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A N N U A L R E P O R T 2 0 1 5

18

CaO) at different operating conditions. We

have initiated a modelling activity to describe

and analyze observed performance trends,

and have applied in-situ X-ray diffraction and

in-situ Infrared Spectroscopy.

• The Chemical Looping Combustion model was

developed further to include hydrogen as fuel.

The model was used to simulate industrial

steam generation processes for refineries and

benchmark against gas boilers.

Application to industry and offshore

• A model for CO

2

capture from refineries using

MEA was established in HYSYS. The model

was automated by developing a HYSYS Visual

Basic tool to manipulate parameters, run case

studies and export results to Excel. The effect

of CO

2

capture rate on the specific reboiler

duty was studied.

• Steam cycle design for an offshore oil and gas

installation with CO

2

capture was performed

keeping in mind the constraints of space

and weight. Three different steam cycle

configurations were designed, modelled, and

simulated. In addition to the energy and mass

balance results, a weight assessment of the

major equipment was done.

• Collaboration with SP4 to include the

attainable region approach for design of

membrane processes.

Integrated assessment

• Review paper “Hydrogen production with CO

2

capture” submitted to International Journal

of Hydrogen Energy. The paper provides

an overview of technology option for H

2

production from fossil fuels with CO

2

capture.

• Sizing and costing has been undertaken for

the Natural Gas Combined Cycle (NGCC)

power plant with solvent capture for MEA and

a Novel Generic Solvent (NGS), and also for

the NGCC with Ca-looping capture.

• CO

2

capture for the NGCC with polymeric

membranes (90% capture rate) was

investigated for three different combustion

configurations: conventional gas turbine, gas

turbine with exhaust gas recirculation (EGR)

and gas turbine with EGR + Supplementary

Firing (SF). The NGCC + EGR option was found

to have the best performance with a capture

penalty of ~10%-points. However, the study

clearly indicates that membrane capture from

the NGCC has its optimum performance at

lower capture rates (~60%).

HIGHL IGHT

From #SINTEF energy blog

Hydrogen cars: The role of fossil fuels and CCS in a cleaner transport system

Kristin Jordal, David Berstad and Petter Nekså

In short, a possible solution for hydrogen

production for cars could be to use fossil fuels.

We will tell you why and how!

Currently, road transport contribution to

global CO

2

emissions is around 23%.