Background and summary of the invention
[0001] The invention relates to a device for the gasification of organic or inorganic materials
such as bulk waste based on wood or other biomass, or even municipal waste, waste
oil, coal, etc., which generates synthesis gas used as fuel for internal combustion
engines and combustion turbines, for example those designed to drive electric generators
in cogeneration units.
[0002] Hitherto known devices for the gasification of organic or predominantly organic materials
such as wood waste, wood chips, straw, sludge, and various forms of biomass, including
municipal and other wastes, predominantly utilize a gasification process based on
combustion, partial combustion, or fluidized bed combustion of material. In these
cases the material is filled from a filling hopper into auger conveyors, through which
it is moved and is heated directly or indirectly during the passage through the auger
conveyors, during which synthesis gas is developed from the ongoing thermochemical
reaction. The synthesis gas is then used as a gaseous fuel for internal combustion
engines of cogeneration units.
[0003] In these known devices, the major problem is maintaining the stability of the gasification
process and achieving a standard high quality of the output synthesis gas, particularly
in achieving a low tar and nitrogen content. Precise regulation of the combustion
process is difficult, and a disadvantage also lies in the high emissions of ash and
other pollutants. The output synthesis gas generally contains tars which are formed
during the combustion of pre-dried material with a moisture content of up to 15%.
Low moisture, which is a prerequisite of effective combustion, has the undesirable
consequence of a high tar content which must subsequently be chemically removed by
washing in order to achieve a sufficient quality of synthesis gas for its combustion
in internal combustion engines.
[0004] In patent application
JP 2001 28 94 22 A, the device for the gasification of material is described through its combustion.
In order to prevent atmospheric air from entering the device and thus reducing the
risk of ignition of the material in the hopper, part of the flue gas from the combustion
chamber is filtered, cooled, and fed into the sealing mechanism which is positioned
before the entry into the combustion chamber. Conversely, the combustion chamber is
supplied with oxygen in order to improve the combustion of the unburnt particles.
During the combustion of the material, which must have a low input relative moisture,
undesirable tars are not formed but neither is a large percentage of nitrogen, so
the output synthesis gas is not of a sufficient quality.
[0005] In patent
EP 186 5045, biomass enters the device from the tray through a supply auger and then passes through
two gasification augers. Below them is positioned a combustion auger, from which both
gasification augers are heated. Small biomass particles pass through a sieve from
the gasification auger into the combustion auger where they are combusted during the
supply of preheated combustion air. Larger particles are returned to the gasification
process. The developed synthesis gas passes through the entire device back to the
beginning, where it is removed. The device according to
EP 186 5045 is designed to allow for a reduction of the nitrogen content in the developed synthesis
gas. Given that the gasification augers are not hermetically separated from the combustion
auger, the disadvantage of the device is that part of the flue gas continuously penetrates
into the gasification augers, so the nitrogen content in the exhaust gas cannot achieve
the zero or negligible value optimal for achieving a high quality of developed synthesis
gas. The tar content in the synthesis gas is also high, since the material passing
through the gasification augers cannot have a high relative moisture due to the subsequent
combustion.
[0006] The task of the invention is to provide a gasification device which would remove
the disadvantages of the known devices, allow for the processing of materials with
a high relative moisture, and achieve a high quality of developed synthesis gas with
a minimum tar and nitrogen content. A further task is to provide a device with lower
emissions, with efficient regulation of the gasification process, and with improved
stability of the entire system.
[0007] This task is solved by creating a device for the production of gaseous fuel from
materials of organic and/or inorganic origin according to the present invention.
[0008] The device includes a filling chamber which is connected to at least one supply auger
conveyor for supplying material from the filling chamber into the gasification reactor.
The gasification reactor comprises at least two heated gasification augers arranged
in rows above beneath each other for a serpentine flow of the material through the
reactor. Gaseous fuel is formed as a synthesis gas from the thermochemical reaction
in the gasification augers and is collected at the outlet which is arranged on the
lowest gasification auger.
[0009] The subject-matter of the invention lies in each horizontal row of gasification augers
being formed by a gasification body whose casing has a closed oval cross-section formed
by an upper base, a bottom base, and convex side walls each with a circular arc profile,
wherein each gasification body contains at least two gasification augers arranged
side by side and mutually partially separated by longitudinal partitions that form
half-grooves for the individual gasification augers. The gasification bodies are heated
by electric heating, wherein at least one electric heating element is arranged parallel
to the lower base and/or to the upper base of each gasification body. The filling
chamber is hermetically sealed to prevent the access of atmospheric air when the material
is being filled. At least one neck leads into the filling chamber for supplying exhaust
gases from the combustion of the synthesis gas in the internal combustion engine.
The filling chamber is further provided with at least one neck for the removal of
exhaust gases from the filling chamber. The device according to the invention allows
for the production of synthesis gas with a lower tar content and almost zero nitrogen
content, because the electric heater allows for the processing of materials with a
higher relative moisture and with perfect regulated heating in the gasification bodies
which, together with the elimination of combustion and with gas-tight closure of the
filling chamber, results in an improved quality of the output gas used as fuel gas.
[0010] In a preferred embodiment of the invention, the filling auger conveyor is arranged
above the uppermost gasification body and is fitted with at least one neck for the
supply of water or steam, at least one neck for the supply of heat, and at least one
neck for the removal of heat. The material fed into the reactor can thus be moisturized
prior to its entry into the first gasification body and preheated to improve the parameters
of the gasification process.
[0011] In another preferred embodiment of the invention, there is a spacer, positioned between
the filling auger conveyor and the uppermost placed gasification body, that contains
a moisture sensor for the material and an additional or alternative supply of water
or steam for adjusting the moisture of the material. According to the measured moisture
values, it is thus possible to make final adjustments to the moisture content of the
material to the optimum value also in the spacer just before the material enters into
the gasification body.
[0012] For ideal mixing and moisturizing of the input material, it is preferred that the
filling chamber has a conical shape in its lower part, and leading into the filling
chamber are the ends of two supply auger conveyors which are separated inside the
filling chamber by a wedge-shaped partition. Towards the opposite ends of the filling
conveyor auger are connected two spacers that lead to a joint outlet neck with a flange
that is connected to the flange of the inlet neck of the uppermost gasification body.
[0013] For universal use for various kinds of organic and inorganic materials, it is preferred
that the device comprises three gasification bodies arranged in horizontal rows one
above the other, wherein inside each gasification body there are arranged, in parallel
in a horizontal plane, four gasification augers separated by longitudinal partitions.
[0014] In a preferred constructional embodiment of the device according to the invention,
the gasification bodies are horizontally separated from each other by vertical supporting
partitions, wherein the electrical heaters are removably placed in gaps between the
adjacent bodies and between the adjacent supporting partitions and the side partitions
on the upper base of each gasification body. This embodiment allows for easier installation,
and repair and replacement of the heaters or their parts. The electric heater preferably
comprises a set of heating elements in the form of tubes whose axes extend perpendicularly
to the axles of the gasification augers. The device is housed in a cabinet with service
holes that allow for the exchange of the heating elements without the need to remove
the outer casing of the reactor.
[0015] In order to uniformly form an airtight seal of the material in the filling chamber,
the filling chamber is preferably provided with two oppositely arranged necks for
the supply of exhaust gases, wherein these necks are interconnected through distribution
piping. The exhaust gases can thus penetrate into the filling chamber uniformly from
both sides. The neck for the release of exhaust gas from the filling chamber is arranged
above the two supply necks.
[0016] Finally, it is advantageous that the front wall of each gasification body is provided
with a common connecting flange for connecting the drives to the axles of the gasification
augers in the gasification body.
[0017] The advantages of the device according to the invention are that it allows for the
generation of high-quality synthesis gas with a minimum content of tars and nitrogen
from various kinds of organic and inorganic materials which may have a relative moisture
content greater than 50%. An advantage is also the even and intense electric heating
of moist material in the gasification bodies with common and uniform heating of several
gasification augers at the same time. Another advantage is the simple prevention of
the inlet of atmospheric air into the gasification process using exhaust gases that
are formed as combustion products of synthesis gas, in an internal combustion engine.
The device, in comparison to known reactors, is characterized by low emissions, efficient
regulation of the gasification process, and improved stability of the entire reactor
system associated with the cogeneration unit.
Description of the drawings
[0018] The invention is described in detail by means of the drawings as follows:
- Figure 1
- is a block diagram of the device according to the invention showing the reactor connected
to a cogeneration unit and other parts of the synthesis gas processing technology
- Figure 2
- shows a perspective overall view of the device
- Figure 3
- shows an exploded perspective view of the assembly of the filling auger conveyors
and gasification bodies with electrical heaters
- Figure 4
- shows a vertical sectional view of the device on the A-A plane of Figure 3
- Figure 5
- shows a detailed perspective view of the filling chamber
- Figure 6
- shows a partial sectional view of the filling auger conveyors and filling chamber
Examples of the preferred embodiments of the invention
[0019] It should be understood that the further described and illustrated specific examples
of the realized invention are presented for illustrative purposes and not as a limitation
of the examples of the realization of the invention to the cases shown herein. Those
skilled in the art shall find, or using routine experimentation will be able to determine,
a greater or lesser number of equivalents to the specific realizations of the invention
that are specifically described here. These equivalents shall also be included into
the scope of the following claims.
[0020] The device
1 is, in the embodiment shown in Figure 1, part of a technological system used to produce
electricity from biomass. Electrical energy is produced by a generator which is part
of a cogeneration unit connected to a transformer
32. The generator is powered by a combustion engine
17, which is continuously supplied by gaseous fuel produced in the device
1 as synthesis gas formed as a thermochemical reaction by the gasification of biomass.
The synthesis gas is removed at the outlet
8 of the device
1, passes through a cooling and cleaning unit
31, to which is connected an auxiliary media unit
33. Prior to entering the internal combustion engine
17 a torch
34 is mounted on the pipe supplying the synthesis gas for the emergency combustion of
synthesis gas in the event of failure of the internal combustion engine
17. The exhaust gases
16 from the combustion engine
17 are led to the filling chamber
2 of the device
1, and hermetically fill it, thus preventing the inlet of atmospheric air contained
in the biomass to the device
1.
[0021] As is seen from Figure 2, the device
1 has a cabinet
25 in which three gasification bodies
7,
7', 7" are stored. The cabinet
25 has, on its sides, a set of service openings
26 for exchanging the heating elements
24 of the electrical heaters
14 arranged between the individual gasification bodies
7, 7', 7". Above the cabinet
25 is a filling chamber
2 into which the biomass (not shown) falls into the hopper (not shown). The filling
chamber
2 has a cubical shape, the bottom of which is conical. On the side of the filling chamber
2 is a neck
15 for the supply of exhaust gas
16. In the upper lid
30 of the filling chamber
2 is an opening for the supply of biomass and a neck
18 for releasing exhaust gases
16 from the filling chamber
2. Exhaust gases
16 are continuously supplied from the internal combustion engine
17 into the filling chamber
2, pass through the biomass in the filling chamber
2 and exit through the neck
18 and a chimney (not shown) into the atmosphere. From the bottom part of the filling
chamber
2 there project two supply augers
3, 3' that transport the biomass from the filling chamber
2 further into the reactor through the spacers
4, 4'connected to the outlet neck
5 with a flange.
[0022] Figure 3 shows that the supply auger conveyors
3, 3' are each fitted with one neck
20 for supplying heat and one neck
21 for removing heat. The spacers
4, 4' then have necks
36 for supplying water or steam and in addition are fitted internally with a sensor
29 for the moisture of the material. Figure 3 also shows the construction of the device
1 inside the cabinet
25, where three gasification bodies
7, 7', 7" are horizontally arranged above each other and are mutually interconnected so that
the material passes through them in a serpentine direction. The upper gasification
body
7 has an inlet neck
6 with a flange which is connected to the flange of the outlet neck
5, through which material falls out from the spacers 4,
4' into the uppermost positioned gasification body
7. The gasification bodies
7,
7', 7" form a floor supported by vertical bearing partitions
23 made of sheet metal. Each gasification body
7, 7', 7" is a sheet metal weldment of elliptical cross-section having a flat upper base
10, a flat lower base
11, and two semi-circular side walls
12. Inside each gasification body
7, 7', 7" are positioned, parallel to each other, four gasification augers
9, partially separated from each other by longitudinal partitions
13. The longitudinal partitions
13 are welded to the lower base
11 and are shaped like open semicircular half-grooves in which the gasification augers
9 are placed. The axles
28 of the gasifying augers
9 project from the front walls of the gasification bodies
7, 7', 7", where there are flanges
27 for connecting the drives (not shown) for the gasification augers
9. On the upper bases
10 of the gasifying bodies
7, 7', 7" are positioned electric heaters
14 comprised of sets of heating elements
24 in the form of tubes, the axes of which run perpendicular to the axles of the gasification
augers
9. The heating elements
24 can thus be removed for replacement from the cabinet
25 through the service openings
26. Each electric heater
14 is bounded by longitudinal support partitions
23 and by side partitions
35 on the side, so it heats up the gasification body
7, 7', 7" arranged above it in an enclosed space.
[0023] Figures 5 and 6 show in detail the filling chamber
2. In its lower part is a wedge-shaped partition
22 that separates the supply auger conveyors
3, 3' from each other. On the sides are two necks
15 for the supply of exhaust gases
16 which are interconnected by distribution pipes
19 for uniform distribution of exhaust gases
16 into the filling chamber
2.
[0024] The device according to the invention can be used to produce fuel gas by the gasification
of organic or inorganic material.
Overview of the positions used in the drawings
[0025]
- 1
- device for the production of gaseous fuel
- 2
- filling chamber
- 3
- supply auger conveyor into the reactor
- 3'
- supply auger conveyor into the reactor
- 4
- spacer
- 4'
- spacer
- 5
- outlet neck with flange
- 6
- inlet neck with flange
- 7
- gasification body
- 7'
- gasification body
- 7"
- gasification body
- 8
- outlet of synthesis gas
- 9
- gasification auger
- 10
- upper base of gasification body
- 11
- lower base of gasification body
- 12
- side wall of gasification body
- 13
- longitudinal partition of gasification body
- 14
- electric heater
- 15
- neck for supply of exhaust gases
- 16
- exhaust gases
- 17
- internal combustion engine
- 18
- neck for the removal/release of exhaust gases
- 19
- distribution pipes for exhaust gases
- 20
- neck for supply of heat
- 21
- neck for removal/release of heat
- 22
- wedge-shaped partition
- 23
- support partition
- 24
- heating element
- 25
- cabinet
- 26
- service opening for heating element replacement
- 27
- connecting flange
- 28
- axle of gasification auger
- 29
- material humidity sensor
- 30
- lid of filling chamber
- 31
- gas cooling and cleaning unit
- 32
- transformer
- 33
- auxiliary media unit
- 34
- torch
- 35
- side partition
- 36
- neck for water or steam inlet
1. A device (1) for the production of gaseous fuel from materials of organic and/or inorganic
origin, including a filling chamber (2) which is connected to at least one supply
auger conveyor (3, 3') for supplying material from the filling chamber (2) into a
reactor which comprises at least two heated gasification augers (9) arranged in at
least two horizontal rows above each other for a serpentine passage of material from
the filling chamber (2) to an outlet (8) of the fuel gas formed by synthesis gas from
a thermochemical reaction in the gasification augers (9), wherein the outlet (8) is
arranged on the lowest positioned gasification auger (9), characterized in that each horizontal row of the gasification augers (9) is formed by a gasification body
(7, 7', 7"), the casing of which has a closed oval cross-section formed by an upper
base (10), a lower base (11) and convex side walls (12) each having a circular arc
profile, wherein each gasifying body (7, 7', 7") contains at least two gasification
augers (9) arranged side by side and mutually partially separated by longitudinal
partitions (13) which form half-grooves for the individual gasification augers (9),
further, parallel to the upper base (10) and/or to the lower base (11) of each gasification
body (7, 7', 7") there is arranged at least one electrical heater (14), and the filling
chamber (2) is hermetically sealed to prevent the inlet of atmospheric air during
the filling of the material, and at least one neck (15) leads into the filling chamber
(2) for supplying exhaust gases (16) from the combustion of the synthesis gas collected
at the outlet (8) of the device (1) in an internal combustion engine (17), and the
filling chamber (2) is fitted with at least one neck (18) for the release of exhaust
gases (16) from the filling chamber (2).
2. A device according to claim 1, characterized in that the filler auger conveyor (3, 3') is positioned above the uppermost positioned gasification
body (7) and is fitted with at least one neck (36) for supplying water or steam to
adjust the moisture of the material, with at least one neck (20) for supplying heat,
and at least one neck (21) for releasing heat.
3. A device according to claim 1 or 2, characterized in that between the filler auger conveyor (3, 3') and the uppermost positioned gasification
body (7) is a spacer (4, 4') containing a sensor (29) for measuring the moisture of
the material and a neck (36) for supplying water or steam to adjust the moisture of
the material.
4. A device according to claims 2 and 3, characterized in that the filling chamber (2) has a conical shape in its bottom part, and leading into
the filling chamber (2) are the ends of two supply auger conveyors (3, 3'), separated
inside the filling chamber (2) by a wedge-shaped partition (22), wherein towards the
opposite ends of the filler auger conveyors (3, 3') there are connected spacers (4,
4') that lead into a common outlet neck (5) with a flange which is connected to the
flange of the inlet neck (6) of the uppermost positioned gasification body (7).
5. A device according to at least one of claims 1 to 4, characterized in that it includes three gasification bodies (7, 7', 7") positioned in horizontal rows one
above the other, wherein in each gasification body (7, 7', 7") there are arranged,
in parallel in a horizontal plane, four gasification augers (9) separated by longitudinal
partitions (13).
6. A device according to at least one of claims 1 to 5, characterized in that the gasification bodies (7, 7', 7") are separated from each other horizontally by
vertical supporting partitions (23), wherein the electric heaters (14) are removably
positioned in the gaps between adjacent bodies (7, 7', 7") and between the adjacent
supporting partitions (23) on the upper base (10) of each gasification body (7, 7',
7"), and are bounded by the side partitions (35).
7. A device according to at least one of claims 1 to 6, characterized in that the electric heater (14) comprises a set of heating elements (24) shaped like tubes,
the axes of which run perpendicular to the axles of the gasification augers (9).
8. A device according to at least one of claims 1 to 7, characterized in that it is housed in a cabinet (25) with service openings (26) for replacing the heating
elements.
9. A device according to at least one of claims 1 to 8, characterized in that the filling chamber (2) is fitted with two oppositely arranged necks (15) for the
supply of exhaust gas (16), wherein the necks (15) are interconnected by distribution
pipes (19), and a neck (18) for releasing exhaust gases (16) from the filling chamber
(2) is positioned above the necks (15).
10. A device according to at least one of claims 1 to 9, characterized in that the front wall of the gasification body (7, 7', 7") is fitted with a common connecting
flange (27) for connecting a drive to the axles (28) of the gasification augers (
9).