问题描述:
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To the best of our knowledge, simultaneous removal of H2S
and CO2 has never been explicitly studied before. Recent
studies 22-24 on simultaneous SO2 and CO2 removal based on a
PFBC/calciner process 1,2 have shown that SO2 inhibits the
reversibility for CO2 capture. The objective of the current study
was to investigate whether H2S has a similar deleterious effect
on sorbent reversibility in a pressurized gasifier (PG)/calciner
process.
2. Experimental Details
The pressurized TGA (PTGA) system consists of a Cahn 100
balance of 1 íg precision, a reactor column, and a control
system. The reactor is made of Inconel 600 alloy, allowing high
temperatures and high pressures to be used. The desired gas
concentrations were achieved by means of computer control of
Co-capture of H2S and CO2.
To the best of our knowledge, simultaneous removal of H2S
and CO2 has never been explicitly studied before. Recent
studies 22-24 on simultaneous SO2 and CO2 removal based on a
PFBC/calciner process 1,2 have shown that SO2 inhibits the
reversibility for CO2 capture. The objective of the current study
was to investigate whether H2S has a similar deleterious effect
on sorbent reversibility in a pressurized gasifier (PG)/calciner
process.
2. Experimental Details
The pressurized TGA (PTGA) system consists of a Cahn 100
balance of 1 íg precision, a reactor column, and a control
system. The reactor is made of Inconel 600 alloy, allowing high
temperatures and high pressures to be used. The desired gas
concentrations were achieved by means of computer control of
Co-capture of H2S and CO2.
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