JP2012197991A - Indirect water cooling and direct air cooling type fire grate combustion apparatus - Google Patents

Indirect water cooling and direct air cooling type fire grate combustion apparatus Download PDF

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JP2012197991A
JP2012197991A JP2011063059A JP2011063059A JP2012197991A JP 2012197991 A JP2012197991 A JP 2012197991A JP 2011063059 A JP2011063059 A JP 2011063059A JP 2011063059 A JP2011063059 A JP 2011063059A JP 2012197991 A JP2012197991 A JP 2012197991A
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grate
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combustion apparatus
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JP5361929B2 (en
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Hajime Iwaida
一 岩井田
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KASUGA SERVICE KK
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Abstract

PROBLEM TO BE SOLVED: To provide a fire grate combustion apparatus which has a simple structure, prevents burn damage in a high temperature part and has excellent durability.SOLUTION: The fire grate combustion apparatus includes a plate like body and is provided with a bent part bent downward in the front end of the plate like body and a bank part extending downward in the rear end of the plate like body, and a plurality of cooling clear-water pipes for circulating cooling clear-water as a heat medium are arranged side by side via air-cooled parts, respectively between the bent part and the bank part.

Description

本発明は間接冷却水冷及び直接空冷式火格子燃焼装置に関する。さらに詳しくは、高温部での焼損を防止すると共に、低温部では過冷却を防ぎ未燃物の生成を防止し、かつ接ガス部における腐食を防止することができる、間接冷却水冷及び直接空冷式火格子燃焼装置に関する。   The present invention relates to an indirect cooling water cooling and direct air cooling grate combustion apparatus. More specifically, indirect cooling water cooling and direct air cooling that prevent burning in the high temperature part, prevent overcooling in the low temperature part, prevent the formation of unburned material, and prevent corrosion in the gas contact part. The present invention relates to a grate combustion apparatus.

固形燃料焚きボイラー燃焼装置及び産業廃棄物を焼却するための焼却燃焼装置として、火格子式燃焼・焼却装置、流動層式燃焼・焼却装置、回転炉式燃焼・焼却装置等が従来採用されている。このうち火格子式燃焼・焼却装置は、ボイラー・焼却炉内に多段に配置された火格子を備え、燃焼・焼却対象燃焼物が火格子に沿って移動しながら焼却される構造を有している。   As a solid fuel-fired boiler combustion device and an incineration combustion device for incinerating industrial waste, a grate combustion / incineration device, a fluidized bed combustion / incineration device, a rotary furnace combustion / incineration device, etc. have been conventionally employed. . Of these, the grate-type combustion / incineration equipment has a grate arranged in multiple stages in the boiler / incinerator, and has a structure in which the combustible / incineration target combustibles are incinerated while moving along the grate. Yes.

ボイラー燃料用に加工された産業廃棄物(加工燃料)には、年々、高分子系のものが多く含まれるようになり、その発熱量も年々高くなっている。そして、産業廃棄物の発熱量が高くなるにしたがって、産業廃棄物・加工燃料を燃焼させる燃焼装置、とりわけ火格子式燃焼装置は、以前にはなかった種々の障害(例えば、高温酸化による焼損、滴下燃焼による焼損、塩素による高温腐食等)が発生するようになった。さらに詳しくは、高分子系加工燃料に含まれる塩素が単独あるいは化合物の塩化水素(HCl)となって高温部では燃焼装置が激しく焼損し、低温部では過冷却による多量の未燃物の発生及び接ガス部などを腐食する問題を惹起している。これらの障害による燃焼装置の損傷を防止することができる火格子が望まれている。   Industrial waste processed for boiler fuel (processed fuel) contains a lot of high-molecular substances year by year, and its calorific value increases year by year. And as the calorific value of industrial waste increases, the combustion device that burns industrial waste and processed fuel, especially the grate-type combustion device, has a variety of obstacles that have not existed before (for example, burnout due to high-temperature oxidation, Burning due to dripping combustion, high temperature corrosion due to chlorine, etc.) has occurred. More specifically, the chlorine contained in the polymer-based processing fuel is singly or as compound hydrogen chloride (HCl), and the combustion device is severely burned in the high temperature part, and a large amount of unburned matter is generated due to supercooling in the low temperature part. This causes a problem of corroding the gas contact part. A grate that can prevent damage to the combustion device due to these obstacles is desired.

火格子の損傷を防ぐために、例えば火格子の材質を高価な耐熱鋼に変えることによって、いくらかの効果はあるものの、満足ができるものではない。しかしながら、ボイラー燃料用に加工された産業廃棄物は、近年ますます高分子系が多く含まれるようになったのに伴い、発熱量も高くなってきた。そのため、火層の燃焼温度もますます上昇し、火格子の材質を改変することに頼るだけでは、材料費が高くなりすぎ、対処することができない。それ程までに、燃焼温度が高温になった。この問題を解決するためには、材料費を考慮しない高級耐熱材の使用による方法と、低級な耐熱材料を消耗品として使用する方法とがある。   In order to prevent the grate from being damaged, for example, changing the grate material to expensive heat-resistant steel has some effect but is not satisfactory. However, industrial wastes processed for boiler fuels have recently increased in calorific value as more and more polymers are included in recent years. For this reason, the combustion temperature of the fire layer also rises more and more, and relying only on modifying the material of the grate is too expensive to deal with. By that time, the combustion temperature became high. In order to solve this problem, there are a method using a high-temperature heat-resistant material that does not consider material costs and a method using a low-temperature heat-resistant material as a consumable.

しかしながら、前者の場合、高級耐熱材のコストに見合う程の耐久性がないのが実情であり、後者の場合、短期間で焼損し、その取り換えのために、操業停止回数が多くなり、設備全体の起動・停止に多くの無駄なエネルギー(電力、助燃油、水など)を消費し、有効な解決方法にはなり得ていないのが実情である。   However, in the former case, the actual situation is that the high-temperature heat-resistant material is not durable enough to meet the cost of the high-grade heat-resistant material, and in the latter case, it burns out in a short period of time, and the number of operation stops increases due to the replacement. In fact, it consumes a lot of wasteful energy (electric power, auxiliary oil, water, etc.) to start and stop the system and cannot be an effective solution.

火格子式燃焼装置の場合、火格子には焼却対象物が置かれるので、焼損される火格子の寿命を延長させ、また火格子の過冷却による不完全燃焼による未燃物発生を低減する程度までに火格子を冷却する必要がある。   In the case of a grate-type combustion device, the incineration object is placed on the grate, so that the life of the grate to be burnt is extended and the generation of unburned material due to incomplete combustion due to overcooling of the grate is reduced. It is necessary to cool the grate by.

火格子の冷却方式としては、通常、空冷式と水冷式とが用いられている。空冷式は、燃焼用空気を火格子下部で供給し、火格子を冷却しながら廃棄物・加工燃料を燃焼させる方式であり、水冷式は空冷式の最も大きな短所である高温焼損を防止するために冷却水管を設け、冷却水管の内部を流動する冷却水により火格子を冷却させる方式である。   As a grate cooling method, an air cooling method and a water cooling method are usually used. The air-cooled type is a method in which combustion air is supplied at the bottom of the grate and the waste and processed fuel are burned while cooling the grate. The water-cooled type is the biggest disadvantage of the air-cooled type in order to prevent high temperature burning. Is provided with a cooling water pipe and the grate is cooled by cooling water flowing inside the cooling water pipe.

前述の問題を解決するために、火格子を水で冷却する水冷方法が有効な手段となりつつあるが、現在採用されている水冷方法は、火格子本体を中空にして、冷却水をその中に通す構造である。   In order to solve the above-mentioned problem, a water cooling method for cooling the grate with water is becoming an effective means, but the water cooling method currently employed is that the grate body is hollow and cooling water is contained therein. It is a structure to pass through.

かかる水冷式の火格子式燃焼装置(以下、「火格子燃焼装置」という)として、特許文献1には、低カロリーの燃焼物を燃やす場合に、冷却効果がよいため、火格子に接触している燃焼物まで冷やし燃焼速度が低下するという問題点を解消することを目的として、前面部にU字状管路が備えられた水冷式火格子が開示されている。   As such a water-cooled grate-type combustion apparatus (hereinafter referred to as “grate-combustion apparatus”), Patent Document 1 describes that when burning low-calorie combustion products, the cooling effect is good. A water-cooled grate having a U-shaped pipe line on the front surface is disclosed for the purpose of solving the problem that the combustion rate is reduced by cooling the burned product.

一方、特許文献2に記載された火格子の場合、図1に示されるように、産業廃棄物が焼却炉(10)内に投入されると、産業廃棄物は、多段式の階段状の形態で構成された火格子(100)を順次通過して、燃焼室(20)内で焼却され、焼却炉の下側に設けられた焼却灰の排出部を通じて排出される。火格子の産業廃棄物移送は、油圧装置(40)によって駆動されるロッド(3)により押圧される。さらに、図2に示されるように、特許文献2の水冷式火格子(100)は、火格子を冷却させる冷却水の流動を案内するための冷却水管(120)と、冷却水管(120)を収容するための冷却水管収容部(115)が形成され、焼却対象物が置かれて焼却がなされる本体(110)と、冷却水管収容部(115)に固定され、本体(110)の熱的状態に応じて膨張または収縮の熱変形をする熱伝達調節部材(130)を備えている。   On the other hand, in the case of the grate described in Patent Document 2, as shown in FIG. 1, when industrial waste is put into the incinerator (10), the industrial waste is in a multistage stepped form. Are sequentially passed through the grate (100) constituted by the above, incinerated in the combustion chamber (20), and discharged through the incineration ash discharge section provided on the lower side of the incinerator. The grate industrial waste transfer is pressed by a rod (3) driven by a hydraulic device (40). Further, as shown in FIG. 2, the water-cooled grate (100) of Patent Document 2 includes a cooling water pipe (120) for guiding the flow of cooling water for cooling the grate, and a cooling water pipe (120). A cooling water pipe housing part (115) for housing is formed, and a main body (110) on which an incineration object is placed and incinerated, and fixed to the cooling water pipe housing part (115), the thermal of the main body (110) A heat transfer adjusting member (130) that thermally expands or contracts depending on the state is provided.

特開2000−240926号公報JP 2000-240926 A 特表2009−500590号公報Special table 2009-500590

しかし、特許文献1の火格子燃焼装置の場合、ボイラー・焼却炉などの負荷が下がり、燃焼が減少するとき、あるいはボイラー・焼却炉が停止する直前など、焼却炉の熱負荷が低くなると、冷却水が火格子を過度に冷却して火格子表面の温度が低くなる。その結果、火格子上の燃焼温度(火層温度)も必要以上に下がり不完全燃焼になるため、未燃物が多く生成され燃焼効率が悪くなる。また、必要以上の火格子の冷却は生成した燃焼熱を冷却水が奪い、このために有効に利用できる熱量が少なくなり装置全体の熱効率の低下を招く。   However, in the case of the grate combustion apparatus of Patent Document 1, when the load on the boiler / incinerator decreases and the combustion decreases, or when the thermal load on the incinerator decreases, such as immediately before the boiler / incinerator stops, Water excessively cools the grate and lowers the grate surface temperature. As a result, the combustion temperature (fired layer temperature) on the grate also decreases more than necessary, resulting in incomplete combustion, resulting in a large amount of unburned matter and poor combustion efficiency. Further, if the grate is cooled more than necessary, the generated heat of combustion is taken away by the cooling water, so that the amount of heat that can be effectively used is reduced and the thermal efficiency of the entire apparatus is lowered.

また、特許文献2において参照符号(130)で示されるように冷却管と火格子の熱膨張差による障害をなくし、熱伝導を損なわないように冷却管と火格子を密着させるための熱伝道率の優れた金具等を必要としない。尚、このような金具を差し込むと火格子と金具、金具と冷却管のそれどれの間に僅かな間隙(境膜)ができ、この間隙が熱伝達を著しく阻害し冷却能力が低下する。また、特許文献2によれば、熱伝達調節部材(130)として、銅又はアルミニウムのような熱膨張係数又は線膨張係数が高く、熱伝導性に良好な金属材料またはこのような金属材料を含む合金からなるとしており、高価な材料に依存している。 Further, as indicated by reference numeral (130) in Patent Document 2, the heat transfer coefficient for eliminating the obstacle due to the difference in thermal expansion between the cooling pipe and the grate and bringing the cooling pipe and the grate into close contact so as not to impair the heat conduction. No need for excellent metal fittings. When such a metal fitting is inserted, a slight gap (film) is formed between the grate and the metal fitting, and between the metal fitting and the cooling pipe, and this gap significantly impedes heat transfer and lowers the cooling capacity. Further, according to Patent Document 2, the heat transfer adjusting member (130) includes a metal material having a high thermal expansion coefficient or linear expansion coefficient such as copper or aluminum and having good thermal conductivity, or such a metal material. It is made of an alloy and relies on expensive materials.

上述のとおり、従来の火格子装置は、火格子の温度は燃焼温度により変化し、燃焼が盛んで燃焼温度が高いときは高くなり、燃焼が緩慢なときは低くなるという問題がある。   As described above, the conventional grate apparatus has a problem that the temperature of the grate varies depending on the combustion temperature, and becomes high when combustion is high and the combustion temperature is high, and becomes low when combustion is slow.

本発明は、上述の従来の火格子燃焼装置の問題点を解消し、構造が簡単で、かつ高温部での焼損を防止し、耐久性に優れ、低温部では過冷却を防ぎ未燃物の発生を抑制し、そのうえコストの低い火格子燃焼装置を提供することを目的としている。   The present invention eliminates the problems of the above-described conventional grate combustion apparatus, has a simple structure, prevents burning at a high temperature part, has excellent durability, prevents overcooling at a low temperature part, An object of the present invention is to provide a grate combustion apparatus that suppresses generation and is low in cost.

請求項1記載の発明は、板状体からなり、
当該板状体の前縁には下方に折れ曲がった折れ曲がり部が設けられ、
当該板状体の後縁部には下方に延びる土手部が設けられ、
前記折れ曲がり部と土手部との間に、熱媒体としての冷却清水を流通させる複数の冷却清水配管がそれぞれ空冷部を介して並置されてなる
ことを特徴とする火格子燃焼装置に関する。
The invention according to claim 1 comprises a plate-like body,
The front edge of the plate-like body is provided with a bent portion bent downward,
A bank portion extending downward is provided at the rear edge of the plate-like body,
The present invention relates to a grate combustion apparatus characterized in that a plurality of cooling fresh water pipes for circulating cooling fresh water as a heat medium are juxtaposed between the bent part and the bank part via air cooling parts.

請求項2記載の発明は、前記空冷部が二つの中間土手部によって画定され、該二つの中間土手部の間に複数のフィンが設けられ、該複数のフィンの間に前記通気孔が設けられ、前記空冷部には通気孔が設けられてなることを特徴とする請求項1記載の火格子燃焼装置に関する。   According to a second aspect of the present invention, the air cooling part is defined by two intermediate bank parts, a plurality of fins are provided between the two intermediate bank parts, and the ventilation holes are provided between the plurality of fins. 2. The grate combustion apparatus according to claim 1, wherein a vent hole is provided in the air cooling section.

請求項3記載の発明は、前記複数の冷却清水配管が、前記板状体に形成された部分円筒面と面接触することを特徴とする請求項1又は2記載の火格子燃焼装置に関する。   The invention according to claim 3 relates to the grate combustion apparatus according to claim 1 or 2, wherein the plurality of cooling fresh water pipes are in surface contact with a partial cylindrical surface formed on the plate-like body.

請求項4記載の発明は、前記火格子が球状黒鉛鋳鉄から製造されてなることを特徴とする火格子燃焼装置に関する請求項1乃至3記載の火格子燃焼装置に関する。
本発明の請求項5の発明は、前記火格子の厚さが10乃至20mmであり、前記フィンの厚さが8乃至15mmであることを特徴とする請求項1乃至4記載の火格子燃焼装置に関する。
The invention according to claim 4 relates to the grate combustion apparatus according to claims 1 to 3, wherein the grate is manufactured from spheroidal graphite cast iron.
According to a fifth aspect of the present invention, the grate combustion apparatus according to any one of the first to fourth aspects, wherein the grate has a thickness of 10 to 20 mm and the fin has a thickness of 8 to 15 mm. About.

本発明の請求項6は、 固形燃料焚きボイラー燃焼装置及び産業廃棄物用の焼却炉装置であって、
該ボイラー燃焼装置及び焼却炉装置の燃焼室内に、多段式の階段状の形態で配設される複数の火格子燃焼装置と、
該燃焼室内で燃焼され、該燃焼装置の下側に設けられた焼却灰の排出部と、
前記火格子燃焼装置を往復移動する油圧装置と
を含み、
前記火格子燃焼装置が、板状体からなり、
当該板状体の前縁には下方に折れ曲がった折れ曲がり部が設けられ、
当該板状体の後縁部には下方に延びる土手部が設けられ、
前記折れ曲がり部と土手部との間に、熱媒体としての冷却清水を流通させる複数の冷却清水配管がそれぞれ空冷部を介して並置され、
前記空冷部には通気孔が設けられてなる
ことを特徴とする産業廃棄物用の焼却炉に関する。
本発明の請求項7は、前記ボイラー燃焼装置が脱気器を備え、前記冷却清水配管が当該脱気器に接続されていることを特徴とする請求項6記載の固形燃料焚きボイラー燃焼装置及び産業廃棄物用の焼却炉装置に関する。
Claim 6 of the present invention is a solid fuel-fired boiler combustion apparatus and an incinerator apparatus for industrial waste,
A plurality of grate combustion apparatuses disposed in a combustion chamber of the boiler combustion apparatus and the incinerator apparatus in a multistage stepped form;
An incinerator ash discharge unit that is combusted in the combustion chamber and provided below the combustion device;
A hydraulic device that reciprocates the grate combustion device,
The grate combustion device is composed of a plate-like body,
The front edge of the plate-like body is provided with a bent portion bent downward,
A bank portion extending downward is provided at the rear edge of the plate-like body,
Between the bent part and the bank part, a plurality of cooling fresh water pipes for circulating cooling fresh water as a heat medium are juxtaposed via the air cooling part,
The present invention relates to an incinerator for industrial waste, wherein the air cooling part is provided with a vent hole.
According to a seventh aspect of the present invention, the boiler combustion apparatus includes a deaerator, and the cooling fresh water pipe is connected to the deaerator. The present invention relates to an incinerator device for industrial waste.

すなわち、本発明に係る火格子冷却装置は、冷却管内の冷却水による冷却と燃焼用空気の空気冷却を組み合わせたもので、冷却水は高温の火格子から放射される輻射熱を吸収して火格子を冷却し、火格子温度が低いとき冷却効果が低下するが、空気冷却部の燃焼空気が接触伝熱によって火格子を冷却する。また空気冷却が効果的に行えるよう空気の通る部分に多数の冷却板(冷却フイン)を設けている。空気冷却は熱容量((比熱KCal/Nm℃)が小さく更に空気量は限定されているため火格子からの伝熱量が少ない。このために燃焼が盛んに行われているときはその冷却効果は小さい。異なる温度の物体面での基本輻射伝熱量は次の式で表され、2物体表面の温度差の4乗差に伝熱する。 That is, the grate cooling apparatus according to the present invention combines cooling with cooling water in the cooling pipe and air cooling of the combustion air, and the cooling water absorbs radiant heat radiated from the high-temperature grate and grate. The cooling effect is reduced when the grate temperature is low, but the combustion air in the air cooling section cools the grate by contact heat transfer. In addition, a large number of cooling plates (cooling fins) are provided in a portion through which air passes so that air cooling can be performed effectively. Air cooling has a small heat capacity ((specific heat KCal / Nm 3 ° C.) and the amount of air is limited, so the amount of heat transferred from the grate is small. The basic radiant heat transfer amount on the object surface at different temperatures is expressed by the following equation, and the heat is transferred to the fourth power difference of the temperature difference between the two object surfaces.

Figure 2012197991
Figure 2012197991

請求項1、2、3、4及び5に係る発明によれば、構造が簡単で、かつ高温部での焼損を防止し、耐久性に優れた火格子燃焼装置を提供することができる。   According to the first, second, third, fourth, and fifth aspects of the present invention, it is possible to provide a grate combustion apparatus that has a simple structure, prevents burning at a high temperature portion, and is excellent in durability.

本発明に係る火格子冷却装置の水冷部は、輻射伝熱による間接冷却方式を採用しているため、冷却水への輻射伝熱量は火格子の温度(燃焼物の火層温度)が高ければ高いほど大きく、火格子の温度が低くければ低いほど相乗的に伝熱量が少なくなる。従って、低燃焼域で燃焼温度が低いとき、火層の温度を下げ過ぎることはなく、適度の燃焼温度(火層温度)を維持し未燃物の発生を防止することができる。   Since the water cooling part of the grate cooling device according to the present invention employs an indirect cooling method by radiant heat transfer, the amount of radiant heat transfer to the cooling water is high if the temperature of the grate (fire layer temperature of the combustion product) is high. The higher the temperature, the lower the temperature of the grate, the lower the amount of heat transfer. Therefore, when the combustion temperature is low in the low combustion region, the temperature of the fire layer is not lowered too much, and an appropriate combustion temperature (fire layer temperature) can be maintained and the generation of unburned matter can be prevented.

また、本発明に係る火格子冷却装置は、火格子と冷却管は熱伝導による熱伝達方式でないため、冷却管と火格子の接触は密着させる必要がなく、間隙を相当に大きくしてもなんら伝熱が損なわれることはない。このことにより、火格子と冷却管の熱膨張差による障害が生じないほどに充分な間隙を設けることができる。   The grate cooling apparatus according to the present invention does not require close contact between the cooling pipe and the grate because the grate and the cooling pipe are not a heat transfer system by heat conduction, and the gap is considerably increased. Heat transfer is not impaired. As a result, a sufficient gap can be provided so as not to cause a failure due to a difference in thermal expansion between the grate and the cooling pipe.

本発明に係る火格子冷却装置では、空気冷却部は接触(対流)伝熱と水冷冷却部と同じように輻射伝熱も行われるが、空気の熱容量(比熱KCal/Nm℃)が小さくまた、必要燃焼空気量が限定されるために冷却空気は少量の接触伝熱で高温になるため、燃焼温度が高い(火格子温度が高い)域では水冷冷却伝熱量に及ばない。このことにより火格子温度の低い低燃焼域で火格子を冷やし過ぎることはない。 In the grate cooling apparatus according to the present invention, the air cooling unit performs radiant heat transfer in the same manner as the contact (convection) heat transfer and the water cooling cooling unit, but the air heat capacity (specific heat KCaI / Nm 3 ° C.) Since the required amount of combustion air is limited, the cooling air becomes high temperature with a small amount of contact heat transfer, and therefore does not reach the water cooling cooling heat transfer amount in the region where the combustion temperature is high (grate temperature is high). This does not overcool the grate in a low combustion zone with a low grate temperature.

空気冷却部の接触(対流)伝熱量の基本式は次の通りである。   The basic formula of the contact (convection) heat transfer amount of the air cooling section is as follows.

Figure 2012197991
Figure 2012197991

本発明に係る火格子冷却装置は、空気冷却部の接触伝熱量は温度差と火格子の表面面積に影響されるので、火格子の表面面積が多くなるように数枚のフィンを設けている。   In the grate cooling apparatus according to the present invention, the amount of contact heat transfer in the air cooling unit is affected by the temperature difference and the surface area of the grate, and therefore, several fins are provided to increase the surface area of the grate. .

従来の焼却炉の構成を示す説明図である。It is explanatory drawing which shows the structure of the conventional incinerator. 図1の焼却炉に適用される火格子燃焼装置の構成を示す斜視図である。It is a perspective view which shows the structure of the grate combustion apparatus applied to the incinerator of FIG. 本発明の一実施形態に係る火格子燃焼装置の一例を示す斜視図である。It is a perspective view which shows an example of the grate combustion apparatus which concerns on one Embodiment of this invention. 図3の火格子燃焼装置を構成する板状体を示す斜視図である。It is a perspective view which shows the plate-shaped body which comprises the grate combustion apparatus of FIG. 図4の板状体の平面図である。It is a top view of the plate-shaped body of FIG. 本発明の火格子燃焼装置を階段状に複数台配設した燃焼装置に適用したときの冷却効果を算出したシミュレーション結果を示す説明図である。It is explanatory drawing which shows the simulation result which computed the cooling effect when applying the grate combustion apparatus of this invention to the combustion apparatus arrange | positioned in multiple steps in step shape. 本発明の火格子燃焼装置を固定燃料焚きボイラー燃焼装置に適用した場合において、火格子装置の冷却清水配管で熱交換された冷却清水を脱気器の給水として使用しない場合のボイラー効率の算出結果を示す説明図である。When the grate combustion apparatus of the present invention is applied to a fixed fuel-fired boiler combustion apparatus, the calculation result of boiler efficiency when cooling fresh water heat-exchanged in the cooling fresh water piping of the grate apparatus is not used as feed water for the deaerator It is explanatory drawing which shows. 本発明の火格子燃焼装置を固定燃料焚きボイラー燃焼装置に適用した場合において、火格子装置の冷却清水配管で熱交換された冷却清水を脱気器の給水として使用した場合のボイラー効率の算出結果を示す説明図である。When the grate combustion apparatus of the present invention is applied to a fixed fuel-fired boiler combustion apparatus, the calculation result of the boiler efficiency when the cooled fresh water heat-exchanged in the cooled fresh water piping of the grate apparatus is used as the feed water for the deaerator It is explanatory drawing which shows.

本発明の火格子燃焼装置について添付図面を参照しながら説明する。
図3は本発明の一実施形態に係る火格子燃焼装置の一例を示す斜視図である。図4は図3の火格子燃焼装置を構成する板状体を示す斜視図である。図5は図4の板状体の平面図である。図6は本発明の火格子燃焼装置を階段状に複数台配設した燃焼装置に適用したときの冷却効果を算出したシミュレーション結果を示す説明図である。図7は本発明の火格子燃焼装置を固定燃料焚きボイラー燃焼装置に適用した場合において、火格子装置の冷却清水配管で熱交換された冷却清水を脱気器の給水として使用しない場合のボイラー効率の算出結果を示す説明図である。図8は本発明の火格子燃焼装置を固定燃料焚きボイラー燃焼装置に適用した場合において、火格子装置の冷却清水配管で熱交換された冷却清水を脱気器の給水として使用した場合のボイラー効率の算出結果を示す説明図である。
The grate combustion apparatus of the present invention will be described with reference to the accompanying drawings.
FIG. 3 is a perspective view showing an example of a grate combustion apparatus according to an embodiment of the present invention. 4 is a perspective view showing a plate-like body constituting the grate combustion apparatus of FIG. FIG. 5 is a plan view of the plate-like body of FIG. FIG. 6 is an explanatory diagram showing a simulation result of calculating a cooling effect when the grate combustion apparatus of the present invention is applied to a combustion apparatus in which a plurality of staircase combustion apparatuses are arranged stepwise. FIG. 7 shows the boiler efficiency in the case where the grate combustion apparatus of the present invention is applied to a fixed fuel-fired boiler combustion apparatus and the cooled fresh water heat-exchanged in the cooled fresh water piping of the grate apparatus is not used as feed water for the deaerator It is explanatory drawing which shows the calculation result. FIG. 8 shows the boiler efficiency when cooling fresh water heat-exchanged in the cooling fresh water piping of the grate device is used as feed water for the deaerator when the grate combustion device of the present invention is applied to a fixed fuel-fired boiler combustion device. It is explanatory drawing which shows the calculation result.

図3〜5を参照すると、参照符号1は本実施形態に係る火格子燃焼装置を示している。参照符号(S)は板状体を示しおり、アルファベットのLを倒した様な形状を呈している。参照符号(S1)は板状体(S)の表側を示している。参照符号(S2)は板状体(S)の裏側を示している。参照符号(2)は板状体(S)の前縁の折れ曲がり部を示している。参照符号(3)は板状体(S)の後縁部に設けられた土手部を示している。参照符号(P)は冷却清水配管を示している。参照符号(4a)、(4b)、(4c)、(4d)は板状体(S)の裏側(S2)の折れ曲がり部(2)と土手部(3)との間に形成された中間土手部を示している。参照符号(5)は中間土手部(4a)と中間土手部(4b)との間、中間土手部(4c)と中間土手部(4d)との間、中間土手部(4e)と土手部(3)との間に設けられたフィンを示している。参照符号(H)は板状体(S)の中間土手部(4a)と中間土手部(4b)との間、中間土手部(4c)と中間土手部(4d)との間に形成されたフィン(5)同士の間に設けられた通気孔を示している。参照符号(L)は火格子燃焼装置(1)の下方を示す矢印である。参照符号(U)は火格子燃焼装置(1)の上方を示す矢印である。   3 to 5, reference numeral 1 indicates a grate combustion apparatus according to the present embodiment. Reference numeral (S) indicates a plate-like body, which has a shape like that of the alphabet L being defeated. Reference numeral (S1) indicates the front side of the plate-like body (S). Reference numeral (S2) indicates the back side of the plate-like body (S). Reference numeral (2) indicates a bent portion of the front edge of the plate-like body (S). Reference numeral (3) indicates a bank provided at the rear edge of the plate-like body (S). Reference numeral (P) indicates a cooling fresh water pipe. Reference numerals (4a), (4b), (4c) and (4d) are intermediate banks formed between the bent part (2) and the bank part (3) on the back side (S2) of the plate-like body (S). Shows the part. Reference numeral (5) denotes between the intermediate bank portion (4a) and the intermediate bank portion (4b), between the intermediate bank portion (4c) and the intermediate bank portion (4d), between the intermediate bank portion (4e) and the bank portion ( The fin provided between 3) is shown. The reference symbol (H) is formed between the intermediate bank portion (4a) and the intermediate bank portion (4b) of the plate-like body (S) and between the intermediate bank portion (4c) and the intermediate bank portion (4d). The ventilation hole provided between fins (5) is shown. Reference numeral (L) is an arrow indicating the lower side of the grate combustion apparatus (1). Reference sign (U) is an arrow indicating the upper side of the grate combustion apparatus (1).

ここで再び図3〜5を参照すると、本実施形態の火格子燃焼装置(1)は板状体(S)を備えている。板状体(S)の前縁には下方に折れ曲がった折れ曲がり部(3)が設けられている。また、板状体(S)の後縁部(3)には下方に延びる土中間手部(4a)、(4b)、(4c)、(4d)が設けられている。折れ曲がり部(2)と土手部(3)との間には、熱媒体としての冷却用の清水(以下、「冷却清水」という)を流通させる複数の冷却清水配管(P)がそれぞれ空冷部として機能するフィン(5)が形成された部位を介して3本互いに平行に並置されている。   3-5 again, the grate combustion apparatus (1) of this embodiment is provided with the plate-shaped body (S). A bent portion (3) bent downward is provided at the front edge of the plate-like body (S). The rear edge (3) of the plate-like body (S) is provided with soil intermediate hands (4a), (4b), (4c) and (4d) extending downward. Between the bent part (2) and the bank part (3), a plurality of cooling fresh water pipes (P) through which cooling water as a heat medium (hereinafter referred to as “cooling fresh water”) is circulated as air cooling parts. Three of them are juxtaposed in parallel with each other through a site where a functioning fin (5) is formed.

ここで、熱媒体として清水を用いているのは、冷却用の配管として耐食性の材質を採用することにより、冷媒として海水を用いることは可能であるが、コストが高くなるため、冷媒として海水を除外した。また、熱媒体として清水を用いると、火格子燃焼装置(1)の板状体(S)から回収した熱を暖房や風呂、ハウス栽培用に二次利用が可能であるという利点もある。本実施形態において冷却部は、中間土手部(4a)と中間土手部(4b)との間、中間土手部(4c)と中間土手部(4d)との間、中間土手部(4e)と土手部(3)との間に設けられたフィン(5)と、板状体(S)の中間土手部(4a)と中間土手部(4b)との間、中間土手部(4c)と中間土手部(4d)との間に形成されたフィン(5)同士の間に設けられた通気孔(H)から構成(画定)されている。図示された例では、中間土手部(4a)と中間土手部(4b)との間、中間土手部(4c)と中間土手部(4d)との間、中間土手部(4e)と土手部(3)との間には、それぞれ、4つのフィン(5)が設けられているが、4つに限定されることはない。また、図示された例では、中間土手部(4a)と中間土手部(4b)との間、並びに中間土手部(4c)と中間土手部(4d)との間に形成されたフィン(5)同士の間には、それぞれ3つの通気孔(H)が設けられているが、3つに限定されることはない。このように通気孔(H)を設けて、冷風を矢印U方向に送風すると、板状体(S)の上面(S1)及び下面(S2)を含む各表面の高温加熱を抑制するだけでなく、焼却炉の被焼却物に対する乾燥及び燃焼を促進するという利点がある。   Here, fresh water is used as the heat medium because it is possible to use seawater as a refrigerant by adopting a corrosion-resistant material as a cooling pipe, but the cost increases, so seawater is used as the refrigerant. Excluded. Moreover, when fresh water is used as the heat medium, there is an advantage that the heat recovered from the plate-like body (S) of the grate combustion apparatus (1) can be secondarily used for heating, bathing, and house cultivation. In the present embodiment, the cooling section includes the intermediate bank section (4a) and the intermediate bank section (4b), the intermediate bank section (4c) and the intermediate bank section (4d), the intermediate bank section (4e) and the bank. Between the fin (5) provided between the part (3) and the intermediate bank part (4a) and the intermediate bank part (4b) of the plate-like body (S), the intermediate bank part (4c) and the intermediate bank It is comprised (defined) from the vent hole (H) provided between the fins (5) formed between the parts (4d). In the illustrated example, between the intermediate bank part (4a) and the intermediate bank part (4b), between the intermediate bank part (4c) and the intermediate bank part (4d), between the intermediate bank part (4e) and the bank part ( The four fins (5) are provided between each of the three (3), but the number is not limited to four. In the illustrated example, fins (5) formed between the intermediate bank portion (4a) and the intermediate bank portion (4b) and between the intermediate bank portion (4c) and the intermediate bank portion (4d). Three ventilation holes (H) are provided between each other, but the number is not limited to three. When the air holes (H) are thus provided and the cool air is blown in the direction of the arrow U, not only the high temperature heating of each surface including the upper surface (S1) and the lower surface (S2) of the plate-like body (S) is suppressed. There is an advantage of promoting drying and combustion of the incinerator to be incinerated.

フィン(5)の数は、その長さ、厚さ、フィン(5)同士の間の間隔といった変数から最適値が決まる。本実施形態においては、板状体(S)とフィン(5)は鋳型によって一体的に形成され、材質としては球状黒鉛鋳鉄FCD500と0.5%のCrが採用される。コストを度外視すれば、SUSの鋳物を採用することも可能であるが、本発明ではコストを重視していることから球状黒鉛鋳鉄の鋳物に比して3.5倍も高価なSUSの鋳物を除外した。また、本実施形態においては、板状体(S)の厚さは10〜20mmであり、フィン(5)の厚さは8〜15mmである。 The optimum value of the number of fins (5) is determined from variables such as the length, thickness, and spacing between the fins (5). In the present embodiment, the plate-like body (S) and the fin (5) are integrally formed by a mold, and the material is spheroidal graphite cast iron FCD500 and 0.5% Cr. It is possible to adopt a SUS casting if the cost is neglected. However, in the present invention, since the cost is emphasized, a SUS casting that is 3.5 times more expensive than a spheroidal graphite cast iron casting is used. Excluded. Moreover, in this embodiment, the thickness of a plate-shaped object (S) is 10-20 mm, and the thickness of a fin (5) is 8-15 mm.

なお、図示された例では、板状体(S)の中間土手部(4a)と中間土手部(4b)との間、中間土手部(4c)と中間土手部(4d)との間に形成されたフィン(5)同士の間には、通気孔(H)が設けられているが、本実施形態の変形例として、間土手部(4a)と中間土手部(4b)との間、中間土手部(4c)と中間土手部(4d)との間に形成されたフィン(5)同士の間に通気孔(H)が設けられていないものも本発明に含まれる。   In the illustrated example, the plate-like body (S) is formed between the intermediate bank portion (4a) and the intermediate bank portion (4b), and between the intermediate bank portion (4c) and the intermediate bank portion (4d). A vent hole (H) is provided between the formed fins (5), but as a modification of the present embodiment, the intermediate bank (4a) and the intermediate bank (4b) are intermediate The present invention includes a case in which the air holes (H) are not provided between the fins (5) formed between the bank portion (4c) and the intermediate bank portion (4d).

再び図3〜5を参照すると、本実施形態の火格子燃焼装置(1)の板状体(S)は、3本の冷却清水配管(P)の上に、板状体(S)の裏側(S2)の折れ曲がり部(2)と中間土手部(4a)との間、中間土手部(4b)と中間土手部(4c)との間、中間土手部(4d)と中間土手部(4e)との間の冷却清水配管(P)の受け入れ部位(Sa)に形成された部分円筒面と、面接触して載置される。冷却清水配管(P)の材質は、熱伝導性が良好で、かつコストの低いものが採用される。   3-5 again, the plate-like body (S) of the grate combustion apparatus (1) of this embodiment is on the back side of the plate-like body (S) on the three cooling fresh water pipes (P). (S2) between the bent part (2) and the intermediate bank part (4a), between the intermediate bank part (4b) and the intermediate bank part (4c), between the intermediate bank part (4d) and the intermediate bank part (4e). Is placed in surface contact with the partial cylindrical surface formed in the receiving part (Sa) of the cooling fresh water pipe (P) between the two. As the material of the cooling fresh water pipe (P), a material having good thermal conductivity and low cost is adopted.

本実施形態の火格子燃焼装置(1)は、産業廃棄物用の焼却炉に採用される。その場合、図1に示される従来の焼却炉(10)の燃焼室(20)内に、図1に図示された多段式の階段状の形態で例えば、前述の本発明の火格子燃焼装置(1)4台が従来の火格子燃焼装置(100)に代えて配設される。いうまでなく、焼却炉(10)内には、図1に示された例と同様に、燃焼室(20)内で焼却され、焼却炉(20)の下側に設けられた焼却灰の排出部(50)と、火格子燃焼装置(1)を往復移動する、油圧装置(40)によって駆動されるロッド(30)とを含んでいる。   The grate combustion apparatus (1) of this embodiment is employed in an incinerator for industrial waste. In that case, for example, in the combustion chamber (20) of the conventional incinerator (10) shown in FIG. 1) Four units are arranged in place of the conventional grate combustion apparatus (100). Needless to say, in the incinerator (10), in the same manner as in the example shown in FIG. 1, the incinerated ash discharged from the incinerator (20) is incinerated in the combustion chamber (20). Part (50) and a rod (30) driven by a hydraulic device (40) that reciprocates the grate combustion device (1).

ここで、図6を参照して、本実施形態の火格子燃焼装置(1)を実際の焼却炉に適用した場合の効果としての、本発明の火格子燃焼装置の予想表面温度のシミュレーション結果を説明する。図6において、参照符号(M)は油圧装置(40)によって駆動されるロッド(30)による往復移動可能な摺動火格子燃焼装置(1)を示し、参照符号(F)は固定火格子燃焼装置(1)を示す。参照符号(1Ga)は4段の階段状に配設された第一火格子燃焼装置群を示し、参照符号(1Gb)は4段の階段状に配設された第二火格子燃焼装置群を示している。参照符号(C)は搬送装置を示している。   Here, with reference to FIG. 6, the simulation result of the predicted surface temperature of the grate combustion apparatus of the present invention as an effect when the grate combustion apparatus (1) of the present embodiment is applied to an actual incinerator is shown. explain. In FIG. 6, reference numeral (M) indicates a sliding grate combustion apparatus (1) capable of reciprocating movement by a rod (30) driven by a hydraulic apparatus (40), and reference numeral (F) is fixed grate combustion. The device (1) is shown. Reference numeral (1Ga) indicates a first grate combustion apparatus group arranged in four steps, and reference numeral (1Gb) indicates a second grate combustion apparatus group arranged in four steps. Show. Reference numeral (C) indicates a transport device.

シミュレーションでは、実際の温度を考慮して、ロータリーキルンを介して焼却炉内に580℃の燃料が投入されると仮定した。また、第一火格子燃焼装置軍(1Ga)と、搬送装置(C)と、第二火格子燃焼装置群(1Gb)とに、15℃の冷風が送風されると仮定した。第一火格子燃焼装置軍(1Ga)の最上段の摺動火格子燃焼装置(1)の表面温度は400℃となり、隣接する固定火格子燃焼装置(1)の表面温度は430℃となり、隣接する摺動火格子燃焼装置(1)の表面温度は440℃となり、隣接する固定火格子燃焼装置(1)の表面温度は430℃となり、搬送装置(C)に落下した直後の燃料の温度は480℃となり、搬送装置(C)から第二火格子燃焼装置群(1Gb)に落下する直前の燃料の温度は260℃となった。さらに、第二火格子燃焼装置軍(1Gb)の最上段の摺動火格子燃焼装置(1)の表面温度は280℃となり、隣接する固定火格子燃焼装置(1)の表面温度は250℃となり、隣接する摺動火格子燃焼装置(1)の表面温度は230℃となり、隣接する固定火格子燃焼装置(1)の表面温度は220℃となった。   In the simulation, it was assumed that 580 ° C. fuel was introduced into the incinerator through the rotary kiln in consideration of the actual temperature. Further, it was assumed that cold air of 15 ° C. was blown to the first grate combustion device army (1Ga), the transfer device (C), and the second grate combustion device group (1Gb). The surface temperature of the uppermost sliding grate combustion device (1) of the first grate combustion device army (1Ga) is 400 ° C., and the surface temperature of the adjacent fixed grate combustion device (1) is 430 ° C. The surface temperature of the sliding grate combustion device (1) is 440 ° C., the surface temperature of the adjacent fixed grate combustion device (1) is 430 ° C., and the temperature of the fuel immediately after dropping on the transfer device (C) is The temperature of the fuel immediately before dropping from the transfer device (C) to the second grate combustion device group (1 Gb) was 260 ° C. Furthermore, the surface temperature of the uppermost sliding grate combustion device (1) of the second grate combustion device army (1Gb) is 280 ° C., and the surface temperature of the adjacent fixed grate combustion device (1) is 250 ° C. The surface temperature of the adjacent sliding grate combustion device (1) was 230 ° C., and the surface temperature of the adjacent fixed grate combustion device (1) was 220 ° C.

水冷式の火格子燃焼装置を用いた焼却炉の場合、焼却炉が部分負荷で運転されることにより焼却量が減少したりして、焼却炉の熱負荷が低くなる場合は、板状体(S)の温度は低くなり、冷却清水配管(P)中を流れる冷却水の温度(約70℃)まで冷却されることがある。しかし、本発明では、中間土手部(4a)と中間土手部(4b)との間、並びに中間土手部(4c)と中間土手部(4d)との間に形成されたフィン(5)同士の間には、それぞれ3つの通気孔(H)が設けられていて、冷却清水による冷却にのみに頼らず、空気による冷却をも取り入れているので、低温腐食を防止し、かつ板状体(S)の効率的な冷却を達成することができるという優れた効果を達成することができるのである。
ここで、図7及び8を参照すると、図8は本発明の火格子燃焼装置を固定燃料焚きボイラー燃焼装置に適用した場合において、火格子装置の冷却清水配管で熱交換された冷却清水を脱気器の給水として使用した場合のボイラー効率の算出結果を示している。図7及び8において、記号[No.1 stoker]は第一ストーカー群を示し、記号[No.2 stoker]は第二ストーカー群を示し、記号「Heat−up steam」は過熱蒸気、記号「Fix grate U」は上段側固定火格子、記号「Fix grate L」は下段側固定火格子、記号「Move grate U」は上段側可動火格子、記号「Move grate L」は下段側可動火格子、記号「Heat−exchange」は熱交換、記号「Transfer」は熱伝導、「to Boiler」はボイラーに導かれることを示している。そして、図8において、参照符号P1及びP2は、第一及び第二の火格子群の冷却清水配管から脱気器への給水配管系統を示す。一方、図7には、第一及び第二の火格子群の冷却清水管から脱気器への給水配管系統への給水配管系統がない。図7及び8の記号「to Boiler」における記載を比較すると、図7では52.8h/mであるのに対して、図8では53.1h/mであり、火格子において冷却用に使用された清水から熱回収されたことが分かる。それゆえ、火格子燃焼装置を固定燃料焚きボイラー燃焼装置に適用する場合は、火格子装置の冷却清水管内の清水は、炉内で熱交換された後、脱気器の給水として供給されることが好ましい。
In the case of an incinerator using a water-cooled grate combustor, if the incinerator is operated at a partial load, the amount of incineration will decrease, and the thermal load of the incinerator will be reduced. The temperature of S) becomes low and may be cooled to the temperature of cooling water (about 70 ° C.) flowing through the cooling fresh water pipe (P). However, in the present invention, the fins (5) formed between the intermediate bank portion (4a) and the intermediate bank portion (4b) and between the intermediate bank portion (4c) and the intermediate bank portion (4d) Three air holes (H) are provided between them, and not only relying on cooling by cooling fresh water but also cooling by air is taken in, so that low-temperature corrosion is prevented and a plate-like body (S It is possible to achieve an excellent effect that it is possible to achieve efficient cooling.
Here, referring to FIGS. 7 and 8, FIG. 8 shows that when the grate combustion apparatus of the present invention is applied to a fixed fuel-fired boiler combustion apparatus, the cooled fresh water subjected to heat exchange by the cooling fresh water piping of the grate apparatus is removed. It shows the calculation results of boiler efficiency when used as water supply for air. 7 and 8, the symbol [No. 1 stoker] indicates the first stalker group, and the symbol [No. 2 stoker] indicates a second stalker group, the symbol “Heat-up steam” is superheated steam, the symbol “Fix grate U” is the upper fixed grate, the symbol “Fix rate L” is the lower fixed grate, the symbol “ “Move rate U” is the upper movable grate, “Move rate L” is the lower movable grate, “Heat-exchange” is the heat exchange, “Transfer” is the heat conduction, and “to Boiler” is the boiler. It shows that it is. In FIG. 8, reference signs P <b> 1 and P <b> 2 indicate a water supply piping system from the cooling fresh water piping of the first and second grate groups to the deaerator. On the other hand, in FIG. 7, there is no feed water piping system from the cooling fresh water pipes of the first and second grate groups to the feed water piping system to the deaerator. Comparing described in symbol "-to Boiler" of FIG. 7 and 8, whereas a 52.8h / m 3 7 a 53.1h / m 3 8, for cooling the grate It can be seen that heat was recovered from the used fresh water. Therefore, when the grate combustion device is applied to a fixed fuel-fired boiler combustion device, the fresh water in the cooling fresh water pipe of the grate device is supplied as deaerator water after heat exchange in the furnace. Is preferred.

本発明によれば、構造が簡単で、かつ高温部での焼損を防止し、耐久性に優れた火格子燃焼装置を提供することができる。また、高温による焼損及び滴下燃焼による焼損や、塩素による高温腐食等の障害で燃焼装置を損傷することを防ぐことができる。   According to the present invention, it is possible to provide a grate combustion apparatus that has a simple structure, prevents burning at a high temperature portion, and is excellent in durability. In addition, it is possible to prevent the combustion apparatus from being damaged due to failures such as burning due to high temperature, burning due to dropping combustion, and high temperature corrosion due to chlorine.

1 火格子燃焼装置
1Ga 第一火格子燃焼装置群
1Gb 第二火格子燃焼装置群
2 折れ曲がり部
3 土手部
4a、4b、4c、4d、4e 中間土手部
5 フィン
H 通気孔
P 冷却清水配管
S1 表側
S2 裏側
Sa 冷却清水配管受け入れ部
DESCRIPTION OF SYMBOLS 1 Grate combustion apparatus 1Ga 1st grate combustion apparatus group 1Gb 2nd grate combustion apparatus group 2 Bending part 3 Bank part 4a, 4b, 4c, 4d, 4e Middle bank part 5 Fin H Ventilation hole P Cooling fresh water piping S1 Front side S2 Back side Sa Cooling fresh water pipe receiving part

Claims (7)

板状体からなり、
当該板状体の前縁には下方に折れ曲がった折れ曲がり部が設けられ、
当該板状体の後縁部には下方に延びる土手部が設けられ、
前記折れ曲がり部と土手部との間に、熱媒体としての冷却清水を流通させる複数の冷却清水配管がそれぞれ空冷部を介して並置されてなる
ことを特徴とする火格子燃焼装置。
It consists of a plate-like body
The front edge of the plate-like body is provided with a bent portion bent downward,
A bank portion extending downward is provided at the rear edge of the plate-like body,
A grate combustion apparatus, wherein a plurality of cooling fresh water pipes for circulating cooling fresh water as a heat medium are juxtaposed between the bent part and the bank part via an air cooling part.
前記空冷部が二つの中間土手部によって画定され、該二つの中間土手部の間に複数のフィンが設けられ、該複数のフィンの間に前記通気孔が設けられ、前記空冷部には通気孔が設けられてなることを特徴とする請求項1記載の火格子燃焼装置。 The air cooling part is defined by two intermediate bank parts, a plurality of fins are provided between the two intermediate bank parts, the air holes are provided between the plurality of fins, and the air cooling part is provided with air holes. The grate combustion apparatus according to claim 1, further comprising: 前記複数の冷却清水配管が、前記板状体に形成された部分円筒面と面接触することを特徴とする請求項1又は2記載の火格子燃焼装置。   The grate combustion apparatus according to claim 1 or 2, wherein the plurality of cooling fresh water pipes are in surface contact with a partial cylindrical surface formed on the plate-like body. 前記火格子が球状黒鉛鋳鉄から製造されてなることを特徴とする火格子燃焼装置に関する請求項1乃至3記載の火格子燃焼装置。   4. The grate combustion apparatus according to claim 1, wherein the grate is manufactured from spheroidal graphite cast iron. 前記火格子の厚さが10乃至20mmであり、前記フィンの厚さが8乃至15mmであることを特徴とする請求項1乃至3記載の火格子燃焼装置。   4. The grate combustion apparatus according to claim 1, wherein the grate has a thickness of 10 to 20 mm, and the fin has a thickness of 8 to 15 mm. 固形燃料焚きボイラー燃焼装置及び産業廃棄物用の焼却炉装置であって、
該ボイラー燃焼装置及び焼却炉装置の燃焼室内に、多段式の階段状の形態で配設される複数の火格子燃焼装置と、
該燃焼室内で焼却され、該焼却炉の下側に設けられた焼却灰の排出部と、
前記火格子燃焼装置を往復移動する油圧装置と
を含み、
前記火格子燃焼装置が、板状体からなり、
当該板状体の前縁には下方に折れ曲がった折れ曲がり部が設けられ、
当該板状体の後縁部には下方に延びる土手部が設けられ、
前記折れ曲がり部と土手部との間に、熱媒体としての冷却清水を流通させる複数の冷却清水配管がそれぞれ空冷部を介して並置され、
前記空冷部には通気孔が設けられてなる
ことを特徴とする産業廃棄物用の焼却炉。
A solid fuel-fired boiler combustion device and an incinerator device for industrial waste,
A plurality of grate combustion apparatuses disposed in a combustion chamber of the boiler combustion apparatus and the incinerator apparatus in a multistage stepped form;
An incinerator ash discharge unit disposed below the incinerator and incinerated in the combustion chamber;
A hydraulic device that reciprocates the grate combustion device,
The grate combustion device is composed of a plate-like body,
The front edge of the plate-like body is provided with a bent portion bent downward,
A bank portion extending downward is provided at the rear edge of the plate-like body,
Between the bent part and the bank part, a plurality of cooling fresh water pipes for circulating cooling fresh water as a heat medium are juxtaposed via the air cooling part,
An incinerator for industrial waste, wherein the air cooling part is provided with a vent hole.
前記ボイラー燃焼装置が脱気器を備え、前記冷却清水配管が当該脱気器に接続されていることを特徴とする請求項6記載の固形燃料焚きボイラー燃焼装置及び産業廃棄物用の焼却炉装置。   The solid fuel-fired boiler combustion apparatus and the incinerator apparatus for industrial waste according to claim 6, wherein the boiler combustion apparatus includes a deaerator, and the cooled fresh water pipe is connected to the deaerator. .
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CN103939889A (en) * 2014-04-11 2014-07-23 大连金鼎热能设备有限公司 Water pipe vortex fire grate biomass particle boiler
CN106524235A (en) * 2015-09-10 2017-03-22 牛铭 Multifunctional wood and coal furnace capable of preventing fire bar melting
CN107588425A (en) * 2017-09-14 2018-01-16 何玲玲 Pipe blows comb table apparatus

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CN103939889A (en) * 2014-04-11 2014-07-23 大连金鼎热能设备有限公司 Water pipe vortex fire grate biomass particle boiler
CN106524235A (en) * 2015-09-10 2017-03-22 牛铭 Multifunctional wood and coal furnace capable of preventing fire bar melting
CN107588425A (en) * 2017-09-14 2018-01-16 何玲玲 Pipe blows comb table apparatus

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