Mel’nick V.N., Trivailo M.S., Karachun V.V.,
Mikul’onok I.O.
National Technical University of Ukraine “KPI”
THE BIOREAKTOR OF COMBUSTIBLE GAS
The utility model relates to biotechnology, namely, to equipment for
processing (recycling, disposal) of organic substances and can be used to
obtain gas from burning of waste from agricultural estates.
The known combustible gas bioreactor
(CGB) for waste of agricultural estates, which contains elastic in the form of
a bag reservoir for the anaerobic fermentation of organic waste in it,
supporting tank, hard case and located in the cavity of the reservoir mixing
device (see, Ukraine Patent for an invention ¹ 28685 , C 02 F 11/04, 2000).
The disadvantage of this CGB is insufficient strength of elastic
reservoir, which reduces reliability.
It is also known aCGB which contains fillable with processed matter
(biomass) metal case with technological pipes and compressor device for the
recirculation blow of body (see, À. ñ. ÑÑÑÐ ¹ 1715715, Ñ 02 F 11/04, 1992).
This CGB disadvantage
is that it does not provide control of temperature of processed biomass, that
slows down the activity of methane-cenerating bacteria and leads to lower
productivity.
As the closest to useful model at technical essence and reached effect
it is taken as the nearest equivalent CGB containing fillable with processed
biomass vertical cylindrical body with pressure relief pipe, massheater and
device for mixing, and covering body with the gap heat-insulating hermetical
jacket with gas sempler at the top and outside joined to pressure relief pipe
bottom (see, Ukraine Patent for an invention ¹ 70885, C 02 F 11/04, 2004).
The disadvantage of
known CGB is significant heat loss and increased dimensions in consideration of
joining of pressure relief pipe to the upper wall of the body and its external
position.
The basis of the utility model is a task to improve CGB, in which by
changing the joining of pressure relief pipe to the body and its location the
heat loss are eliminated and dimensions oh CGB are reduced.
A task is solved that in CGB, which contains fillable with processed
biomass vertical body with pressure relief pipe, heater and a device for mixing
and covering body with the gap heat-insulating hermetical jacket with gas sampler
at the top, according to a utility model the new is that pressure relief pipe
is joined to the bottom and body and is located with the gap concerning its
upper wall.
These distinctive features comparing with the nearest equivalent
eliminate tube contact with the surrounding environment that reduces heat loss
and dimensions. This improves the heating of biomass, especially the lower, the
coldest part that activates the vital activity of bacteria increases the
intensity of the made by them gas and improves productivity.
The drawing schematically shows announced CGB section (fig. 1).
Fig. 1
CGB contains fillable with processed biomass 1 vertical body 2 with
pressure relief pipe 3, heater 4 and a device for mixing 5 as well as covering
with the gap body 2 heat-insulating jacket 6 with gas sampler 7 at the top.
Pressure relief pipe 3 is connected to the bottom of body 2 and forms a gap 8
with its upper wall (cover) 9.
In the best performance pipe 3, on which it is fixed a heater 4, it is
desirable to produce of a material which has a larger than body 2 thermal
conductivity, such as aluminum, copper or brass, that promotes a more equitable
distribution of heat in the height of biomass in the tank.
Device 5 for mixing biomass 1 is fixed on the lid 9 of body 2 and
contains set on a shaft of gear-motor 10 disk 11with vanes 12 and body 2 has
closing nipples 13, 14 for a fresh and remove of the spent biomass.
The CGB works in next way.
Diluted with water
biomass is placed in body 2 and warm temperatures to 25-35 º C, after what
in definitive time anaerobic fermentation with gas emission appears there. Gas
generated by bacteria enters through the pipe 3 into gaps 15 between the body 2
and its jacket 6 and, partly giving heat to the lower parts of biomass 1,
removes through the nipple 7 for use.
As gas outlet pipe 3 contacts with the biomass 1, that is not present in
the nearest analogue, and transmits its accumulated heat with gas in the volume
of biomass, instead of transferring it to the air surrounding jacket in
analogue, so expenditure of energy for biomass heating (with heater) are
reduced. Thus, flowing through pipe 3, gas extra warms central parts of
biomass, that is also not present in the nearest analogue, resulting increasing
of evenness distribution of heat along height of biomass. Increase of
uniformity of heat along the height of biomass intensifies its processing of
bacteria, that increases gassing and therefore productivity.
Reducing of heat loss and reduce of the size while increasing
productivity increases the efficiency of CGB.