H2A Case Study: Future Central Biomass
Project Summary
| Full Title: |
H2A Case Study: Advanced (2025) Hydrogen from Biomass via Gasification and Catalytic Steam Reforming |
| Project ID: |
230 |
| Principal Investigator: |
Darlene Steward |
| Keywords: |
Biomass; hydrogen production; gasifier; water gas shift (WGS); catalytic steam reforming |
Purpose
The purpose of this analysis was to determine the production cost of hydrogen from biomass via the
FERCO indirectly-heated gasifier.
Performer
| Principal Investigator: |
Darlene Steward |
| Organization: | National Renewable Energy Laboratory (NREL) |
| Address: | 1617 Cole Blvd. Golden, CO 80401-3393 |
| Telephone: | 303-275-3837 |
| Email: | Darlene_Steward@nrel.gov |
Sponsor(s)
Period of Performance
Project Description
| Type of Project: |
Analysis |
| Category: |
Hydrogen Fuel Pathways |
| Methodology/Approach: |
Material and energy balances in Aspen PlusĀ®, equipment costing in Questimate, cash flow analysis, sensitivity analysis (ref. Spath et al) |
| Models Used: |
H2A Production Model |
| Outputs: |
Production cost of hydrogen |
Products/Deliverables
| Notes/Comments: |
The systems examined are based on the Battelle/FERCO indirectly-heated biomass gasifier, conventional catalytic steam reforming, water gas shift, and pressure swing adsorption purification. The indirectly-heated biomass gasifier uses hot sand, circulating between the char combustor and the gasifier, to provide the heat necessary for gasification. Steam is used as the fluidizing gas; no oxygen (as pure oxygen or air) is fed to the gasifier. The biomass feedstock is assumed to be a woody biomass, represented as hybrid poplar. |
Date Last Updated: 09/29/2008