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Auto Industry Analysis Report

Mar. 3, 2007 No.554


Development of New On-board Hydrogen Power Technologies:
DME Reforming, Organic Hydride, Hydrogen Inclusion Storage, and More

Reports on DOE's Hydrogen Posture Plan and
automotive technologies exhibited at FC EXPO 2007



  Development of fuel cell vehicles is now shifting from the first generation, with fuel cells onboard existing auto-bodies, to the second generation, in which the bodies for fuel cell vehicles themselves are developed. As a result, an increasing number of demonstration vehicles have been developed and, during the course of development, the developers faced a need of increasing their vehicle's resistance against high temperatures. Meanwhile, efforts are being made worldwide to build the necessary infrastructure of fuel supply toward the time goal set to 2015.

  Introduced below are the Hydrogen Posture Plan (published in December 2006 by the US Department of Energy) that set the time schedule to the hydrogen-powered society and the targeted price of hydrogen, the trial calculation of the cost of manufacturing on-board hydrogen fuel by Japan Hydrogen & Fuel Cell Demonstration Project (JHFC), and the new technologies exhibited at the FC EXPO 2007 that may be applied to on-board hydrogen systems.

(Note) The Third International Hydrogen & Fuel Cell Expo (FC EXPO 2007) held in February 2007 at Tokyo Big Sight, Japan (held by Read Exhibitions Japan, Ltd.), drew more than 500 exhibitors.

  Among the technologies from the FC EXPO 2007 and outlined below are hydrogen manufacture by dimethyl ether (DME) reformation (Osaka Gas), hydrogen manufacture by electrolysis of ammonia (Acta, Italy), on-board hydrogen system by organic hydride (Hitachi), and hydrogen inclusion storage (Kurita Water Industries). They all represent greater advantages in principle over the onboard systems of pressurized gases.


■US DOE: Time schedule to the hydrogen-powered society (December 2006)

  The Bush administration ended PNGV (Partnership for a New Generation of Vehicles; an industrial-governmental joint project aimed at drastically increasing automotive fuel efficiency) that was introduced by the Clinton administration. Nevertheless, President Bush announced the "Hydrogen Initiative" in the State of the Union Message for 2003, aimed at conversion to the hydrogen energy society.

  In December 2006, the US Department of Energy published "Hydrogen Posture Plan - An integrated Research, Development and Demonstration Plan" in which the time schedule toward the hydrogen-powered society by the US government was clarified.

(Note) The Hydrogen Posture Plan summarizes a series of energy measures being promoted by the US government according to the Energy Policy Act of 2005. It contains inclusive reports, all arising from hydrogen, ranging from fuel cell vehicles to the manufacture, transport, storage and distribution of the fuel hydrogen as well as electric power generation using stationary fuel cells.
  The Hydrogen Posture Plan covers National Energy Policy, Energy Policy Act of 2005, DOE Strategic Plan, A National Vision of America's Transition to a Hydrogen Economy to 2003 and Beyond, and a National Hydrogen Energy Roadmap.

■US DOE's time schedule toward the hydrogen-powered society (announced in December 2006)
Transional Phase Period Outlines
I. Technology Development 2000-2030 Research to meet technology performance and cost targets and establish technology readiness
II. Initial Market Penetration 2010-2025 Portable power and stationary/transport systems are validated; infrastructure investment begins with governmental policies
III. Expantion of Markets
and Infrastructure
2015-2035 H2 power and transport systems commercially available infrastructure business case realized
IV. Fully Developed
Markets and Infrastructure
2025- H2 power and transport systems commercially available in all regions; national infrastructure
Source: Hydrogen Posture Plan, Dec. 2006, United States Department of Energy

■Targeted cost of hydrogen set to $2~3/gge

  The DOE report introduces the outcome of past efforts on the manufacture and storage of fuel hydrogen, and future goals of the same.

  On the ground that the fuel cell vehicles (FCV) must be equal to or better than, in terms of fuel economy, the gasoline-fueled vehicles or the hybrid vehicles that are expected to penetrate the market, the report sets the targeted cost of hydrogen prevailing in 2015 at $2~3/gge (gge: per gallon of gasoline equivalent; 1 gge is roughly equivalent to the heating value of 1kg of hydrogen).

(Note) The US DOE has defined the priority ratio of fuel economy of FCV to gasoline-fueled vehicles to be 2.4, and that to hybrid vehicles to be 1.66. DOE has also estimated the price of gasoline before tax to be $1.29/gallon in 2015 (DOE's Energy Information Administration Annual Energy Outlook 2005). Consequently, DOE calls that the price of hydrogen must be $2/gge for the FCV to compete with hybrid vehicles, and $3/gge to compete with gasoline-fueled vehicles.

■US DOE's trial calculation: Cost of hydrogen by on-site reformation of natural gas to be $3.10/gge today, $2.0/gge in the future

  Since transporting hydrogen costs some money, it is believed, at least in the penetration phase of FCV, it is economical to manufacture hydrogen by reforming natural gas at the site of hydrogen supply.

  The US DOE has built the world's first energy station for producing electricity and hydrogen from natural gas and, based on the result of the station operation, evaluates that hydrogen can be supplied at $3.10/gge once such an energy station is built in a large number (the cost of hydrogen at the energy station was $5.00/gge in 2003). The Department also estimates the price can be reduced to $2.0/gge by 2015 by means of engineering improvement.

■US DOE's trial calculation: Cost breakdown of hydrogen by natural gas reforming at $3.10/gge
Natural gas Infrastructure Running cost Other costs
30% 44% 18% 8%
Source: Hydrogen Posture Plan, December 2006, United States Department of Energy


■Japanese targets: 50,000 FCVs in 2010

  Japanese Government is also making special efforts toward the commercial application of fuel cells based on the report presented by the Fuel Cell Implementation Strategy Study Group, an advisory organ of the Agency for Natural Resources and Energy under the Ministry of Economy, Trade and Industry. The Group estimates the market penetration of FCVs to be 50,000 vehicles in 2010.

■FCV penetration goals in Japan
Time Phase Measures
2000-2005 Infrastructure and
technical demonstration
Technical development strategies
Systems and other infrastructures
Demonstration testsFuel quality standards
2005-2010 Introductory stage
50,000 vehicles in 2010
Fuel supply and other systems
Positive use by public institutions and industries
2nd phase FC technology development strategy
2010- Market penetration
5,000,000 vehicles in 2020
Consolidation of fuel supply system
Cost reduction
Introduction to general consumers
Source: Fuel Cell Implementation Strategy Study Group (an advisory organ of the Agency for Natural Resources and Energy under the Ministry of Economy, Trade and Industry)

  In 2000, the Ministry of Economy, Trade and Industry began subsidizing the Japan Hydrogen & Fuel Cell Demonstration Project as a measure to achieve the above goals. Phase 1 of the subsidy measure ended in March 2006. The manufacturers involved in the project exhibited their FCVs and other results of development efforts, by means of test driving and panels, at the FC EXPO 2007.

■Japan Hydrogen & Fuel Cell Demonstration Project: Outcome of Phase 1 (ended March 2006)
FCV feasibility study   Public road tests of FCVs (including buses) by 8 auto manufacturers to gather, analyze and evaluate data about drivability, reliability and fuel efficiency.
Demonstration study
of hydrogen supply
facilities for FCVs
  Nine hydrogen stations completed based on 9 different fuels and manufacturing methods (desulfurized gasoline reforming, naphtha reforming, LPG reforming, liquefied hydrogen storage, methanol reforming, pressurized hydrogen storage, alkali electrolysis, kerosene reforming, and city gas reforming)

■Energy efficiency of hydrogen station 65~77%, calculated cost of hydrogen manufacture ¥1,100~¥2,000/kg

  Based on the result of evaluation of the demonstration station, the JHFC Project has determined the efficiency of energy conversion to be 65 to 77% when liquefied fuel, gaseous fuel and electricity were supplied to the hydrogen station and hydrogen was manufactured there.

  Based further on that energy conversion efficiency level, the cost of manufacturing hydrogen by the on-site reforming process in the commercialized stage was estimated at ¥100 to ¥180/Nm3 (¥1,100 to ¥2,000/kg) versus ¥40 to ¥80/Nm3, targeted price for the popular penetration of FCVs.

  The project revealed, once again, the need for further technical development and cost reduction, among others, in terms of hydrogen supply before all conditions are met for market penetration of FCVs.

■JHFC Project's trial calculation of energy efficiency of the on-site hydrogen manufacturing process
Process Naphtha reforming Methanol reforming City gas reforming Alkaline water
electrolysis
Energy efficiency 65% 76.6% 73% 71%
Source: JHFC Seminar on "Hydrogen Station Area Test Results" (FY2005)
(Notes) 1. Energy efficiency is based on the low heating value (LHV).
2. Energy efficiency was calculated under the following conditions: Hydrogen manufacturing capacity of a hydrogen station at 27.0kg/h; the station's supply capacity of 351kg per day (13 hours, 10 vehicles per hour average, 20 vehicles per hour maximum); average fill of 2.7kg per vehicle; vehicle's hydrogen tank pressure of 35MPa; a reforming oven of on-site hot reforming process using hydrocarbon material having an oven temperature of 790°C and pressure of 1.1MPa.
3. Trial calculation of the cost of manufacturing hydrogen assumes the following: Production scale of 300NM3/h, raw material cost of ¥35,000 to ¥47,000/kL, construction cost of ¥470M to ¥590M; and targeted depreciation time of 5 to 10 years.


■New technologies for on-board hydrogen system at FC EXPO 2007: Organic hydride technology by Hitachi, hydrogen inclusion storage by Kurita Water Industries

  The demonstration FCVs currently running in Japan carry a 35MPa or 70MPa pressurized hydrogen tank. Since the amount of hydrogen storage cannot be increased by increasing the pressure alone, each fill is not large enough for desired driving distance.

  Introduced below are some of the technologies that were exhibited at FC EXPO 2007, namely hydrogen manufacture by dimethyl ether (DME) reformation (Osaka Gas), hydrogen manufacture by electrolysis of ammonia (Acta, Italy), on-board hydrogen system by organic hydride (Hitachi), and hydrogen inclusion storage (Kurita Water Industries). They all represent greater advantages in principle over the onboard systems of pressurized gases.

■Osaka Gas: Hydrogen manufacturing technology by dimethyl ether reforming

  Dimethyl ether (DME:CH3OCH3) is suitable for manufacturing hydrogen by reforming at lower temperatures compared to methane, the main component of natural gas. DME is liquefied at 0.6MPa under normal temperature, and it also has portability similar to that of propane or butane.

  Osaka Gas, as a member of JOGMEC (Japan Oil, Gas and Metals National Corporation), is currently in the process of developing technology for producing hydrogen from DME. The company recently announced it had completed a compact reforming device for use on FCVs. The device, featuring a Cu-Zn-alumina catalyst that was also developed by the company, has durability over 3,000 hours.

Dimethyl ether reforming device developed by Osaka Gas
Dimethyl ether reforming device developed by Osaka Gas

■Osaka Gas: Hydrogen manufacturing technology by dimethyl ether reforming
Estimation of the volume and mass of the entire fuel system, and the same
of the fuel portion of the system, assuming the required amount of fuel of
the FCV for running 500km to be 6kg (effective amount of hydrogen 5.8kg).
The company has concluded that the on-board DME reforming is the best on-board hydrogen supply system.
  Hydrogen gas(35MPa) Hydrogen gas(70MPa) Metal hydride
(Hydrogen content 3%)
DME reforming
System volume (L) 316 157 653 127
Fuel volume (L) 210 105 50 37
System mass (kg) 117 62 692 178
Fuel mass (kg) 6 6 200 24
Source: "Development of a dimethyl ether vapor reforming system for fuel cells" (Tetsuya Takemoto, et al)
No.51 Study Reporting Session of the Kansai Branch of the Japan Institute of Energy,
P32-35 (taken from leaflets distributed at FC EXPO 2007).

■Acta: Hydrogen manufacturing technology by ammonia electrolysis

  Acta, an Italian venture company (represented in Japan by Sumitomo Corporation), has developed a platinum-free catalyst, made by dispersing extremely fine cobalt, nickel, iron and other base metals 0.3 to 0.7nm (nanometer) in size over a special resin, then reduced on a porous carbon film.

  Acta exhibited technology for generating hydrogen under normal temperature and pressure by applying the catalytic technology to developing a new catalyst used for electrolysis of ammonia.

■Ammonia as an ideal carrier of hydrogen
Hydrogen and nitrogen are produced from electrolysis of ammonia.
Since the produced gases do not contain CO or other components that affect the
performance of fuel cells, Acta's process does not require refining of hydrogen.
Ammonia contains 17.6% of hydrogen per mass.
Does not contain carbon and thus does not generate CO2 when used on FCVs.
Easy to liquefy, store and transport (ammonia pipelines exist in US).
Energy requirement for electrolysis of ammonia is 5% of that required for electrolysis of water
(theoretical value).

■Hitachi: Hydrogen supply to FCVs by an organic hydride system

  Studies are under way in many places with regard to chemical reaction between hydrogen and benzene (C6H6), naphthalene (C10H8), etc., to turn them into cyclohexane (C6H12), decalin (C10H18) or other forms of organic hydride for ease of transporting and storing. Hitachi exhibited its technology to reform organic hydride, transported to the fuel station, in an on-board reforming device and produce hydrogen which is then supplied as fuel for fuel cell vehicles.

Hydrogen supply system for fuel cell vehicles using organic hydride as hydrogen carrier
Hydrogen supply system for fuel cell vehicles using organic hydride as hydrogen carrier

■Organic hydride system proposed by Hitachi
Hydrogen storage capacity of the organic hydride system is the same as a 70MPa cylinder.
Transportable and storable in liquid form under normal temperature and pressure.
Zero CO2 emission from vehicles.Existing gasoline infrastructure can be used.
After being reduced to benzene or naphthalene by the on-board reforming device, the source
liquid is pumped out at the fuel station from the vehicle and returned to the organic
hydride plant where hydrogen is added and it is regenerated as cyclohexane or delican.

■Kurita Water Industries: Inclusion technology for storing hydrogen in molecular form

  Kurita Water Industries announced a clathrate compound process for storing hydrogen in the included form in which the hydrogen molecules are included in the crystalline lattice of the host material. Compared to the use of hydrogen storing alloys in which the hydrogen molecules are broken into hydrogen atoms and stored in the crystalline lattice of the metal, the hydrogen molecules are stored directly in the inclusion storage process. This means the system requires less energy to store and discharge hydrogen.

■Kurita Water Industries: Inclusion technology for storing hydrogen in the molecular form
Kurita Water Industries: Inclusion technology for storing hydrogen in the molecular form
Source: Kurita pamphlets distributed at FC EXPO 2007

■Kurita Water Industries: Hydrogen inclusion storage (clathrate compound) technology
Lighter in weight than hydrogen storage alloy system and lower in pressure (safer) than compressed
hydrogen system; suited for repetitive use (environmental and economic advantages).
  Inclusion technology Other storage technologies Targets
(FCV tank)
Hydrogen storage alloys High-pressure compression
Mass density (wt%) 6 (target) 2-3 4-5 >5
Volume density (kg-H2/m3) 50 (target) 22-50 25 50 or higher
Storage pressure (MPa) <1 <1 70 <1
Repetitive use Possible Unlikely Possible 2,000 times or more
Safety ×

  Kurita Water Industries has not disclosed the identity of the host material. Kurita exhibited an image of using its inclusion storage technology. Kurita also exhibited solid methanol solidified by the clathrate compound process instead of hydrogen.

(Note) Methane hydrate, one of the deep-sea resources being studied as a promising source of
energy in the future, is a form of methane gas that is included in water and then crystallized.

Image of the flow of hydrogen by the hydrogen inclusion technology
Image of the flow of hydrogen by the hydrogen inclusion technology
Hydrogen is stored in the white powder inside the pressured tank (far-left).
When the valve is opened, hydrogen flows out and is supplied to fuel cells.

■Hydrogen supply devices to fuel cell vehicles

  Special hoses and couplers that do not allow hydrogen gas leakage are required to supply pressurized hydrogen from the dispenser to the fuel tank onboard the fuel cell vehicle. Necessary efforts are being made in the development of these auxiliary components as more hydrogen supply stations are erected.

■Main exhibits of hydrogen gas supply hoses and couplers
Exhibitor Description
WEH GAS
TECHNOLOGY
■Quick-fill nozzles for self-service stations
  Self-service hydrogen gas filling stations are likely to be a common scene as the market penetration of FCVs develops. WEH GAS TECHNOLOGY envisages drivers filling hydrogen in their vehicles as they do now at self-service gasoline stations.
  Nozzles on display resemble those currently found in gasoline stations. Allowed to test its operation, the reporter thought the nozzle was very light and clean even for female drivers. (Represented in Japan by Hamai Industries)
Nitto Kohki ■High-pressure (70MPa) hydrogen fill couplers
  (1) Locking mechanism to ensure safety during fill operation, (2) Easy attaching and detaching mechanism in conjunction with the vehicle side receptacle.
Yokohama Rubber
Iwatani Industrial Gases
■Resin hoses for 35MPa-class hydrogen infrastructures
  Improvements over conventional products: (1) 4-folds greater bendability (2) Approx, 50% greater flexibility, (3) Approx. 30% reduction of hydrogen gas permeability, (4) Approx. 35% reduction in hose mass.

Hydrogen fill nozzle by WEH GAS TECHNOLOGY
Hydrogen fill nozzle by WEH GAS TECHNOLOGY

High-pressure )70MPa) hydrogen fill coupler by Nitto Kohki
High-pressure (70MPa) hydrogen fill coupler by Nitto Kohki

Resin hose for 35MPa-class hydrogen infrastructures (ibarHG35) by Yokohama Rubber and Iwatani Industrial Gases
Resin hose for 35MPa-class hydrogen infrastructures (ibarHG35)
by Yokohama Rubber and Iwatani Industrial Gases


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