Technical Field
[0001] This invention relates to gasification melting equipment and a method for supplying
combustion air to a melting furnace of gasification melting equipment.
Background Art
[0002] Gasification melting equipment is at the very core of a gasification melting facility,
generally comprising a gasification furnace that performs pyrolysis of waste such
as municipal solid waste and industrial waste to produce a produced gas (pyrolysis
gas and char), and a melting furnace having an introduction port through which the
produced gas is introduced into the melting furnace through a gas duct linked to the
gasification furnace: the pyrolysis gas (combustible gas) in the produced gas is combusted
in the melting furnace to melt the ash in the produced gas into a molten slag.
[0003] As shown in Figs. 7 and 8, this type of gasification melting equipment comprises
an melting furnace 80 with a primary combustion chamber 82 having an upper inner wall
(i.e., an inner wall at the top of the melting furnace 80) to which a clinker 84 tends
to adhere. This clinker 84 grows to prevent maintaining the produced gas retention
time necessary for proper combustion of the produced gas introduced from the gas duct
86 into the primary combustion chamber 82, thus decreasing combustion efficiency,
or prevent maintaining a proper shape of the primary combustion chamber 82 for the
swirling produced gas flow in the primary combustion chamber to decrease the slag
conversion rate (the trapping of ash contained in the produced gas). Besides, the
gasification melting equipment has a risk that the clinker 84 having grown will block
off the primary combustion chamber 82, or fall to damage the melting furnace 80 or
block off the slag discharge hole.
[0004] There is conventionally described a technique for preventing an adherence of clinker
in a melting furnace of gasification melting equipment as discussed above in Patent
Document 1. The melting furnace discussed in Patent Document 1 comprises a side wall
and a ceiling wall that constitute a primary combustion chamber, and a plurality of
combustion gas supply nozzles each having an opened tip and being provided to the
side wall and ceiling wall. The combustion gas supply nozzles blow combustion gas
(combustion air) therefrom into the primary combustion chamber, thereby promoting
mixing of the combustion gas and produced gas for quick temperature rise to prevent
clinker from adhering to the upper inner wall of the primary combustion chamber of
the melting furnace.
[0005] This melting furnace, however, has room for improvement of the locations of the combustion
air supply nozzles for supplying combustion air for primary combustion in the melting
furnace, in order to prevent the clinker from adhering to the upper inner wall of
the primary combustion chamber of the melting furnace.
Patent Document 1: Japanese Patent Application Laid-Open No. 2003-4214
Disclosure of the Invention
[0006] The present invention provides gasification melting equipment and a method for supplying
combustion air to a melting furnace of gasification melting equipment, which make
it possible to more effectively prevent the adherence of clinker onto the upper inner
wall of the primary combustion chamber of the melting furnace in gasification melting
equipment comprising a gasification furnace, a melting furnace, and a gas duct that
links these furnaces.
[0007] To achieve the object, the gasification melting equipment pertaining to the present
invention comprises a gasification furnace that pyrolyzes waste to produce a produced
gas, a melting furnace that has a produced gas introduction port and combusts a pyrolysis
gas contained in the produced gas introduced through the produced gas introduction
port to convert ash in the produced gas into a molten slag, and a gas duct that links
the gasification furnace and the melting furnace to lead the produced gas produced
in the gasification furnace to the produced gas introduction port. The produced gas
introduction port is provided to the upper side wall of a primary combustion chamber
of the melting furnace, and the gas duct is provided with first combustion air supply
nozzles at positions near the produced gas introduction port, the first combustion
air supply nozzles supplying at least 70% of the total amount of combustion air supplied
to the primary combustion chamber of the melting furnace.
[0008] The present invention is also a method for supplying combustion air to a melting
furnace of gasification melting equipment comprising a gasification furnace that pyrolyzes
waste to produce a produced gas by, a melting furnace that has a produced gas introduction
port, for combusting a pyrolysis gas contained in the produced gas introduced through
the produced gas introduction port and converting ash in the produced gas into a molten
slag, and a gas duct that links the gasification furnace and the melting furnace to
lead the produced gas produced in the gasification furnace to the produced gas introduction
port: the method comprises providing the produced gas introduction port to an upper
side wall of a primary combustion chamber of the melting furnace, providing first
combustion air supply nozzles to the gas duct at positons near the produced gas introduction
port, and supplying, from the first combustion air supply nozzles, at least 70% of
the total amount of combustion air supplied to the primary combustion chamber of the
melting furnace.
[0009] According to the above-mentioned gasification melting equipment and method for supplying
combustion air to a melting furnace of gasification melting equipment, the first combustion
air supply nozzles, which are provided to the gas duct at positons near the produced
gas introduction port provided to the upper side wall of the primary combustion chamber
of the melting furnace, supply at least 70% of the total amount of combustion air
supplied to the primary combustion chamber of the melting furnace: the produced gas
and the combustion air supplied from the first combustion air supply nozzles, which
air accounts for the majority of the total amount of combustion air, can be mixed
in a state that the calorific power of the produced gas led from the gasification
furnace through the gas duct to the primary combustion chamber is high. This makes
it possible to raise the internal furnace temperature at the upper part of the primary
combustion chamber of the melting furnace over the melting temperature of the ash
contained in the produced gas to prevent clinker from adhering to the upper inner
wall of the primary combustion chamber of the melting furnace.
Brief Description of the Drawings
[0010]
[Fig. 1] Fig. 1 is a diagram of the overall configuration of the gasification melting
equipment pertaining to an embodiment of the present invention;
[Fig. 2] Fig. 2 is a plan view of the main components of the gas duct and swirling
flow melting furnace in Fig. 1;
[Fig. 3] Fig. 3 is a side view along the arrow III in Fig. 2;
[Fig. 4] Fig. 4 is a side view along the arrow IV in Fig. 2;
[Fig. 5] Fig. 5 is a cross section along the V-V line in Fig. 3;
[Fig. 6] Fig. 6 is a graph of the relation between the allocation ratio η of the amount
of combustion air supplied by the first combustion air supply nozzles provided to
the gas duct with respect to the total amount of combustion air for the primary combustion
chamber of the swirling flow melting furnace, and the internal furnace temperature
T at the upper part of the primary combustion chamber;
[Fig. 7] Fig. 7 is a plan view showing how clinker adheres to the upper inner wall
of the primary combustion chamber of the swirling flow melting furnace; and
[Fig. 8] Fig. 8 is a side view showing how clinker adheres to the upper inner wall
of the primary combustion chamber of the swirling flow melting furnace.
Best Mode for Carrying Out the Invention
[0011] An embodiment of the present invention will now be described through reference to
the drawings. Fig. 1 is a diagram of the overall configuration of the gasification
melting equipment pertaining to an embodiment of the present invention.
[0012] The gasification melting equipment 10 shown in Figs. 1 to 5 comprises a fluidized
bed gasification furnace 20, a swirling flow melting furnace 30, and a gas duct 40.
In the fluidized bed gasification furnace 20, a produced gas B containing pyrolysis
gas and char is produced by pyrolysis of waste A. The swirling flow melting furnace
30 has a produced gas introduction port 33, through which the produced gas B from
the fluidized bed gasification furnace 20 is introduced into the swirling flow melting
furnace 30. In the swirling flow melting furnace 30, the pyrolysis gas (combustible
gas) in the produced gas B is combusted, while the ash in the produced gas B is converted
into molten slag. The gas duct 40 links the fluidized bed gasification furnace 20
and the swirling flow melting furnace 30 to lead the produced gas B produced in the
fluidized bed gasification furnace 20 to the produced gas introduction port 33 of
the swirling flow melting furnace 30.
[0013] The swirling flow melting furnace 30 has a primary combustion chamber 31 and a secondary
combustion chamber 32. The produced gas B from the fluidized bed gasification furnace
20 is supplied through the gas duct 40 to the primary combustion chamber 31 of the
swirling flow melting furnace 30 to form a swirling flow within the primary combustion
chamber 31. The primary combustion chamber 31 has a ceiling wall, which has a top
provided with a second combustion air supply nozzle 34 (one is depicted). The second
combustion air supply nozzle 34 has an opened tip to blow combustion air f2 into the
primary combustion chamber 31 from the tip.
[0014] Figs. 2 to 4 show the main components of the gas duct 40 and the swirling flow melting
furnace 30: Fig. 2 is a plan view; Fig. 3 is a side view along the arrow III in Fig.
2; and Fig. 4 is a side view along the arrow IV in Fig. 2.
[0015] As shown in Fig. 2, the produced gas introduction port 33 is placed in the upper
side wall of the primary combustion chamber 31 of the swirling flow melting furnace
30, and the gas duct 40 is connected to this produced gas introduction port 33. The
gas duct 40 is provided with a plurality of (six are depicted) first combustion air
supply nozzles 41a to 41c and 42a to 42c, at positions near the produced gas introduction
port 33A. Each of the first combustion air supply nozzles 41a to 41c and 42a to 42c
has an opened tip to blow combustion air f1 from the tip into the primary combustion
chamber 31, being placed in an attitude inclined along the flow direction of the produced
gas B (see Fig. 2).
[0016] More specifically, the first combustion air supply nozzles 41a to 41c are provided
to the outer side wall 43 of the gas duct 40 so as to be vertically aligned and supply
combustion air from the outer side wall 43 while being inclined along the flow direction
of the produced gas B. On the other hand, the first combustion air supply nozzles
42a to 42c are provided in the inner side wall 44 of the gas duct 40 so as to be vertically
aligned and supply combustion air from the inner side wall 44 while being inclined
along the flow direction of the produced gas B.
[0017] Fig. 5 is a cross section along the V-V line in Fig. 3. As shown in Fig. 5, the first
combustion air supply nozzle 41a is provided so as to blow the combustion air f1 toward
the intersection point P1 of the produced gas introduction port 33 and the duct width
center line CL of the gas duct 40 near the produced gas introduction port 33 in plan
view, in order to raise the temperature inside the furnace (the temperature inside
the chamber) at the upper part of the primary combustion chamber 31. In other words,
the nozzle 41a is positioned so that an extension of the axis of the first combustion
air supply nozzle 41a in plan view passes through the intersection point P1.
[0018] If the first combustion air supply nozzle 41a were placed so as to blow the combustion
air f1 toward a location upstream from the point of intersection P1 in plan view (such
as a point P2), the temperature could rise inside the gas duct 40 to allow clinker
to block off the gas duct 40. Conversely, if the first combustion air supply nozzle
41a were placed so as to blow the combustion air f1 toward a location downstream from
the point of intersection P1 in plan view (such as a point P3), the combustion time
during which the produced gas B mixed with the combustion air should be collided with
the inner wall of the primary combustion chamber 31 could be so insufficient that
the effect of raising the internal furnace temperature of the upper part of the primary
combustion chamber 31 could not be easily obtained.
[0019] Also, if the first combustion air supply nozzle 41a were provided so as to blow the
combustion air f1 toward a location at an outer side of the duct width center line
CL with respect to the point of intersection P1 in plan view (such as a point P4),
the combustion time during which the produced gas B mixed with the combustion air
should be collided with the inner wall of the primary combustion chamber 31 could
be so insufficient that the effect of raising the internal furnace temperature of
the upper part of the primary combustion chamber 31 could not be easily obtained.
On the other hand, if the first combustion air supply nozzle 41a were provided so
as to blow the combustion air f1 toward a location at an inner side of the duct width
center line CL with respect to the point of intersection P1 in plan view (such as
a point P5), the combustion air f1 could hinder the swirling flow in the primary combustion
chamber 31 to lower the slag conversion ratio (ash capture ratio).
[0020] Accordingly, preferable is that the first combustion air supply nozzle 41a is so
placed as to blow the combustion air f1 toward the intersection point P1 of the produced
gas introduction port 33 and the duct width center line CL in plan view, as mentioned
above. The same holds true for the other combustion air supply nozzles 41b and 41c
and 42a to 42c. For this reason, the combustion air supply nozzles 41a to 41c pertaining
to this embodiment are provided to the side wall 43 of the gas duct 40 at an outer
side of the duct width center line CL, and disposed so as to blow combustion air from
the side wall 43 toward the point of intersection P1, while the combustion air supply
nozzles 42a to 42c are provided to the side wall 44 of the gas duct 40 at an inner
side of the duct width center line CL, and disposed so as to blow combustion air from
this side wall 44 toward the point of intersection P1.
[0021] The swirling flow melting furnace 30, differently from a conventional melting furnace
in which a plurality of combustion air supply nozzles are dispersedly placed in an
upper part of the primary combustion chamber, is adapted to supply combustion air
for the primary combustion chamber of the swirling flow melting furnace 30 only from
the first combustion air supply nozzles 41a to 41c and 42a to 42c placed in the gas
duct 40 at positions near the produced gas introduction port 33 provided to an upper
side wall of the primary combustion chamber 31 of the swirling flow melting furnace
30, and from the second combustion air supply nozzle 34 placed in the ceiling wall
of the primary combustion chamber 31. Concerning the allocation ratio of the amount
of the combustion air supplied by the first combustion air supply nozzles 41a to 41c
and 42a to 42c to the amount of combustion air supplied by the second combustion air
supply nozzle 34, the ratio is set such that the first combustion air supply nozzles
41a to 41c and 42a to 42c supply at least 70% of the total amount of combustion air
supplied to the primary combustion chamber 31.
[0022] Fig. 6 is a graph of the relation between the allocation ratio η of the amount of
combustion air supplied by the first combustion air supply nozzles provided to the
gas duct 40 with respect to the total amount of combustion air for the primary combustion
chamber of the swirling flow melting furnace 30, and the internal furnace temperature
T at the upper part of the primary combustion chamber.
[0023] As shown in Fig. 6, the allocation ratio η of 46% resulted in a measured value for
the internal furnace temperature T of 1015°C to 1149°C (average of 1082°C); the allocation
ratio η of 63% resulted in a measured value for the internal furnace temperature T
of 1154°C to 1198°C (average of 1176°C); and the allocation ratio η of 84% resulted
in a measured value for the internal furnace temperature T of 1165°C to 1238°C (average
of 1201°C). These test results gave the conclusion that the allocation ratio η of
at least 70% permits the internal furnace temperature T at the upper part of the primary
combustion chamber to be raised over 1200°C that is higher than the melting point
of the ash contained in char. In short, the results shown in Fig. 6 taught us that
the allocation ratio η should be set to at least 70%.
[0024] The amount of the combustion air in the fluidized bed gasification furnace 20 (the
amount of forced air E shown in FIG. 1) and the amount of combustion air for the primary
combustion chamber supplied from the first combustion air supply nozzles 41a to 41c
and 42a to 42c and the second combustion air supply nozzle 34 are both favorably from
1.0 to 1.2 in terms of the air ratio (the air ratio is the ratio of the amount of
supplied air to the minimum amount of air required for completely combusting the combustibles
in the waste serving as the raw material). This is for an efficient combustion of
the produced gas that is the mixture of solid fuel and gas fuel: neither the excessively
low nor high air ratio can provide a required internal furnace temperature at the
upper part of the primary combustion chamber. Concerning a flow speed of the combustion
air for the primary combustion chamber supplied by the first and second combustion
air supply nozzles, which speed is determined by the blower capacity and the piping
design, a relatively high flow speed of 30 to 100 m/s, for example, will promote the
mixing of the combustion air and the produced gas to improve combustion efficiency.
[0025] The speed of the produced gas supplied from the fluidized bed gasification furnace
20 to the swirling flow melting furnace 30 is preferably set to 15 to 25 m/s (preferably
18 to 20 m/s). While the high supply speed is preferable, the excessively high speed
let the collision pressure against the inner wall of the primary combustion chamber
31 of the swirling flow melting furnace 30 rise excessively to cause the adhesion
of clinker: therefore, the speed is preferably controlled no higher than the above
maximum of 25 m/s.
[0026] Next will be described a method for supplying melting furnace combustion air in gasification
melting equipment 10 configured as above.
[0027] In the fluidized bed gasification furnace 20, the forced air E which is forced-introduced
from the lower portion of the furnace bed fluidizes a fluid media C such as sand with
to form a fluidized bed. Then, waste A is thrown into the fluidized bed gasification
furnace 20 and pyrolyzed (gasified) in the fluidized bed. Non-combustibles D contained
in the waste A and not gasified are discharged out of the furnace from the lower portion
of the fluidized bed.
[0028] The produced gas B (pyrolyzed gas and char) produced in the fluidized bed gasification
furnace 20 is led through the gas duct 40 to the produced gas introduction port 33
of the swirling flow melting furnace 30. This produced gas B, while mixed with the
combustion air f1 for the primary combustion chamber supplied from the first combustion
air supply nozzles 41a to 41c and 42a to 42c placed to the gas duct 40 at positions
near the produced gas introduction port 33, is introduced from the produced gas introduction
port 33 into the primary combustion chamber 31 of the swirling flow melting furnace
30, thereby forming a swirling flow in the primary combustion chamber 31. Furthermore,
the produced gas G is mixed with the combustion air f2 for the primary combustion
chamber supplied from the second combustion air supply nozzle 34 placed in the ceiling
wall of the primary combustion chamber 31, thus being combusted in the primary combustion
chamber 31. On the supply of the combustion airs f1 and f2 for the primary combustion
chamber, at least 70% (such as 75%) of the total amount of combustion air for the
primary combustion chamber of the swirling flow melting furnace 30 is supplied by
the first combustion air supply nozzles 41a to 41c and 42a to 42c.
[0029] This method makes it possible to mix the produced gas B, which is led from the gasification
furnace 20 to the primary combustion chamber 31 through the gas duct 40 and has a
high calorific power, and the combustion air f1 supplied from the first combustion
air supply nozzles 41a to 41c and 42a to 42c, which air accounts for the majority
of the total amount of combustion air, thus allowing the produced gas B to be combusted
all at once. This makes it possible to raise the internal furnace temperature at the
upper part of the primary combustion chamber 31 over 1200°C, the melting point of
the ash contained in char, to prevent clinker from adhering onto the upper inner wall
of the primary combustion chamber 31.
[0030] The melted ash flows down the inner wall of the primary combustion chamber 31, and
flows down the bottom of the swirling flow melting furnace (slag separation component)
along with the ash melted in the lower portion of the primary combustion chamber 31,
thus discharged to the outside through a slag tap hole 35, as molten slag H. The produced
gas led from the primary combustion chamber 31 to the secondary combustion chamber
32 is mixed with combustion air G for the secondary combustion chamber and completely
combusted in the secondary combustion chamber 32. Flue gas J that has undergone complete
combustion in the secondary combustion chamber 32 is discharged from the swirling
flow melting furnace 30, and is released into the atmosphere through a heat recovery
device, bag filter, and so forth.
[0031] Thus, the method for supplying combustion air to the melting furnace of gasification
melting equipment according to the present invention makes it possible to prevent
clinker from adhering onto the upper inner wall of the primary combustion chamber
31 of the swirling flow melting furnace 30. Accordingly, there can be prevented a
damage of the swirling flow melting furnace 30 or a block off of the slag tap hole
35 due to dropped clinker, block off of the primary combustion chamber 31 of the swirling
flow melting furnace 30 due to the growth of clinker, and a decrease in combustion
efficiency and a decrease in the slag conversion ratio due to the adhesion or growth
of clinker. As a result, stable operation of the gasification melting equipment 10
in the proper state can be carried out over an extended period.
[0032] In short, according to the gasification melting equipment and the method for supplying
combustion air to the melting furnace of gasification melting equipment pertaining
to the present invention, providing first combustion air supply nozzles to a gas duct
near a produced gas introduction port provided to an upper side wall of the primary
combustion chamber of the melting furnace and supplying at least 70% of the total
amount of combustion air supplied to the primary combustion chamber of the melting
furnace from these nozzles make it possible to mix the produced gas, which is led
from the gasification furnace through the gas duct to the primary combustion chamber
and has a high calorific power of the produced gas, and the combustion air supplied
from the first combustion air supply nozzles, which air accounts for the majority
of the total amount of combustion air, thereby raising the internal furnace temperature
at the upper part of the primary combustion chamber of the melting furnace over the
melting temperature of the ash contained in the produced gas to prevent clinker from
adhering onto the upper inner wall of the primary combustion chamber of the melting
furnace. This makes it possible to prevent a damage of the melting furnace, block
off of the slag tap hole due to dropped clinker, block off of the primary combustion
chamber of the melting furnace due to the growth of clinker, and a decrease in combustion
efficiency and a decrease in the slag conversion ratio due to the adhesion or growth
of clinker, thus allowing stable operation of the gasification melting equipment in
the proper state to be carried out over an extended period.
[0033] In this, it is preferable that the first combustion air supply nozzles be placed
so as to blow the combustion air toward the intersection point of the produced gas
introduction port and the duct width center line of the gas duct near the produced
gas introduction port in plan view. This makes it possible to prevent the rise of
the temperature in the gas duct and block off of the gas duct by clinker, while ensuring
sufficient combustion time during which the produced gas containing the combustion
air collides with the inner wall of the primary combustion chamber to raise the internal
furnace temperature at the upper part of the primary combustion chamber.
[0034] In this case, the first combustion air supply nozzles are preferably placed in the
gas duct in an attitude for blowing combustion air toward the intersection point while
inclined along the duct width center line. This enables combustion air to be smoothly
supplied from the nozzles to the primary combustion chamber.
[0035] More preferable is that the first combustion air supply nozzles include a nozzle
that is placed in a side wall of the gas duct at an outer side of the duct width center
line and blows combustion air from the side wall toward the intersection point, and
a nozzle that are placed in a side wall of the gas duct at an inner side of the duct
width center line and blows combustion air from the side wall toward the intersection
point. This enables a sufficient quantity of combustion air to be supplied from both
side walls of the gas duct toward the above-mentioned point of intersection. Furthermore,
since the first combustion air supply nozzles are placed so as to supply combustion
air while being inclined along the duct width center line, the combustion air supplied
from the outer side wall and the combustion air supplied from the inner side wall
have few elements interfering with each other.
[0036] In the present invention, combustion air may be supplied to the primary combustion
chamber of the melting furnace by just the above-mentioned first combustion air supply
nozzles and a second combustion air supply nozzle placed in a ceiling wall of the
primary combustion chamber of the melting furnace.
1. Gasification melting equipment, comprising:
a gasification furnace that pyrolyzes waste to produce a produced gas;
a melting furnace that has a produced gas introduction port and combusts a pyrolysis
gas contained in the produced gas introduced through the produced gas introduction
port to convert ash in the produced gas into a molten slag; and
a gas duct that links the gasification furnace and the melting furnace to lead the
produced gas produced in the gasification furnace to the produced gas introduction
port,
wherein the produced gas introduction port is provided to an upper side wall of a
primary combustion chamber of the melting furnace, and
the gas duct is provided with first combustion air supply nozzles that supply at least
70% of the total amount of combustion air supplied to the primary combustion chamber
of the melting furnace, at positions near the produced gas introduction port.
2. The gasification melting equipment according to Claim 1,
wherein the first combustion air supply nozzles are placed so as to blow combustion
air toward an intersection point of the produced gas introduction port and a duct
width center line of the gas duct near the produced gas introduction port in plan
view.
3. The gasification melting equipment according to Claim 2,
wherein the first combustion air supply nozzles are placed in the gas duct in an attitude
for blowing combustion air toward the point of intersection while being inclined along
the duct width center line.
4. The gasification melting equipment according to Claim 3,
wherein the first combustion air supply nozzles include a nozzle that is placed in
a side wall of the gas duct at an outer side of the duct width center line and blows
combustion air from the side wall toward the intersection point, and a nozzle that
is placed in a side wall of the gas duct at an inner side of the duct width center
line and blows combustion air from the side wall toward the point of intersection.
5. The gasification melting equipment according to any of Claims 1 to 4,
wherein a second combustion air supply nozzle is provided to a ceiling wall of the
primary combustion chamber of the melting furnace, and
combustion air is supplied to the primary combustion chamber of the melting furnace
by only the first and second combustion air supply nozzles.
6. A method for supplying combustion air to a melting furnace of gasification melting
equipment including a gasification furnace that pyrolyzies waste to produce a produced
gas, a melting furnace that has a produced gas introduction port, for combusting a
pyrolysis gas contained in the produced gas introduced through the produced gas introduction
port and converting ash in the produced gas into a molten slag, and a gas duct that
links the gasification furnace and the melting furnace to lead the produced gas produced
in the gasification furnace to the produced gas introduction port, the method comprising:
providing the produced gas introduction port to an upper side wall of a primary combustion
chamber of the melting furnace;
providing first combustion air supply nozzles to the gas duct at positions near the
produced gas introduction port; and
supplying at least 70% of the combustion air out of the total amount of combustion
air supplied to the primary combustion chamber of the melting furnace, from the first
combustion air supply nozzles.
7. The method for supplying combustion air to a melting furnace of gasification melting
equipment according to Claim 6,
wherein combustion air is blown from the first combustion air supply nozzles toward
an intersection point of the produced gas introduction port and the duct width center
line of the gas duct near the produced gas introduction port in plan view.
8. The method for supplying combustion air to a melting furnace of gasification melting
equipment according to Claim 7,
wherein the first combustion air supply nozzles are placed in the gas duct in an attitude
for blowing combustion air toward the intersection point while being inclined along
the duct width center line.
9. The method for supplying combustion air to a melting furnace of gasification melting
equipment according to Claim 8,
wherein the first combustion air supply nozzles include a nozzle that is placed in
a side wall of the gas duct at an outer side of the duct width center line and blows
combustion air from the side wall toward the point of intersection, and a nozzle that
is placed in a side wall of the gas duct at an inner side of the duct width center
line and blows combustion air from the side wall toward the intersection point.
10. The method for supplying combustion air to a melting furnace of gasification melting
equipment according to any of Claims 6 to 9,
further comprising providing a second combustion air supply nozzle to a ceiling wall
of the primary combustion chamber of the melting furnace, and
wherein combustion air is supplied to the primary combustion chamber of the melting
furnace by only the first and second combustion air supply nozzles.