Hydrogen Fueling Infrastructure Analysis
Project Summary
| Full Title: |
IEA Hydrogen Annex 13 Transportation Applications Analysis |
| Project ID: |
142 |
| Principal Investigator: |
S.M. Schoenung |
| Brief Description: |
The goal of this analysis is to aid decisions regarding hydrogen stations and components. Gaseous and liquid hydrogen refueling alternatives, various vehicle configurations, driving cycle implications, and cost variations are considered. |
| Keywords: |
Hydrogen; infrastructure; refueling; electrolyzer; reformer; pipeline; tailpipe emissions |
Purpose
To contribute to the discussion on preferred choice of fueling options and hydrogen distribution alternatives.
Performer
| Principal Investigator: |
S.M. Schoenung |
| Organization: | Longitude 122 West |
| Address: | 1010 Doyle Street, Suite 10 Menlo Park, CA 94025 |
| Telephone: | 650-329-0845 |
| Email: | schoenung@aol.com |
Sponsor(s)
Period of Performance
| Start: |
May 2000
|
| End: |
June 2002
|
Project Description
| Type of Project: |
Analysis |
| Category: |
Environmental, Hydrogen Fuel Pathways, Vehicle Options |
| Objectives: |
Cost of hydrogen dispensed to vehicle; vehicle fuel economy; footprints for refueling stations; local emissions |
| Technologies Considered: |
1. Bulk liquid hydrogen from an existing central reformer transported to the refueling station by truck, stored as a cryogenic liquid and dispensed to the vehicle as a liquid.
2. Bulk liquid hydrogen from an existing central reformer transported to the refueling station by
truck, stored as a cryogenic liquid and dispensed to the vehicle as a gas.
3. Bulk gaseous hydrogen transported to the refueling station by existing pipeline, stored as a
compressed gas at 5000 psi and dispensed to the vehicle as a gas. This case is valid only
where there is a nearby pipeline. (Pipeline construction costs were not considered.)
4. Gaseous hydrogen generated at the refueling station from natural gas by steam methane
reforming, stored as a compressed gas at 5000 psi and dispensed to the vehicle as a gas.
5. Gaseous hydrogen generated at the refueling station from natural gas by a partial oxidation
process, stored as a compressed gas and dispensed to the vehicle as a gas.
6. Gaseous hydrogen generated at the refueling station by electrolysis, stored as a compressed
gas at 5000 psi and dispensed to the vehicle as a gas. (For the present analysis, grid
electricity is assumed to power the electrolyzer. Renewable electricity may be considered
later.) |
| Methodology/Approach: |
Excel spreadsheet |
| Outputs: |
Capital cost of fueling components; delivered cost of hydrogen; footprint area; fuel economy; CO emissions; NOx emissions; HC emissions; greenhouse gas emissions |
| Sensitivities Studied: |
Impact of under-utilization of the refueling stations; impact of cost of on-site hydrogen production units |
| Timeframe Studied: |
2005 - 2015 |
Products/Deliverables
| |
Description: Conference Paper Publication Title: Proceedings of the 2001 Hydrogen Program Review Meeting Article/Abstract Title: IEA Hydrogen Annex 13 Transportation Applications Analysis Publisher: U.S. Department of Energy Type of Publication: Conference Paper Author Name(s): Schoenung, Susan
(PDF 248 KB) Download Adobe Reader.
Publication Date:
May 2002
|
Date Last Updated: 12/18/2006