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25 March 2024
Milan Padhi
Pertamina Technology Day
Energy Transition / Hydrogen
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Transition…
… shaping a new energy
system beyond fossil / coal
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Direct use of power is growing in the 2 nd phase of the energy transition power-to-heat, heat pumps, battery powered
electric vehicles
1
Integrated energy system
Source:Achatech, Leopoldina, Akademieunion Increasing coupling of the energy sectors
Continuous technological development and increasing energy efficiency
Basic technologies
development of RE, first expansion
of RE development of efficiency technologies
Systemic integration
flexibilization, digitization, direct power usage, storage system evolution of a new energy market
Systemic combustibles/fuels high negative residual loads,
large scale electrolysis synthetic fuels for transport and industry
Final defossilization
Abolition of fossil energy sources, RE imports, conclusion of energy supply transformation
2
3
4
1990 2010 2030 2050
-25%
up to
-55%
up to
-85%
up to
-100%
Electricity to Fuel
Fuel to Electricity
6 Restricted © Siemens Energy, 2024
Heat integration
Waste heat utilization Heat production
(Heat Pumps)
E n h a n c e d h e a t p r o d u c t i o n a n d
u t i l i z a t i o n
Electrification
Electrical heating
(Inductive & Turbo heating)
Electrification of drives E l e c t r i f i c a t i o n
a l o n g t h e i n d u s t r i a l v a l u e
c h a i n
Low carbon energy
Hybrid heat and power Combined heat &
power H i g h e f f i c i e n t
a n d r e l i a b l e p r o v i s i o n o f h e a t
a n d p o w e r
Power to X
S o l u t i o n s f o r t h e h y d r o g e n i n f r a s t r u c t u r e
Gas compression &
handling Hydrogen production
E-fuel production
Microgrid*
Modernization and upgrades
Energy Storage
(Redox flow / CAES / BESS)
Automation, control systems and digitalization including energy and asset management Services and O&M
Pathways for the Energy Transitions
Process Decarbonization
*Enablers of electrification
Fuels Cells
Carbon Capture
(DAC & Point Source)
U s i n g N e x t G e n s o l u t i o n s f o r
d e e p d e c a r b o n i z a t i o n
CO2Utilization
Key Enablers
D e v e l o p i n g H y b r i d s o l u t i o n s b u i l d i n g f l e x i b i l i t y, r e s i l i e n c e
& d i g i t a l i z a t i o n
Energy System Design (Scenario simulation for various
sectors - mining, refinery, chemicals, etc.)
Grid Stability Analysis
Clean Energy Certification
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“Sector Coupling”
Key lever for decarbonization of all end-user sectors
Shares in global CO
2emissions by sectors The role of hydrogen – a versatile molecule
Transport Buildings
Industry
Power
Leverage green electricity in other sectors
Share on CO2emissions: 58%
Share of Renewables: 11%
Successful integration of renewables in Power
Share on CO2emissions: 42%
Share of Renewables: 27%
Sector Coupling
42%
9%
23%
26%
Source:2022 data from IEA and own estimates
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October 2023
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SES S Solution Development: Power-to-X/ Hybrid categories
Decarbonization solutions for power generation
Energy conversion Category
Electrons
Molecules
Electrons
Energy systems with storage and re-electrification
#1c
Power-to-X
#2
#1a
Molecules Electrons Heat / Molecules
Decarbonization solutions for industrial processes
#1b
Hybrid categories
Power-to-X
Electrons
Electrons
9 Restricted © Siemens Energy, 2024
#1a Decarbonization solutions for power generation Main offtake: electricity
Renewable power
Batteries
Grid connection Optional
Electrons
H₂-ready gas turbine
Optional
Natural gas
Electricity Hydrogen E-Liquids
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#1b Decarbonization solutions for industrial processes Main offtake: electricity, heat, molecules
Renewable power
Batteries
Grid connection Electrolysis
H₂compression
& auxiliaries Heat pump
Heat water
storage Heat
Molecules Electrons
Heat Optional
H₂-Storage
Electricity Hydrogen E-Liquids
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#1c Energy systems with storage and re-electrification Main offtake: electricity
Renewable power
Batteries
Grid connection Electrolysis
H₂compression
& auxiliaries
Electrons Optional
H₂Re-Electrification via
H₂-ready
gas turbine or Fuel cell H₂-Storage
Electricity Hydrogen E-Liquids
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#2 Power-to-X
Main offtake: hydrogen / methanol / ammonia / kerosene / SAF
Renewable power
Batteries
Grid connection Electrolysis
H₂compression
& auxiliaries
Synthesis
processes Molecules
Optional
Methanol Ammonia
SAF Kerosene CO₂-Capture
Molecules
Electricity Hydrogen E-Liquids
13 Restricted © Siemens Energy, 2024 Renewable power
Batteries
Grid connection Electrolysis
H₂compression
& auxiliaries
Synthesis
processes Molecules
H₂-Storage
Electricity Hydrogen E-Liquids Optional
Electrons H₂Re-Electrification
via H₂-ready
gas turbine or Fuel cell
Methanol Ammonia
SAF Kerosene CO₂-Capture
Energy Landscape
Hybrid and Power-to-X categories
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Chemical Processes
Power-to-Fuel pathways
Renewables
(on-grid/off-grid)
Liquid fuel infrastructure Syngas generation
Electrolysis, Carbon capture and Air separation
Air traffic
Road transport Marine
or
or Electrolysis
Hydrogen storage
Carbon Capture
CO2 Carbon
Source Air Separation Unit
N2
Air
H2 Wind Park
PV-Park
Chemical Processes
NH3
Synthesis
Product Refining
MeOH Synthesis
MtO Synthesis
OtJ Synthesis
Product Refining
MtG Synthesis
Gasoline
By-Product Refining
RWGS
Fischer- Tropsch
Product Refining SAF
SAF Ammonia
MeOH
MtO Methanol to Olefins
OtJ Olefins to Jet Fuel
MtG Methanol to Gasoline
RWGS Reverse Water-Gas Shift reaction SAF Sustainable Aviation Fuel
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Hydrogen properties
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Hydrogen Properties
Physical properties
a. Lightest element. Diatomic.
b. Gas at ambient temperature c. Boiling point → - 253
oC d. Melting point → - 259
oC
e. Odorless, colourless and tasteless f. Nontoxic, non-corrosive
g. Low density → 0.08375 kg/m
3h. Expansion ratio of 848
i. High diffusivity
Chemical properties
a. Flammable 4%<x<75%, forms water,
exothermic. Flammable in presence of oxidizer and ignition.
b. Flame is pale blue and almost invisible in daylight
c. HHV 141.86 MJ/kg or 39.39 kWh/kg d. LHV 119.93 MJ/kg or 33.33 kWh/kg e. Wobbe index 40.9 MJ/Nm
3f. Causes embrittlement in many materials
Named in 1783 by Antoine-Laurent Lavoisier
90 percent of all atoms and 75
percent of the mass
of the universe
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Hydrogen FunFacts
57 Important Facts About Hydrogen That You Should Know - The Fact File www.thefactfile.org/hydrogen-facts/
Hydrogen is transparent to visible and infrared light, and to ultraviolet light at certain wavelengths
Hydrogen is approximately 14 times lighter than air. It is the lightest chemical element. It is so light that Earth’s gravity
cannot hold it in the atmosphere and little “free” hydrogen atoms are found on Earth.
Hydrogen has the greatest heat conductivity of all elements.
Kinetic energy is distributed faster through it than any other gas.
The first hydrogen cooled generator was available in 1938.
Hydrogen’s principal industrial application is in the
manufacturing of ammonia for the fertilizer market, fossil fuel
processing in refineries, catalytic hydrogenation of unsaturated
animal and vegetable oils and fats are hydrogenated (to make
margarine and vegetable shortening) and as a primary rocket
fuel as the preferred propellant for space vehicles.
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Hydrogen Heat Content
Higher heating value in kWh/kg
39.39 33.33
Lower heating value in kWh/kg
1.1818 1 mmBTU H 2 =
7.44 Kg of H 2
1mmBTU = 293.071kWh
Higher heating value in kWh/kg comparison
39 Hydrogen 16 16 Methane 14 Propane 11.6 Diesel
Gas mixtures are volumetric (hydrogen mixtures with CH
4is calculated in % volume).
Not sufficiently confused?
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There are different ways to produce hydrogen
Why is a colourless gas is given different colours?
Colours! Overview Production method
Grey/black Hydrogen: Produced from fossil hydrocarbons with CO
2emissions (traditional business)
Steam reforming or Gasification 98% of today’s production at 1.5 – 2.5 $/kg
Blue Hydrogen: Produced from fossil hydrocarbons with CCS
1Steam reforming or Gasification Low-carbon hydrogen. Can be a
transitional technology, as still cheaper than green hydrogen
Turquoise
2Hydrogen: Produced from methane via pyrolysis with pure solid carbon remaining
Pyrolysis Technology not yet mature. Future
solutions for gas production companies
Red
3Hydrogen: Produced from nuclear energy through electrolysis
Electrolysis Partly limited social acceptance. Potential
for existing NPPs, but too expensive in the long term for new builds
Green Hydrogen: Produced from renewable energy through electrolysis
Electrolysis Large RES requirement, higher price
(2 – 6 $/kg, but significant cost reduction potential), water source required
1CCS: Carbon Capture and Storage |2Sometimes also referred as “cyan” hydrogen |3Sometimes also referred as “purple”, “pink” | 4 From PV – “yellow” hydrogen
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Electrolysis
21 Restricted © Siemens Energy, 2024
- +
-
+ What is electrolysis?
• A DC electrical power source is connected to two electrodes which are placed in the water
• An electrolyte allows the charge exchange and is the namesake of the various
technologies
• Hydrogen will appear at the cathode, Oxygen at the anode
• The production rate is proportional to the total electrical charge
Current + 2H2OO2+ 2H2
Electrolysis of water is the separation of water into oxygen
and hydrogen gas with an electric current
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″Water will be the coal of the future. Energy of tomorrow will be water that was split by electricity″*
1888
A method of industrial synthesis of hydrogen and oxygen through electrolysis was developed by Dmitry Lachinov.
1800
William Nicholson and Anthony Carlisle discovered electrolysis, the separation of water into hydrogen and oxygen by direct current and established a new field in chemistry: The electrochemistry.
1http://www.linde-gas.at/internet.lg.lg.aut/de/images/1007_rechnen_sie_mit_wasserstoff_v110550_169419.pdf
* This was a statement by
Jules-Gabriel Verne, 1828 – 1905
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There are three considerable technologies of water electrolysis
Not possible, not available In development/limited
Existing/available
Alkaline Electrolysis PEM Electrolysis High temperature
+ - OH-
KOH electrolyte Anode Cathode
Diaphragm
½ O2 H2
+ - H+ Water
Anode Cathode Gas tight membrane
½ O2 H2
+ -
Water steam Anode Cathode Solid oxides
½ O2 H2 O2-
KOH3 KOH3 60 – 90 ºC
Industrially mature
Polymer membrane Water
RT4– 80 ºC Industrially mature
Ceramic membrane Steam
700 – 900 ºC Lab/demo Electrolyte
Circulated medium Operational temperature1 Technical maturity1 Field experience1 Cold start capability2 Intermittent operation2
Scalability up to multi Giga Watt2 Reverse (fuel cell) mode1
Source: 1Fraunhofer |2IndWede |3KOH: Potassium hydroxide |4Room temperature
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Microbial
electrolysis cell (MEC)
Anion Exchange membrane (AEM) Solid oxide (Ceramic
electrochemical) Proton Exchange
membrane (PEM) Alkaline (Microporous
Separator) Type / Technology
Phosphate species DVB polymer support
with KOH Metal oxide (Y2O3
stabilized ZrO2) PFSA membrane
Na or KOH (Usually Aqueous KOH) Electrolyte / Membrane
Water (Liquid) Water (Liquid)
Water (Steam) Water (Liquid)
Water (Liquid) Reactant
Stainless steel and Ni Nickel & Ni Alloys
Perovskite electrode Platinum /Pt -Pd /
Iridium oxide Ni & Ni-MO alloys /Ni
coated SS Electrode
10-20
>3 0 -20
20-40 Min Load (%)
1
<33 1
<70 1-30
Operating Pressure (bar)
4-30 50-60
800 -1000 60-200
50-80 Operating Temp (°C)
67-90
<74 80-90
70-80 68-77
System Efficiency (%)
NA
~30,000 20,000 – 90,000
50,000 – 90,000 60,000 – 100,000
Stack Life (hrs)
~98 99.99
~99.99 99.9 - 99.9999
99.5 - 99.9999 H2 Purity (%)
NA 57-69
45-55 50-80
50-70 Power Consumption
KWh/Kg of H2
TRL 5 TRL 5
TRL 5-7 TRL 8-9
TRL 9 TRL
Review of existing electrolyzer technologies
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Proton exchange membrane (PEM) electrolysis The efficient way for green hydrogen
How does PEM electrolysis work
• Electrodes are attached on both sides of the proton exchange membrane
• Proton exchange membrane is the electrolyte
• Proton exchange membrane acts as separator to prevent mixing of the gas products
Advantages of PEM electrolysis
• High power density
• Extended dynamic operation range and direct coupling to renewables (rapid response)
• High efficiency
• High gas purities
• Low maintenance needs
1973
J. H. Russell released his works to PEM electrolysis and the high potential.
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Operational performance
Clean by nature
Competitiveness
Focus on Proton Exchange Membrane (PEM) electrolyzer system technology
• Small footprint compared to alkaline systems
• Lower OPEX compared to alkaline systems due to maintenance free stack
• Competitive hydrogen price per kg at green electricity prices below 3 ct/kWh
• Fast start-up and shut-down
• Highest operational flexibility
• Cold start capability
• Highest hydrogen purity >99.9%
• No aggressive chemical electrolyte
• No contaminants – only water, hydrogen and oxygen in the system
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Silyzer 300
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Technology expertise in Electrolysis
Our electrolyzer portfolio scales up by factor 10 every 4 – 5 years
0.1 MW 1 MW 10 MW 100+ MW 1,000+ MW
2011 2015 2018 2023 Next step
Silyzer 100 Lab-scale demo
Silyzer 300 Co-Development with
partners in verticals Silyzer 300 plant
Silyzer 200
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April 2023
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333 kg/h Hydrogen production
>75.5%
Plant efficiency (HHV
1)
17.5 MW Power demand
<1 min, enabled for PFRS
2Start-up time
10%/s in 0 – 100%
Dynamics in range
40% single stack Minimal load
15.0 x 7.5 x 3.7 m Dimension full stack array
35.5 x 15.5 x 9.0 m Dimension system plant
~95%
Plant availability
10 l/kg H
2Demin water consumption
99.9999%
Dry gas quality
3Customized Delivery pressure
Silyzer 300 Fact Sheet
1Plant efficiency includes rectifier, transformer, transformer cooling and gas cooling 2Primary Frequency Response Service |3With DeOxo |4Operating Hours
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Maintenance free stack 80,000 OH
1Easy exchange of stacks
No cleaning effort
Worldwide service coverage
Silyzer 300
Latest and most powerful product line in the double-digit megawatt class
High performance
High efficiency: System >76%
Modular: H
2production range 100 – 2,000 kg/h
Digitally enabled
Data Driven Operation and Service Secure Remote Support
MindSphere
High availability
Advanced design for low degradation Robust industrial design
Flexible operation
Fast start-up and shut-down High dynamics High Gas purity No hazardous chemicals Power factor compensation (optional) No permanent operating personnel required
Maintenance friendly
1Operating Hours
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Impression of our factory
32 Restricted © Siemens Energy, 2024
Silyzer 300 production concept
Stack
Electrolyzer reference plant
• Pre-engineered basic design
• Integrated solution with strong partner approach
• Turn-key possible
Electrolysis System
• Minimize on-site installation
• Maximum of standardization by defined interfaces
• Build to print pre-engineered
Localized decentral packaging
Cost efficient central stack factory
• High level of Automatization
• Large quantities and strong supply chain management
• Strong partner relation of key components
• High quality by pre-assembling
• Transportable units
• Strong local content Group Array
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System
Reference Plants
Scope Joint Venture
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Electrolyzer system – Standardized and pre-engineered plant will be adapted to the customers requirements
Nitrogen Air Power
O2
Water H2 Cooling water Communication
Electrolysis Plant Extended scope Electrolysis System
SILYZER 300 System Grid Connection/
Medium Voltage Switchgear 400/230V Low voltage Distri- bution Cabinet Overall Control System Spare Parts Onsite Package (Optional)
Building Infrastructure
O2Exhaust Pipe/
Blow-Off Lance
Nitrogen Supply (Optional) Cooling System (Optional)
Control air supply
Water Refinement
Demineralization (Optional) Water Treatment
Gas pipeline Chemical proc.
Filling station
Transformer/
Rectifier
System Remote Control System Cabinet
Control & Safety
UPS 220V AC (Optional)
Including
• Heat exchangers
• Gas separators
• Internal piping
• Steel frames
PEM Stack Array
PEM Stack
PEM Stack
Water
Refinement loop
Compressed Air (Optional)
Waste water Tap water Waste water DSL/Internet
XXXX XXXX
XXXX
XXXX
XXXX XXXX
XXXX XXXX
Further Compression H2Exhaust
Pipe/Blow-Off Lance Gas buffer tank Compression DeOxo Dryer
Gas cooler H2
XXXX
XXXX XXXX
XXXX XXXX
Gas cooler O2
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The modular Silyzer 300 concept lowers specific price while upscaling
Modular concept to cover wide production rate
Stack Stack array Customized solution Plant
Scale up to the necessary demand
Transformer Rectifier Control
system
+ -
Water
refinement LV supply
+ -
12 or 24 stacks
n+1
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50MW Optimized plant design for fast installation, low cost & maintenance friendliness
Plant layout 50 x 50 m
• Pre-fabricated and pre-tested stack groups for reduced onsite effort
• Compact footprint
• Standard industrial building
• No indoor crane necessary
• Separate rooms for power electronics
• Future upgrades compatible
50 m
50 m
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Optimized plant design for fast installation, low cost and maintenance friendliness
Plant layout with building (71m X 55m )
• Pre-fabricated and pre-tested stack groups for reduced onsite effort
• Compact footprint
• Standard industrial building
• No indoor crane necessary
• Separate rooms for power electronics
• Future upgrades compatible
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Ready to deliver large-scale electrolysis systems + capacity increase in Germany is locked and loaded
Implementation of modern robots
Fully automated production line
Industry 4.0 Digitalization implemented
Capacity growth plan locked-in and layouts finalized
Additional 1 GW per year depending on demand
2021 Erlangen 2023 Berlin + Erlangen
2025
Berlin
1 GW 3 GW 1GW/
250 MW - 750 MW year
Inhouse design allows for internal and external local packaging
Packaging will be established depending
on the development of the markets
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Industrial scale production of Electrolyzer with up to 1GW in 2023 and 3GW in 2025
Mülheim
Erlangen Berlin
PEM multi-Gigafactory Product development
Electrolyzer Packaging
▪
Joint Venture Manufacturing in Berlin
▪
Industrial scaling up to 1GW in 2023 and 3GW in 2025 (1 GW expansion each 12 month)
▪
Highly automated PEM manufacturing according to latest production standards
▪
R&D for electrolysis technology
▪
Operations, engineering, sales and service
▪
Partially automated PEM production (ending 2023)
▪
Siemens Energy internal and external partners for final assembly to prepare for optionality acc. Market trends
▪
Packager will be established locally in main markets to facilitate local value add Array
Stacks
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Our in-house engineering facilitates optimized plant design, future upgrades and extensions
Next-level in-house engineering
Customer Benefits
• Accelerated project design and execution incl. time-efficient onsite installation
• Digital data exchange between customers and involved project stakeholders
• Cost-optimized customer solution
• Allowing future project upgrades, extensions and modifications
Silyzer 300 array system design with 24 stacks
• Future-proof system design & engineering
• Integrated digital engineering tools
• Pre-fabricated groups, optimized array system design and plant configurations based on modular building-blocks
• Pre-defined interfaces
• Digitally stored system configurations
• Supporting project from project start until end-of-life
Next-level in-house engineering
Pre-fabricated group of 4 stacks
for Silyzer 300 50 MW plant design based on Silyzer 300
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Digital value add through data collection and enhanced processing
Data collection of fleet & manufacturing
Improve
Plan & Predict Monitor
Optimize operations to optimize costs, cash flow and minimize degradation? How can the performance be improved?
When does the system need to be serviced? When does a stack need to be exchanged?
What is the current status of your plant? Enable predictive maintenance and plant optimization
Data collection &
processing
Data of
~300 000 OH* collected
Gigafactory Berlin
(stack manufacturing data) Project sites in operation
(selected number shown) Future project sites (exemplary)
*OH: operating hours
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We distinguish different efficiency levels depending on solution scope
1ISO conditions: 15 °C, 1013 mbar, 0 m, 60% rel. hum.
Transformer heat loss
Rectifier heat loss
Rectifier cooling system
Cooling pump system
Gas
cooler Others Com-
pression Control
cabinet
PEM Stack Array Auxiliaries
H
2atm
60°C
H
2atm
30°C
P
owerH
210°C 35 bar
View for 17.5 MW 24 stacks:
Air cooled ISO conditions1
>76.0%
>76.5%
PEM array heat loss
+ …
-
MV
LV
Silyzer System
>76.0% Plant without
compression
>75.5% Plant with compression
>72%
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Sustainable Energy Systems Unrestricted use © Siemens Energy, 2023
43 1Transformer, Rectifier, Cooling system
Ambient conditions influence performance guarantees and plant design/cost
Auxil iary Pow er Con sumption (kW )
40
15
10 30
100
25
20 35
0 20 60 80 120 140 160
Ambient Temperature (°C)
Cooling
Technology Fin-Fan Cooler dry Fin-Fan Cooler wet Chiller
Approximate power consumption of auxiliaries
1for 17.5 MW, if air cooled
Δ 120 kW ≙ 1% pt plant efficiency loss
Higher ambient temperatures cause
efficiency losses when the plant is air cooled
April 2023
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Infinitely variable plant operation
• Power controlled operation based on real power price with 15 min time frames (see example on right side)
• Dynamics: Maximal ramp rate in array 10% per second
power change possible
• Always fast ramp-up
Future-proof flexible hydrogen production –
Silyzer 300 plant supports renewable sources and offers grid services
Real plant data from an exemplary electrolyzer
Operating Set point
Target power selection
Power consump- tion electrolyzer
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Silyzer 300 electrolyzer: Fast ramp-up time and renewables- proof flexibility
1Power in Stand-by
Rectifier load H2Delivery to Terminal Point H2Ventilation
Time (s) 100 %
<0,2%1
0s 10s 40 s
…
X X+20 s X+30 s20 %
Rectifier start-up
Power
Stand-by Stand-by
Grid service Hydrogen production
H
2System pressurized
Rectifier ramp-down
Norm al start
Start 0 – 100% H
2Dynamics
≥ 10 %/s< 1 min, enabled for grid service Low standby consumption – no warm-up Future proof flexible hydrogen production
Startup behaviour of plant w/o gas management
Ready to initialize
Nitrogen consumption
No continuous consumption Only for maintenanceRestricted © Siemens Energy, 2024 46
Product offering Applications Power demand
Customer Project
Country Year
Container solution 100 kW/200 kW
(peak) Paul Scherrer Institut
Energy System Integration Platform Switzerland
2015
Container solution 300 kW
Air Liquide, Duisburg Argon purification/
Use of H
2for HRS Germany
2015
Container solution 300 kW
Karlsruhe Institute of Technology
Energy Lab 2.0 Germany
2016
We have started our Silyzer portfolio with our lab-scale pilot product Silyzer 100 in all applications
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Our references for industry, mobility and energy applications
Product offering Applications Power demand
Customer Project
Country Year
Pilot Silyzer 200 3.80 MW/6 MW (peak)
Municipality of Mainz Energiepark Mainz
Germany 2015
Silyzer 200 1.25 MW
Municipality of Haßfurt Greenpeace Energy Wind Gas Haßfurt
Germany 2016
Silyzer 200 5 MW
H&R Ölwerke Schindler GmbH H&R
Germany 2017
Pilot Silyzer 300 Voestalpine, Verbund, 6 MW
Austrian Power Grid (APG) H2Future
1Austria 2019
Silyzer 200 2.5 MW
Food and Beverage Company Food and Beverage
Sweden 2019
Silyzer 200 1.25 MW
Australian Gas Infrastructure Group (AGIG)
Hydrogen Park SA (HyP SA)
Australia 2020
Silyzer 200 2.50 MW
Limeco Power-to-Gas
(Methane) Switzerland
2020
Silyzer 200 1.25 MW
Renewable Investor Power-to-Liquid
Germany 2020
Silyzer 200 2.5 MW
Salzgitter AG SALCOS
Germany 2020
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1This project has received funding from the Fuel Cells and Hydrogen 2 Joint Undertaking under grant agreement No 735503.
This Joint Undertaking receives support from the European Union’s Horizon 2020 research and innovative programme and Hydrogen Europe and NERGHY
Restricted © Siemens Energy, 2024 48
Our references for industry, mobility and energy applications
Product offering Applications Power demand
Customer Project
Country Year
Silyzer 200 1.25 MW
State Power Investment Corporation China (SPIC) Power-to-Hydrogen
China 2021
Silyzer 200 1.25 MW
Dubai Electricity and Water Authority (DEWA)
DEWA Expo 2020 UAE
2021
Silyzer 200 1.25 MW
Solarbelt FairFuel gGmbH Werlte
Germany 2021
Silyzer 200 1.25 MW
Highly Innovative Fuels (HIF) Haru Oni
Chile 2022
Silyzer 300 8.5 MW
Siemens AG,
SWW Wunsiedel GmbH Wunsiedel
Germany 2022
Silyzer 300 up to 20 MW
Air Liquide Oberhausen
Germany 2022
Silyzer 300 50 MW
European Energy Kassø
Denmark 2023
Silyzer 300 70 MW
Ørsted FlagshipONE
Sweden 2023
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Projects completed or in implementation based on Silyzer 300 Scale-up is already happening
8.5 MW up to 20 MW 50 MW
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Wunsiedel
Green hydrogen for industry, grid services and mobility
Our partners:
Siemens AG, WUNH2, SWW Wunsiedel GmbH
Oberhausen
Green hydrogen for Air Liquide pipeline infrastructure
Our partner:
Air Liquide
e-Methanol Kassø
Green hydrogen for CO2-neutral
shipping at large- scale
Our partner:
European Energy
NormandHy
Renewable electricity
Engineering and Long Lead Started
Our Partner:
Air Liquide
200 MW
H2Future Linz
Green hydrogen for the steel making process
Our partners:
VERBUND, voestalpine,
Austrian Power Grid (APG),TNO, K1-MET
6 MW 50 MW
Hy4Chem-El Ludwigshafen
Hydrogen as raw material for chemical plant
Our partner:
BASF
FlagshipONE
Green hydrogen for CO2-neutral shipping at large- scale
Our partner:
Ørsted
70 MW
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Air Liquide Normand’Hy
Industrial-scale hydrogen
electrolyzer plant to decarbonize industry and mobility
200 MW
Power demand based on Silyzer 300
4 tons
of green hydrogen per hour
250 000 tons
of carbon dioxide emissions will be avoided
Copyright ATAUB Architectes
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FlagshipONE
Largest commercial product plant for CO 2 neutral e-Methanol for marine use
Project Use cases
• Customer: FlagshipONE
• Investor: Ørsted
• Country: Sweden
• Installation: expected 2025
• Product: Silyzer 300
Challenge
• Europe’s largest commercial e-Methanol product facility
• Blueprint: Liquid Wind plans 10 facilities by 2030
• FlagshipTWO electrolyzers capacity of 140 MW planned
Solutions
• 4x PEM Silyzer 300
• Plant wide electrification and automation system, digitalization solutions (digital twins), power distribution and compressor systems
• E-Methanol from hydrogen and biogenic carbon dioxide
Hydrogen for e-Methanol
Decarbonize the world’s shipping industry
70 MW
power demand based on Silyzer 300
50.000 tones
of e-Methanol per year from 2025
10 more plants
by 2030
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FlagshipONE
Largest Power-to-X plant for e-Methanol for shipping with our partner Ørsted
70 MW
power demand based on Silyzer 300
50.000 tons
of e-Methanol per year from 2025
Blueprint: 10 more
plants by 2030
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BASF Hy4Chem-El
Industrial-scale electrolyzer to supply hydrogen as raw material to chemical plant
54 MW
Power demand based on Silyzer 300 Capacity to produce
8,000 tons
of green hydrogen per year from 2025
up to 72 000 tons
of carbon dioxide emissions will be avoided
per year at BASF site Ludwigshafen
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KASSØ POWER-TO-X
First large-scale e-Methanol project in Europe
Project Use cases
• Partner: Solar Park Kassø ApS (100%
owned by European Energy)
• Country: Denmark
• Site: Kassø Solar Park
• Installation: expected 2023
• Commercial
operation: expected 2023
• Product: Silyzer 300
Challenge
• Fast track project (bid and execution)
• First 3 Array plant
• First large-scale e-Methanol plant build by customer
Solutions
• 3 full Arrays Silyzer 300
• Transformers, rectifiers, Arrays and demin water plant. T3000 automation for Silyzers
• Supervision for installation, commissioning by SE Denmark
• Powered by largest solar park in Scandinavia Hydrogen for e-Methanol (MAERSK)
Hydrogen for fuel blending (Circle K)
50 MW
power demand based on Silyzer 300
1000 kg
of green hydrogen per hour
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KASSØ POWER-TO-X
First large-scale e-Methanol project in Europe with our partner European Energy
50 MW
power demand based on Silyzer 300
1000 kg
of green hydrogen per hour Powered by
Solar Park KASSØ
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TRAILBLAZER PROJECT OBERHAUSEN
Renewable hydrogen for Air Liquide pipeline infrastructure
2,680 kg
of green oxygen per hour
335 kg
of green hydrogen per hour
Project
Partners: Air Liquide
Country: Germany
Installation: 2023 Commissioning: 2023 Product: Silyzer 300
Use cases
Potential
• Connect hydrogen production to both existing hydrogen and oxygen pipelines
• First step: up to 20 MW capacity
• Potential to expand to 30 MW total planned capacity
Solutions
• Operation of a full 24-stack array Silyzer 300
• Electrolyzer will be integrated into existing local hydrogen and oxygen pipeline infrastructure of Air Liquide
• First electrolyzer to be built in the framework of the partnership between Air Liquide and Siemens Energy
• One of the largest renewable hydrogen and oxygen production plants of Germany
Hydrogen for the Industry
Hydrogen for mobility
Funded by the German Federal Ministry of Economic Affairs and Energy
up to 20 MW
based on Silyzer 300
11 plant incl. additional auxiliaries such as compression for hydrogen and oxygen
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Trailblazer Project, Oberhausen
Green Hydrogen for Air Liquide Pipeline Intrastructure
Up to 20 MW
based on Silyzer 300
335 kg
of green hydrogen per hour
2,680 kg
of green oxygen per hour
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750,000 liters
of e-methanol per year from 2023 (130,000 liters of e-gasoline)
>55 m liters
e-fuel per year planned from 2025
Project Use cases
Challenge
• Huge wind energy potential in Magallanes
• Existing industry and port infrastructure Perfect conditions to export green energy from Chile to the world
Solutions
• Production of e-gasoline and e-methanol at one of the best spots worldwide for wind energy
• Co-developer Siemens Energy realizing the system integration from wind energy to e-fuel production
• International Partners like Porsche and AME
>550 m liters
e-fuel per year planned from 2027
E-Fuel for Porsche cars
Potential for adding Kerosene or Diesel production in future phases Methanol for ship motors
HARU ONI PILOT PROJECT
First integrated plant for climate-neutral e-fuel production from wind and water
Customer: HIF (Highly Innovative Fuels) Off-taker: Porsche AG
Country: Chile, Patagonia Installation: 2022
Product: Power-to-methanol solution based on SE Electrolyzer
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July 2022
60 Oct 2022
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Preconditions for ramping up green hydrogen production
• Massive ramp-up of renewable energy generation with competitive price level
• Facilitation by local government e.g. for permitting
• Cost decrease for key equipment
• Long term offtake agreements
Potential of PEM electrolysis
• Electrolysis can react flexibly to changes in power supply or H
2demand
• Small footprint facilitates brown field integration
• Utilization of high purity Oxygen
How to get from grey to green:
preconditions and potential of electrolysis
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Wrap Up
References / Use cases and applications
4
Overview of PEM Auxiliaries and operational aspects
3
A deeper dive into PEM (Silyzer 300)
2
Electrolysis & its types
1
We went through a broad overview of below topics
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BREAK
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Case review &
Future collaboration
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Heat integration
Waste heat utilization Heat production
(Heat Pumps)
E n h a n c e d h e a t p r o d u c t i o n a n d
u t i l i z a t i o n
Electrification
Electrical heating
(Inductive & Turbo heating)
Electrification of drives E l e c t r i f i c a t i o n
a l o n g t h e i n d u s t r i a l v a l u e
c h a i n
Low carbon energy
Hybrid heat and power Combined heat &
power H i g h e f f i c i e n t
a n d r e l i a b l e p r o v i s i o n o f h e a t
a n d p o w e r
Power to X
S o l u t i o n s f o r t h e h y d r o g e n i n f r a s t r u c t u r e
Gas compression &
handling Hydrogen production
E-fuel production
Microgrid*
Modernization and upgrades
Energy Storage
(Redox flow / CAES / BESS)
Automation, control systems and digitalization including energy and asset management Services and O&M
Pathways for the Energy Transitions
Process Decarbonization
*Enablers of electrification
Fuels Cells
Carbon Capture
(DAC & Point Source)
U s i n g N e x t G e n s o l u t i o n s f o r
d e e p d e c a r b o n i z a t i o n
CO2Utilization
Key Enablers
D e v e l o p i n g H y b r i d s o l u t i o n s b u i l d i n g f l e x i b i l i t y, r e s i l i e n c e
& d i g i t a l i z a t i o n
Energy System Design (Scenario simulation for various
sectors - mining, refinery, chemicals, etc.)
Grid Stability Analysis
Clean Energy Certification
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The energy trilemma – the good, the bad and the ugly?
Energy Transition Energy Trilemma
Energy Transition is the change of fuel source, from fossil-based fuels to
renewable sources to ensure sustainability.
Sustainable
Renewable sources involves
intermittency. Hence reliability and security is important. Use of storage devices is important.
Security Affordable
PV solar electricity is lowest among all types. But storage increases the cost of energy. Achieving affordable energy is a necessity.
Sustainability* –
“meeting the needs of the present without compromising the ability of future generations to meet their own needs”.
* As defined by UN Brundtland Commission 1987
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Power: Transition towards renewable energy
Hydrogen as storage, BESS planned for grid stabilization, Grid transformation
Renewable
electricity generation
Grid
Integration
Conversion / Storage
PEM electrolysis
H2
Generation Grid
stabilization
Solar Wind
Intermittent Renewables
Continuous Renewables
Re-Conversion/
Electricity Generation
Grid Storage
Consumer
Natural Gas
Industry
Commercial Residential
Product
(With reduced carbon intensity)
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Green hydrogen cost – Driven by 3 main criteria
Capex, Electricity price & Operating hours
Source: International Renewable Energy Agency (IRENA)’s GREEN HYDROGEN – A GUIDE TO POLICY MAKING (2020).
Electricity required to produce 1 kg of hydrogen η=70%
HHVeff is 56.27kWh.
@50 USD/MWh, cost of electricity is
= $2.8/kg in H
2LCOH Current cost of green H
2produced from PV Solar electricity is
= ~$6.6/kg ($49.1/mmbtu)
$3.8
$2.8
Operating hours Operating hours
Capex Electricity price
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Case study – Scenario 1
Cilacap
• Solar – 400MWp
Assumptions:
• Solar power profiles are taken from open source (renewable Ninja).
• LCOE considered for Solar – 50.9 USD/MWh
• Electrolysis technology EPC cost is used for all scenarios @ USD 1100 / kW
• WACC is assumed to be 8% for all scenarios.
• Standard inflation of 2%.
• Calculations are based on 30-year plant life.
• 3% Capex for O&M cost assumed
• 6 Electrolyzer sizes evaluated.
50MW…100MW …150MW …
200MW… 250MW… 300MW
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Case study – Scenario 2
Cilacap
• Solar – 400MWp
• Geothermal – 50MW
Assumptions:
• Solar power profiles are taken from open source (renewable Ninja).
• LCOE considered for Solar – 50.9 USD/MWh
• LCOE considered for Geothermal – 70 USD/MWh
• Electrolysis technology EPC cost is used for all scenarios @ USD 1100 / kW
• WACC is assumed to be 8% for all scenarios.
• Standard inflation of 2%.
• Calculations are based on 30-year plant life.
• 3% Capex for O&M cost assumed
• 6 Electrolyzer sizes evaluated.
50MW…100MW …150MW …
200MW… 250MW… 300MW
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Case study – Scenario 3
Cilacap
• Solar – 400MWp
• Geothermal – 100MW
Assumptions:
• Solar power profiles are taken from open source (renewable Ninja).
• LCOE considered for Solar – 50.9 USD/MWh
• LCOE considered for Geothermal – 70 USD/MWh
• Electrolysis technology EPC cost is used for all scenarios @ USD 1100 / kW
• WACC is assumed to be 8% for all scenarios.
• Standard inflation of 2%.
• Calculations are based on 30-year plant life.
• 3% Capex for O&M cost assumed
• 6 Electrolyzer sizes evaluated.
50MW…100MW …150MW …
200MW… 250MW… 300MW
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Pertamina’s Sustainability Initiatives
Source: Pertamina%20Performance%20FY%202023.pdf
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Projects
Source: Public Media
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Energy System Design
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Energy System Design (ESD)
Energy system
Combination of energy conversion technologies, energy storages, loads, grids and industrial processes.
Design
Technology selection and sizing, including operationObjective
Achieve minimum total expenditures, CO2emissions, or primary energy consumption.
Optimization
Solving a mathematical optimization problem
Constraints
Limits on the energy system such as time of use tariffs, CO2 emissions, CAPEX, OPEX, land space, interconnect limits, tax incentives etc…ESD optimizes the design of an energy system
with respect to a certain objective under given
constraints.
• Can you help me size thetechnologies for my hybrid plant / microgrid?
• What is my optimum path to decarbonization? (Utilities, industrial sector, cities, states)
• If I were to build a green hydrogen production system at a particular location, how would it optimally dispatch? What would be the levelized cost?
• What is the optimum asset configuration for my power plant/PtX/… project? What synergies can be used?
• What is the impact of regulations and subsidy schemes?
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Design Challenge – Multi-Modal Energy Systems
Renewable Generation
Electrical Storage
Green H₂ derivatives
Electrolysis | H₂ Generation
Future energy supply Electricity, Steam, Heat, H₂
Existing Power Plant
H₂ for transport H₂ export H₂ storage
Thermal Storage
Grid Import/Export
Steam Generation Transmission
Limitations Efficiency Operational Expenditures Capital Expenditures
Availability
Decarbonization targets
Capacities
Alternatives
Natural gas Steam Electricity
Water Hydrogen
H
2Cooling
Liquid fuels CO2 CO2-Emissions
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Energy System Design facilitates the techno-economic optimization of energy systems
PE: Primary energy
Energy System Design Technology related input data
•Performance models and parameters
• Component cost models
Selection
[…]
examples
… (economic) dispatch of technologies sizing, and
example Size
[…]
• Optimization objective
• Climate/weather data
• Commodity prices
• Load profiles
Site specific input data
• Technology pre-selection
• Renewable
generation profiles
€/$ CO
2PE
Results
• Technology selection
• Optimal capacities
• Optimal operation schedule
• Economical and ecological data Perfect starting
point as real data potentially available
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Exemplary applications of Energy System Design
[1] Siemens Energy AG, Haru Oni Site, Haru Oni hydrogen plant | 2022 | Siemens Energy Global (siemens-energy.com), last visited 23.02.2023 [2] Siemens Energy AG, Island grids:Omnivise Hybrid Control Innovations| 2021 | Siemens Energy Global (siemens-energy.com), last visited 23.02.2023
[3] Siemens Energy AG, Dec