamics (2)

0

10

20

30

40

50

60

70

80

90

100

110

120

130

140

150

160

1,0 1,2 1,4 1,6 1,8 2,0 2,2 2,4 2,6 2,8 3,0

Tem

pe

ratu

r T

[°C

]

Spez. Entropie s [kJ/kg/K]

T-s-Diagramm ORC-Kreisprozess (N-Butan)

2

1

3

4

6

5

po

pu

Page 9: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 9

• Power cycle with real fluid quantities (h,v,s)

– FluidEXL Graphics libraries are used [1]

– Currently available fluid libraries o N- and Iso-Butan

o Propan

o R134a

o Water and air

o Ammonia-Water mixture

o Water-Lithiumbromid mixture

– Other fluid libraries can be easily implemented

if an Excel add-in is available

Thermodynamics (3)

[1] FluidEXL Graphics, H.-J. Kretzschmar, Hochschule Zittau/Görlitz Germany, http://thermodynamics.hs-zigr.de

Page 10: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 10

• Optimization of power cycle

– Cycle is automatically optimized to given temperature

levels of thermal water and cooling water/air

Thermodynamics (4)

Page 11: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 11

• Two operation modes for coupling of heat and

power station are implemented

– Serial Mode

– Parallel mode

Thermodynamics (5)

Page 12: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 12

• Validation of power cycles

– Done for ORC-Process with

N-Butane and Kalina-

Process KCS34

– Comparison to results from

literature i.e. [2]

– Agreement is very good for

Kalina and ORC at 150°C

(for ORC at 100, 125, 175°C

Köhler used different fluids)

Thermodynamics (6)

[2] Köhler Silke, Geothermisch angetriebene Dampfkraftprozesse, Dissertation am GeoForschungszentrum

Potsdam, 2006

Page 13: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 13

• Motivation

• Program Overview

– Input Data

– Thermodynamics

– Investment Costs

– Earnings and Amortisation Time

• Sensitivity Studies

• Conclusions and Acknowledgement

Table of Content

Page 14: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 14

• Investment costs 𝐶𝐼 are estimated from

thermodynmic quantities 𝑋𝐼 via cost functions [3]

• Coefficients 𝐶𝑂 , 𝑋𝑂 , 𝛼

are evaluated from

literature or existing

projects via curve fits

Investment Costs (1)

[3] Bejan, Tsarsaronis, Moran, Thermal Design & Optimization, Wiley&Sons

𝐶𝐼 = 𝐶𝑂 ∙𝑋𝐼𝑋𝑂

𝛼

Page 15: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

15

Investment Costs Management

Assembly

Commissioning

Drilling

Heat and Power Statuion

District Heating Grid

Piping

Measurement and Control

Additional Costs

Operating Costs

direct

indirect

Electricity

Personell

Maintainance

Earnings from

Sale of Heat

and Power

Heat

Connection

Fees

During construction

Variable

Revenues

Fixed

Revenues

Investment Costs (2)

During operation

Page 16: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 16

• Drilling costs

– Curve fit from existing geothermal projects

– Costs as function of drilling depth

• Inflation rate is taken into account for all costs

Investment Costs (3)

Page 17: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 17

• Components of heat and power station

– Direct Costs for components

o Heat exchangers

o Pumps

o Turbine

o Piping 0.66 ∗ 𝐶𝐶

o Measurement and Control 0.1 ∗ 𝐶𝐶

o Miscellaneous 0.2 ∗ 𝐶𝐶

– Indirect costs

o Management 0.8 ∗ 𝐶𝐷

o Assemly 0.15 ∗ 𝐶𝐷

o Commissioning

Investment Costs (4)

𝐶𝐶

𝐶𝐷

Page 18: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 18

• District heating grid

– Data used from 14 existing district heating grids to

define simple input parameters and cost functions

– Calculation of heating pipe

length from length of waste

water grid

– Calculation of costs from

o Number of connected people

o Shape of the Community

(area, length/width ratio)

Investment Costs (5)

Page 19: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 19

• Motivation

• Program Overview

– Input Data

– Thermodynamics

– Investment Costs

– Earnings and Amortisation Time

• Sensitivity Studies

• Conclusions and Acknowledgement

Table of Content

Page 20: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 20

• From sale of heat

– Typically 2000 to 4000 OH/year

– Typically ~40 €/MWh

• From sale of renewable electricity

– Typically 8000 OH/year

– Currently ~220 €/MWh in Germany due to EEG

Earnings

Page 21: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 21

• Net present value method is used

– 𝐾0 > 0 Profitable

– 𝐾0 ≤ 0 Nonprofitable

Amortisation Time (1)

n

tnnn

qEIK

1

0

1

Income - Expenses Discount Factor

Page 22: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 22

• Example: Profitable (𝐾0> 0) after 16 years

Amortisation Time (2)

-150

-100

-50

0

50

100

0 2 4 6 8 10 12 14 16 18 20 22 24 26 28 30

Kap

italw

ert

[M

io. €

]

Zeit [a]

Page 23: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 23

• Motivation

• Program Overview

– Input Data

– Thermodynamics

– Investment Costs

– Earnings and Amortisation Time

• Sensitivity Studies

• Conclusions and Acknowledgement

Table of Content

Page 24: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

• Amortisation time versus

thermal water temperature

7. November 2013 Prof. Dr.-Ing. S. Lecheler 24

Sensitivity Analysis (1)

10 10 10 12

16

20

30

45

210 195 180 165 150 135 120 105

Thermalwasser-Temperatur [°C]

Amortisationszeit

Page 25: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

• Amortisation time versus

thermal water mass flow

7. November 2013 Prof. Dr.-Ing. S. Lecheler 25

Sensitivity Analysis (2)

11 12

13 14

16

18

20

24

210 195 180 165 150 135 120 105

Thermalwasser-Massenstrom [kg/s]

Amortisationszeit

Page 26: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

• Amortisation time versus interest rate

7. November 2013 Prof. Dr.-Ing. S. Lecheler 26

Sensitivity Analysis (3)

28

22

19

17 16

14 13 13

87654321

Zinssatz [%]

Amortisationszeit

Page 27: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 27

• Motivation

• Program Overview

– Input Data

– Thermodynamics

– Investment Costs

– Earnings and Amortisation Time

• Sensitivity Studies

• Conclusions and Acknowledgement

Table of Content

Page 28: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 28

• Excel programs were developed for easy and

fast estimation of amortisation times for

geothermal projects (ORC, Kalina, heat pumps)

• They can be used for a first estimation at new

locations with only a few available input data

• Data from a few existing projects are used for

cost functions

• More validation data are needed for component

costs of real geothermal projects!

Conclusions

Page 29: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 29

• Thanks to the following students for their support

– Mr. Jens Junkerdorf (Diploma thesis 2007)

– Mr. Jens Reichert (Diploma thesis 2008)

– Mr. Timo Schneider (Diploma thesis 2009)

– Mr. Frank Hitschke 2011 (Student project 2011)

Acknowledgement

Page 30: A Program for first Estimation of Power Output, Costs and ... 008.pdfo Turbine o Piping 0.66∗𝐶 o Measurement and Control 0.1∗𝐶 o Miscellaneous 0.2∗𝐶 –Indirect costs

7. November 2013 Prof. Dr.-Ing. S. Lecheler 30

Contact

Prof. Dr.-Ing. Stefan Lecheler

Technische Thermodynamik (MB5/1)

Fakultät für Maschinenbau

Universität der Bundeswehr München

85577 Neubiberg

Phone.: 089 6004 2357

E-Mail: [email protected]

www.unibw.de/mb/fakultaet/we5/we51