Apparatus and method for conversion of animal litter biomass into useful energy

Abstract

A method of converting animal litter biomass into useful energy includes the steps of both combusting and pyrolising the biomass, of mixing the resultant combustible gas from the pyrolysis step with the gases from the combustion step, of igniting the mixture of gases ad and feeding the hot mixture of gases to a thermal recuperator; and apparatus therefor.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

Further aspects and advantages of the present invention will become better understood with reference to the description in association with the following Figures, in which similar references used in different Figures denote similar components, wherein:

FIG. 1 is a diagrammatic vertical cross section of an apparatus for the conversion of animal litter biomass in accordance with the present invention;

FIG. 2 is a horizontal section taken through one embodiment of the apparatus shown in FIG. 1;

FIG. 3 is a horizontal section taken through an alternative embodiment of the apparatus shown in FIG. 1; and

FIG. 4 is a fragmented view on the line 4-4 in FIG. 3.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

With reference to the annexed drawings the preferred embodiment of the present invention will be herein described for indicative purpose and by no means as of limitation.

Referring first to FIG. 1 there is shown diagrammatically an apparatus 1 for the conversion of animal litter biomass into useful energy, the apparatus including a generally hollow cylindrical body 2 enclosing a primary combustion zone 4 of frusto-conical form vertically oriented centrally within the body 2, the zone 4 having an upper region 5a and a lower region 5b. The zone 4 has connected at its top part a feed tube 6 which registers with an opening 7 in the top 8 of the body 2.

A feed hopper 10 is disposed vertically above the opening 7 and has a rotatable drive spindle 9 carrying a plurality of comminuting paddles 11; the hopper 10 has an outlet 13 feeding onto a rotating feed table 14 provided with a discharge station 15 selectively aligned with the opening 7 and the outlet 13. In use feedstock, namely the biomass, is fed into the hopper 10 wherein it is comminuted prior to delivery to the combustion zone 4.

Alternatively, as it would be obvious to one skilled in the art, the feedstock, typically fed from a conveyor (not shown), can be directed into the hopper 10 free of any spindle 9 and paddles 11, or even directly fed into the feed tube 6 through opening 7, without deviating from the scope of the present invention.

At the base of the combustion zone 4 there is provided a circular rotatable grate 20 the diameter of which is greater than the base dimension of the zone 4 which is spaced therefrom to provide a path in use for the centrifugal conveyance of incandescent biomass. The biomass located in the upper region of the combustion zone 4 is heated and dried by the heat generated by the incandescent biomass to form a pyrolysis zone. At the center of the grate 20 is a foraminous conical plenum chamber 22 for the introduction of air into the combustion zone 4, an air inlet pipe 24 being connected thereto and extending therefrom the exterior of the body 2. A drive shaft 26 for the grate 20 extends through the pipe 24 for rotating the grate. A solid waste collection area 30 is defined beneath the rotatable grate 20 and a discharge outlet 32 is provided for that area and leads to a removal station 34.

A secondary, normal combustion zone 40 is defined externally of the primary zone 4 and is provided with perforated air distributor tubes or sparge pipes 42 to provide air for the combustion.

Both the zones 4 and 40 are contained within a central cylindrical core 50, which is provided with suitable outlets 52 and 54 respectively for said zones, a gas discharge conduit 53 connecting the zone 4 to the outlet 52.

A gas mixing chamber 60 is defined between the core 50 and the wall of the body 2 at the exit from the zones 4 and 40 and in this chamber the gases arising from pyrolysis and the combustion zones are mixed. Thence the mixture of gases flows through into a heat exchange zone 59 including a tube bank 61 formed in the annular space between the core 50 and the wall of the body 2. In FIG. 2 the post-combustion zone tube bank 61 extends substantially throughout the whole of the annular space, the tubes 61′ being held in tube plates 63 and being disposed in spaced relation one to the other with baffles 62′ accommodated within the interstices between the tubes. The successive baffles 62′ are alternately raised and lowered along the tubes 61′ to force the hot gaseous product to vertically flow through the tubes 61′, as illustrated by the alternating orientations of arrows around the baffles 62′ in FIG. 2. In FIG. 3 the annular space is only partially, e.g. half, filled with a demi-tube bank 61 with tubes 61″, the remainder of the space being provided with offset baffles 62″. Baffles 62′ and 62″, essentially vertically oriented, are provided as shown to enhance in practice the turbulence of gases and to lengthen residence to time thereby to optimize the various steps of mixing and suppression of noxious emissions and heat transfer efficiency.

In use comminuted poultry litter biomass is fed from the hopper 10 into the feed tube 6 of the combustion zone 4 and descends onto the grate 20 and forms a bed of biomass typically extending up into the tube as shown in order to prevent heat losses there through. The temperature of the zone 4 is initially raised to a level appropriate for the ignition of the biomass and air is provided through the plenum 22. The biomass is burned only at the bottom (lower region 5b) of the zone (smothered combustion) and that combustion energy allows the pyrolysis phenomenon in the biomass column thereabove (upper region 5a), and the hot gases of pyrolysis exit therefrom through the conduit 53 and the outlet 52 into the mixing chamber 60.

An incandescent layer or cake of biomass gradually radiates on the rotating grate 20 to pass from the pyrolysis zone 4 into the normal combustion zone 40 supplied with air through sparge pipes 42, the gas being generated passing through the outlet 54 into the mixing chamber 60 after providing more energy to the biomass in zone 4 for pyrolysis.

In the embodiment of FIG. 2 the gas from zone 4 and the combustion gases emanating from zone 40 are mixed in the chamber 60 and pass through the tubes 61′ of the substantially full tube bank 61. The gases after their passage through the tubes 61′ enter into a further, ignition chamber 68, separated from the mixing chamber 60 by separation wall 67, provided with a pilot flame igniter 69 and any remaining unburnt gas is combusted and all the gases from the chamber 68 pass over the tubes 61′, thereby effectively reheating the mixture of gases from pyrolysis zone 4 and those from combustion zone 40 passing through the tubes, thus improving efficiency and contributing to the destruction of any harmful elements that might give rise to atmospheric pollution. All gaseous products of combustion exhaust through a common outlet 70 of the body 2 whence they pass to a thermal recuperator (not shown) for appropriate usage.

In the embodiment of FIG. 3 the tube bank 61 is not so long but the gases from zones 4 and 40 are again mixed in chamber 60 and pass through the tubes 61″. The mixture of gases then flow through a zone in which turbulence is promoted by the baffles 62″ and eventually enter an ignition chamber 68 wherein any remaining unburnt gas is ignited by the igniter 69. The resulting gas exhausts from the chamber 68 into a space 71 (FIG. 4) defined over the offset baffles 62″ before flowing around the tubes 61″ of the tube bank 61 to provide reheat for the gases passing therethrough for the same purpose as described above in relation to FIG. 2, the final mixture of gases then exhausting through outlet 70 for passage to a thermal recuperator.

The baffles are provided to improve turbulence and simultaneously increase residence time of the gases to enhance heat transfer and the consumption of potentially noxious elements in the gases.

The present invention thus provides a relatively simple and yet effective means of disposing of a waste biomass product in a useful ‘green’ energy way, thus reducing the time and cost of conventional disposal.

Although the present invention has been described with a certain degree of particularity, it is to be understood that the disclosure has been made by way of example only and that the present invention is not limited to the features of the embodiments described and illustrated herein, but includes all variations and modifications within the scope and spirit of the invention as hereinafter claimed.

Claims

1. A method of converting animal litter biomass into useful energy, said method comprising the steps of: feeding said biomass in comminuted form into a primary combustion zone comprising an upper region and a lower region;partially combusting the biomass at the lower region of the primary combustion zone at an elevated temperature in the presence of a combustion-sustaining medium thereby to provide heat into the upper region thereof for pyrolysis to generate combustible gases;subjecting partially combusted incandescent biomass in the lower region to air flow to generate combustion gases;mixing the combustion gases and the combustible gases in a mixing chamber;igniting the resultant mixture of gases thereof to produce a hot gaseous product; andpassing the hot gaseous product to a thermal recuperator for expending and exploiting the heat energy thus produced.

2. The method of claim 1, wherein the incandescent biomass is combusted in a further combustion zone surrounding the zone and the combustion gases therefrom are mixed with the combustible gases from the pyrolysis of the biomass.

3. The method of claim 1, wherein the hot gaseous product passes to a heat exchange zone wherein it is caused to undergo heat exchange with the mixture of gases from the mixing chamber.

4. The method of claim 3, wherein turbulence is imparted to the flow of gases within the heat exchange zone by the provision of baffles thereby to lengthen the residence time of gases within the zone and to enhance both the suppression of noxious elements within the gases and the heat transfer efficiency.

5. An apparatus for the conversion of animal litter biomass into useful energy, the apparatus comprising: a primary combustion zone incorporating a chamber of frusto-conical form;a feed entry to the primary combustion zone;a feed conduit contiguous with said primary combustion zone and connected to the feed entry at a relatively upper region of the primary combustion zone;a combustible gas outlet for the primary pyrolysis combustion zone formed in the upper region;a rotatable grate situated at the lower region of the primary combustion zone;a means for rotating the grate;a combustion-sustaining fluid distributor located at the lower region;a secondary normal combustion zone on the grate circumscribing the lower region of the primary pyrolysis combustion zone;a combustion exhaust gas outlet from the secondary combustion zone;a gas mixing zone downstream of the combustible gas outlet and the combustion exhaust gas outlet wherein in use the respective combustion gases and the combustible gas mix;an ignition station for the resultant mixture of gases, the gas mixing zone comprising at least a partial tube bank for reheating and suppression of pollutant emissions; anda final gas discharge flue for the resultant gases.

6. The apparatus of claim 5, wherein gas mixing zone includes a heat exchange zone for expending and exploiting the heat energy of the hot mixture thus produced.

7. The apparatus of claim 5, wherein the apparatus is of generally cylindrical form.

8. The apparatus of claim 5, wherein comminuting means is provided for comminuting the biomass feedstock.

9. The apparatus of claim 8, wherein the comminuting means comprises a hopper with a rotatable armature provided with blades.

10. The apparatus of claim 9, wherein a rotatable disc is disposed beneath outlet of the hopper for feeding the comminuted feedstock into the feed conduit.

11. The apparatus of claim 5, wherein the combustion-sustaining fluid medium distributor is of foraminous conical form incorporating a plenum chamber with a medium feed conduit connected thereto.

12. The apparatus of claim 6, wherein the gas mixing zone comprises a full tube bank of coiled tubes.

13. The apparatus of claim 6, wherein the gas mixing zone comprises a demi-tube bank of coiled tubes.

14. The apparatus of claim 6, wherein baffles are provided in the heat exchange zone.

15. The apparatus of claim 5, wherein a solid waste collection area is defined beneath the rotatable grate, and a discharge outlet is provided therefor and leads to a removal station.

16. The apparatus of claim 5, wherein the secondary normal combustion zone is defined externally of the primary combustion zone, the secondary zone being provided with air distributor tubes.