Abstract
As part of Task 2, Gas Cleanup and Cost Estimates, Nexant investigated the appropriate process scheme for removal of acid gases from black liquor-derived syngas for use in both power and liquid fuels synthesis. Two 3,200 metric tonne per day gasification schemes, both low-temperature/low-pressure (1100 deg F, 40 psi) and high-temperature/high-pressure (1800 deg F, 500 psi) were used for syngasproduction. Initial syngas conditions from each of the gasifiers was provided to the team by the National Renewable Energy Laboratory and Princeton University. Nexant was the prime contractor and principal investigator during this task; technical assistance was provided by both GTI and Emery Energy.
Original language | American English |
---|---|
Number of pages | 51 |
State | Published - 2006 |
Bibliographical note
Work performed by Nexant, Inc., San Francisco, CaliforniaNREL Publication Number
- NREL/SR-510-39944
Keywords
- biomass
- black liquor
- fluidized catalytic cracking
- National Renewable Energy Laboratory (NREL)
- natural gas liquids expanders
- Nexant
- NREL
- scaling
- small modular
- steam methane reforming
- syngas
- synthesis gas