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Ms. Elisabet Fjermestad Hagen<br />

Norsk Hydro ASA<br />

Operating Agent for the<br />

Norwegian Research Council<br />

INTRODUCTION<br />

IEA Hydrogen Implementing Agree­<br />

ment Annex 16 concerns Hydrogen<br />

from Carbon­Containing Materials.<br />

The overall objective is to promote the<br />

processes for hydrogen production from<br />

fossil and biomass resources while<br />

keeping CO 2 emissions at a minimum.<br />

The activities are organised in three<br />

Subtasks:<br />

Hydrogen From Carbon­Containing Materials<br />

A: Large­scale integrated hydrogen<br />

production<br />

B: Hydrogen from biomass<br />

C: Small stationary reformers for<br />

distributed hydrogen production<br />

Subtask A is organised <strong>by</strong> the IEA<br />

Greenhouse Gas Programme. Subtask<br />

B and C are organised as work groups<br />

involving energy companies, suppliers,<br />

and institutes.<br />

Annex 16 has members from a large<br />

number of countries in Europe, the USA,<br />

Japan and Singapore. Current member<br />

<strong>de</strong>tails are listed in Appendix 1.<br />

TASK DESCRIPTION,<br />

ACTIVITIES AND<br />

RESULTS IN 2005<br />

The work in Subtasks A and C has<br />

report for Subtask B is currently being<br />

report for Task 16, together with recom­<br />

mendations for follow­up activities, will<br />

be submitted to the IEA HIA Executive<br />

committee for its Spring 2006 meeting.<br />

Subtask A is complete. An indus­<br />

try­led project, Subtask A focused on<br />

<strong>de</strong>signing a precombustion <strong>de</strong>carboni­<br />

sation (PCDC) power plant for <strong>de</strong>mon­<br />

stration purposes. It also investigated<br />

the potential for cost reduction through<br />

modularisation and standardisation of<br />

proven plant components. The task was<br />

divi<strong>de</strong>d into two stages.<br />

results of all relevant studies and review<br />

the process options on a common<br />

technical and economic basis. The aim<br />

was to examine each option with respect<br />

to cost and technical risk and select a<br />

small subset of preferred options. The<br />

results from this comparison were used<br />

to select a process scheme for a <strong>de</strong>­<br />

tailed engineering study in the second<br />

stage.<br />

The engineering study was mainly<br />

CCP (CO 2 Capture Project) is an inter­<br />

national initiative that inclu<strong>de</strong>s eight of<br />

the world’s leading energy companies:<br />

BP, Chevron Texaco, ENI, Hydro, En­<br />

Cana, Shell, Statoil, and Suncor Energy.<br />

The CCP’s objective is to <strong>de</strong>velop new<br />

low­cost technology options for CO 2<br />

capture and storage. Jacobs Consul­<br />

tancy, part of the international Jacobs<br />

Engineering Group, was selected to<br />

execute this study.<br />

The study contains a <strong>de</strong>tailed engi­<br />

neering evaluation of a complete natural<br />

plant based on air­blown autothermal re­<br />

forming. The study also covers integra­<br />

tion aspects, investigates cost reduction<br />

potential through standardization and<br />

repeat manufacturing, and provi<strong>de</strong>s a<br />

<strong>de</strong>tailed economic analysis, including<br />

a sensitivity analysis for gas price and<br />

availability. In addition, a market evalua­<br />

tion has been performed to estimate the<br />

“The work in<br />

Subtasks A<br />

and C has been<br />

completed, and<br />

reports have been<br />

report for Subtask<br />

B is currently being<br />

prepared <strong>by</strong> its<br />

1<br />

Subtask reports and<br />

report for Task 16<br />

will be submitted<br />

to the IEA HIA<br />

Executive committee<br />

for its Spring<br />

2006 meeting.”

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