PEM Fuel Cells for Submarines
Industrial Solutions and Services
Your Success is Our Goal
Fuel Cell
Applications for
electric energy
production
Emergency power supply
(PEFC)
Frighter
Emission-free and noiseless
operation (PEFC)
Bus
Delivery trucks
Elektrischer Antrieb
Bahn
Energy storage with gases
(PEFC)
Storage system for
regenerative energies
Space Shuttle
Grid-independent operation
(SOFC, PEFC)
Decentral
Power plants
Railroad
H2/O2
Reformer gas/Air
H2/Air
Passenger car
Emission-free and energy-
efficient operation (PEFC)
Electrical propulsion
(SOFC, PEFC)
Air-independent power supply
(PEFC)
Emission-free and noiseless
operation (PEFC)
Gas tanker
Electrical propulsion
(SOFC, PEFC)
Air-independent propulsion
(PEFC)
Submarine
Reformer gas/Air
Fig. 1:
Possible applications
for generating
electrical energy
Fuel cells allow the direct generation of electric
power from hydrogen and oxygen with a consid-
erably better efficiency and no pollutant emission
compared to conventional combustion engines.
Their operation is noiseless.
In addition to these basic advantages, the fuel
cell with a solid, ion conducting, polymeric mem-
brane (Polymer Electrolyte Membrane – PEM)
has further positive properties:
• Quick switch-on, switch-off behavior
• Low voltage degradation and long service life
• Favorable load and temperature cycle behavior
• Overload possibility
• Low operating temperature (80°C)
• Absence of a liquid corrosive electrolyte.
All these characteristics make the PEM fuel cell
(PEM FC) an ideal power unit.
Aboard submarines they show their outstanding
advantages against conventional AIP systems
(Air Independent Propulsion) using oxygen and
hydrogen, carried on board.
The new submarines of class U 212 A are
equipped with PEM FC modules with an electri-
cal output of 30 to 40 kW each, which have been
developed since 1985 on behalf of the German
Ministry of Defense. The new type U 214 class
submarines will be fitted with 120 kW fuel cell
modules which have been developed by
Siemens in a next step.
The basic suitability of fuel cell
technology onboard submarines
has been demonstrated by
installing a 100 kW FC power
plant with alkaline
fuel cells on the
submarine U1 of
the Federal German
Navy in 1988.
During the tests the
performance of additional
equipment such as H2
and O2 components has been
proven.
Further possible applications of PEM FCs for
power generation are listed below (see also
Fig. 1, left side):
Using hydrogen and oxygen
• Operation in spacecrafts
• Component in a long-term energy storage
system (consisting of solar cells, an electrol-
yser system and a hydrogen/oxygen storage
system)
Using hydrogen and air
• Zero emission operation of electrically driven
vehicles
Using reformer gas and air
• Power supply far distant from a public power
supply system
• Safe, low emission power supply on cargo
vessels especially in harbor
• Utilization of boil-off gases aboard gas tankers
• Power supply e.g. for drives on rail vehicles
Concentrating on manufacture and development
of fuel cells for AIP applications, Siemens
demonstrated its technological competence in
projects for air-breathing PEM fuel cells, e.g.
– Fork lift truck
– Micro co-generation
– Propulsion systems for busses.
The Siemens R&D activities in the fields of
Direct Methanol Fuel Cells (DMFC) and Solid
Oxide Fuel Cells (SOFC) are not presented in this
brochure.
Introduction
OxygenHydrogen
Energy
Water
3
Cover photo: 30–40 kW module (top)
and 120 kW module (below)
Both the basic function and the design
of the PEM FC are very simple (Fig. 2):
the electrochemical element at which
the chemical energy is converted into
electrical energy is the membrane
electrode unit. It consists of the poly-
mer electrolyte, the gas diffusion elec-
trodes with a platinum catalyst and
carbon sheets on each side.
After the abstraction of the electrons
from hydrogen – they flow from the
anode via the electrical load to the
cathode – the resulting protons
migrate from the anode to the cathode
where they combine with oxygen (and
the electrons) to water. The theoretical
voltage of an H2/O2 fuel cell is 1.48 V
(referred to the upper heat value of
hydrogen). At zero load conditions,
slightly more than 1 V per cell is avail-
able.
The cooling units or bipolar plates in
combination with carbon diffusion lay-
ers distribute the reactants uniformly
across the area of the cell, conduct the
electrons across the stack, remove the
heat from the electrodes and separate
the media from each other.
PEM
fuel cell
Fig. 3: Components of cell Fig. 5: Comparison of cells: 120 kW type (front)
30–40 kW type (back)
4
Fig. 3 shows the two core compo-
nents of a cell with outside dimen-
sions of 400 mm x 400 mm. As used
in 30–40 kW modules.
Fig. 5 compares the bipolar plate of
the 30–40 kW modules to the 120 kW
type. Two cells of the 120 kW type
produce about twice the power of one
cell of the 30–40 kW type with nearly
the same active area.
The in principle high development
potential in regard to the membrane
material is shown in Fig. 4. With
improved materials the power density
can nearly be doubled.
The voltage of a PEM FC referred to
the operating time is stable, degrada-
tion rates are less than 2 µV/h for the
30–40 kW module (Fig. 6).
Cooling unit
Membrane
electrode unit
Cooling unit
400 mm
1500
1000
500
CelloutputPz
0
W
1.1
V
0.9
0.7
0.5
CellVoltageUz
0 500 1000 1500 2000A
CurrentI
TKW
pO2
pH2
pK
Aact
= ~80°C
= 2.3 bar abs.
= 2.0 bar abs.
= 5.0 bar abs.
= 1163 cm2
Dow (G 29)
Naf 115 (D 14)
Naf 117 (A 37)
Dow
Naf 115
Naf 117
60
56
54
52
50
Module
voltage
[V]
Degradation of voltage (single cell):
(55.75-55.56V)/72cells/1.500h = 1.76µV/h
1000
500
0
Module
Current
[I]
55.75V 55.56V
Operating time [h]2000 600400 800 1500
pO2
: 2,3 bar a
pH2
: 2,0 bar a
Temp.: 80° C
Fakt.: 1163 cm2
Zellenzahl: 72
Electrical load
Polymer
electrolyte
Product water
H2O + O2
Oxygen
O2
Hydrogen
H2
Waste heat
4e–
H+
Anode Cathode
H+
H+
H+
O2+4e–=
2H2O
20- -
20--+4H+=
4e–=2H2–
4H+
Fig. 2: Functional principle
Fig. 4: Potential output increase when
using various electrolytes
Fig. 6: Voltage degradation referred to operating time
(measurement from 30–40 kW module)
Fuel cell
modules
Fuel cell
power plant
The fuel cells need additional auxiliaries
for their operation. The FC stack,
valves, piping and sensors form the FC
module, the corresponding module
electronics controls the proper opera-
tion of the FC process. The ancillaries
comprise the equipment for supplying
H2, O2 and N2, for reactant humidifica-
tion, for product water, waste heat and
residual gas removal. The FC stack and
the ancillaries are installed in a contain-
er which is filled with inert gas (N2) at
3.0 bar abs. to prevent a release of H2
and/or O2 in the case of leakage.
The FC module can be operated at vari-
ous static load currents. Currents
below 650 A for 30–40 kW modules or
below 560 A for 120 kW modules
respectively can be applied in continu-
ous operation. The output power/cur-
rent characteristics for 30–40 kW
modules are shown in Fig. 7.
For currents above the rated current
the loading time is limited due to the
insufficient heat removal at such work-
ing points. Even loads up to the double
of the rated current can be applied for
a short time.
At the rated operating point, the over-
all efficiency is approximately 59%
referred to the lower heat value of H2
(LHV). It increases in the part load
range, reaching a maximum of approxi-
mately 69% at a load factor of some
20% of the rated current (approx.
100 A) (Fig. 8).
The properties of the 30–40 kW and
120 kW modules are listed in the
table.
Suitable operating conditions for fuel
cell modules are provided for subma-
rine application by a fuel cell system in
which fuel cell modules are connected
• to the hydrogen and oxygen supply
• to disposal units such as for
– cooling
– residual gas
– reaction water
• to auxiliary systems such as for
– inert gas drying
– nitrogen supply
– evacuating system
• to the propulsion/ship’s system as
the purpose of the whole FC system.
Operator control and visualization of
the fuel cell system is effected by the
integrated platform management sys-
tem, or directly by the control panel of
the fuel cell system.
Fig. 10 gives a simplified impression of
the AIP system.
The fuel cell system in its entirety –
the complete fuel cell power plant,
especially the supply and disposal sys-
tems described above for AIP opera-
tion including spatial and functional
integration on board – has been devel-
oped by HDW (Howaldtswerke
Deutsche Werft AG).
The new submarine classes U 212 A
and U 214 are equipped with the new
fuel cell power plant by HDW with the
PEM fuel cell modules by Siemens.
Fig. 9 shows PEM fuel cell modules
assembled in a test rack.
6
Technical data
Rated power 30–40 kW 120 kW
Voltage, about 50–55 V 215 V
Efficiency at
rated load 59% 58%
Efficiency at
20% load 69% 68%
Operating
temperature 80°C
H2 pressure 2.3 bar abs.
O2 pressure 2.6 bar abs.
Dimensions H = 48 cm 50 cm
W = 48 cm 53 cm
L = 145 cm 176 cm
Weight
(without module
electronics) 650 kg 900 kg
Propulsion switchboard
Feeding of
propulsion/ship’s system
H2 supply
O2 supply
Removal • Waste heat
• Product water
• Residual gas
Integrated Platform
Management System (IPMS)
FUEL CELL
MODULES
Fuel cell system
Control panel
Module electronics
Control and monitoring
kW
0
ModuleoutputPM
0 A
Module current IM
TKW
pO2
pH2
pK
Aact
n
Membrane: Nafion 117
= ~80°C
= 2.3 bar abs.
= 2.0 bar abs.
= 5.0 bar abs.
= 1163 cm2
= 72 Cells
60
200 400 600 800 1000
10
20
30
50
1200
40
%
0
Overallefficiencyηo
0 A
Module current IM
TKW
pO2
pH2
pK
Aact
n
Membrane: Nafion 117
= ~80°C
= 2.3 bar abs.
= 2.0 bar abs.
= 5.0 bar abs.
= 1163 cm2
= 72 Cells
100
100 200 300 400 500
20
40
60
80
600
After the successful development
the FC modules are now under
manufacturing. They have proven
their performance and reliability in
extensive tests including long term
tests. They are an integral part of
an AIP system for modern sub-
marines like that of Class U 212 A
(30–40 kW modules) and U 214
(120 kW modules).
The field for use of PEM FC will
be widened when suitable reform-
ers produce hydrogen from liquid
fuels, e.g. methanol. Then it may
be possible that fuel cells can
become the sole power source
of submarines of the future.
Using PEM fuel cells and replac-
ing oxygen with air, they are an
interesting alternative for environ-
mental-friendly power generation,
e.g. for vehicles in cities.
In general: the excellent operating
performance of PEM fuel cells like
high efficiency and noiseless oper-
ation can lead to a promising
future upon further reduction in
manufacturing and operating
costs.
Fig. 7: Module output referred to load current
(measurement from 30–40 kW module)
Fig. 8: Efficiency (measurement from 30–40 kW module)
Fig. 10: Integrated AIP system
Outlook
7
Fig. 9: PEM fuel cell modules assembled in a test rack
Order No. E10001-A930-A35-V3-7600
Dispo No. 16600
Printed in Germany
174D6077 PA 08012.
Our
Program
Systems Engineering and
Quality Management
Propulsion Systems
Air-Independent
Propulsion (AIP)
Electrical Systems
Integrated Platform
Management System
Auxiliary Systems
Engineering
Logistics
Service
Published by
Siemens AG
Industrial Solutions
and Services
Marine Solutions
P.O. Box 10 56 09
D-20038 Hamburg
Tel. +49/40/28 89-27 00
Fax +49/40/28 89-36 80
marine.solutions@hbg.siemens.de
Siemens AG
Industrial Solutions
and Services
Marine Solutions
Postfach 32 40
D-91050 Erlangen
Tel. (0 91 31) 7-2 71 79
Fax (0 91 31) 7-2 68 35
marine.solutions@erl9.siemens.de
www.marine-solutions.de
Siemens Aktiengesellschaft Subject to change without prior notice
© Siemens AG 2001
All rights reserved
Solutions

U6000 power 73385 fuel cells_version1_e

  • 1.
    PEM Fuel Cellsfor Submarines Industrial Solutions and Services Your Success is Our Goal
  • 2.
    Fuel Cell Applications for electricenergy production Emergency power supply (PEFC) Frighter Emission-free and noiseless operation (PEFC) Bus Delivery trucks Elektrischer Antrieb Bahn Energy storage with gases (PEFC) Storage system for regenerative energies Space Shuttle Grid-independent operation (SOFC, PEFC) Decentral Power plants Railroad H2/O2 Reformer gas/Air H2/Air Passenger car Emission-free and energy- efficient operation (PEFC) Electrical propulsion (SOFC, PEFC) Air-independent power supply (PEFC) Emission-free and noiseless operation (PEFC) Gas tanker Electrical propulsion (SOFC, PEFC) Air-independent propulsion (PEFC) Submarine Reformer gas/Air Fig. 1: Possible applications for generating electrical energy
  • 3.
    Fuel cells allowthe direct generation of electric power from hydrogen and oxygen with a consid- erably better efficiency and no pollutant emission compared to conventional combustion engines. Their operation is noiseless. In addition to these basic advantages, the fuel cell with a solid, ion conducting, polymeric mem- brane (Polymer Electrolyte Membrane – PEM) has further positive properties: • Quick switch-on, switch-off behavior • Low voltage degradation and long service life • Favorable load and temperature cycle behavior • Overload possibility • Low operating temperature (80°C) • Absence of a liquid corrosive electrolyte. All these characteristics make the PEM fuel cell (PEM FC) an ideal power unit. Aboard submarines they show their outstanding advantages against conventional AIP systems (Air Independent Propulsion) using oxygen and hydrogen, carried on board. The new submarines of class U 212 A are equipped with PEM FC modules with an electri- cal output of 30 to 40 kW each, which have been developed since 1985 on behalf of the German Ministry of Defense. The new type U 214 class submarines will be fitted with 120 kW fuel cell modules which have been developed by Siemens in a next step. The basic suitability of fuel cell technology onboard submarines has been demonstrated by installing a 100 kW FC power plant with alkaline fuel cells on the submarine U1 of the Federal German Navy in 1988. During the tests the performance of additional equipment such as H2 and O2 components has been proven. Further possible applications of PEM FCs for power generation are listed below (see also Fig. 1, left side): Using hydrogen and oxygen • Operation in spacecrafts • Component in a long-term energy storage system (consisting of solar cells, an electrol- yser system and a hydrogen/oxygen storage system) Using hydrogen and air • Zero emission operation of electrically driven vehicles Using reformer gas and air • Power supply far distant from a public power supply system • Safe, low emission power supply on cargo vessels especially in harbor • Utilization of boil-off gases aboard gas tankers • Power supply e.g. for drives on rail vehicles Concentrating on manufacture and development of fuel cells for AIP applications, Siemens demonstrated its technological competence in projects for air-breathing PEM fuel cells, e.g. – Fork lift truck – Micro co-generation – Propulsion systems for busses. The Siemens R&D activities in the fields of Direct Methanol Fuel Cells (DMFC) and Solid Oxide Fuel Cells (SOFC) are not presented in this brochure. Introduction OxygenHydrogen Energy Water 3 Cover photo: 30–40 kW module (top) and 120 kW module (below)
  • 4.
    Both the basicfunction and the design of the PEM FC are very simple (Fig. 2): the electrochemical element at which the chemical energy is converted into electrical energy is the membrane electrode unit. It consists of the poly- mer electrolyte, the gas diffusion elec- trodes with a platinum catalyst and carbon sheets on each side. After the abstraction of the electrons from hydrogen – they flow from the anode via the electrical load to the cathode – the resulting protons migrate from the anode to the cathode where they combine with oxygen (and the electrons) to water. The theoretical voltage of an H2/O2 fuel cell is 1.48 V (referred to the upper heat value of hydrogen). At zero load conditions, slightly more than 1 V per cell is avail- able. The cooling units or bipolar plates in combination with carbon diffusion lay- ers distribute the reactants uniformly across the area of the cell, conduct the electrons across the stack, remove the heat from the electrodes and separate the media from each other. PEM fuel cell Fig. 3: Components of cell Fig. 5: Comparison of cells: 120 kW type (front) 30–40 kW type (back) 4 Fig. 3 shows the two core compo- nents of a cell with outside dimen- sions of 400 mm x 400 mm. As used in 30–40 kW modules. Fig. 5 compares the bipolar plate of the 30–40 kW modules to the 120 kW type. Two cells of the 120 kW type produce about twice the power of one cell of the 30–40 kW type with nearly the same active area. The in principle high development potential in regard to the membrane material is shown in Fig. 4. With improved materials the power density can nearly be doubled. The voltage of a PEM FC referred to the operating time is stable, degrada- tion rates are less than 2 µV/h for the 30–40 kW module (Fig. 6). Cooling unit Membrane electrode unit Cooling unit 400 mm
  • 5.
    1500 1000 500 CelloutputPz 0 W 1.1 V 0.9 0.7 0.5 CellVoltageUz 0 500 10001500 2000A CurrentI TKW pO2 pH2 pK Aact = ~80°C = 2.3 bar abs. = 2.0 bar abs. = 5.0 bar abs. = 1163 cm2 Dow (G 29) Naf 115 (D 14) Naf 117 (A 37) Dow Naf 115 Naf 117 60 56 54 52 50 Module voltage [V] Degradation of voltage (single cell): (55.75-55.56V)/72cells/1.500h = 1.76µV/h 1000 500 0 Module Current [I] 55.75V 55.56V Operating time [h]2000 600400 800 1500 pO2 : 2,3 bar a pH2 : 2,0 bar a Temp.: 80° C Fakt.: 1163 cm2 Zellenzahl: 72 Electrical load Polymer electrolyte Product water H2O + O2 Oxygen O2 Hydrogen H2 Waste heat 4e– H+ Anode Cathode H+ H+ H+ O2+4e–= 2H2O 20- - 20--+4H+= 4e–=2H2– 4H+ Fig. 2: Functional principle Fig. 4: Potential output increase when using various electrolytes Fig. 6: Voltage degradation referred to operating time (measurement from 30–40 kW module)
  • 6.
    Fuel cell modules Fuel cell powerplant The fuel cells need additional auxiliaries for their operation. The FC stack, valves, piping and sensors form the FC module, the corresponding module electronics controls the proper opera- tion of the FC process. The ancillaries comprise the equipment for supplying H2, O2 and N2, for reactant humidifica- tion, for product water, waste heat and residual gas removal. The FC stack and the ancillaries are installed in a contain- er which is filled with inert gas (N2) at 3.0 bar abs. to prevent a release of H2 and/or O2 in the case of leakage. The FC module can be operated at vari- ous static load currents. Currents below 650 A for 30–40 kW modules or below 560 A for 120 kW modules respectively can be applied in continu- ous operation. The output power/cur- rent characteristics for 30–40 kW modules are shown in Fig. 7. For currents above the rated current the loading time is limited due to the insufficient heat removal at such work- ing points. Even loads up to the double of the rated current can be applied for a short time. At the rated operating point, the over- all efficiency is approximately 59% referred to the lower heat value of H2 (LHV). It increases in the part load range, reaching a maximum of approxi- mately 69% at a load factor of some 20% of the rated current (approx. 100 A) (Fig. 8). The properties of the 30–40 kW and 120 kW modules are listed in the table. Suitable operating conditions for fuel cell modules are provided for subma- rine application by a fuel cell system in which fuel cell modules are connected • to the hydrogen and oxygen supply • to disposal units such as for – cooling – residual gas – reaction water • to auxiliary systems such as for – inert gas drying – nitrogen supply – evacuating system • to the propulsion/ship’s system as the purpose of the whole FC system. Operator control and visualization of the fuel cell system is effected by the integrated platform management sys- tem, or directly by the control panel of the fuel cell system. Fig. 10 gives a simplified impression of the AIP system. The fuel cell system in its entirety – the complete fuel cell power plant, especially the supply and disposal sys- tems described above for AIP opera- tion including spatial and functional integration on board – has been devel- oped by HDW (Howaldtswerke Deutsche Werft AG). The new submarine classes U 212 A and U 214 are equipped with the new fuel cell power plant by HDW with the PEM fuel cell modules by Siemens. Fig. 9 shows PEM fuel cell modules assembled in a test rack. 6 Technical data Rated power 30–40 kW 120 kW Voltage, about 50–55 V 215 V Efficiency at rated load 59% 58% Efficiency at 20% load 69% 68% Operating temperature 80°C H2 pressure 2.3 bar abs. O2 pressure 2.6 bar abs. Dimensions H = 48 cm 50 cm W = 48 cm 53 cm L = 145 cm 176 cm Weight (without module electronics) 650 kg 900 kg
  • 7.
    Propulsion switchboard Feeding of propulsion/ship’ssystem H2 supply O2 supply Removal • Waste heat • Product water • Residual gas Integrated Platform Management System (IPMS) FUEL CELL MODULES Fuel cell system Control panel Module electronics Control and monitoring kW 0 ModuleoutputPM 0 A Module current IM TKW pO2 pH2 pK Aact n Membrane: Nafion 117 = ~80°C = 2.3 bar abs. = 2.0 bar abs. = 5.0 bar abs. = 1163 cm2 = 72 Cells 60 200 400 600 800 1000 10 20 30 50 1200 40 % 0 Overallefficiencyηo 0 A Module current IM TKW pO2 pH2 pK Aact n Membrane: Nafion 117 = ~80°C = 2.3 bar abs. = 2.0 bar abs. = 5.0 bar abs. = 1163 cm2 = 72 Cells 100 100 200 300 400 500 20 40 60 80 600 After the successful development the FC modules are now under manufacturing. They have proven their performance and reliability in extensive tests including long term tests. They are an integral part of an AIP system for modern sub- marines like that of Class U 212 A (30–40 kW modules) and U 214 (120 kW modules). The field for use of PEM FC will be widened when suitable reform- ers produce hydrogen from liquid fuels, e.g. methanol. Then it may be possible that fuel cells can become the sole power source of submarines of the future. Using PEM fuel cells and replac- ing oxygen with air, they are an interesting alternative for environ- mental-friendly power generation, e.g. for vehicles in cities. In general: the excellent operating performance of PEM fuel cells like high efficiency and noiseless oper- ation can lead to a promising future upon further reduction in manufacturing and operating costs. Fig. 7: Module output referred to load current (measurement from 30–40 kW module) Fig. 8: Efficiency (measurement from 30–40 kW module) Fig. 10: Integrated AIP system Outlook 7 Fig. 9: PEM fuel cell modules assembled in a test rack
  • 8.
    Order No. E10001-A930-A35-V3-7600 DispoNo. 16600 Printed in Germany 174D6077 PA 08012. Our Program Systems Engineering and Quality Management Propulsion Systems Air-Independent Propulsion (AIP) Electrical Systems Integrated Platform Management System Auxiliary Systems Engineering Logistics Service Published by Siemens AG Industrial Solutions and Services Marine Solutions P.O. Box 10 56 09 D-20038 Hamburg Tel. +49/40/28 89-27 00 Fax +49/40/28 89-36 80 marine.solutions@hbg.siemens.de Siemens AG Industrial Solutions and Services Marine Solutions Postfach 32 40 D-91050 Erlangen Tel. (0 91 31) 7-2 71 79 Fax (0 91 31) 7-2 68 35 marine.solutions@erl9.siemens.de www.marine-solutions.de Siemens Aktiengesellschaft Subject to change without prior notice © Siemens AG 2001 All rights reserved Solutions