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WO2014126268A1 - Smokeless, odorless, dustless incineration device - Google Patents

Smokeless, odorless, dustless incineration device Download PDF

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Publication number
WO2014126268A1
WO2014126268A1 PCT/JP2014/054248 JP2014054248W WO2014126268A1 WO 2014126268 A1 WO2014126268 A1 WO 2014126268A1 JP 2014054248 W JP2014054248 W JP 2014054248W WO 2014126268 A1 WO2014126268 A1 WO 2014126268A1
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WO
WIPO (PCT)
Prior art keywords
exhaust gas
furnace
incinerator
signal
temperature
Prior art date
Application number
PCT/JP2014/054248
Other languages
French (fr)
Japanese (ja)
Inventor
健仁 福富
Original Assignee
トマス技術研究所
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Filing date
Publication date
Application filed by トマス技術研究所 filed Critical トマス技術研究所
Publication of WO2014126268A1 publication Critical patent/WO2014126268A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/50Control or safety arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/12Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating using gaseous or liquid fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • F23G5/165Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber arranged at a different level
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/24Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a vertical, substantially cylindrical, combustion chamber
    • F23G5/245Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a vertical, substantially cylindrical, combustion chamber with perforated bottom or grate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/06Arrangements of devices for treating smoke or fumes of coolers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L9/00Passages or apertures for delivering secondary air for completing combustion of fuel 
    • F23L9/02Passages or apertures for delivering secondary air for completing combustion of fuel  by discharging the air above the fire
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2203/00Furnace arrangements
    • F23G2203/40Stationary bed furnace
    • F23G2203/401Stationary bed furnace with support for a grate or perforated plate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2203/00Furnace arrangements
    • F23G2203/40Stationary bed furnace
    • F23G2203/403Stationary bed furnace with substantial cylindrical combustion chamber

Definitions

  • the present invention applies to general waste such as garbage, paper and wood scraps from households and offices due to normal consumer life, industrial waste such as rubber products and plastics that are no longer needed at production factories and construction sites, and many others.
  • the present invention relates to a pollution-free incineration apparatus that prevents emission of pollutant substances such as soot, odors, and dust floating in the exhaust gas in the incinerator when the incinerator is combusted and incinerated.
  • the Food Recycling Law which is intended to recycle raw materials such as feed and fertilizer, has been enforced for unsold food, leftover food, or food waste generated in the food manufacturing process.
  • automobile tires that have become worn out and are no longer used due to problems with safe driving have been developed by the Automobile Recycling Law. Recycling technology has been developed.
  • the current situation is that they are piled up and left for a long time. Also, it is generally prohibited for individuals to incinerate general waste and industrial waste on their own due to the problem of polluting the environment by causing harmful substances such as black smoke, nitrogen oxides and dioxins to be polluted. It has been.
  • 2001-99414 discloses that the outer wall of the first combustion chamber and the combustion gas second combustion chamber, which suppresses the discharge of oxydine by raising the temperature to 800 ° C., kneaded with red clay and water added to the calcined gypsum.
  • a waste incinerator that can withstand high temperatures and easily repair the outer wall of a combustion chamber that has been peeled off by building a metal mesh plate that has been coated and cured with a metal mesh is disclosed.
  • JP 2004-321958 A discloses that, in order to remove the acid gas discharged from the incinerator for municipal waste and industrial waste, the sodium bicarbonate powder added in the exhaust gas flue is brought into contact with the acid gas in the exhaust gas.
  • An incinerator exhaust gas treatment method for reacting and recovering the produced neutralized salt is also disclosed. None of the waste incinerators and exhaust gas treatment methods described above are superior in that the durability of the furnace body is improved compared to the previous prior art, and that the waste combustibility and exhaust gas treatability are remarkable. Technology. However, the incinerator or incineration method that has been developed to date is an incineration technology that supplies the amount of air necessary for the incinerated product to burn, so that the incineration time is long and the tar contained in the exhaust gas is contained in the inner wall of the incinerator. There was a point that should be markedly improved with respect to the effect of suppressing the scattering of smoke, odors and harmful substances.
  • 2008-57906 discloses an incinerator that burns an incinerated product by supplying excess air, and an exhaust gas combustion burner and an exhaust gas extinguishing burner while maintaining the exhaust gas generated in the incinerator at a high temperature.
  • the above-mentioned small incinerator and low-pollution incineration equipment developed by the applicant of the present application combusts and incinerates the incinerated object at a supercharged air ratio, so that the waste is completely ashed and the exhaust gas is also smokeless and odorless
  • the exhaust gas is rapidly cooled from high temperature to low temperature, generation and resynthesis of dioxins are suppressed, and it is discharged into the atmosphere with low or no pollution.
  • the present inventors have found that smoke and odor generated by incomplete combustion even if the incinerated material causes a collapse of cargo during combustion in an incinerator, floating dust, soaring deposited ash, etc.
  • a pollution-free incinerator furnace
  • the exhaust gas combustion burner It was found that the purpose can be achieved by providing an air supply blower for burning incinerators, a mist nozzle, etc., and controlling these control circuits through a smoke concentration sequencer controller.
  • the present invention is configured based on the knowledge, and the gist of the present invention is that an exhaust gas collecting outlet is provided on the upper side of the upper chamber separated from the upper and lower chambers by installing a grate in the furnace and opened and closed on the furnace wall.
  • An incinerator input device having a flexible heat-resistant door, an incinerator combustion burner directed to the incinerator on the grate inserted from the incinerator input device, and a door that can be opened and closed in the lower chamber
  • An incinerator ash scraper outlet is provided and an incinerator combustion air supply blower is provided on the furnace wall via a furnace air quantity adjustment damper.
  • the exhaust gas collecting outlet of the incinerator is supplied from an exhaust gas cooling air supply blower.
  • An exhaust gas cooling tower with built-in air induction pipes with a number of air nozzle holes for ejecting the air to be exhausted in the direction of crossing the exhaust gas flow paths, and a projector and a light receiver relative to the exhaust gas outlet side of the exhaust gas cooling tower Install it on the opposite side
  • a smoke concentration indicator that outputs a high output signal and a proportional control signal of the smoke concentration deviation output signal with an arithmetic control that compares the smoke concentration detection value of the smoke concentration indicator converter that measures the transmission density with a preset target concentration value.
  • the internal temperature setting signal for comparing the internal temperature setting signal is received.
  • the internal temperature deviation signal of the internal temperature sequencer controller and the composite signal connecting the high output signal of the soot concentration sequencer controller described above are received.
  • connect the burner relay controller for burning the incinerator to control the burner burner that injects the amount of fuel required to raise the temperature inside the furnace and completely burn the incinerator and soot.
  • the mist nozzle that opens the water supply solenoid valve and injects mist-like water is installed above the upper chamber of the incinerator.
  • a smokeless odorless dustless incinerator configured by connecting a control circuit that operates by receiving a proportional control signal of a sensor controller to the above-described exhaust gas cooling air supply blower.
  • the invention having the above-described structure is a smokeless odorless dustless incinerator configured to be connected to an in-furnace air amount adjusting damper of an air supply blower for burning incinerated objects as necessary.
  • the smokeless, odorless, dustless incinerator of the present invention configured as described above is an incineration object, for example, when two old 12-inch automobile tires that are no longer needed are stacked and incineration is attempted. Even if the phenomenon of cargo collapse occurs, the smoke concentration detection value of the gas discharged from the exhaust gas tower is stable, colorless and smokeless, and dust-free. During this time, the combustion time until the tires were incinerated was completely incinerated in 1 hour. Since old tires, which are generally considered difficult to be incinerated, are incinerated with no smoke, no odor, and no dust, there is no room for doubt of environmental pollution in the incineration of combustible garbage, paper waste and wood waste from homes and offices.
  • Table 1 shows the measurement and analysis of pollutants such as dioxin concentration and sulfur oxide emission in exhaust gas or incineration ash when industrial waste such as rubber products and plastics that are no longer needed is incinerated with the incinerator of the present invention. Results are shown. The measurement results for all substances are much lower than the legally stipulated values, suggesting pollution-free.
  • FIG. 1 shows an embodiment of the present invention.
  • FIG. 2 shows another embodiment of the present invention.
  • FIG. 1 shows a cross-sectional view of an embodiment of the present invention.
  • FIG. 2 shows a cross-sectional view of another embodiment of the present invention.
  • 1 is an incinerator (or also called a combustion furnace), and the furnace wall is constructed of a heat-resistant metal material, an iron shell, or an amorphous refractory or a refractory brick, and is built in a heat-resistant structure.
  • the incinerator 1 is provided with an exhaust gas collecting outlet 3 above the upper chamber A separated from the upper and lower chambers A and B by installing a grate 2 in the furnace, and a heat-resistant door 4 that can be opened and closed on the furnace wall. And an incineration object combustion burner 7 directed to the incineration object 6 on the grate 2 input from the incineration object input device 5.
  • the incinerator charging device 5 and the incinerator combustion burner 7 are preferably provided on the opposite furnace wall surfaces as shown in the drawing, but may be provided on the same furnace wall surface due to the problem of the incinerator installation location. It may also be provided separately on the adjacent furnace wall.
  • the other lower chamber B is provided with an incineration ash outlet 9 having a door 8 that can be freely opened and closed, and an incinerated combustion air supply blower 11 is provided on the furnace wall via a furnace air amount adjusting damper 10.
  • the incinerator 1 covers general waste such as garbage and paper waste, industrial waste such as rubber products and plastics, and many other types of combustible waste that are thrown into the grate 2 from the incinerator input device 5. It is provided with a structure that burns and burns with kerosene and gas fluid fuel fired from the incineration combustion burner 7 and drops the incinerated ash that has fallen from the grate 2 and accumulated from the incineration ash scraper 9 .
  • Reference numeral 12 denotes an exhaust gas cooling tower.
  • the exhaust gas cooling tower 12 discharges while cooling the exhaust gas having high-temperature heat, and the air supplied from the exhaust gas cooling air supply blower 14 into the air induction pipe 13 made of a heat-resistant metal material.
  • the air guide pipe 13 having a large number of air nozzle holes 15 ejected in the direction of crossing the exhaust gas flow paths is built in, and is connected so as to stand at the exhaust gas collecting outlet 3 of the incinerator 1. That is, the exhaust gas cooling tower 12 rapidly cools the exhaust gas exhausted while rising from the exhaust gas collecting outlet 3 of the incinerator 1 with the air ejected from the air nozzle hole 15, and suppresses the generation and resynthesis of dioxins.
  • the structure Provided in the structure.
  • Reference numeral 16 denotes an umbrella member.
  • the umbrella member 16 is a member that is held up to prevent rain, snow, and the like, and is necessary so that rain does not enter the exhaust gas cooling tower 12 and interfere with the furnace equipment and combustion work of the incinerator 1. It can be attached accordingly, and its shape and mounting structure are not particularly limited.
  • the smokeless odorless dustless incinerator of the present invention is provided with the exhaust gas cooling tower 12 at the exhaust gas collecting outlet 3 of the incinerator 1 as described above, and further detects the smoke concentration of the exhaust gas at the exhaust gas outlet side of the exhaust gas cooling tower 12.
  • the control circuit is configured to supply a gas or air necessary for pollution-free operation such as an air supply blower alone or in combination.
  • Reference numeral 17 denotes a soot concentration indicator converter.
  • a light receiver 18 and a projector 19 are installed on the opposite sides of the exhaust gas outlet of the exhaust gas cooling tower 12, and light is transmitted while being partially shielded by soot or dust in the exhaust gas. Is converted into electricity (current), and the converted output is calculated to measure the light transmission density.
  • Reference numeral 20 denotes a smoke concentration sequencer controller, which is an arithmetic control for comparing the smoke concentration detection value obtained by electrically converting the light transmission concentration output signal transmitted from the smoke concentration indicating converter 17 with a preset target set concentration value.
  • the state where the smoke concentration detection value of the exhaust gas discharged from the 12 exhaust gas outlets is higher than a predetermined target set concentration value is set as a high output signal H, and conversely, the control is performed when the smoke concentration detection value is lower than the target set concentration value.
  • a controller that outputs the signal P.
  • the high output signal H of the smoke concentration sequencer controller 20 is transmitted to the in-furnace temperature sequencer controller 23, the burner relay controller 24 for burning the incinerator, the burner relay controller 27 for non-gas combustion, and the electromagnetic valve 29 for water supply.
  • the proportional control signal P is provided in a circuit that transmits to the exhaust gas cooling air supply blower 14 of the exhaust gas cooling tower 12.
  • the in-furnace temperature sequencer controller 23 that receives the high output signal of the smoke concentration sequencer controller 20 is preset with an electric signal obtained by converting the detected temperature of the in-furnace thermometer 21 provided in the upper chamber side A of the incinerator 1.
  • the in-furnace temperature sequencer controller 23 is provided in a composite receiving circuit that receives the composite signal of the high output signal H of the smoke concentration sequencer controller 20 and the in-furnace temperature deviation signal of the temperature controller 22. Further, the furnace temperature sequencer controller 23 receives the composite signal of the high output signal H of the smoke concentration sequencer controller 20 and the furnace temperature deviation signal of the temperature controller 22, and uses the furnace temperature deviation signal for the incinerator. It is provided in a circuit that transmits to the combustion burner relay controller 24 and the exhaust gas combustion burner relay controller 27.
  • the burner relay controller 24 for incineration combustion connected to the in-furnace temperature sequencer controller 23 receives one or both of the composite signals transmitted by the in-furnace temperature sequencer controller 23. While the high output signal H is received, the smoke concentration detection value is higher than the target concentration. Therefore, the incineration object is burned while the burning power of the incineration combustion burner 7 is increased and the unburned substances such as smoke and dust are completely burned. 6 is burned. When only the furnace temperature deviation is received, the heating power of the incinerated combustion burner 7 is adjusted according to the sign of the deviation signal and its magnitude. Further, while receiving the composite signal of the high output signal H and the furnace temperature deviation signal at the same time, the incinerator combustion burner 7 is controlled while being controlled by both signals.
  • the burner relay controller 24 for burning the incinerator is incinerated on the grate 2 while receiving either one of the high output signal H and the in-furnace temperature deviation signal or both. It is provided in a circuit for controlling the temperature inside the furnace to completely burn the fuel such as kerosene and gas injected from the burner 7 to be incinerated, dioxin, soot and dust in the incinerator 6 and exhaust gas. . Further, the exhaust gas collecting outlet 3 of the upper chamber A of the incinerator 1 contains smoke, odor, dust, etc. of completely unburned substances mixed in the exhaust gas circulating in the incinerator 1 or the exhaust gas flowing out to the exhaust gas cooling tower 12. An exhaust gas combustion burner 25 for complete combustion is provided.
  • the exhaust gas combustion burner 25 receives the in-furnace temperature deviation signal of the in-furnace temperature sequencer 23 and the high output signal H of the soot concentration sequencer controller 20 via the ignition continuation timer 26, and the in-furnace temperature sequencer controller.
  • An exhaust gas combustion burner relay controller 27 for receiving the 23 furnace temperature deviation signal is connected. That is, the exhaust gas combustion burner relay control 27 controls the incineration combustion burner relay control while receiving either one of the composite signal connecting the high output signal H and the in-furnace temperature deviation signal or both of them.
  • exhaust gas floating in the furnace, unburned gas, dust, soot, odor, and dust flowing into the exhaust gas outlet 3 are completely burned while adjusting the amount of fuel injected from the exhaust gas combustion burner 25.
  • a switch is provided when the exhaust gas combustion burner 25 repeats ignition and extinguishing by providing an ignition continuation timer 26 in the high output signal transmission circuit of the smoke concentration sequencer controller 20.
  • Reference numeral 28 denotes a mist nozzle provided on the upper stage side of the upper chamber A of the incinerator 1.
  • the mist nozzle 28 is provided with a water supply electromagnetic valve 29 having a relay circuit that receives and operates either one of the composite signal that connects the high output signal H and the furnace temperature deviation signal, or both signals, When the incinerated object 6 collapses during incineration and dust or soot is mixed with the exhaust gas and receives a high output signal H, or when the furnace temperature rises above the set temperature and receives an in-furnace temperature deviation signal or When both signals are received at the same time, the mist of water sprayed from the water supply solenoid valve 29 of the relay circuit settles on the surface of the soaring dust, and the water is incinerated with the oxygen in the furnace. Extinguish suffocation by blocking objects and maintain the target temperature.
  • the exhaust gas cooling air supply blower 14 receives the proportional signal P of the smoke concentration sequencer controller 20 and supplies the required amount of air to the exhaust gas cooling tower 12.
  • a quantity adjusting device (not shown) is connected. That is, the exhaust gas cooling air supply blower 14 is air that is forcibly sent to the supercharged air state in the exhaust gas cooling tower 12 from a large number of air nozzle holes 15 ejected in the direction of crossing the exhaust gas flow paths.
  • the exhaust gas passing through the gas is rapidly cooled to a low temperature to prevent dioxins from being re-synthesized, and the unburned substances such as rising unburned gas, odor and dust are pushed back to the incinerator 1 to promote complete combustion. .
  • the present invention constructed as described above is a smokeless odorless dustless incinerator, as shown in FIG. 2 as another embodiment, for the simplification and weight reduction of the main body device and an inexpensive production cost, and for the same blower purpose,
  • the exhaust gas cooling air supply blower 14 and the incinerated substance combustion air supply blower 11 may be combined into a structure that can be shared by one blower power source.
  • the smokeless odorless dustless incinerator of the present invention having the above-described structure is configured to dispose of general waste or combustible waste that is input from the incinerator input device 5 of the incinerator 1 onto the grate 2 or sequentially input.
  • the smokeless, odorless and dusty incinerator of the present invention can be incinerated with smokeless, odorless and dustless to rubber products which are considered to be flame retardant and easily generate many harmful substances in addition to general waste. It is likely to be widely used in residential areas and even in scenic islands surrounded by the blue sea.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Incineration Of Waste (AREA)
  • Air Supply (AREA)

Abstract

Provided is a device for incinerating discarded material such as everyday garbage, unwanted rubber products, and plastics, without generating smoke, odors, or dust. An incineration material (6), which has been placed on a fire grating (2) of an incineration furnace (1), is incinerated without generating smoke, odors, or dust, by controlling an incineration material combustion burner (7) and an exhaust gas combustion burner (25) and a mist nozzle (28) provided in an exhaust gas collective outflow port (3), and an air supply blower used for cooling the exhaust gas, and, as needed, by controlling a blower (11) used for burning the incineration material. This control is performed using a high-output signal (H) or a proportional control signal (P) transmitted from a smoke concentration sequencer controller (20) of a smoke concentration instruction converter (17), which is provided on the exhaust gas outlet side of an exhaust gas cooling tower (12) provided at the exhaust gas collective outflow port (3) of the incineration furnace (1).

Description

無煙無臭無ダスト焼却装置Smokeless, odorless, and dust incinerator
 本発明は、通常の消費生活によって家庭や事務所から出される生ごみや紙屑や木屑などの一般ゴミ、生産工場や建築現場で不要になって捨てられるゴム製品やプラスチックなどの産業廃棄物その他多くの種類の燃焼性廃棄物を焼却炉で燃焼させ焼却する際に、焼却炉内の排ガス中に浮遊する煤煙、臭気やダストなどの公害物質の排出を防止した無公害焼却装置に関するものである。 The present invention applies to general waste such as garbage, paper and wood scraps from households and offices due to normal consumer life, industrial waste such as rubber products and plastics that are no longer needed at production factories and construction sites, and many others. The present invention relates to a pollution-free incineration apparatus that prevents emission of pollutant substances such as soot, odors, and dust floating in the exhaust gas in the incinerator when the incinerator is combusted and incinerated.
 食品の売れ残りや食べ残しあるいは食品製造過程において発生する食品廃棄物には、飼料や肥料等の原料に再生利用する事を目的とした食品リサイクル法が施行されている。さらに摩耗し安全走行上の問題から使われなくなった自動車のタイヤは、自動車リサイクル法からリサイクル処理技術が開発されているが、多額な処理費用がかかるため、大半が処理される事なく空き地に高く山積みされ長い間放置されているのが現状である。また一般ごみや産業廃棄物を個人が勝手に焼却する事は、黒煙や窒素酸化物やダイオキシンなどの有害物質を排出して環境を汚染しまた人体に多大な悪影響を及ぼす問題から、一般に禁じられている。この様な問題から、従来から一般ごみや産業廃棄物の燃焼性を向上させてダイオキシン類などの難分解性有機塩素化合物の排出を低減する焼却炉が多く開発されまた多くの特許公報で紹介されている。例えば特開平5−26422号公報には「温度の低い燃焼用空気または水洗浄後の排ガスを通過する間隔をもつ二重のケーシング構造の火炉壁にする事で火炉壁が冷却されるため炉本体の損傷を防止し、さらに内面ケーシングに複数の空気噴出用穴を設ける事により燃焼用空気として炉内へ投入されるため燃焼効率を向上すると共に煙突から排出される排ガスの白煙発生が防止される構造の廃棄物焼却炉」が開示されている。また特開2001−99414号公報には「ごみ第1燃焼室と温度800℃に上げてオキドシンの排出を抑制する燃焼ガス第2燃焼室の外壁を焼石こうに赤土と水を加えて混練したものを金属メッシュに塗り付けて硬化した金属メッシュ板で築造する事で、高温度に耐えかつ剥がれた燃焼室の外壁も簡単に補修できるごみ焼却炉」が開示されている。さらに特開2004−321958号公報には「都市ごみや産業廃棄物の焼却炉から排出される酸性ガスを除去するため、排ガス煙道で添加した重曹粉体と排ガス中の酸性ガスを接触させ、反応させ、生成した中和塩を回収する焼却炉の排ガス処理方法」も開示されている。
 上記した何れの廃棄物焼却炉も排ガス処理方法も、それ以前の従来技術に比較して炉体の耐久性が改善されまた廃棄物の燃焼性や排ガスの処理性にも顕著な効果を示す優れた技術である。しかしながら、今日まで開発された焼却炉または焼却方法は、被焼却物が燃焼するに必要な量の空気を供給する焼却技術であるため、被焼却時間が長くまた排ガス中に含まれるタールが炉内壁に付着して炉体を汚し、さらに煤煙や臭気や有害物質の飛散抑制効果についても顕著に改善すべき点があった。
 この様な問題点を解消したのが本件出願人らが先に出願した焼却炉で、特開2004−245478号公報の「被焼却物を過給気状態で焼却する燃焼室と排ガス中の未燃ガスを800℃以上のダイオキシン類熱分解温度に昇温する再燃焼室からなる焼却炉本体の排ガス側に、排ガス温度を800℃以上から200℃以下に急冷する冷却筒を設置した小型焼却炉」、さらに特開2008−57906号公報の「投入焼却物を過剰な空気を供給して燃焼する焼却炉と該焼却炉で発生した排ガスを高温度に保ちながら排ガス燃焼バーナーと排ガス消煙用バーナーで燃焼し、さらに排ガスを低温度に急速冷却する排ガス冷却塔を接続し、必要によっては排ガス浄化槽を設けて排ガス煙突を接続した低公害焼却処理装置」がある。本件出願人が開発した上記の小型焼却炉および低公害焼却処理装置は、被焼却物を過給気状態の空気比で燃焼しかつ焼却するため廃棄物が完全に灰化すると共に排ガスも無煙無臭化し、しかも排ガスを高温度から低温度に急速冷却するためダイオキシン類の発生と再合成を抑制し、大気中に低公害または無公害で排出する。しかしながら、焼却容積が小さい焼却炉において、火格子上に長尺状の如き被焼却物の大量をランダムに積み重ねて焼却するときあるいは空箱の様に容積空間の大きい燃焼性組立物を焼却するとき、被焼却物の燃焼中に突然の荷崩れを起こして炉内排ガスの流れを一瞬乱し、不完全燃焼で発生する煤煙や臭気や浮遊するダストや舞い上がった堆積灰の一部が、排気路に沿って流れる排ガスに混じって押し流され、煙突から排出される問題が懸念された。
The Food Recycling Law, which is intended to recycle raw materials such as feed and fertilizer, has been enforced for unsold food, leftover food, or food waste generated in the food manufacturing process. In addition, automobile tires that have become worn out and are no longer used due to problems with safe driving have been developed by the Automobile Recycling Law. Recycling technology has been developed. The current situation is that they are piled up and left for a long time. Also, it is generally prohibited for individuals to incinerate general waste and industrial waste on their own due to the problem of polluting the environment by causing harmful substances such as black smoke, nitrogen oxides and dioxins to be polluted. It has been. Because of these problems, many incinerators have been developed in the past to improve the combustibility of general waste and industrial waste and reduce the discharge of persistent organic chlorine compounds such as dioxins, and have been introduced in many patent publications. ing. For example, in Japanese Patent Laid-Open No. 5-26422, “the furnace body is cooled because the furnace wall is cooled by making the furnace wall into a double casing structure having a space through which low-temperature combustion air or exhaust gas after water washing passes. In addition, by providing a plurality of air jet holes in the inner casing, combustion air is injected into the furnace to improve combustion efficiency and prevent generation of white smoke in the exhaust gas discharged from the chimney. A waste incinerator having a structure is disclosed. Japanese Patent Laid-Open No. 2001-99414 discloses that the outer wall of the first combustion chamber and the combustion gas second combustion chamber, which suppresses the discharge of oxydine by raising the temperature to 800 ° C., kneaded with red clay and water added to the calcined gypsum. A waste incinerator that can withstand high temperatures and easily repair the outer wall of a combustion chamber that has been peeled off by building a metal mesh plate that has been coated and cured with a metal mesh is disclosed. Furthermore, JP 2004-321958 A discloses that, in order to remove the acid gas discharged from the incinerator for municipal waste and industrial waste, the sodium bicarbonate powder added in the exhaust gas flue is brought into contact with the acid gas in the exhaust gas. An incinerator exhaust gas treatment method for reacting and recovering the produced neutralized salt is also disclosed.
None of the waste incinerators and exhaust gas treatment methods described above are superior in that the durability of the furnace body is improved compared to the previous prior art, and that the waste combustibility and exhaust gas treatability are remarkable. Technology. However, the incinerator or incineration method that has been developed to date is an incineration technology that supplies the amount of air necessary for the incinerated product to burn, so that the incineration time is long and the tar contained in the exhaust gas is contained in the inner wall of the incinerator. There was a point that should be markedly improved with respect to the effect of suppressing the scattering of smoke, odors and harmful substances.
This problem has been solved by an incinerator previously filed by the applicants of the present application, as disclosed in Japanese Patent Application Laid-Open No. 2004-245478, “Combustion chamber for burning incinerated material in supercharged state and unexposed in exhaust gas. A small incinerator equipped with a cooling cylinder that rapidly cools the exhaust gas temperature from 800 ° C to 200 ° C on the exhaust gas side of the incinerator main body consisting of a recombustion chamber that raises the combustion gas temperature to 800 ° C or higher dioxin pyrolysis temperature Further, “Japanese Patent Application Laid-Open No. 2008-57906 discloses an incinerator that burns an incinerated product by supplying excess air, and an exhaust gas combustion burner and an exhaust gas extinguishing burner while maintaining the exhaust gas generated in the incinerator at a high temperature. There is a low-pollution incineration processing apparatus that is connected to an exhaust gas cooling tower that burns at a low temperature and further rapidly cools the exhaust gas to a low temperature. The above-mentioned small incinerator and low-pollution incineration equipment developed by the applicant of the present application combusts and incinerates the incinerated object at a supercharged air ratio, so that the waste is completely ashed and the exhaust gas is also smokeless and odorless In addition, since the exhaust gas is rapidly cooled from high temperature to low temperature, generation and resynthesis of dioxins are suppressed, and it is discharged into the atmosphere with low or no pollution. However, in an incinerator with a small incineration volume, when incinerating a large amount of incinerated objects such as long ones on a grate at random or incinerating a combustible assembly with a large volume space such as an empty box The incinerators suddenly collapse during combustion, disturbing the flow of the exhaust gas in the furnace for a moment, and smoke, odors, floating dust and soaring accumulated ash generated by incomplete combustion are part of the exhaust channel. There was concern about the problem of being swept away by the exhaust gas flowing along
特開平5−26422号公報JP-A-5-26422 特開2001−99414号公報JP 2001-99414 A 特開2004−321958号公報JP 2004-321958 A 特開2004−24578号公報Japanese Patent Laid-Open No. 2004-24578 特開2008−57906号公報JP 2008-57906 A
 本発明者らは上記の様な問題に鑑み、焼却炉において被焼却物が燃焼中に荷崩れを例え起こしても不完全燃焼で生じる煤煙と臭気、浮遊するダストさらには舞い上がった堆積灰などが排ガスに混じって排ガス煙突から排出される事のない無公害焼却装置(炉)を提供する事を目的に種々検討した結果、燃焼炉に被焼却物の燃焼用着火バーナーの他に排ガス燃焼用バーナーや被焼却物燃焼用空気供給ブロアやミストノズルなどを設けかつこれらの制御回路を煤煙濃度シーケンサ制御器を介して複合制御する事によって、その目的が達成できる事を知見した。 In view of the problems as described above, the present inventors have found that smoke and odor generated by incomplete combustion even if the incinerated material causes a collapse of cargo during combustion in an incinerator, floating dust, soaring deposited ash, etc. As a result of various studies for the purpose of providing a pollution-free incinerator (furnace) that is not mixed with the exhaust gas and discharged from the exhaust gas chimney, in addition to the ignition burner for burning the incinerated material in the combustion furnace, the exhaust gas combustion burner It was found that the purpose can be achieved by providing an air supply blower for burning incinerators, a mist nozzle, etc., and controlling these control circuits through a smoke concentration sequencer controller.
 本発明はその知見に基づいて構成したもので、その要旨は、炉内に火格子を架設して上下室に分離した上段室の上方側には排ガス集合流出口を設けまた炉壁には開閉自在な耐熱ドアをもつ被焼却物投入装置と該被焼却物投入装置から投入された火格子上の被焼却物に指向する被焼却物燃焼用バーナーを設けさらに下段室には開閉自在なドアをもつ焼却灰掻出口を設けかつ炉壁に炉内空気量調整ダンパを介して被焼却物燃焼用空気供給ブロアを設けてなる焼却炉の前記排ガス集合流出口には排ガス冷却用空気供給ブロアから供給される空気を排ガス流路交錯方向に噴出する多数のエアノズル孔を穿設した空気誘導用パイプを内蔵した排ガス冷却塔を接続すると共に、該排ガス冷却塔の排ガス出口側に投光器と受光器を相対向する側に設置して光透過濃度を測定する煤煙濃度指示変換器の煤煙濃度検出値と予め設定した目標設定濃度値を比較する演算制御で煤煙濃度偏差出力信号の高出力信号と比例制御信号を電気信号で出力する煤煙濃度シーケンサ制御器を設け、さらに焼却炉の上室側に設けた炉内温度計の検出温度を電気信号に変換した炉内温度検出信号と温度調節計の炉内設定温度を電気信号に変換した炉内温度設定信号を比較する炉内温度シーケンサ制御器の炉内温度偏差信号と前記した煤煙濃度シーケンサ制御器の高出力信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間は炉内温度を上昇させ被焼却物と煤煙を完全燃焼させるのに必要な量の燃料を噴射する被焼却物燃焼バーナーを制御する被焼却物燃焼用バーナーリレー制御器を接続し、さらに前記した炉内温度シーケンサ制御器の炉内温度偏差信号と前記した煤煙濃度シーケンサ制御器から着火継続タイマーを介して送信される電気信号の高出力信号を接続した複合信号のいずれか一方の信号またはその両者の信号を受信する間は焼却炉の排ガス集合流出口に流れ込む未燃焼物質を完全燃焼させるに必要な燃料を噴射する排ガス燃焼用バーナーを制御する排ガス燃焼用バーナーリレー制御器を接続すると共に、煤煙濃度シーケンサ制御器の高出力信号と前記した炉内温度シーケンサ制御器の炉内温度偏差信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間はリレー回路が作動して給水用電磁弁を開放し霧状の水を噴射するミストノズルを焼却炉の上段室の上方側に設け、さらにまた煤煙濃度シーケンサ制御器の比例制御信号を受信して作動する制御回路を前記した排ガス冷却用空気供給ブロアに接続して構成した無煙無臭無ダスト焼却装置である。さらに上記した構造の発明には必要に応じて被焼却物燃焼用空気供給ブロアの炉内空気量調整ダンパに接続して構成した無煙無臭無ダスト焼却装置である。 The present invention is configured based on the knowledge, and the gist of the present invention is that an exhaust gas collecting outlet is provided on the upper side of the upper chamber separated from the upper and lower chambers by installing a grate in the furnace and opened and closed on the furnace wall. An incinerator input device having a flexible heat-resistant door, an incinerator combustion burner directed to the incinerator on the grate inserted from the incinerator input device, and a door that can be opened and closed in the lower chamber An incinerator ash scraper outlet is provided and an incinerator combustion air supply blower is provided on the furnace wall via a furnace air quantity adjustment damper. The exhaust gas collecting outlet of the incinerator is supplied from an exhaust gas cooling air supply blower. An exhaust gas cooling tower with built-in air induction pipes with a number of air nozzle holes for ejecting the air to be exhausted in the direction of crossing the exhaust gas flow paths, and a projector and a light receiver relative to the exhaust gas outlet side of the exhaust gas cooling tower Install it on the opposite side A smoke concentration indicator that outputs a high output signal and a proportional control signal of the smoke concentration deviation output signal with an arithmetic control that compares the smoke concentration detection value of the smoke concentration indicator converter that measures the transmission density with a preset target concentration value. A furnace equipped with a sequencer controller, and a furnace temperature detection signal obtained by converting the detected temperature of the in-furnace thermometer provided on the upper chamber side of the incinerator into an electrical signal, and the furnace set temperature of the temperature controller converted into an electrical signal The internal temperature setting signal for comparing the internal temperature setting signal is received. The internal temperature deviation signal of the internal temperature sequencer controller and the composite signal connecting the high output signal of the soot concentration sequencer controller described above are received. In the meantime, connect the burner relay controller for burning the incinerator to control the burner burner that injects the amount of fuel required to raise the temperature inside the furnace and completely burn the incinerator and soot. Further, either one of the composite signal obtained by connecting the furnace temperature deviation signal of the furnace temperature sequencer controller described above and the high output signal of the electrical signal transmitted from the smoke concentration sequencer controller described above via the ignition continuation timer. While receiving the signal or both signals, connect the burner relay controller for exhaust gas combustion that controls the burner for exhaust gas combustion that injects the fuel necessary to completely burn the unburned material flowing into the exhaust gas collecting outlet of the incinerator And a relay circuit while receiving either one of the composite signal connecting the high output signal of the smoke concentration sequencer controller and the in-furnace temperature deviation signal of the in-furnace temperature sequencer controller or both of them. The mist nozzle that opens the water supply solenoid valve and injects mist-like water is installed above the upper chamber of the incinerator. It is a smokeless odorless dustless incinerator configured by connecting a control circuit that operates by receiving a proportional control signal of a sensor controller to the above-described exhaust gas cooling air supply blower. Further, the invention having the above-described structure is a smokeless odorless dustless incinerator configured to be connected to an in-furnace air amount adjusting damper of an air supply blower for burning incinerated objects as necessary.
 上記の様に構成された本発明の無煙無臭無ダスト焼却装置は、被焼却物例えば不要になった12インチの自動車用古タイヤ2本を積み重ねて焼却を試みたところ、燃焼中に2回の荷崩れを現象を起こしても、排出ガス塔から排出される該ガスの煤煙濃度検出値は安定して無色無煙、しかも無ダスト。この間のタイヤが灰化されるまでの燃焼時間は1時間で完全焼却された。一般に焼却され難いとされる古タイヤを無煙無臭無ダストで焼却される為、家庭や事務所から出される燃え易い生ごみや紙屑や木屑の焼却に環境汚染問題を起す疑いを挟む余地もない。
 表1は、不要になったゴム製品やプラスチックなどの産業廃棄物を本発明の焼却装置で焼却したとき、排ガス中または焼却灰中のダイオキシン類濃度や硫黄酸化物排出量など公害物質の測定分析結果を示す。いずれの物質の測定結果も各法律規定値よりも遥かに低い値を示し、無公害性を示唆するものである。
Figure JPOXMLDOC01-appb-T000001
The smokeless, odorless, dustless incinerator of the present invention configured as described above is an incineration object, for example, when two old 12-inch automobile tires that are no longer needed are stacked and incineration is attempted. Even if the phenomenon of cargo collapse occurs, the smoke concentration detection value of the gas discharged from the exhaust gas tower is stable, colorless and smokeless, and dust-free. During this time, the combustion time until the tires were incinerated was completely incinerated in 1 hour. Since old tires, which are generally considered difficult to be incinerated, are incinerated with no smoke, no odor, and no dust, there is no room for doubt of environmental pollution in the incineration of combustible garbage, paper waste and wood waste from homes and offices.
Table 1 shows the measurement and analysis of pollutants such as dioxin concentration and sulfur oxide emission in exhaust gas or incineration ash when industrial waste such as rubber products and plastics that are no longer needed is incinerated with the incinerator of the present invention. Results are shown. The measurement results for all substances are much lower than the legally stipulated values, suggesting pollution-free.
Figure JPOXMLDOC01-appb-T000001
 図1は本発明の一実施例を示す。
 図2は本発明の他の一実施例を示す。
FIG. 1 shows an embodiment of the present invention.
FIG. 2 shows another embodiment of the present invention.
 次に本発明の無煙無臭無ダスト焼却装置の構造について図面を参照しながら詳細に説明する。
 図1は本発明の一実施例を断面図で示す。図2は本発明の他の一実施例を断面図で示す。図1において、1は焼却炉(または燃焼炉ともいう)で、炉壁が耐熱性金属材料の鉄皮あるいはさらに不定形耐火物や耐火煉瓦を内張りを施し、耐熱構造物に築造されている。焼却炉1は、炉内に火格子2を架設して上下室AとBに分離した上段室Aの上方側には排ガス集合流出口3を設け、また炉壁には開閉自在な耐熱ドア4をもつ被焼却物投入装置5と被焼却物投入装置5から投入された火格子2上の被焼却物6に指向する被焼却物燃焼バーナー7を設けて構成されている。尚、被焼却物投入装置5と被焼却物燃焼バーナー7は、図面の様に相対向する側の炉壁面に設ける事が好ましいが、焼却炉設置場所の問題から同一炉壁面内に設けてもよくまた隣接する炉壁面に分離して設けてもよい。他方の下段室Bには、開閉自在なドア8をもつ焼却灰出口9を設け、かつ炉壁に炉内空気量調整ダンパ10を介して被焼却物燃焼空気供給ブロア11を設けている。すなわち焼却炉1は、被焼却物投入装置5から火格子2上に投入された生ごみや紙屑などの一般ごみやゴム製品やプラスチックなどの産業廃棄物その他多くの種類の燃焼性廃棄物を被焼却物燃焼バーナー7から噴射される灯油、ガスの流動性燃料の火焔で燃焼し焼却し、火格子2上から落下し堆積した焼却灰を焼却灰掻出口9から掻きだす構造に設けられている。12は排ガス冷却塔である。排ガス冷却塔12は、高温度の熱を保有する排ガスを冷却しながら排出するもので、耐熱性金属材料製の空気誘導用パイプ13の中に排ガス冷却用空気供給ブロア14から供給される空気を排ガス流路交錯方向に噴出する多数のエアノズル孔15を穿設した空気誘導用パイプ13を内蔵した構造で、焼却炉1の排ガス集合流出口3に立設する様に接続されている。すなわち、排ガス冷却塔12は、焼却炉1の排ガス集合流出口3から上昇しながら排気される排ガスをエアノズル孔15から噴出する空気で急速冷却するもので、ダイオキシン類の発生および再合成を抑制する構造に設けられている。16は傘部材である。傘部材16は雨や雪などを防ぐためにさしかざす部材であって、雨などが排ガス冷却塔12から侵入し焼却炉1の炉体設備や燃焼作業に支障を来たさぬ様に必要に応じて取付けられるもので、その形状や取付構造についても特に限定するものでもない。本発明の無煙無臭無ダスト焼却装置は、上記の様に焼却炉1の排ガス集合流出口3に排ガス冷却塔12を設け、さらに該排ガス冷却塔12の排ガス出口側で排ガスの煤煙濃度を検知しながらまた被焼却物燃焼中に突然起こった被焼却物の荷崩れによる排ガスの異常変化にも無煙無臭無ダストの焼却操業が行える様に、被焼却物燃焼用バーナーや排ガス燃焼用バーナーや各種の空気供給ブロアなどの無公害操業に必要な量のガスや空気を単独または複合で送給する制御回路を設けて構成されている。
 17は煤煙濃度指示変換器で、排ガス冷却塔12の排ガス出口側に受光器18と投光器19を相対向する側に設置し、排ガス中の煤煙やダストなどによって一部が遮光されながら透過する光を電気(電流)変換し、この変換出力を演算して光透過濃度を測定するものである。20は煤煙濃度シーケンサ制御器で、煤煙濃度指示変換器17から送信された光透過濃度出力信号を電気変換した煤煙濃度検出値と予め設定した目標設定濃度値を比較する演算制御で、排ガス冷却塔12の排ガス出口から排出される排ガスの煤煙濃度検出値が予め定めた目標設定濃度値より高い状態を高出力信号Hとし、その反対に煤煙濃度検出値が目標設定濃度値より低いときを比例制御信号Pとし出力する制御器である。さらに煤煙濃度シーケンサ制御器20の高出力信号Hは炉内温度シーケンサ制御器23や被焼却物燃焼用バーナーリレー制御器24や非ガス燃焼用バーナーリレー制御器27さらには給水用電磁弁29に送信し、比例制御信号Pは排ガス冷却塔12の排ガス冷却用空気供給ブロア14に送信する回路に設けられている。煤煙濃度シーケンサ制御器20の高出力信号を受信する炉内温度シーケンサ制御器23は、焼却炉1の上室側Aに設けた炉内温度計21の検出温度を変換した電気信号と予め設定した炉内設定温度の電気信号を比較し演算し出力する温度調節計22の炉内温度偏差信号を受信する複合受信回路に設けられている。すなわち、炉内温度シーケンサ制御器23は、煤煙濃度シーケンサ制御器20の高出力信号Hと温度調節計22の炉内温度偏差信号の複合信号を受信する複合受信回路に設けている。さらに炉内温度シーケンサ制御器23は、煤煙濃度シーケンサ制御器20の高出力信号Hと温度調節計22の炉内温度偏差信号の複合信号を受信し、該炉内温度偏差信号を被焼却物用燃焼バーナーリレー制御器24と排ガス燃焼用バーナーリレー制御器27に送信する回路に設けられている。炉内温度シーケンサ制御器23に接続された被焼却物燃焼用バーナーリレー制御器24は、該炉内温度シーケンサ制御器23が送信する複合信号のいずれか一方の信号またはその両者の信号を受信し高出力信号Hを受信する間は、煤煙濃度検出値が目標設定濃度よりも高いため、被焼却物燃焼バーナー7の火力を強めて煤煙やダストなどの未燃焼物質を完全燃焼しながら被焼却物6を燃焼させる。また炉内温度偏差のみを受信した場合は、該偏差信号の正負とその大きさに応じて被焼却物燃焼バーナー7の火力を調整する。さらに高出力信号Hと炉内温度偏差信号の複合信号を同時に受信する間は、両者の信号に制御されながら被焼却物燃焼バーナー7が制御される。すなわち、被焼却物燃焼用バーナーリレー制御器24は、高出力信号Hと炉内温度偏差信号のいずれか一方の信号またはその両者の信号を受信している間は、火格子2上の焼却物を焼却する被焼却物燃焼バーナー7から噴射される灯油やガスなどの燃料さらに被焼却物6や排ガス中のダイオキシンや煤煙やダストなどを完全燃焼する炉内温度に制御する回路に設けられている。
 さらに焼却炉1の上段室Aの排ガス集合流出口3には、該焼却炉1内を巡回する排ガスや排ガス冷却塔12に流出する排ガス中に混じる完全未燃焼物質の煤煙や臭いやダストなどを完全燃焼させるための排ガス燃焼用バーナー25が設けられている。さらに該排ガス燃焼用バーナー25には、炉内温度シーケンサー23の炉内温度偏差信号と煤煙濃度シーケンサ制御器20の高出力信号Hを着火継続タイマー26を介して受信しまた炉内温度シーケンサ制御器23の炉内温度偏差信号を受信する排ガス燃焼用バーナーリレー制御器27が接続されている。すなわち、排ガス燃焼用バーナーリレー制御27は、高出力信号Hと炉内温度偏差信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間は、焼却物燃焼用バーナーリレー制御器24と同様に、排ガス燃焼バーナー25から噴射される燃料の供給量を調整しながら炉内を浮遊する排ガスや未燃ガスや粉塵または排ガス流出口3に流れ込む煤煙や臭気やダストを完全燃焼するに必要な炉内温度に制御する回路に設けると共に、煤煙濃度シーケンサ制御器20の高出力信号の送信回路に着火継続タイマー26を設ける事によって排ガス燃焼用バーナー25が着火と消火を繰り返す際にスイッチの摩耗や不具合や時間差による未燃ガスの大気流失を防止しかつ焼却炉1を巡回する未燃ガスや排ガス冷却塔12に流れ込む未燃焼物質や臭気やダストの焼却時間を延長する作用がある。
 28は、焼却炉1の上段室Aの上段側に設けたミストノズルである。ミストノズル28は、前記した高出力信号Hと炉内温度偏差信号を接続する複合信号のいずれか一方の信号または両者の信号を受信し作動するリレー回路をもつ給水用電磁弁29が設けられ、焼却燃焼時に被焼却物6が荷崩れを起こして粉塵や煤煙などが排ガスに混じって高出力信号Hを受信しまた設定温度以上に炉温が上昇して炉内温度偏差信号を受信したときまたはその両者の信号を同時に受信したときはリレー回路の給水用電磁弁29から噴射された霧状の水が舞い上がった粉塵などの表面に付着して沈静化しまたその水が炉内の酸素と被焼却物を遮る事で窒息消火し設定目標温度を維持する。さらに排ガス冷却用空気供ブロア14には、前記した煤煙濃度シーケンサ制御器20の比例信号Pを受信し排ガス冷却塔12に必要な量の空気を供給する該排ガス冷却用空気供給ブロア用の空気供給量調整装置(図示せず)が接続されている。すなわち、排ガス冷却用空気供給ブロア14には、排ガス流路交錯方向に噴出する多数のエアノズル孔15から排ガス冷却塔12内を過給気状態に強制的に送り込まれる空気で、該排ガス冷却塔12を通過する排ガスを低温度に急速冷却させてダイオキシン類の再合成を防止すると共に、上昇する未燃ガスや臭気やダストなどの未燃性物質を焼却炉1に押し戻し完全燃焼を促す効果を奏する。
 上記の様に構成された本発明は無煙無臭無ダスト焼却装置は、他の一実施例として図2で示す様に、本体装置の簡素化や軽量化と安価な製作コストさらに同じブロア目的から、排ガス冷却用空気供給ブロア14と被焼却物燃焼用空気供給ブロア11とは一つのブロア動力源で共用できる構造に纏めてもよい。
 さらに上記の様な構造の本発明の無煙無臭無ダスト焼却装置は、焼却炉1の被焼却物投入装置5から火格子2上に投入されあるいは逐次投入される一般ごみや燃焼性廃棄物を、被焼却物燃焼バーナー7で燃焼させながらかつ排ガス冷却塔12の排ガス出口に設置した煤煙濃度指示変換器17の煤煙濃度シーケンサ制御器20が出力する高出力信号Hまたは比例制御信号Pを受信しながら該焼却物燃焼バーナー7、排ガス燃焼用バーナー25、ミストノズル28さらに排ガス冷却用空気供給ブロア14さらには被焼却物燃焼用空気供給ブロア11などを制御しながら無煙無臭無ダストで焼却する。
Next, the structure of the smokeless odorless dustless incinerator of the present invention will be described in detail with reference to the drawings.
FIG. 1 shows a cross-sectional view of an embodiment of the present invention. FIG. 2 shows a cross-sectional view of another embodiment of the present invention. In FIG. 1, 1 is an incinerator (or also called a combustion furnace), and the furnace wall is constructed of a heat-resistant metal material, an iron shell, or an amorphous refractory or a refractory brick, and is built in a heat-resistant structure. The incinerator 1 is provided with an exhaust gas collecting outlet 3 above the upper chamber A separated from the upper and lower chambers A and B by installing a grate 2 in the furnace, and a heat-resistant door 4 that can be opened and closed on the furnace wall. And an incineration object combustion burner 7 directed to the incineration object 6 on the grate 2 input from the incineration object input device 5. The incinerator charging device 5 and the incinerator combustion burner 7 are preferably provided on the opposite furnace wall surfaces as shown in the drawing, but may be provided on the same furnace wall surface due to the problem of the incinerator installation location. It may also be provided separately on the adjacent furnace wall. The other lower chamber B is provided with an incineration ash outlet 9 having a door 8 that can be freely opened and closed, and an incinerated combustion air supply blower 11 is provided on the furnace wall via a furnace air amount adjusting damper 10. In other words, the incinerator 1 covers general waste such as garbage and paper waste, industrial waste such as rubber products and plastics, and many other types of combustible waste that are thrown into the grate 2 from the incinerator input device 5. It is provided with a structure that burns and burns with kerosene and gas fluid fuel fired from the incineration combustion burner 7 and drops the incinerated ash that has fallen from the grate 2 and accumulated from the incineration ash scraper 9 . Reference numeral 12 denotes an exhaust gas cooling tower. The exhaust gas cooling tower 12 discharges while cooling the exhaust gas having high-temperature heat, and the air supplied from the exhaust gas cooling air supply blower 14 into the air induction pipe 13 made of a heat-resistant metal material. The air guide pipe 13 having a large number of air nozzle holes 15 ejected in the direction of crossing the exhaust gas flow paths is built in, and is connected so as to stand at the exhaust gas collecting outlet 3 of the incinerator 1. That is, the exhaust gas cooling tower 12 rapidly cools the exhaust gas exhausted while rising from the exhaust gas collecting outlet 3 of the incinerator 1 with the air ejected from the air nozzle hole 15, and suppresses the generation and resynthesis of dioxins. Provided in the structure. Reference numeral 16 denotes an umbrella member. The umbrella member 16 is a member that is held up to prevent rain, snow, and the like, and is necessary so that rain does not enter the exhaust gas cooling tower 12 and interfere with the furnace equipment and combustion work of the incinerator 1. It can be attached accordingly, and its shape and mounting structure are not particularly limited. The smokeless odorless dustless incinerator of the present invention is provided with the exhaust gas cooling tower 12 at the exhaust gas collecting outlet 3 of the incinerator 1 as described above, and further detects the smoke concentration of the exhaust gas at the exhaust gas outlet side of the exhaust gas cooling tower 12. In addition, in order to enable smokeless, odorless, and dustless incineration operations in response to abnormal changes in the exhaust gas caused by the collapse of the incinerated material, which occurred suddenly during the combustion of the incinerated material, The control circuit is configured to supply a gas or air necessary for pollution-free operation such as an air supply blower alone or in combination.
Reference numeral 17 denotes a soot concentration indicator converter. A light receiver 18 and a projector 19 are installed on the opposite sides of the exhaust gas outlet of the exhaust gas cooling tower 12, and light is transmitted while being partially shielded by soot or dust in the exhaust gas. Is converted into electricity (current), and the converted output is calculated to measure the light transmission density. Reference numeral 20 denotes a smoke concentration sequencer controller, which is an arithmetic control for comparing the smoke concentration detection value obtained by electrically converting the light transmission concentration output signal transmitted from the smoke concentration indicating converter 17 with a preset target set concentration value. The state where the smoke concentration detection value of the exhaust gas discharged from the 12 exhaust gas outlets is higher than a predetermined target set concentration value is set as a high output signal H, and conversely, the control is performed when the smoke concentration detection value is lower than the target set concentration value. A controller that outputs the signal P. Further, the high output signal H of the smoke concentration sequencer controller 20 is transmitted to the in-furnace temperature sequencer controller 23, the burner relay controller 24 for burning the incinerator, the burner relay controller 27 for non-gas combustion, and the electromagnetic valve 29 for water supply. The proportional control signal P is provided in a circuit that transmits to the exhaust gas cooling air supply blower 14 of the exhaust gas cooling tower 12. The in-furnace temperature sequencer controller 23 that receives the high output signal of the smoke concentration sequencer controller 20 is preset with an electric signal obtained by converting the detected temperature of the in-furnace thermometer 21 provided in the upper chamber side A of the incinerator 1. It is provided in a composite receiving circuit that receives an in-furnace temperature deviation signal of the temperature controller 22 that compares, calculates and outputs an electrical signal of the set temperature in the furnace. That is, the in-furnace temperature sequencer controller 23 is provided in a composite receiving circuit that receives the composite signal of the high output signal H of the smoke concentration sequencer controller 20 and the in-furnace temperature deviation signal of the temperature controller 22. Further, the furnace temperature sequencer controller 23 receives the composite signal of the high output signal H of the smoke concentration sequencer controller 20 and the furnace temperature deviation signal of the temperature controller 22, and uses the furnace temperature deviation signal for the incinerator. It is provided in a circuit that transmits to the combustion burner relay controller 24 and the exhaust gas combustion burner relay controller 27. The burner relay controller 24 for incineration combustion connected to the in-furnace temperature sequencer controller 23 receives one or both of the composite signals transmitted by the in-furnace temperature sequencer controller 23. While the high output signal H is received, the smoke concentration detection value is higher than the target concentration. Therefore, the incineration object is burned while the burning power of the incineration combustion burner 7 is increased and the unburned substances such as smoke and dust are completely burned. 6 is burned. When only the furnace temperature deviation is received, the heating power of the incinerated combustion burner 7 is adjusted according to the sign of the deviation signal and its magnitude. Further, while receiving the composite signal of the high output signal H and the furnace temperature deviation signal at the same time, the incinerator combustion burner 7 is controlled while being controlled by both signals. In other words, the burner relay controller 24 for burning the incinerator is incinerated on the grate 2 while receiving either one of the high output signal H and the in-furnace temperature deviation signal or both. It is provided in a circuit for controlling the temperature inside the furnace to completely burn the fuel such as kerosene and gas injected from the burner 7 to be incinerated, dioxin, soot and dust in the incinerator 6 and exhaust gas. .
Further, the exhaust gas collecting outlet 3 of the upper chamber A of the incinerator 1 contains smoke, odor, dust, etc. of completely unburned substances mixed in the exhaust gas circulating in the incinerator 1 or the exhaust gas flowing out to the exhaust gas cooling tower 12. An exhaust gas combustion burner 25 for complete combustion is provided. Further, the exhaust gas combustion burner 25 receives the in-furnace temperature deviation signal of the in-furnace temperature sequencer 23 and the high output signal H of the soot concentration sequencer controller 20 via the ignition continuation timer 26, and the in-furnace temperature sequencer controller. An exhaust gas combustion burner relay controller 27 for receiving the 23 furnace temperature deviation signal is connected. That is, the exhaust gas combustion burner relay control 27 controls the incineration combustion burner relay control while receiving either one of the composite signal connecting the high output signal H and the in-furnace temperature deviation signal or both of them. Similarly to the vessel 24, exhaust gas floating in the furnace, unburned gas, dust, soot, odor, and dust flowing into the exhaust gas outlet 3 are completely burned while adjusting the amount of fuel injected from the exhaust gas combustion burner 25. Is provided in a circuit for controlling the temperature in the furnace necessary for the operation, and a switch is provided when the exhaust gas combustion burner 25 repeats ignition and extinguishing by providing an ignition continuation timer 26 in the high output signal transmission circuit of the smoke concentration sequencer controller 20. To prevent the unburned gas from being lost to the atmosphere due to wear, malfunction or time difference, and to flow into the unburned gas or exhaust gas cooling tower 12 circulating around the incinerator 1 There is action to extend the baked substance and odors and dust of incineration time.
Reference numeral 28 denotes a mist nozzle provided on the upper stage side of the upper chamber A of the incinerator 1. The mist nozzle 28 is provided with a water supply electromagnetic valve 29 having a relay circuit that receives and operates either one of the composite signal that connects the high output signal H and the furnace temperature deviation signal, or both signals, When the incinerated object 6 collapses during incineration and dust or soot is mixed with the exhaust gas and receives a high output signal H, or when the furnace temperature rises above the set temperature and receives an in-furnace temperature deviation signal or When both signals are received at the same time, the mist of water sprayed from the water supply solenoid valve 29 of the relay circuit settles on the surface of the soaring dust, and the water is incinerated with the oxygen in the furnace. Extinguish suffocation by blocking objects and maintain the target temperature. Further, the exhaust gas cooling air supply blower 14 receives the proportional signal P of the smoke concentration sequencer controller 20 and supplies the required amount of air to the exhaust gas cooling tower 12. A quantity adjusting device (not shown) is connected. That is, the exhaust gas cooling air supply blower 14 is air that is forcibly sent to the supercharged air state in the exhaust gas cooling tower 12 from a large number of air nozzle holes 15 ejected in the direction of crossing the exhaust gas flow paths. The exhaust gas passing through the gas is rapidly cooled to a low temperature to prevent dioxins from being re-synthesized, and the unburned substances such as rising unburned gas, odor and dust are pushed back to the incinerator 1 to promote complete combustion. .
The present invention constructed as described above is a smokeless odorless dustless incinerator, as shown in FIG. 2 as another embodiment, for the simplification and weight reduction of the main body device and an inexpensive production cost, and for the same blower purpose, The exhaust gas cooling air supply blower 14 and the incinerated substance combustion air supply blower 11 may be combined into a structure that can be shared by one blower power source.
Furthermore, the smokeless odorless dustless incinerator of the present invention having the above-described structure is configured to dispose of general waste or combustible waste that is input from the incinerator input device 5 of the incinerator 1 onto the grate 2 or sequentially input. While burning with the incinerator combustion burner 7 and receiving the high output signal H or the proportional control signal P output from the soot concentration sequencer controller 20 of the soot concentration indicating converter 17 installed at the exhaust gas outlet of the exhaust gas cooling tower 12 The incineration combustion burner 7, exhaust gas combustion burner 25, mist nozzle 28, exhaust gas cooling air supply blower 14, incinerator combustion air supply blower 11, and the like are incinerated with no smoke and no odor and no dust.
 本発明の無煙無臭無ダスト焼却装置は、一般ごみの他に難燃性で多くの有害物質を発生し易いとされるゴム製品まで、無煙無臭無ダストで焼却する事が出来る。住宅地さらには青い海に囲まれた風光明媚な島々でも広く使用される可能性が高い。 The smokeless, odorless and dusty incinerator of the present invention can be incinerated with smokeless, odorless and dustless to rubber products which are considered to be flame retardant and easily generate many harmful substances in addition to general waste. It is likely to be widely used in residential areas and even in scenic islands surrounded by the blue sea.
 1 焼却炉
 2 火格子
 3 排ガス集合流出口
 4 耐熱ドア
 5 被焼却物投入装置
 6 被焼却物
 7 焼却物燃焼用バーナー
 8 ドア
 9 焼却灰掻出口
10 炉内空気量調整ダンパ
11 被焼却物燃焼用空気供給ブロア
12 排ガス冷却塔
13 空気誘導用パイプ
14 排ガス冷却用空気供給ブロア
15 エアノズル孔
16 傘部材
17 煤煙濃度指示変換器
18 受光器
19 投光器
20 煤煙濃度シーケンサ制御器
21 炉内温度計
22 温度調節計
23 炉内温度シーケンサ制御器
24 被焼却物燃焼用バーナーリレー制御器
25 排ガス燃焼用バーナー
26 着火継続タイマー
27 排ガス燃焼用バーナーリレー制御器
28 ミストノズル
29 給水用電磁弁
DESCRIPTION OF SYMBOLS 1 Incinerator 2 Grate 3 Exhaust gas outlet 4 Heat-resistant door 5 Incinerated material input device 6 Incinerated material 7 Incinerated material combustion burner 8 Door 9 Incinerated ash scraper 10 In-furnace air quantity adjustment damper 11 Incinerated material combustion Air supply blower 12 Exhaust gas cooling tower 13 Air induction pipe 14 Exhaust gas cooling air supply blower 15 Air nozzle hole 16 Umbrella member 17 Smoke concentration indicator converter 18 Light receiver 19 Smoke device 20 Smoke concentration sequencer controller 21 Furnace thermometer 22 Temperature adjustment Total 23 In-furnace temperature sequencer controller 24 Burner relay controller 25 for combustion of incineration material Exhaust gas combustion burner 26 Ignition continuation timer 27 Exhaust gas combustion burner relay controller 28 Mist nozzle 29 Solenoid valve for water supply

Claims (2)

  1.  炉内に火格子を架設して上下室に分離した上段室の上方側には排ガス集合流出口を設けまた炉壁には開閉自在な耐熱ドアをもつ被焼却物投入装置と該被焼却物投入装置から投入された火格子上の被焼却物に指向する被焼却物燃焼用バーナーを設けさらに下段室には開閉自在なドアをもつ焼却灰掻出口を設けかつ炉壁に炉内空気量調整ダンパを介して被焼却物燃焼用空気供給ブロアを設けてなる焼却炉の前記排ガス集合流出口に排ガス冷却用空気供給ブロアから供給される空気を排ガス流路交錯方向に噴出する多数のエアノズル孔を穿設した空気誘導用パイプを内蔵した排ガス冷却塔を接続すると共に、該排ガス冷却塔の排ガス出口側に投光器と受光器を相対向する側に設置して光透過濃度を測定する煤煙濃度指示変換器の煤煙濃度検出値と予め設定した目標設定濃度値を比較する演算制御で煤煙濃度偏差出力信号の高出力信号と比例制御信号を電気信号で出力する煤煙濃度シーケンサ制御器を設け、さらに焼却炉の上室側に設けた炉内温度計の検出温度を電気信号に変換した炉内温度検出信号と温度調節計の炉内設定温度を電気信号に変換した炉内温度設定信号を比較する炉内温度シーケンサ制御器の炉内温度偏差信号と前記した煤煙濃度シーケンサ制御器の高出力信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間は炉内温度を上昇させ被焼却物と煤煙を完全燃焼させるのに必要な量の燃料を噴射する被焼却物燃焼バーナーを制御する被焼却物燃焼用バーナーリレー制御器を接続し、さらに前記した炉内温度シーケンサ制御器の炉内温度偏差信号と前記した煤煙濃度シーケンサ制御器から着火継続タイマーを介して送信される電気信号の高出力信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間は焼却炉の排ガス集合流出口に流れ込む未燃焼物質を完全燃焼させるに必要な燃料を噴射する排ガス燃焼用バーナーを制御する排ガス燃焼用バーナーリレー制御器を接続すると共に、煤煙濃度シーケンサ制御器の高出力信号と前記した炉内温度シーケンサ制御器の炉内温度偏差信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間はリレー回路が作動して給水用電磁弁を開放し霧状の水を噴射するミストノズルを焼却炉の上段室の上方側に設け、さらにまた煤煙濃度シーケンサ制御器の比例制御信号を受信して作動する制御回路を前記した排ガス冷却用空気供給ブロアに接続して構成した事を特徴とする無煙無臭無ダスト焼却装置。 An incinerator input device having an exhaust gas collecting outlet on the upper side of the upper chamber separated from the upper and lower chambers by installing a grate in the furnace, and an incinerator input device having a heat-resistant door that can be opened and closed on the furnace wall A burner for burning the incineration object directed to the incineration object on the grate introduced from the apparatus is provided, and an incineration ash scraper with an openable / closable door is provided in the lower chamber, and the furnace air amount adjustment damper is provided on the furnace wall A large number of air nozzle holes for injecting the air supplied from the exhaust gas cooling air supply blower in the direction of crossing the exhaust gas passages are drilled at the exhaust gas collecting outlet of the incinerator provided with an air supply blower for incineration object combustion. A smoke concentration indicating converter for measuring a light transmission density by connecting a flue gas cooling tower having a built-in air induction pipe and installing a projector and a light receiver on opposite sides of the flue gas outlet of the flue gas cooling tower The smoke concentration detection value of A smoke concentration sequencer controller that outputs the high output signal of the smoke concentration deviation output signal and the proportional control signal as an electrical signal is provided for operation control that compares the target set concentration value set for the purpose, and further provided on the upper chamber side of the incinerator The in-furnace temperature sequencer controller that compares the in-furnace temperature detection signal that converts the detected temperature of the in-furnace thermometer into an electric signal and the in-furnace temperature setting signal that converts the in-furnace set temperature of the temperature controller into an electric signal While receiving either one of the temperature deviation signal and the composite signal that connects the high output signal of the soot concentration sequencer controller, or both signals, the furnace temperature is raised and the incinerator and soot are completely An incinerator combustion burner relay controller for controlling an incinerator combustion burner for injecting an amount of fuel necessary for combustion is connected, and an in-furnace temperature deviation signal of the in-furnace temperature sequencer controller described above is connected. While receiving either one or both of the composite signals connecting the high output signal of the electrical signal transmitted from the soot concentration sequencer controller through the ignition continuation timer, the exhaust gas collective flow of the incinerator Connected to the burner relay controller for exhaust gas combustion that controls the burner for exhaust gas combustion that injects the fuel necessary to completely burn the unburned substances flowing into the outlet, and the high output signal of the smoke concentration sequencer controller and the above-mentioned furnace While receiving one or both of the composite signals that connect the temperature deviation signal in the furnace of the temperature sequencer controller, the relay circuit operates to open the water supply solenoid valve and inject mist water A control circuit that operates by receiving a proportional control signal of the smoke concentration sequencer controller. A smokeless, odorless, dustless incinerator characterized by being connected to an air supply blower for exhaust gas cooling.
  2.  炉内に火格子を架設して上下室に分離した上段室の上方側には排ガス集合流出口を設けまた炉壁には開閉自在な耐熱ドアをもつ被焼却物投入装置と該被焼却物投入装置から投入された火格子上の被焼却物に指向する被焼却物燃焼用バーナーを設けさらに下段室には開閉自在なドアをもつ焼却灰掻出口を設けかつ炉壁に炉内空気量調整ダンパを介して被焼却物燃焼用空気供給ブロアを設けてなる焼却炉の前記排ガス集合流出口に排ガス冷却用空気供給ブロアから供給される空気を排ガス流路交錯方向に噴出する多数のエアノズル孔を穿設した空気誘導用パイプを内蔵した排ガス冷却塔を接続すると共に、該排ガス冷却塔の排ガス出口側に投光器と受光器を相対向する側に設置して光透過濃度を測定する煤煙濃度指示変換器の煤煙濃度検出値と予め設定した目標設定濃度値を比較する演算制御で煤煙濃度偏差出力信号の高出力信号と比例制御信号を電気信号で出力する煤煙濃度シーケンサ制御器を設け、さらに焼却炉の上室側に設けた炉内温度計の検出温度を電気信号に変換した炉内温度検出信号と温度調節計の炉内設定温度を電気信号に変換した炉内温度設定信号を比較する炉内温度シーケンサ制御器の炉内温度偏差信号と前記した煤煙濃度シーケンサ制御器の高出力信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間は炉内温度を上昇させ被焼却物と煤煙を完全燃焼させるのに必要な量の燃料を噴射する被焼却物燃焼バーナーを制御する被焼却物燃焼用バーナーリレー制御器を接続し、さらに前記した炉内温度シーケンサ制御器の炉内温度偏差信号と前記した煤煙濃度シーケンサ制御器から着火継続タイマーを介して送信される電気信号の高出力信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間は焼却炉の排ガス集合流出口に流れ込む未燃焼物質を完全燃焼させるに必要な燃料を噴射する排ガス燃焼用バーナーを制御する排ガス燃焼用バーナーリレー制御器を接続すると共に、煤煙濃度シーケンサ制御器の高出力信号と前記した炉内温度シーケンサ制御器の炉内温度偏差信号を接続する複合信号のいずれか一方の信号またはその両者の信号を受信する間はリレー回路が作動して給水用電磁弁を開放し霧状の水を噴射するミストノズルを焼却炉の上段室の上方側に設け、さらにまた煤煙濃度シーケンサ制御器の比例制御信号を受信して作動する制御回路を前記した排ガス冷却用空気供給ブロアに接続すると共に被焼却物燃焼用空気供給ブロアの空気量調整ダンパーに接続して構成した事を特徴とする無煙無臭無ダスト焼却装置。 An incinerator input device having an exhaust gas collecting outlet on the upper side of the upper chamber separated from the upper and lower chambers by installing a grate in the furnace, and an incinerator input device having a heat-resistant door that can be opened and closed on the furnace wall A burner for burning the incineration object directed to the incineration object on the grate introduced from the apparatus is provided, and an incineration ash scraper with an openable / closable door is provided in the lower chamber, and the furnace air amount adjustment damper is provided on the furnace wall A large number of air nozzle holes for injecting the air supplied from the exhaust gas cooling air supply blower in the direction of crossing the exhaust gas passages are drilled at the exhaust gas collecting outlet of the incinerator provided with an air supply blower for incineration object combustion. A smoke concentration indicating converter for measuring a light transmission density by connecting a flue gas cooling tower having a built-in air induction pipe and installing a projector and a light receiver on opposite sides of the flue gas outlet of the flue gas cooling tower The smoke concentration detection value of A smoke concentration sequencer controller that outputs the high output signal of the smoke concentration deviation output signal and the proportional control signal as an electrical signal is provided for operation control that compares the target set concentration value set for the purpose, and further provided on the upper chamber side of the incinerator The in-furnace temperature sequencer controller that compares the in-furnace temperature detection signal that converts the detected temperature of the in-furnace thermometer into an electric signal and the in-furnace temperature setting signal that converts the in-furnace set temperature of the temperature controller into an electric signal While receiving either one of the temperature deviation signal and the composite signal that connects the high output signal of the soot concentration sequencer controller, or both signals, the furnace temperature is raised and the incinerator and soot are completely An incinerator combustion burner relay controller for controlling an incinerator combustion burner for injecting an amount of fuel necessary for combustion is connected, and an in-furnace temperature deviation signal of the in-furnace temperature sequencer controller described above is connected. While receiving either one or both of the composite signals connecting the high output signal of the electrical signal transmitted from the soot concentration sequencer controller through the ignition continuation timer, the exhaust gas collective flow of the incinerator Connected to the burner relay controller for exhaust gas combustion that controls the burner for exhaust gas combustion that injects the fuel necessary to completely burn the unburned substances flowing into the outlet, and the high output signal of the smoke concentration sequencer controller and the above-mentioned furnace While receiving one or both of the composite signals that connect the temperature deviation signal in the furnace of the temperature sequencer controller, the relay circuit operates to open the water supply solenoid valve and inject mist water A control circuit that operates by receiving a proportional control signal of the smoke concentration sequencer controller. A smokeless, odorless and dustless incinerator characterized by being connected to an air supply blower for cooling exhaust gas and connected to an air amount adjusting damper of an air supply blower for burning incinerated materials.
PCT/JP2014/054248 2013-02-15 2014-02-17 Smokeless, odorless, dustless incineration device WO2014126268A1 (en)

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JP5903182B1 (en) 2015-07-15 2016-04-13 エス・イー・シーエレベーター株式会社 Smokeless incinerator and system using the same

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0814522A (en) * 1994-06-24 1996-01-19 Yoshida Seisakusho:Kk Anti-fogging device of inspection window for burning furnace
JPH102534A (en) * 1996-06-14 1998-01-06 Nippon Spindle Mfg Co Ltd Combustion control method of incinerator and device therefor
JP2004245478A (en) * 2003-02-13 2004-09-02 Takehito Fukutomi Small incinerator
JP2008057906A (en) * 2006-09-01 2008-03-13 Takehito Fukutomi Low pollution incinerating device
JP2008089269A (en) * 2006-10-04 2008-04-17 Taisei Denki Seisakusho:Kk Low pollution incineration controller

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0814522A (en) * 1994-06-24 1996-01-19 Yoshida Seisakusho:Kk Anti-fogging device of inspection window for burning furnace
JPH102534A (en) * 1996-06-14 1998-01-06 Nippon Spindle Mfg Co Ltd Combustion control method of incinerator and device therefor
JP2004245478A (en) * 2003-02-13 2004-09-02 Takehito Fukutomi Small incinerator
JP2008057906A (en) * 2006-09-01 2008-03-13 Takehito Fukutomi Low pollution incinerating device
JP2008089269A (en) * 2006-10-04 2008-04-17 Taisei Denki Seisakusho:Kk Low pollution incineration controller

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