| Authors |
H. Ida, M. Ono, N. Takasu, JFE Engineering; T. Ebinuma, National Institute
of Advanced Industrial Science/Technology
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| Source |
Carbon Management Technology Conference,
7–9 February 2012,
Orlando, Florida, USA
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| Preview |
Abstract
Carbon capture and storage (CCS) offers one of the most promising ways for
reducing the accumulation of greenhouse gases in the atmosphere. Currently
available post-combustion CO2 capture technologies lack the desired energy
efficiency, we have developed a CO2 capture technology which converts CO2 to a
hydrate under substantially atmospheric temperature and pressure
conditions.
Being cooled to a low temperature of 5 degree Celsius and a pressure of 2.2
MPa, CO2 containing water can separate out the only CO2 component as a solid
called a hydrate. This technology has long been known to enable separate CO2
from a mixed gaseous stream. However, practical application had been considered
difficult due to the high operating cost of high pressure and low temperature
conditions. We have discovered a phenomenon in which formation of the hydrate
of CO2 is produced under significantly eased conditions of pressure and
temperature by using a semi-clathrate hydrate such as tetra-n-butyl
ammonium bromide and other quaternary ammonium compounds. These quaternary
ammonium compounds form a semiclathrate hydrate crystal with water molecules
under atmospheric pressure.
Our preliminary result of X-ray diffraction shows that there are empty
dodecahedral cages. Therefore, semi-clathrate hydrates can be used to separate
small gas molecules that fit in these dodecahedral cages. We have found that
they could encage CO2 molecules at higher selectivity than nitrogen and oxygen.
We have performed a bench scale experiment to encage CO2 under substantially
atmospheric pressure and temperature conditions such that pressure of 0.12 MPa
and temperature of 18 degree Celsius, confirming the possibility of CO2 capture
under those conditions. Our feasibility study has revealed that the
operating
costs of carbon capture will be half compared to a conventional chemical
absorption process.
We expect to conduct larger scale tests in the future, preconditioned on a CCS
plant for CO2 capture of flue gas from thermal power plants and steel works
assumed CCS scale from 0.3 million to 1 million tons per year. The improved CO2
capture process with minimized energy demand will play a significant role for
the reduction of CO2 emissions.
1.Introduction
Atmosphere carbon dioxide is a focus of attention as one of the greenhouse
gases (GHG) which cause global warming. Early implementation of effective
measures to prevent global warming is strongly desired. One conceivable measure
for preventing global-scale warming is separation and capture of the CO2
contained in flue gas discharged into the atmosphere from thermal power plants,
steel works, factories, and other facilities in the course of industrial
activity, followed by fixation and effective utilization. This approach, if
possible, would make an important contribution to prevention of global
warming.
Various methods for separation and capture of CO2 from flue gas have been
proposed, including chemical absorption using an amine solution, physical
adsorption using an adsorbent, and membrane separation methods, among others.
However, in order to realize practical application of these technologies, the
cost of CO2 separation and capture must be substantially reduced, as this
accounts for a large part of the total cost of carbon dioxide capture and
storage (CCS).
This paper presents a hydrate-based CO2 separation and capture method which has
the potential for large cost reduction in comparison with conventional
techniques in CO2 separation and capture technology.
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