The Future of Fuel Cells
| CONTENTS 11pg 57K 11fig 1. Abstract 2. Introduction 3. Background 4. How does a fuel cell work? 5. Types of fuel cells 6. Fuel cells for electric power production 7. Fuel cells for transportation 8. Solid oxide fuel cell (SOFC) 9. Direct alcohol fuel cell (DAFC) 10. Polymer electrolyte fuel cell (PEFC) 11. Phosphoric acid fuel cell (PAFC) 12. Molten carbonate fuel cell (MCFC) 13. Alkaline fuel cell (AFC) 14. Fuels 15. Forms of energy 16. Temperament vs temperature 17. Fuel cells vs heat engines 18. Second law analysis of fuel cells 19. Companies involved in research 20. Conclusions 21. Notes 22. References 23. Symbols 24. Revision History >>>Copyright >>>http://www.benwiens.com/index.html 2002May03 by Ben Wiens...applied energy scientist 1. ABSTRACT 2. INTRODUCTION 3. BACKGROUND 4. HOW A FUEL CELL
WORKS
Fig 1 Alkaline fuel cell often uses hydrogen and oxygen as fuel The alkaline fuel cell as shown in Fig 1 is one of the oldest and most simple type of fuel cell. This is the type of fuel cell that has been used in space missions for some time. Hydrogen and oxygen are commonly used as the fuel and oxidant. The electrodes are made of porous carbon plates which are laced with a catalyst...which is a substance that accelerates chemical reactions. The electrolyte is potassium hydroxide. At the anode, the hydrogen gas combines with hydroxide ions to produce water vapor. This reaction results in electrons that are left over. These electrons are forced out of the anode and produce the electric current. At the cathode, oxygen and water plus returning electrons from the circuit form hydroxide ions which are again recycled back to the anode. The basic core of the fuel cell consisting of the manifolds, anode, cathode and electrolyte is generally called the stack. 5. TYPES OF FUEL
CELLS |
| Type | Abbreviation | Operating temp | Uses |
| Solid Oxide | SOFC | 500-1000°C | All sizes of CHP |
| Direct Alcohol | DAFC | 50-100°C | Buses, cars, appliances, small CHP |
| Polymer Electrolyte | PEFC | 50-100°C | Buses, cars |
| Phosphoric Acid | PAFC | 200°C | Medium CHP |
| Molten Carbonate | MCFC | 600°C | Large CHP |
| Alkaline | AFC | 50-250°C | Used in space vehicles |
| Fig 2 Different types of fuel cells
Scientists keep changing their minds every few years
about which of the above fuel cells will be the most popular in the
future. As of 2002May there are three types of fuel cells that
appear to be the most promising. The Solid Oxide Fuel Cell or
SOFC is the most likely contender for both large and small
electric powerplants in the 1 kw and above size. The Direct
Alcohol Fuel Cell or DAFC appears to be the most promising as a
battery replacement for portable applications such as cellular
phones and laptop computers. It is difficult to tell at this moment which
fuel cell will be most practical for transportation applications
such as automobiles and buses. The Polymer Electrolyte Fuel Cell
PEFC is the most practical if we have a developed hydrogen economy.
Many automobile manufacturers however believe that the DAFC will be much
simpler than the PEFC so it will be the winner for vehicular applications.
Others say that the much higher efficiency of the SOFC and its ability to
use most any fuel will make it a logical choice for vehicular applications
as well. Proponents claim the startup time problem of the SOFC can be
overcome by using supercapacitor batteries for the first few minutes of
operation. 6. FUEL CELLS FOR ELECTRIC POWER
PRODUCTION
Fig 3 Chart showing projected efficiencies of different future electricity generating powerplants There is a rapid trend in North America to
deregulate the production of electric power. One of the benefits of
deregulation is that it will promote CHP...combined heat and power,
also known as cogeneration. North America will likely generate much
of its electricity by burning fossil fuel for the next 10-40 years. CHP
will conserve fuel by utilizing the thermal energy that is produced as a
result of generating electricity. Because thermal energy cannot be
piped efficiently for long distances, CHP powerplants will
generally need to be much smaller than the present ones which are
often around 200,000 kw. 7. FUEL CELLS FOR TRANSPORTATION
Fig 4 Estimated efficiencies [1] of different automobiles using liquid hydrocarbon fuel Fuel cells are being proposed to replace Otto or
Diesel engines because they could be reliable,
simple, quieter, less polluting, and have even
greater economy. 8. SOLID OXIDE FUEL CELL
(SOFC)
Fig 5 Simple type [2] SOFC suitable for 1-30 kw powerplants The Solid Oxide Fuel Cell is considered to be the most
desirable fuel cell for generating electricity from hydrocarbon
fuels. This is because it is simple, highly efficient,
tolerant to impurities, and can at least partially internally
reform hydrocarbon fuels. 9. DIRECT ALCOHOL FUEL CELL
(DAFC)
Fig 6 A small simple 30 kw Direct Methanol Fuel Cell Figure 6 illustrates a type of DMFC that could be used in
a 30 kw system. Even smaller ones for use as battery replacements
do away with the air blower and the separate methanol water tank and pump.
Such fuel cells are not much different than batteries in
construction. |
| 10. POLYMER ELECTROLYTE FUEL CELL
(PEFC) The PEFC is considered the darling fuel cell by proponents of the hydrogen economy. Automobiles emitting pure water from their tailpipes are envisioned. It is not likely that there will be hydrogen pipelines supplying homes, businesses and service stations in the near future however. Many companies are proposing that PEFC systems would extract hydrogen from hydrocarbon fuels such as methanol or natural gas. While the efficiency of the PEFC when running on hydrogen and no air pressurization is high, practical systems that use fuel reforming and air compression suffer in efficiency. Small 30 kW AC powerplants will likely be 35% fuel to electricity efficient, 200 kW units 40% and large units 45%. Figure 4 shows that an automobile powerplant including an electric motor would have an efficiency of about 35%. There has been some progress made in storing hydrogen in different materials such as hydrides or carbon. If such materials can be perfected this would dramatically increase the chances for the PEFC success for automotive applications. The complex reformer would not be necessary, however unless hydrogen is universally available through pipelines across the country, the hydrogen would have to be manufactured locally by service stations. This is possible for larger city service stations but not really practical for small out of the way ones. The PEFC generally operates at 80°C which makes it ideal for small applications and allows reasonably inexpensive materials to be used. Unfortunately, this low a temperature is quite near the ambient temperature which hampers disposing of excess heat--present automobile engines dispose of heat at up to 100°C. A catalyst is also required to promote the chemical reaction at the low temperatures involved. Previously the platinum catalysts used in the stack made this type of fuel cell expensive. New techniques for coating very thin layers of catalyst on the polymer electrolyte have reduced the cost of the catalyst to around $150 per automobile. The PEFC is particular in that only hydrogen fuel can be used in the cell. Hydrocarbon fuels must be reformed carefully. Even small amounts of carbon monoxide in the cell can poison the catalyst--often permanently. If a reformer is used, this also requires a few minutes warm up time. Stored hydrogen must be used in the startup phase. Such problems make the PEFC running on stored hydrogen sound more appealing. A larger manufacturing plant running continuously has a much better chance of supplying very pure hydrogen. A liquid cooling system is required. This means that there is pure water inside the cells. Ballard has tested the fuel cell at below freezing temperatures and there was no damage to the stack. It appears that the stack coolant must be drained after shutdown. I do not know what repeated freeze-thaw cycling would do to the hydrated stack even if drained. Larger than 1 kw PEFC are generally pressurized to increase the chemical reaction at the low temperatures involved. Air compression to about 3 atmospheres or higher must be used for the fuel cell to have a reasonable power density. On small systems this results in a substantial loss of efficiency. The air compressors also add considerable complexity to the fuel cell. On automobiles and buses two air compressors are often used. One is a turbocharger and the second is a supercharger. Many experts feel that the DAFC will replace the PEFC once problems are solved. There is however a chance that a gasoline reformer will be perfected. If such a fuel cell system can be made to be reliable and inexpensive, then the PEFC will have a much better chance of being successful. Many experts however are not sure this is possible. 11. PHOSPHORIC ACID FUEL CELL
(PAFC) 12. MOLTEN CARBONATE FUEL CELL
(MCFC) 13. ALKALINE FUEL CELL
(AFC) 14. FUELS
Fig 7 Different forms of energy shown in a chart To properly evaluate different types of fuel cells it is
desirable to understand basic theoretical energy concepts. To
understand energy concepts, it is beneficial to have a proper naming
system that covers all the basic types of different energy in the
universe. This is because it is often difficult or impossible to convert
certain types of energy into different forms. The system of energy
used in this web-booklet is based on a plural energy system where
all the different types of energy are two word forms such as chemical
energy. The basis of this two word naming system is borrowed from
chemistry, however typically it is not labeled as the plural energy
system. Engineers do not like to use this chemistry naming system,
however it is the simplest and easiest to understand. The
plural energy system is shown as a bar chart in Fig 7. At the head of the
chart of "simple forms" is einstein energy which is...a term for
the concept of the total energy in the universe or a particular system.
When referring to the fact that energy is conserved in the universe
it should be mentioned that it is einstein energy that is conserved,
because other forms may not be. All einstein energy can be logically
divided into either external energy or internal energy. The
major difference between external energy and internal energy is the fact
that internal energy can never be completely converted into external
energy. 16. TEMPERAMENT vs TEMPERATURE
Fig 8 Virtual photons are closely coupled and real photons travel alone through space A fuel cell creates electricity, which is a form
of external energy, directly from the energy in chemical fuels without an
intermediate conversion into thermal energy. When a hydrogen atom
bonds to an oxygen molecule, not as much total energy is required in the
newly formed water molecule as in the separate hydrogen and oxygen
molecules. A certain amount of energy can be released. When the
hydrogen-oxygen bonding occurs, the excess energy under ideal conditions
can be released in a single package for each newly created bond. In
other words the excess energy is not dribbled out in multiple randomly
sized amounts of energy. This single package is called a virtual
photon and is illustrated in Fig 8. Photons are not marble like
objects but rather tiny localized vibrations of energy that travel
through the substratum or continuum of space. They cannot be
detected and so are called virtual. They are referred to as a
package because this energy does not split up traveling to its
destination and neither do two packages join together. This virtual
photon can under ideal conditions be transferred directly to other
chemical system through, for example close contact, without being spilled
to the surroundings. Such a transfer of energy can be equated to the
transfer of grains of sugar from one tank to another through a pipe. No
sugar would be spilled to the outside environment. Real
photons on the other hand are packages of energy that have broken
away as separate entities. It is as if the pipe between the tanks of
sugar is missing and the sugar spills on the floor. Light is
composed of such real photons. 17. FUEL CELLS vs HEAT
ENGINES
Fig 9 Heat engines are theoretically at a disadvantage compared to fuel cells The virtual photons that are transferred during
the chemical reactions in a fuel cell have a very high
temperament somewhere between 3,500° and 20,000° Kelvin.
It is this extremely high temperament that allows the fuel cell to be
theoretically so efficient. Generally textbooks relate Carnot's Law
only to the amount of external energy that can be extracted from thermal
energy systems. The same law however does apply to all internal energy
systems whether nuclear, chemical or thermal etc. The amount of external
energy that can be extracted from all types of internal energy is called
the carnot ratio. The carnot ratio for virtual photons of 3,500°K
is however about 92% under normal conditions. This is much higher
than for real photons in a gas turbine with a mean temperament of 1000°K
and a carnot ratio of 72%. The carnot ratio is based on a
particular ambient temperature of the surroundings. The carnot ratio only
relates to the absolute temperature scale where 0°C=273.15°K
degrees. 18. SECOND LAW ANALYSIS OF FUEL
CELLS
Fig 10 Exergic energy loss diagram for proposed 30 kw AC powerplants operating on hydrocarbon fuel In Fig 10 the exergic energy efficiency of three
proposed fuel cells are compared when operating on hydrocarbon fuel. The
fuel cell process is divided into six subsystems. In each subsystem
there are inefficiencies involved that reduce the exergic energy that is
left in the system. In all cases, the electricity that is extracted is
still considered to be part of the exergic energy of the system. It
appears that the SOFC 30 kw system will have an efficiency of 1.4 times
that of the PEFC and 1.3 times that of the DMFC. |
| SOFC | PEFC | DMFC | |||||||
|---|---|---|---|---|---|---|---|---|---|
| Subsystem | Y-eff | BE | YE | Y-eff | BE | YE | Y-eff | BE | YE |
| 0. Hydrocarbon fuel | - | - | 100.0 | - | - | 100.0 | - | - | 100.0 |
| 1. Reformer/Burner | 95% | 5.0 | 95.0 | 80% | 20.0 | 80.0 | 100% | 0 | 100.0 |
| 2. Stack electrical | 86% | 14.0 | 82.0 | 64% | 28.5 | 51.5 | 47% | 53.2 | 46.8 |
| 3. Stack thermal | 0% | 27.0 | 55.0 | 0% | 1.5 | 50.0 | 0% | 1.4 | 45.4 |
| 4. Pressurization | 98% | 1.0 | 54 | 78% | 10.8 | 39.2 | 90% | 4.6 | 40.8 |
| 5. System | 98% | 1.0 | 53.0 | 95% | 2.0 | 37.2 | 98% | 0.8 | 40.0 |
| 6. Inverter | 94% | 3.0 | 50.0 | 94% | 2.2 | 35.0 | 94% | 2.5 | 37.5 |
| Fig 11 Exergic energy efficiency of subsystems in 30 kw AC
powerplants operating on hydrocarbon fuel
19. SOME COMPANIES INVOLVED IN
RESEARCH 20. CONCLUSIONS 21. NOTES 22. REFERENCES 23.
SYMBOLS 24. REVISION
HISTORY COPYRIGHT © 1999-2004 by Ben Wiens Energy Science Inc. All rights reserved. |