Patent Grant
10612777
The present invention relates to a method for dry-distilling and incinerating wastes, such as waste tires.
As a method for incinerating wastes, such as waste tires, there has been known, for example, a method in which a part of wastes held in a dry distillation furnace is burnt, the remainder of the wastes is subjected to dry distillation (pyrolysis) by the combustion heat, and the combustible gas produced by the dry distillation is introduced from the dry distillation furnace into a combustion furnace to burn the combustible gas (refer to, for example, Patent Literature 1).
According to the method described in Patent Literature 1, the temperature in the combustion furnace due to the combustion of the combustible gas is detected as the combustion temperature of the combustible gas. Further, the amount of oxygen to be supplied to the dry distillation furnace is regulated to feedback-control the dry distillation gasification of the wastes in the dry distillation furnace such that the temperature in the combustion furnace becomes a predetermined temperature (hereinafter may be abbreviated to “the set temperature”), i.e. such that the combustible gas is burnt at the set temperature. Here, the amount of oxygen to be supplied to the dry distillation furnace is controlled by adjusting the degree of opening of a valve provided in an oxygen supply passage that connects an oxygen supply source and the dry distillation furnace.
Further, the foregoing incineration method is based on batch processing. Hence, there has been known a method in which, for example, two such dry distillation furnaces are provided for one such combustion furnace, and the two dry distillation furnaces are alternately operated so as to perform continuous processing (refer to, for example, Patent Literature 2).
According to the method described in Patent Literature 2, when alternately operating the two dry distillation furnaces, the wastes in a second dry distillation furnace are ignited to start dry distillation in the final stage of the dry distillation of the wastes in a first dry distillation furnace. Then, a combustible gas to be burnt in the combustion furnace is switched from a combustible gas produced in the first dry distillation furnace to a combustible gas produced in the second dry distillation furnace.
Patent Literature 1: Japanese Patent: Application Laid-Open No. 2-13580
Patent Literature 2: Japanese Patent No. 4050189
However, when switching the combustible gas to be burnt in the combustion furnace from the combustible gas produced in one dry distillation furnace to the combustible gas produced in the other dry distillation furnace, if the switching does not smoothly proceed, the temperature in the foregoing combustion furnace becomes significantly lower than the set temperature in some cases. If this happens, it is required to burn a fuel, such as a heavy oil, to maintain the temperature in the combustion furnace at the predetermined temperature, inconveniently making an increase in running cost unavoidable.
An object of the present invention is to provide a dry distillation gasification waste incineration method that resolves such an inconvenience and enables a reduction in running cost for switching a combustible gas to be burnt in the combustion furnace from a combustible gas produced in one dry distillation furnace to a combustible gas produced in the other dry distillation furnace.
To this end, a dry distillation gasification waste incineration method in accordance with the present invention is a dry distillation gasification waste incineration method in which a plurality of dry distillation furnaces are provided for one combustion furnace, wastes held in each of the dry distillation furnaces are dry-distilled in sequence thereby to produce a combustible gas, and control is carried out such that a temperature in the combustion furnace becomes a predetermined first temperature in a case where the combustible gas is introduced into the combustion furnace and burnt, the method including: a step of supplying oxygen required for the dry distillation of the wastes to a first dry distillation furnace while controlling a degree of opening of a first valve provided in a first oxygen supply passage such that the temperature in the combustion furnace becomes a first temperature by the combustion of the combustible gas in the case where the combustible gas is produced by dry-distilling wastes held in the first dry distillation furnace by using the oxygen supplied to the first dry distillation furnace through the first oxygen supply passage from an oxygen supply source and the combustible gas is introduced into the combustion furnace and burnt; a step of detecting presence of wastes in a second dry distillation furnace while control is being carried out such that the temperature in the combustion furnace becomes the first temperature by the combustion of the combustible gas produced in the first dry distillation furnace and then igniting the wastes held in the second dry distillation furnace by using oxygen supplied to the second dry distillation furnace through a second oxygen supply passage from the oxygen supply source; and a step of dry-distilling the wastes held in the second dry distillation furnace by using oxygen supplied to the second dry distillation furnace through the second oxygen supply passage from the oxygen supply source so as to produce a combustible gas and introducing the combustible gas produced in the second dry distillation furnace into the combustion furnace to start combustion.
In the dry distillation gasification waste incineration method according to the present invention, first, a combustible gas is produced in the first dry distillation furnace by dry-distilling wastes held in a furnace by using oxygen supplied to the first dry distillation furnace through the first oxygen supply passage from the oxygen supply source. Further, when the combustible gas is introduced into the combustion furnace and burnt, the oxygen required for dry-distilling the wastes is supplied to the first dry distillation furnace while controlling the degree of opening of the first valve provided in the first oxygen supply passage.
Here, the degree of opening of the first valve is controlled such that the temperature in the combustion furnace becomes a predetermined first temperature by the combustion of the combustible gas, which has been produced in the first dry distillation furnace, in the combustion furnace. In other words, the degree of opening of the first valve is controlled such that the combustible gas produced in the first dry distillation furnace is burnt at the predetermined first temperature in the combustion furnace.
Next, while the control is being carried out such that the temperature in the combustion furnace becomes the first temperature by the combustion of the combustible gas, which has been produced in the first dry distillation furnace, in the combustion furnace, the presence of the wastes held in the second dry distillation furnace is detected and the wastes held in the second dry distillation furnace are ignited. The wastes held in the second dry distillation furnace are ignited using the oxygen supplied to the second dry distillation furnace through the second oxygen supply passage from the oxygen supply source.
Subsequently, after the wastes held in the second dry distillation furnace are ignited, the wastes are subjected to dry distillation by using the oxygen supplied to the second dry distillation furnace through the second oxygen supply passage from the oxygen supply source. Then, the combustible gas produced by the dry distillation is introduced into the combustion furnace and the combustion is started, thereby enabling smooth switching of the combustible gas to be burnt in the combustion furnace from the combustible gas produced in the first dry distillation furnace to the combustible gas produced in the second dry distillation furnace.
In the dry distillation gasification waste incineration method in accordance with the present invention, while the control is being carried out such that the temperature in the combustion furnace becomes the first temperature, the wastes held in the second dry distillation furnace are ignited, the combustible gas produced in the second dry distillation furnace is introduced into the combustion furnace, and the combustion is begun without waiting for the dry distillation of the wastes in the first dry distillation furnace to reach the final stage, as in the foregoing prior art. Hence, in the dry distillation gasification waste incineration method in accordance with the present invention, the temperature in the combustion furnace does not fall significantly below the predetermined first temperature and it is not required to burn a fuel, such as a heavy oil, to maintain the temperature in the combustion furnace at the predetermined temperature, thus enabling a reduction in running cost.
In the dry distillation gasification waste incineration method according to the present invention, when introducing and burning the combustible gas, which has been produced in the second dry distillation furnace, into the combustion furnace, the oxygen required for the dry distillation of the wastes is supplied to the second dry distillation furnace while controlling the degree of opening of the second valve provided in the second oxygen supply passage such that the temperature in the combustion furnace reaches the first temperature by the combustion of the combustible gas.
Further, in the dry distillation gasification waste incineration method according to the present invention, the operation for switching the combustible gas burnt in the combustion furnace from the combustible gas produced in the first dry distillation furnace to the combustible gas produced in the second dry distillation furnace hereinafter may be abbreviated to “the switching operation”) may take any one of the three modes described below.
First, a first mode of the switching operation includes: a step of igniting the wastes held in the second dry distillation furnace and forming a fire bed by controlling a degree of opening of a second valve in the case where the degree of opening of the first valve reaches a first predetermined degree of opening; a step of decreasing the degree of opening of the second valve and supplying a sufficient amount of oxygen required to maintain the fire bed to the second dry distillation furnace through the second oxygen supply passage from the oxygen supply source in the case where, after the fire bed is formed, the degree of opening of the first valve increases beyond the first predetermined degree of opening, and then decreases until reaching a second predetermined degree of opening which is smaller than the first predetermined degree of opening; and a step of increasing the degree of opening of the second valve to dry-distill the wastes held in the second dry distillation furnace so as to produce a combustible gas by using the oxygen supplied to the second dry distillation furnace through the second oxygen supply passage from the oxygen supply source and to start the introduction of the combustible gas, which has been produced in the second dry distillation furnace, into the combustion furnace in a case where the degree of opening of the first valve increases again until reaching a third predetermined degree of opening, which is larger than the second predetermined degree of opening, while control is being carried out such that the temperature in the combustion furnace becomes the first temperature by the combustion of the combustible gas produced in the first dry distillation furnace.
While the control is being carried out such that the temperature in the combustion furnace becomes the first temperature by the combustion of the combustible gas produced in the first dry distillation furnace, the degree of opening of the first valve gradually increases with the progress of the dry distillation of the wastes held in the first dry distillation furnace, and the remaining amount of the wastes in the first dry distillation furnace can be known from the degree of opening of the first valve. Therefore, according to the first mode of the switching operation, when the degree of opening of the first valve reaches the first predetermined degree of opening while the control is being carried out such that the temperature in the combustion furnace becomes the first temperature by the combustion of the combustible gas produced in the first dry distillation furnace, it is determined that the dry distillation of the wastes in the first dry distillation furnace is approaching the final stage, and the wastes held in the second dry distillation furnace are ignited. In the second dry distillation furnace, after the ignition, the degree of opening of the second valve provided in the second oxygen supply passage is controlled thereby to stabilize the combustion of the wastes held in the second dry distillation furnace, and a fire bed is formed.
In the second dry distillation furnace, it is possible to start the dry distillation of wastes in the furnace immediately after the fire bed is formed. At this point, however, a sufficient amount of wastes still remains in the first dry distillation furnace, so that the combustible gas can be produced by the dry distillation of the wastes.
In the case where a sufficient amount of wastes remains in the first dry distillation furnace, if the combustible gas produced in the first dry distillation furnace is excessively supplied to the combustion furnace, then the combustion of the combustible gas in the combustion furnace causes the temperature in the combustion furnace to rise, making it difficult to control the temperature to become the first temperature. For this reason, in the first dry distillation furnace, the degree of opening of the first valve shifts to decrease after increasing beyond the first predetermined degree of opening.
Therefore, in the second dry distillation furnace, when the degree of opening of the first valve shifts to decrease and reaches a second predetermined degree of opening, which is smaller than the first predetermined degree of opening, the degree of opening of the second valve is decreased to supply a sufficient amount of oxygen required to maintain the fire bed into the furnace. Thus, in the second dry distillation furnace, the fire bed is being maintained, whereas the dry distillation of the wastes held in the furnace is not yet started. This state is, in other words, a state in which the dry distillation of the wastes held in the furnace can be immediately started as necessary (hereinafter may be referred to as “the standby state”).
Next, in the first dry distillation furnace, the wastes that can produce the combustible gas gradually decrease, and the degree of opening of the first valve gradually increases to control the temperature in the combustion furnace due to the combustion of the combustible gas to become the first temperature. Then, it eventually becomes impossible to control the temperature in the combustion furnace to become the first temperature merely by the combustion of the combustible gas produced in the first dry distillation furnace.
Accordingly, in the second dry distillation furnace, the degree of opening of the first valve increases again to control the temperature in the combustion furnace to become the first temperature and when the degree of opening of the first valve reaches a third predetermined degree of opening, which is larger than the second predetermined degree of opening, the degree of opening of the second valve is increased to start the dry distillation of the wastes held in the furnace. The dry distillation of the wastes in the second dry distillation furnace is performed using the oxygen supplied to the second dry distillation furnace through the second oxygen supply passage from the oxygen supply source. When the dry distillation of the wastes in the second dry distillation furnace is begun, the combustible gas is produced by the dry distillation and the introduction of the combustible gas into the combustion furnace is begun.
As a result, in the combustible furnace, the combustible gas produced in the first dry distillation furnace and the combustible gas produced in the second dry distillation furnace are burnt together, thus making it possible to prevent the temperature in the combustion furnace from significantly decreasing.
Meanwhile, in the first dry distillation furnace, the wastes that can produce the combustible gas further decrease and the combustible gas produced by the dry distillation of the wastes gradually decreases accordingly. Then, the combustible gas produced by the dry distillation of the wastes runs out in the end.
As a result, the combustible gas burnt in the combustion furnace can be smoothly switched from the combustible gas produced in the first dry distillation furnace to the combustible gas produced in the second dry distillation furnace.
Further, the second aspect of the switching operation includes: a step of igniting the wastes held in the second dry distillation furnace and forming a fire bed by controlling a degree of opening of a second valve in the case where the degree of opening of the first valve reaches a first predetermined degree of opening; a step of igniting a combustion device provided in the combustion furnace in a case where the temperature in the combustion furnace decreases and reaches a second predetermined temperature, which is lower than the first temperature; and a step of producing a combustible gas by subjecting the wastes held in the second dry distillation furnace to dry distillation by using oxygen supplied to the second dry distillation furnace through the second oxygen supply passage from the oxygen supply source and starting the introduction of the combustible gas produced in the second dry distillation furnace into the combustion furnace in a case where, after the combustion device is ignited, the temperature in the first dry distillation furnace shifts to decrease and reaches a third predetermined temperature whereas the temperature in the combustion furnace recovers the first temperature.
In the second aspect of the switching operation, the ignition of the wastes held in the second dry distillation furnace and the formation of the fire bed can be performed in exactly the same manner as that of the first aspect of the switching operation. However, depending on the timing of the ignition of the wastes held in the second dry distillation furnace, there are some cases where, during the process of forming the fire bed, the wastes that can produce the combustible gas in the first dry distillation furnace decrease and the temperature in the combustion furnace cannot be controlled to become the first temperature merely by the combustion of the combustible gas produced in the first dry distillation furnace.
In this case, if the temperature in the combustion furnace decreases and reaches the second predetermined temperature, which is lower than the first temperature, then it becomes necessary to carry out control such that the temperature in the combustion furnace becomes the first temperature by igniting the combustion device provided in the combustion furnace. Further, in this case, as the wastes that can produce the combustible gas in the first dry distillation furnace decrease, the temperature in the first dry distillation furnace shifts to decrease and reaches the third predetermined temperature.
Hence, according to the second aspect of the switching operation, when the combustion device is ignited and the temperature in the combustion furnace recovers the first temperature after the temperature in the first dry distillation furnace decreases to the third predetermined temperature, the dry distillation of the wastes held in the second dry distillation furnace is immediately started without shifting to the standby state. When the dry distillation of the wastes held in the second dry distillation furnace is started, the combustible gas is produced by the dry distillation and the introduction of the combustible gas into the combustion furnace is started.
Thus, the second aspect of the switching operation makes it possible to smoothly switch the combustible gas burnt in the combustion furnace from the combustible gas produced in the first dry distillation furnace to the combustible gas produced in the second dry distillation furnace.
Further, a third aspect of the switching operation includes: a step of igniting the wastes held in the second dry distillation furnace and forming a fire bed by controlling a degree of opening of a second valve in the case where the degree of opening of the first valve reaches a first predetermined degree of opening; and a step of producing a combustible gas by subjecting the wastes held in the second dry distillation furnace to dry distillation by using oxygen supplied to the second dry distillation furnace through the second oxygen supply passage from the oxygen supply source and starting the introduction of the combustible gas, which has been produced in the second dry distillation furnace, into the combustion furnace in a case where, after the fire bed is formed, the degree of opening of the first valve increases beyond the first predetermined degree of opening and then decreases to reach a fourth predetermined degree of opening, which is larger than the first predetermined degree of opening whereas the temperature in the combustion furnace temporarily decreases and then recovers the first temperature.
In the third aspect of the switching operation, the ignition of the wastes held in the second dry distillation furnace and the formation of the fire bed can be performed in exactly the same manner as that of the first aspect of the switching operation. However, depending on the timing of the ignition of the wastes held in the second dry distillation furnace, there are some cases where, during the process of forming the fire bed, the wastes that can produce the combustible gas in the first dry distillation furnace decrease and the degree of opening of the first valve gradually increases to control the temperature in the combustion furnace due to the combustion of the combustible to become the first temperature.
In this case, the degree of opening of the first valve increases beyond the first predetermined degree of opening and then decreases until reaching the fourth predetermined degree of opening, which is larger than the first predetermined degree of opening. Further, the temperature in the combustion furnace temporarily decreases and then recovers the first temperature due to an increase in the degree of opening of the first valve, i.e. an increase in the combustible gas produced in the first dry distillation furnace.
Therefore, according to the third aspect of the switching operation, if the degree of opening of the first valve reaches the fourth predetermined degree of opening whereas the temperature in the combustion furnace temporarily decreases and then recovers the first temperature, then the dry distillation of the wastes held in the second dry distillation furnace is immediately started without shifting to the standby state. When the dry distillation of the wastes in the second dry distillation furnace is started, the combustible gas is produced by the dry distillation and the introduction of the combustible gas into the combustion furnace is started.
Thus, the third aspect of the switching operation makes it possible to smoothly switch the combustible gas burnt in the combustion furnace from the combustible gas produced in the first dry distillation furnace to the combustible gas produced in the second dry distillation furnace.
Further, in the dry distillation gasification waste incineration method according to the present invention, there are some cases where the temperature in the combustion furnace significantly increases without being controlled to become the first temperature.
Therefore, in the dry distillation gasification waste incineration method according to the present invention, preferably, the degree of opening of the first valve or the second valve is locked at a predetermined degree of opening when the temperature in the combustion furnace reaches the fourth predetermined temperature, which is higher than the first temperature, and the locked degree of opening of the first valve or the second valve is released when the temperature in the combustion furnace reaches a temperature below the fourth predetermined temperature.
The dry distillation gasification waste incineration method in accordance with the present invention makes it possible to restrict the amount of the combustible gas to be introduced into the combustion furnace by locking the degree of opening of the first valve or the second valve at a predetermined degree of opening when the temperature in the combustion furnace reaches the fourth predetermined temperature, which is higher than the first temperature. As a result, the temperature in the combustion furnace can be controlled to become the first temperature.
The locking of the degree of opening of the first valve or the second valve is released when the temperature in the combustion furnace reaches a temperature below the fourth predetermined temperature, thus restoring normal control.
In the dry distillation gasification waste incineration method in accordance with the present invention, two or three or more dry distillation furnaces may be provided for one combustion furnace insofar as a plurality of dry distillation furnaces are provided, the two dry distillation furnaces, for example, being provided in the present invention.
Further, the dry distillation gasification waste incineration method in accordance with the present invention includes a step of loading new wastes in the first dry distillation furnace after removing, from the first dry distillation furnace, the wastes that have been ashed in the first dry distillation furnace at the time of the dry distillation of wastes held in the second dry distillation furnace, wherein the dry distillation of the wastes in the first dry distillation furnace and the dry distillation of the wastes in the second dry distillation furnace are alternately repeated.
According to the dry distillation gasification waste incineration method in accordance with the present invention, in the case where one such combustion furnace is provided with two such dry distillation furnaces, the wastes that can produce the combustible gas run out in the first dry distillation furnace and the wastes are ashed while the wastes in the second dry distillation furnace are being subjected to dry distillation.
Therefore, when the wastes in the second dry distillation furnace are being subjected to dry distillation, the wastes that have been ashed in the first dry distillation furnace are removed and new wastes are loaded into the first dry distillation furnace to prepare for the next dry distillation. The preparation for the next dry distillation can be performed in the same manner as that for the second dry distillation furnace, and the combustion furnace can be continuously operated by alternately repeating the dry distillation of the wastes in the first dry distillation furnace and the dry distillation of the wastes in the second dry distillation furnace.
The following will describe an embodiment of the present invention in more detail with reference to the accompanying drawings.
The dry distillation gasification waste incineration method according to the present embodiment is implemented by using a dry distillation gasification incineration apparatus 1 illustrated in
The dry distillation gasification incineration apparatus 1 includes two dry distillation furnaces 2a, 2b, which hold wastes A, such as waste tires, and perform dry distillation gasification and incineration of the wastes, and a combustion furnace 4 connected to the dry distillation furnaces 2a, 2b through gas passages 3a, 3b.
Formed in the upper surface portions of the dry distillation furnaces 2a, 2b are loading ports 6a, 6b provided with openable/closable loading doors 5a, 5b, respectively, so that the wastes A can be loaded into the dry distillation furnaces 2a, 2b through the loading ports 6a, 6b. Further, with the loading doors 5a, 5b closed, the interiors of the dry distillation furnaces 2a, 2b are substantially shut off from the outside. The dry distillation furnaces 2a, 2b may be provided with weighing instruments (not illustrated), which measure a predetermined amount of the wastes A before the wastes A are loaded into the dry distillation furnaces 2a, 2b through the loading ports 6a, 6b.
Formed on the outer peripheral portions of the dry distillation furnaces 2a, 2b are water jackets, which are cooling structures, (not illustrated) isolated from the interiors of the dry distillation furnaces 2a, 2b. Water is supplied to the water jackets by a water supply apparatus, which is not illustrated, such that the water inside the water jackets is maintained at a predetermined water level.
The lower portions of the dry distillation furnaces 2a, 2b have bottom doors 7a, 7b, which are movable downward. With the bottom doors 7a, 7b closed, the interiors of the dry distillation furnaces 2a, 2b are substantially shut off from the outside. Formed at the bottom portions of the bottom doors 7a, 7b are vacant chambers 8a, 8b isolated from the interiors of the dry distillation furnaces 2a, 2b. The vacant chambers 8a, 8b are in communication with the interiors of the dry distillation furnaces 2a, 2b through a plurality of air supply nozzles 9a, 9b provided on the bottom doors 7a, 7b.
Dry distillation oxygen supply passages 10a, 10b are connected to the vacant chambers 8a, 8b, respectively, at the bottoms of the dry distillation furnaces 2a, 2b. The dry distillation oxygen supply passages 10a, 10b are connected to an oxygen supply source 12, which is composed of a forced draft fan and the like, through an oxygen supply passage 11. The dry distillation oxygen supply passages 10a, 10b are provided with control valves 13a, 13b, respectively. The degrees of opening of the control valves 13a, 13b are controlled by valve drives 14a, 14b. In this case, the valve drives 14a, 14b are controlled by a controller 15 composed of an electronic circuit, including a CPU and the like.
Further, ignition units 16a, 16b for igniting the wastes A held in the dry distillation furnaces 2a, 2b are installed at the lower portions of the div distillation furnaces 2a, 2b. The ignition units 16a, 16b are composed of ignition burners or the like and adapted to burn a fuel supplied through fuel supply passages 18a, 18b from fuel supply units 17a, 17b, thereby supplying combustion flames to the wastes A. A fuel, such as light oil, is retained in the fuel supply units 17a, 17b.
The combustion furnace 4 is comprised of a burner 19, which mixes a combustible gas produced by the dry distillation of the wastes A and oxygen (air) required for the complete combustion thereof, and a combustion unit 20 which burns a combustible gas mixed with oxygen (air). The combustion unit 20 is in communication with the burner 19 on the downstream side of the burner 19. Gas passages 3a, 3b are connected to the upstream side of the burner 19 through dumpers 21a, 21b, respectively, and the combustible gas produced by the dry distillation of the wastes A in the dry distillation furnaces 2a, 2b is introduced into the burner 19 through the gas passages 3a, 3b.
Formed on the outer peripheral portion of the burner 19 is a vacant chamber (not illustrated) isolated from the interior of the burner 19. The vacant chamber is in communication with the interior of the burner 19 through a plurality of nozzle holes (not illustrated) drilled in the inner peripheral portion of the burner 19. A combustion oxygen supply passage 22 branched from the oxygen supply passage 11 is connected to the vacant chamber. The combustion oxygen supply passage 22 is laid out to pass through the combustion unit 20 in the middle, so that the oxygen (air) preheated inside the combustion unit 20 is supplied to the vacant chamber.
The combustion oxygen supply passage 22 is provided with a control valve 23. The degree of opening of the control valve 23 is controlled by a valve drive 24. In this case, the valve drive 24 is controlled by the controller 15.
A combustion unit 25 is installed on the upstream side of the burner 19. The combustion unit 25 is comprised of an ignition burner or the like, and burns a fuel supplied from a fuel supply unit 26 through a fuel supply passage 27, thereby igniting a combustible gas introduced into the burner 19 or preheating the combustion furnace 4. A fuel, such as light oil, is retained in the fuel supply unit 26.
A hot water boiler 28 heated by the combustion exhaust from the combustion in the combustion furnace 4 is installed on the downstream side of the combustion unit 20. Water is supplied to the hot water boiler 28 from a water supply unit, which is not illustrated, and the hot water heated by making use of the combustion heat of the wastes A is used for air conditioning or the like.
Provided on the outlet side of the hot water boiler 28 is a duct 29a through which the combustion exhaust cooled in the hot water boiler 28 is discharged, the duct 29a being connected to the upper end of an air-cooled heat exchanger 31 through an on-off valve 30. Air supplied through a forced draft fan or the like, which is not illustrated, is circulated through the air-cooled heat exchanger 31 and carries out heat exchange with the combustion exhaust introduced through the duct 29a, thereby cooling the combustion exhaust. The combustion exhaust cooled by the air-cooled heat exchanger 31 is taken out through a duct 29b connected to the lower part of the air-cooled heat exchanger 31 through an on-off valve 32.
Meanwhile, a duct 29c is branched from the duct 29a on the upstream side of the on-off valve 30, and the duct 29c is connected to the upper end of a rapid cooling tower 34 through an on-off valve 33. The rapid cooling tower 34 is provided with a spray 35, which cools the combustion exhaust, which is introduced through the duct 29c, by sprinkling water thereto. The spray 35 is connected to a water supply unit (not illustrated), which supplies cooling water, and an air compressor (not illustrated).
The combustion exhaust cooled by the rapid cooling tower 34 is taken out from a duct 29d connected to the lower portion of the rapid cooling tower 34 through an on-off valve 36. The duct 29d merges with the duct 29b on the downstream side of the on-off valves 32, 36.
The duct 29b is connected to one end of a bug filter 37. Slaked lime and activated carbon supplied from a drug silo 38 are mixed with the combustion exhaust introduced to the bug filter 37 through the duct 29b, thereby carrying out desulfurization and deodorization.
The bug filter 37 is provided with a filter section and a recovery section, which recovers ash or the like separated from the combustion exhaust by filter section. An air compressor (not illustrated) is connected to the filter section to clean the filter section. A duct 29e is connected to the other end of the bug filter 37, and the duct 29e is connected to a chimney 40 through an inducing fan 39, which draws in the combustion exhaust in the combustion furnace 4. Thus, the combustion exhaust circulated through the duct 29e is released into the atmosphere from the chimney 40.
Further, a duct 29f for discharging the combustion exhaust when the hot water boiler 28 is not used is provided on the downstream side of the combustion furnace 4, the duct 29f being connected to the duct 29a on the downstream side of the hot water boiler 28 through an on-off valve 41. Further, in the dry distillation gasification incineration apparatus 1 according to the present embodiment, the combustion furnace 4 has a temperature sensor 42, which detects a temperature Tc in the combustion furnace 4 and which is provided at a position facing the downstream side of the burner 19. The detection signals of the temperature sensor 42 are input to the controller 15.
Referring now to
To incinerate the wastes A in the dry distillation gasification incineration apparatus 1, the loading door 5a of the dry distillation furnace 2a is first opened, with the bottom door 7a closed, and the wastes A, such as waste tires, are put in the dry distillation furnace 2a through the loading port 6a. If the dry distillation furnace 2a is provided with the weighing instrument, then a predetermined amount of wastes A is measured by the weighing instrument before the wastes A are loaded into the dry distillation furnace 2a through the loading port 6a.
Then, the controller 15 detects that the loading of the wastes A into the dry distillation furnace 2a has been completed and the wastes A are present in the dry distillation furnace 2a. The completion of the loading of the wastes A into the dry distillation furnace 2a can be detected by, for example, providing a limit switch that turns ON when the loading door 5a and the bottom door 7a are closed, and by detecting that the limit switch is ON. Further, if the dry distillation furnace 2a is provided with the weighing instrument, then the weighing instrument may be provided with a loading completion button so as to detect the operation state of the loading completion button. In addition, the completion of the loading may be detected by detecting that the foregoing two limit switches are ON and also by detecting the operation state of the loading completion button.
Subsequently, the loading door 5a is closed to place the interior of the dry distillation furnace 2a in a tightly sealed state, and then, prior to the ignition of the wastes A, the combustion unit 25 of the combustion furnace 4 is actuated at time t0 illustrated in
Then, as illustrated in
If the controller 15 detects that the loading of the wastes A into the dry distillation furnace 2a has been completed, the wastes A are present in the dry distillation furnace 2a, and the dumper 21a is open, then the ignition unit 16a of the dry distillation furnace 2a is actuated in a predetermined time from time t1, e.g. in five minutes, to time t2. Thus, the fuel supplied from the fuel supply unit 17a through the fuel supply passage 18a is burnt by the ignition unit 16a, thereby igniting the wastes A to start the partial combustion of the wastes A.
Next, in the dry distillation furnace 2a, the valve drive 14a is controlled by the controller 15, and the degree of opening Va of the control valve 13a is increased in steps during the period of time t2 to t3. This causes the partial combustion of the wastes A in the dry distillation furnace 2a to gradually expand by the oxygen (air) supplied from the oxygen supply source 12 and become stable, thus forming a fire bed at the bottom part of the wastes A. Upon the formation of the fire bed, the ignition unit 16a is stopped, and the dry distillation of the rest of the wastes A is started by the heat of the partial combustion of the wastes A, thus starting the production of the combustible gas. The production of the combustible gas can be detected by, for example, a rise in temperature detected by a temperature sensor (not illustrated) provided at a position facing the dry distillation furnace 2a of a gas passage 3a.
The internal space of the dry distillation furnace 2a is suctioned by the inducing fan 39 through the combustion furnace 4, so that the combustible gas is introduced into the burner 19 through the gas passage 3a. In the burner 19, the valve drive 24 is driven by the controller 15 to set the degree of opening of the control valve 23 at the predetermined degree of opening, and oxygen (air) is supplied from the oxygen supply source 12 through the oxygen supply passage 11 and the combustion oxygen supply passage 22. Therein, the combustible gas is mixed with the oxygen (air) supplied through the combustion oxygen supply passage 22 and ignited by a combustion flame supplied from the combustion unit 25, thus starting the combustion in the combustion unit 20.
Until the fire bed is formed, the temperature Tc in the combustion furnace 4 due to the combustion of the combustible gas slightly fluctuates up and down in the vicinity of 800° C. for a while, but eventually, as the production of the combustible gas becomes active and natural combustion is started, the temperature Tc gradually increases and reaches a predetermined first temperature (hereinafter referred to as “the first set temperature”), e.g. 930° C., at time t3.
When the temperature Tc in the combustion furnace 4 reaches the first set temperature due to the combustion of the combustible gas, the combustion unit 25 is stopped, and after time t3, the controller 15 starts the feedback control of the production of the combustible gas in the dry distillation furnace 2a. Thus, the degree of opening Va of the control valve 13a is controlled such that the temperature Tc in the combustion furnace 4 reaches the first set temperature by the combustion of the combustible gas.
While the production of the combustible gas is being feedback-controlled by the controller 15 such that the temperature Tc in the combustion furnace 4 becomes the first set temperature, if the temperature Tc in the combustion furnace 4 decreases and reaches a second set temperature, e.g. 875° C., which is lower than the first set temperature, then the combustion unit 25 is actuated again to heat the combustion furnace 4 by the heating power of the combustion unit 25. The combustion unit 25 is stopped when the temperature Tc in the combustion furnace 4 restores the first set temperature.
The combustion exhaust generated by the combustion of the combustible gas in the combustion unit 20 is cooled by the heat exchange in the hot water boiler 28 with the water circulated through the hot water boiler 28 and discharged into the duct 29a. Alternatively, the combustion exhaust is discharged into the duct 29a through the duct 29f without passing through the hot water boiler 28 by opening the on-off valve 41.
If the combustion exhaust passes through the hot water boiler 28, the combustion exhaust discharged into the duct 29a is introduced into the air-cooled heat exchanger 31 from the duct 29a to be further cooled by the heat exchange with air circulated through the air-cooled heat exchanger 31, and discharged into the duct 29b. At this time, the on-off valves 30, 32 located before and after the air-cooled heat exchanger 31 are open, while the on-off valves 33, 36 located before and after the rapid cooling tower 34 are closed.
Further, if the combustion exhaust discharged into the duct 29a does not pass through the hot water boiler 28, then the combustion exhaust is introduced into the rapid cooling tower 34 from the duct 29c and cooled by the cooling water sprinkled from a spray 35, and discharged into the duct 29b through the duct 29d. At this time, the on-off valves 30, 32 located before and after the air-cooled heat exchanger 31 are closed, while the on-off valves 33, 36 located before and after the rapid cooling tower 34 are open.
Subsequently, the combustion exhaust discharged into the duct 29b is mixed with slaked lime and activated carbon supplied from the drug silo 38 to carry out desulfurization and deodorization, and introduced to the bug filter 37 so as to remove ash, dust and the like, before being discharged into the duct 29e and then released into the atmosphere through the chimney 40.
Until time t3 at which the feedback control of the production of the combustible gas in the dry distillation furnace 2a is started, the degree of opening Va of the control valve 13a is increased in steps to increase the temperature Tc in the combustion furnace 4 by the combustion of the combustible gas. However, if the degree of opening Va is increased after the temperature Tc in the combustion furnace 4 reaches the first set temperature, then the temperature Tc in the combustion furnace 4 continues to increase beyond the first set temperature, because a sufficient amount of the wastes A that enables the combustible gas to be produced by dry distillation still remains in the dry distillation furnace 2a at that point of time.
Therefore, as illustrated in
Therefore, after time t4, the degree of opening Va of the control valve 13a is controlled by the controller 15 through the valve drive 14a such that the degree of opening Va of the control valve 13a repeats slight increases and decreases, indicating an increasing trend as a whole via a degree of opening Va0 (e.g. 50%) and a degree of opening Va1 (e.g. 53%) until time t5 (a first increasing phase). During the period of time t4 to t5, the remaining amount of the wastes A that can produce the combustible gas by dry distillation in the dry distillation furnace 2a further decreases; however, during this period, the degree of opening Va of the control valve 13a is increased, so that the wastes A that are sufficient for producing more combustible gas remain. As a result, when time t5 is reached, further increasing the degree of opening Va of the control valve 13a will cause the temperature Tc in the combustion furnace 4 to excessively increase, making it difficult to maintain the temperature Tc at the first set temperature.
Therefore, the degree of opening Va of the control valve 13a is controlled by the controller 15 through the valve drive 14a such that, after reaching a maximum at time t5 via a degree of opening Va1 (e.g. 53%), the degree of opening Va of the control valve 13a repeats slight increases and decreases, indicating a decreasing trend as a whole via a degree of opening Va1 (e.g. 50%) until time t6 (a second decreasing phase). During the period of time t5 to t6, the remaining amount of the wastes A that can produce the combustible gas by dry distillation in the dry distillation furnace 2a further decreases. When time t6 is reached, further decreasing the degree of opening Va of the control valve 13a will cause the temperature Tc in the combustion furnace 4 to excessively decrease, making it difficult to control the temperature Tc to become the first set temperature.
Therefore, the degree of opening Va of the control valve 13a is controlled by the controller 15 through the valve drive 14a such that, after reaching a minimum at time t6 via a degree of opening Va2 (e.g. 50%), the degree of opening Va of the control valve 13a repeats slight increases and decreases, indicating a rapidly increasing trend as a whole via a degree of opening Va3 (e.g. 60%), and reaches a degree of opening Va1 (e.g. 80%) at time t7 (a second increasing phase). During the period of time t6 to t7, the wastes A that can produce the combustible gas by dry distillation in the dry distillation furnace 2a are mostly lost. However, at time t7, the production of the combustible gas by the dry distillation of the wastes A in a second dry distillation furnace 2b is started and the combustible gas produced in the second dry distillation furnace 2b is introduced into the combustion furnace 4, as will be discussed hereinafter.
Hence, after starting the introduction of the combustible gas, which has been produced in the second dry distillation furnace 2b, into the combustion furnace 4, the controller 15 controls the degree of opening Va of the control valve 13a such that the temperature Tc in the combustion furnace 4 obtained by combining the combustion of the combustible gas produced in the first dry distillation furnace 2a and the combustion of the combustible gas produced in the second dry distillation furnace 2b becomes the first set temperature. Thus, the degree of opening Va of the control valve 13a is controlled by the controller 15 through the valve drive 14a such that the degree of opening Va of the control valve 13a repeats slight increases and decreases, indicating a decreasing trend as a whole (a third decreasing phase).
However, in the third deceasing phase, the production of a small amount of the combustible gas continues in the first dry distillation furnace 2a, so that the interaction with the combustible gas produced in the second dry distillation furnace 2b may cause the temperature Tc in the combustion furnace 4 to rapidly increase and exceed the first set temperature Tc at, for example, time t8.
Therefore, if the temperature Tc in the combustion furnace 4 reaches a predetermined temperature (a fourth predetermined temperature Tc in claim 6), e.g. 915° C., which is higher than the first set temperature, the controller 15 locks the degree of opening Va of the control valve 13a at a predetermined degree of opening Va5, e.g. 60%, through the valve drive 14a. The control for locking the degree of opening Va of the control valve 13a at the degree of opening Va5 by the controller 15 is released when the temperature Tc in the combustion furnace 4 is reset to the first set temperature. Thereafter, the controller 15 increases the degree of opening Va of the control valve 13a to a predetermined degree of opening Va6, e.g. 80%, through the valve drive 14a, locks the degree of opening Va of the control valve 13a at the degree of opening Va6, and ashes the wastes A in the dry distillation furnace 2a.
Further, while the degree of opening Va of the control valve 13a is being locked at the predetermined degree of opening Va6 by the controller 15, the temperature Tc in the combustion furnace 4 may increase and reach a predetermined temperature, e.g. 915° C. (the fourth predetermined temperature in claim 6), which is higher than the first set temperature, as indicated by the virtual line in
In this case, therefore, the controller 15 decreases the degree of opening Va of the control valve 13a and locks the degree of opening Va at a predetermined degree of opening Va7, e.g. 50%, through the valve drive 14a. The control for locking the degree of opening Va of the control valve 13a at the degree of opening Va7 by the controller 15 is released when the temperature Tc in the combustion furnace 4 reaches a temperature below a predetermined temperature that is higher than the first set temperature.
Although not illustrated, after the wastes A in the dry distillation furnace 2a are ashed, the controller 15 decreases the degree of opening Va of the control valve 13a at a predetermined rate through the valve drive 14a until the control valve 13a is closed.
In the dry distillation furnace 2a, when the ashing of the wastes A is completed and the control valve 13a is closed, the bottom door 7a is moved down to discharge the wastes A which have been ashed, and the bottom door 7a is reset to the original position thereof. Then, the loading door 5a is opened, and the wastes A, such as waste tires, are loaded into the dry distillation furnace 2a through the loading port 6a to prepare for the next processing.
In the first aspect of the dry distillation gasification waste incineration method according to the present embodiment, as illustrated in
Subsequently, after the controller 15 detects that the loading of the wastes A into the dry distillation furnace 2b is complete and that the wastes A are present in the dry distillation furnace 2b, when the degree of opening Va of the control valve 13a in the dry distillation furnace 2a reaches a predetermined degree of opening Va0, e.g. 50%, at time t41 in the first increasing phase, the dumper 21b is opened, the valve drive 14b in the dry distillation furnace 2b is driven by the controller 15 to set the degree of opening Vb of the control valve 13b to a predetermined degree of opening, e.g. 25%, and oxygen (air) is supplied to the dry distillation furnace 2b from the oxygen supply source 12 through the oxygen supply passage 11 and the dry distillation oxygen supply passage 10b, as illustrated in
Subsequently, when the degree of opening Va of the control valve 13a in the dry distillation furnace 2a reaches the first predetermined degree of opening Va1, e.g. 53%, at time t42 in the first increasing phase, the ignition unit 16b of the dry distillation furnace 2b is actuated. As a result, the wastes A in the dry distillation furnace 2b are ignited by the combustion of a fuel supplied from the fuel supply unit 17b through the fuel supply passage 18b, thus starting the partial combustion of the wastes A.
The detection of the completion of the loading of the wastes A into the dry distillation furnace 2b and the presence of the wastes A in the dry distillation furnace 2b by the controller 15 can be performed in the same manner as that for the dry distillation furnace 2a.
The wastes A in the dry distillation furnace 2b may alternatively be ignited when the degree of opening Va of the control valve 13a reaches the first predetermined degree of opening Va1 and the temperature in the dry distillation furnace 2a reaches, for example, 200° C. The wastes A in the dry distillation furnace 2b can be securely ignited at a proper timing by detecting both the degree of opening Va of the control valve 13a and the temperature in the dry distillation furnace 2a.
Subsequently, in the dry distillation furnace 2b, the valve drive 14b is controlled by the controller 15 to increase the degree of opening Vb of the control valve 13b in steps. This causes the partial combustion of the wastes A in the dry distillation furnace 2b to gradually expand by the oxygen (air) supplied from the oxygen supply source 12 and become stable, thus forming a fire bed on the bottom part of the wastes A. Upon the formation of the fire bed, the ignition unit 16b is stopped.
Subsequently, when the degree of opening Va of the control valve 13a in the dry distillation furnace 2a reaches a second predetermined degree of opening Va2, e.g. 50%, which is smaller than the first predetermined degree of opening Va1, at time t51 in the second decreasing phase, the valve drive 14b is controlled by the controller 15 to decrease the degree of opening Vb of the control valve 13b to, for example, 15%, and a sufficient amount of oxygen (air) required to maintain the fire bed is supplied to the dry distillation furnace 2b from the oxygen supply source 12 through the oxygen supply passage 11 and the dry distillation oxygen supply passage 10b.
As a result, the dry distillation furnace 2b is placed in a state in which the dry distillation of the wastes A held in the furnace has not yet started, whereas the fire bed is being maintained, i.e. in a standby state in which the dry distillation of the wastes A can be immediately started as necessary. While the dry distillation furnace 2b is in the standby state, the degree of opening Vb of the control valve 13b is maintained at an opening that allows a sufficient amount of oxygen (air) required for maintaining the fire bed to be supplied to the dry distillation furnace 2b.
Subsequently, when the degree of opening Va of the control valve 13a in the dry distillation furnace 2a reaches a third predetermined degree of opening Va3, e.g. 60%, which is larger than the second predetermined degree of opening Va2, at time t61 in the second increasing phase, the valve drive 14b is controlled by the controller 15 in the dry distillation furnace 2b to increase the degree of opening Vb of the control valve 13b. This causes the standby state to be cleared, so that the dry distillation of the wastes A held in the dry distillation furnace 2b is started, and the combustible gas produced in the dry distillation furnace 2b is introduced into the burner 19 of the combustion furnace 4 through a gas passage 3b. The production of the combustible gas can be detected by, for example, a rise in temperature detected by a temperature sensor (not illustrated) provided at a position facing the dry distillation furnace 2b of a gas passage 3b, as with the case of the dry distillation furnace 2a.
Subsequently, after the introduction of the combustible gas, which has been produced in the second dry distillation furnace 2b, into the combustion furnace 4 is started, the controller 15 controls the degree of opening Va of the control valve 13a such that the temperature Tc in the combustion furnace 4 obtained by combining the combustion of the combustible gas produced in the first dry distillation furnace 2a and the combustion of the combustible gas produced in the second dry distillation furnace 2b becomes the first set temperature, as described above. Thus, the degree of opening Va of the control valve 13a reaches a maximum degree of opening Va4, e.g. 80%, beyond the third predetermined degree of opening Va3, and then shifts to the decreasing trend (the third decreasing phase).
Subsequently, at time t8, the controller 15 locks the degree of opening Va of the control valve 13a at a predetermined degree of opening Va5 through the valve drive 14a, and also controls the degree of opening Vb of the control valve 13b such that the temperature Tc in the combustion furnace 4 due to the combustion of the combustible gas produced in the dry distillation furnace 2b becomes the first set temperature, thus feedback-controlling the production of the combustible gas in the dry distillation furnace 2b. Meanwhile, the generation of the combustible gas in the dry distillation furnace 2a completely stops, and the combustible gas to be burnt in the combustion furnace 4 is switched from the combustible gas produced in the dry distillation furnace 2a to the combustible gas produced in the dry distillation furnace 2b.
Thus, the first aspect of the dry distillation gasification waste incineration method according to the present embodiment makes it possible to smoothly switch the combustible gas to be burnt in the combustion furnace 4 from the combustible gas produced in the dry distillation furnace 2a to the combustible gas produced in the dry distillation furnace 2b.
Referring now to
In the dry distillation gasification incineration apparatus 1, the operation for igniting the wastes A in the dry distillation furnace 2b can be performed by the controller 15 actuating the ignition unit 16b when the degree of opening Va of the control valve 13a in the dry distillation furnace 2a reaches the first predetermined degree of opening Va1, as described above. Further, the operation for forming a fire bed in the wastes A in the dry distillation furnace 2b can be performed by the controller 15 controlling the valve drive 14b to increase the opening Vb of the control valve 13b in steps, as described above.
However, depending on the timing of the ignition of the wastes Ain the dry distillation furnace 2b, there are cases where, during the process of forming the fire bed, the wastes A that can produce the combustible gas in the dry distillation furnace 2a decrease and the temperature Tc in the combustion furnace 4 can no longer be controlled to the first set temperature T1, e.g. 955° C., merely by the combustion of the combustible gas produced in the dry distillation furnace 2a.
In this case, as illustrated in
Therefore, in the second aspect of the dry distillation gasification waste incineration method according to the present embodiment, the dry distillation of the wastes A in the dry distillation furnace 2b is immediately started without shifting to the standby state in the case where the temperature Tc in the combustion furnace 4 decreases to the temperature T2, the combustion unit 25 is ignited, and the temperature Td in the dry distillation furnace 2a decreases to a third predetermined temperature Td2 (e.g. a temperature that is lower than the maximum temperature Td1 by 10° C.) and then the temperature Tc in the combustion furnace 4 recovers the first set temperature T1 at time t11. When the dry distillation of the wastes A in the dry distillation furnace 2b is started, the combustible gas is produced by the dry distillation and the introduction of the combustible gas into the combustion furnace 4 is started.
Thus, the second aspect of the dry distillation gasification waste incineration method according to the present embodiment makes it possible to smoothly switch the combustible gas to be burnt in the combustion furnace 4 from the combustible gas produced in the dry distillation furnace 2a to the combustible gas produced in the dry distillation furnace 2b.
Referring now to
In the dry distillation gasification incineration apparatus 1, the operation for igniting the wastes A in the dry distillation furnace 2b can be performed by the controller 15 actuating the ignition unit 16b when the degree of opening Va of the control valve 13a in the dry distillation furnace 2a reaches the first predetermined degree of opening Va1, as described above. Further, the operation for forming a fire bed in the wastes A in the dry distillation furnace 2b can be performed by the controller 15 controlling the valve drive 14b to increase the opening Vb of the control valve 13b in steps, as described above.
However, depending on the timing of the ignition of the wastes A in the dry distillation furnace 2b, there are some cases where, during the process of forming the fire bed, the wastes A that can produce the combustible gas in the dry distillation furnace 2a decrease, and the degree of opening Va of the control valve 13a gradually increases in order to control the temperature Tc in the combustion furnace 4 to the first set temperature Tc.
In this case, after exceeding the first predetermined degree of opening Va1, the degree of opening Va of the control valve 13a continues to increase without decreasing to become the degree of opening Va2, and then decreases to reach a predetermined degree of opening Va11, which is larger than the first predetermined degree of opening Va1. Further, at this time, the temperature Tc in the combustion furnace 4 temporarily decreases and then recovers the first set temperature T1 due to an increase in the degree of opening of the control valve 13a, i.e. an increase in the combustible gas produced in the dry distillation furnace 2a.
Therefore, in the third aspect of the dry distillation gasification waste incineration method according to the present embodiment, the dry distillation of the wastes A in the dry distillation furnace 2b is immediately started without shifting to the standby state in the case where the degree of opening Va of the control valve 13a continues to increase without decreasing to become the degree of opening Va2 after exceeding Va1, and then decreases to reach the degree of opening Va11, which is larger than the degree of opening Va1, whereas the temperature Tc in the combustion furnace 4 temporarily decreases and then recovers the first set temperature T1. When the dry distillation of the wastes A in the dry distillation furnace 2b is started, the combustible gas is produced by the dry distillation and the introduction of the combustible gas into the combustion furnace 4 is started.
Thus, the third aspect of the dry distillation gasification waste incineration method according to the present embodiment makes it possible to smoothly switch the combustible gas to be burnt in the combustion furnace 4 from the combustible gas produced in the dry distillation furnace 2a to the combustible gas produced in the dry distillation furnace 2b.
Further, according to the dry distillation gasification waste incineration method according to the present embodiment, the switching of the combustible gas to be burnt in the combustion furnace 4 from the combustible gas produced in the dry distillation furnace 2b to the combustible gas produced in the dry distillation furnace 2a can be performed in the same manner as that for switching from the combustible gas produced in the dry distillation furnace 2a to the combustible gas produced in the dry distillation furnace 2b. Hence, the dry distillation gasification waste incineration method according to the present embodiment makes it possible to continuously operate the dry distillation gasification incineration apparatus 1 by alternately repeating the dry distillation of the wastes A in the two dry distillation furnaces 2a, 2b for the single combustion furnace 4.
Further, in the dry distillation gasification waste incineration method according to the present embodiment, the valve drives 14a, 14b are controlled by the single controller 15. Alternatively, however, a plurality of controllers may be provided to separately control the valve drives 14a, 14b.
1 . . . Dry distillation gasification incineration apparatus; 2a, 2b . . . Dry distillation furnace; 4 . . . Combustion furnace; 10a, 10b . . . Oxygen supply passage; 12 . . . Oxygen supply source; 15 . . . Controller; and A . . . Wastes.
| Number | Date | Country | Kind |
|---|---|---|---|
| PCT/JP2016/052725 | Jan 2016 | WO | international |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2017/002930 | 1/27/2017 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2017/131158 | 8/3/2017 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 4913069 | Schultz | Apr 1990 | A |
| 5313894 | Ishikawa | May 1994 | A |
| 5619938 | Kaneko | Apr 1997 | A |
| 20040103831 | Pope | Jun 2004 | A1 |
| Number | Date | Country |
|---|---|---|
| H02-135280 | May 1990 | JP |
| H08-94043 | Apr 1996 | JP |
| H09-14623 | Jan 1997 | JP |
| 2005-009830 | Jan 2005 | JP |
| 2005-345078 | Dec 2005 | JP |
| 4050189 | Dec 2007 | JP |
| 2006117855 | Nov 2006 | WO |
| Entry |
|---|
| International Search Report, dated Mar. 21, 2017 (Mar. 21, 2017), 2 pages. |
| Number | Date | Country | |
|---|---|---|---|
| 20190032917 A1 | Jan 2019 | US |
