Biomedical Engineering Reference
In-Depth Information
TABLE 9.4
Global Kinetic Rate of Gasification of Model Compound in SCW
Mettanant
et al. (2009b)
Lee et al.
(2002)
Kabyemela
et al. (1997)
Blasi et al. (2007)
Feed
Waste water from
wood gasifier/TOC
Rice husk
Glucose/
COD
Glucose
Reactor
Plug
Batch
Plug
Plug
Temperature (K)
723
821
673
873
740
1023 573
673
Residence time (s)
60
120
3600
16
50
0.02
2
Solid content
7
15 g(Toc)/l
9.4 mol/l
0.6 mol/l
0.007 mol/l
Preexponential,
A (s 2 1 )
897
184
897
6
29
Activation energy,
E (kJ/mol)
76
77.4
71
6
3.9
96
k g (s 2 1 )
0.002
0.003
0.0002
0.006 0.01
0.55 0.15
9.9
9.7 REACTOR DESIGN
Because SCWG is likely to enter the market once its major development bar-
riers are removed this section discusses important considerations for design of
an SCWG reactor. The discussion is based on limited information available in
laboratory units and on the design of thermal gasifiers (see Chapter 8).
The major design parameters for an SCWG reactor are temperature, resi-
dence time, pressure, catalysts, and feed concentration. Important design con-
siderations for auxiliary or support equipment are (1) waste heat-recovery
exchanger and feed-preheating system, (2) the biomass feed system, and
(3) product separation. The following subsections present a brief discussion
of some of the design parameters.
9.7.1 Reactor Temperature
The temperature and pressure of an SCWG must be above the critical value of
374.21 C and 22.089 MPa, respectively. As explained in Section 9.4.7 ,pressure
has a minor effect on biomass conversion, but the effect of gasification tempera-
ture is a major one (see also Section 9.4.1 ).
Because feedstock (biomass and water) must be heated to the reaction tem-
perature using energy from an external source, the lower the designed reactor
temperature, the lower the energy required for feed preheat and the more effi-
cient the process. The gasification temperature should be above 600 Cforarea-
sonable hydrogen yield, but it can be lower if catalysts are used.
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