JPH05332522A - Method of igniting waste food containing salt - Google Patents

Method of igniting waste food containing salt

Info

Publication number
JPH05332522A
JPH05332522A JP4163564A JP16356492A JPH05332522A JP H05332522 A JPH05332522 A JP H05332522A JP 4163564 A JP4163564 A JP 4163564A JP 16356492 A JP16356492 A JP 16356492A JP H05332522 A JPH05332522 A JP H05332522A
Authority
JP
Japan
Prior art keywords
catalyst
gas
carbon
dechlorine
ignited
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP4163564A
Other languages
Japanese (ja)
Inventor
Sadashige Okada
貞重 岡田
Toshimitsu Ukai
利光 鵜飼
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP4163564A priority Critical patent/JPH05332522A/en
Publication of JPH05332522A publication Critical patent/JPH05332522A/en
Pending legal-status Critical Current

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  • Chimneys And Flues (AREA)
  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PURPOSE:To enable food containing salt to be ignited while its bad odor or soot smoke being removed by a method wherein chlorine gas of primary combustion and discharged gas containing carbon are secondary ignited and passed through a dechlorine catalyst. CONSTITUTION:As a dried noodle to be wasted is ignited, chlorine gas generated under decomposition of salt contained in the noodle is guided to a secondary combustion chamber 14 together with generated gas in a combustion furnace 6, carbon is ignited by an air blowing fan 15 and a heavy oil burner 16 to generate carbon oxide gas A. contact decomposing chamber 17 having refractory materials lined up in its inner surface is cooperatively arranged at the secondary combustion chamber 14. Dechlorine catalyst 18 is filled in it. The dechlorine catalyst 18 is made such that iron oxide powder and crushed zeorite are mixed and made into sphere particles and they are applied as raw baked and mixed catalyst having many voids in the baked surface. Hydrochloric acid gas is decomposed while dechlorine catalyst 18 being contacted and passed, and then chlorine is fixed to the catalyst 18 through its ion exchange. Accordingly, the discharged gas got from the contact decomposing chamber becomes non-pollution and non-smoke state.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、食品売場から回収され
た麺類、漬物等の含塩廃棄食品の焼却方法に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for incinerating salt-containing waste food such as noodles, pickles and the like collected from food counters.

【0002】[0002]

【従来の技術】従来では廃棄食品の一部を飼料としてい
るが、大部分は埋立てられているのが現状であり、腐敗
臭による公害問題となっている。そこで、廃棄食品を焼
却することが試されているが、含有する食塩が難燃剤的
作用をすることから燃焼し難く、このためカーボンの生
成を促進すると共に、毒性の塩酸ガスを発生するため的
確な焼却方法が見つからないのである。特に、麺類で
は、それに含まれる澱粉が糊化し粘着性の糊膜を形成し
て空気を遮断することから一層燃焼し難く、その焼却処
理が困難とされている。
2. Description of the Related Art Conventionally, a part of waste food is used as feed, but most of it is currently landfilled, which causes pollution problem due to putrid odor. Therefore, it has been tried to incinerate waste food, but it is difficult to burn it because the contained salt acts as a flame retardant, which promotes the formation of carbon and produces toxic hydrochloric acid gas. I can't find a proper incineration method. Particularly, in noodles, the starch contained therein is gelatinized to form an adhesive glue film to block air, so that it is more difficult to burn, and it is considered difficult to incinerate it.

【0003】[0003]

【発明が解決しようとする課題】そこで本発明は、澱粉
を多く含む麺類やその他の含塩食品も燃焼できて、塩酸
ガスによる焼却炉の腐食或いは大気汚染等を解消し、悪
臭や煤煙による弊害を解消できる焼却方法を提供するも
のである。
Therefore, according to the present invention, noodles containing a large amount of starch and other salt-containing foods can be burned, and corrosion of the incinerator due to hydrochloric acid gas, air pollution, etc. can be eliminated, and harmful effects of bad odor and soot can be solved. It is intended to provide an incineration method that can eliminate the problem.

【0004】[0004]

【課題を解決するための手段】このため本発明は、含塩
廃棄食品を熱風で乾燥し、その乾燥された廃棄食品を、
その熱風排気ガスの一部が送られる一次燃焼炉で燃焼し
てその焼却灰を取り出し、一次燃焼の塩素ガス及びカー
ボンを含んだ排ガスを二次燃焼してカーボンを炭酸ガス
とすると共に、銅及び/或いは鉄を、ゼオライトに混合
させて素焼きして成る脱塩素触媒に通過させることで塩
素を固定除去して排気する方法としている。なお、一次
燃焼炉の温度を700〜900゜Cに保持し、脱塩素触媒の設
置部を300〜500゜Cに保持するのが最適である。また、
脱塩素触媒を通過した二次燃焼排気ガスを、上水にて水
洗した後、大気中に放散することが望ましい。
Therefore, according to the present invention, salt-containing waste food is dried with hot air, and the dried waste food is
A part of the hot air exhaust gas is burned in the primary combustion furnace to remove the incineration ash, and the exhaust gas containing chlorine gas and carbon of the primary combustion is secondarily burned to convert carbon to carbon dioxide gas, and copper and Alternatively, chlorine is fixed and removed by passing iron through a dechlorination catalyst obtained by mixing iron with zeolite and calcination, and exhausting. It is optimum that the temperature of the primary combustion furnace is maintained at 700 to 900 ° C and the dechlorination catalyst installation part is maintained at 300 to 500 ° C. Also,
It is desirable that the secondary combustion exhaust gas that has passed through the dechlorination catalyst be washed with clean water and then released into the atmosphere.

【0005】ここで、一次燃焼炉で燃焼させる前に含塩
廃棄食品を熱風乾燥させるのは、燃焼を良好にするため
であり、熱風乾燥によって含塩廃棄食品をさらに細切れ
に砕き易くなると共に、麺類では澱粉による粘着性を解
いて糊膜の形成を阻止するのである。
Here, the reason why the salt-containing waste food is dried with hot air before being burned in the primary combustion furnace is to improve the combustion, and the hot-air drying makes it easier to break the salt-containing waste food into smaller pieces. In noodles, the tackiness of starch is released to prevent the formation of a glue film.

【0006】また、一次燃焼炉の温度は700〜900゜Cに
保持することが望ましく、乾燥された廃棄食品にバーナ
ー噴射で燃焼させるのである。この際、廃棄食品は乾燥
されて細切れとなっていることから良好に焼却できるの
である。また、乾燥用の熱風排気ガスの一部を一次燃焼
炉に送ることにより一次燃焼炉が乾燥熱風の余熱で高温
状態を保持できるのである。
Further, it is desirable to maintain the temperature of the primary combustion furnace at 700 to 900 ° C, and burn the dried waste food by burner injection. At this time, since the waste food is dried and shredded, it can be incinerated well. Further, by sending a part of the hot air exhaust gas for drying to the primary combustion furnace, the primary combustion furnace can maintain a high temperature state by the residual heat of the dry hot air.

【0007】一次燃焼の排ガスをバーナー等で二次燃焼
して脱塩素触媒に通過させるのは、排ガスに含まれるカ
ーボンを二次燃焼して炭酸ガスとし、さらに塩素ガスを
脱塩素触媒で除去するためである。ここで脱塩素触媒と
して、銅及び/或いは鉄を、ゼオライトに混合させ素焼
き成形した混合触媒とするのは、銅や鉄との接触で塩素
を良好に固定するのであり、ゼオライトの添加は成形性
と安価にするためである。なお、脱塩素触媒の設置部の
温度を300〜500゜Cに保持することが最適である。
The primary combustion exhaust gas is secondarily burned by a burner or the like and passed through the dechlorination catalyst. Carbon contained in the exhaust gas is secondarily burned into carbon dioxide gas, and further chlorine gas is removed by the dechlorination catalyst. This is because. Here, as the dechlorination catalyst, a mixed catalyst obtained by mixing copper and / or iron with zeolite and bisque-molding is to fix chlorine well in contact with copper or iron. And to make it cheap. It is optimal to keep the temperature of the installation site of the dechlorination catalyst at 300 to 500 ° C.

【0008】さらに、脱塩素触媒を通過した二次燃焼排
気ガスを、上水にて水洗するのは、僅かにカーボン等が
残留する最悪事態を考慮して除去するためであり、無公
害ガスとして大気中に放散するのである。
Further, the secondary combustion exhaust gas that has passed through the dechlorination catalyst is washed with clean water in order to remove it in consideration of the worst situation in which carbon or the like remains slightly, and as a pollution-free gas. It diffuses into the atmosphere.

【0009】[0009]

【作用】熱風で乾燥することで乾燥時間を早め、その熱
風排気ガスの一部を一次燃焼炉に送って余熱利用すると
共に、乾燥された廃棄食品を一次燃焼炉で燃焼してロス
トルから落下した焼却灰を取り出す。一次燃焼の排気ガ
スは塩素ガス及びカーボンを含んでおり、これを二次燃
焼して脱塩素触媒に通過させることで塩素が固定除去さ
れ、カーボンは炭酸ガスとして排気されるのである。
[Operation] The drying time is shortened by drying with hot air, and a part of the hot air exhaust gas is sent to the primary combustion furnace to utilize the residual heat, and the dried waste food is burned in the primary combustion furnace and dropped from the rustle. Take out the incineration ash. The exhaust gas of the primary combustion contains chlorine gas and carbon, and by secondary combustion of this gas and passing it through a dechlorination catalyst, chlorine is fixedly removed, and carbon is exhausted as carbon dioxide gas.

【0010】[0010]

【実施例】以下、本発明の詳細を、図示装置にしたがっ
て説明する。本例は廃棄食品としてうどん麺とそば麺の
廃棄麺を混合使用したものであり、そのまま捨てたスト
ックフィダー1からロータリ型熱風乾燥機2に投入され
て、廃棄麺は乾燥機内で回転しながら乾燥されるのであ
る。乾燥機内の温度は、その排気ガスが260〜300゜Cを
保持するように制御する。これにより、食塩を含んだ湿
潤廃棄麺が乾燥され、コンベア4に落下する。
The details of the present invention will be described below with reference to the illustrated apparatus. In this example, waste noodles such as udon noodles and buckwheat noodles are mixed and used as waste food. The discarded stock feeder 1 is put into a rotary hot air dryer 2 and the waste noodles are dried while rotating in a dryer. Is done. The temperature inside the dryer is controlled so that the exhaust gas maintains 260 to 300 ° C. As a result, the wet waste noodles containing salt are dried and dropped onto the conveyor 4.

【0011】つぎに、乾燥廃棄麺はコンベア4で中間ホ
ッパ5を介して一次燃焼炉6に送られる。なお、乾燥機
2の排気ガスは集塵機7によって除塵された後、循環フ
ァン8によって一部が乾燥機2の熱風発生炉3に戻さ
れ、残余は燃焼炉6へ吹き込まれる。また、燃焼炉6
は、燃焼用空気ファン9と重油バーナー10を備えて炉
温800゜Cに制御している。
Next, the dried waste noodles are sent to the primary combustion furnace 6 by the conveyor 4 via the intermediate hopper 5. After the exhaust gas of the dryer 2 is removed by the dust collector 7, a part of the exhaust gas is returned to the hot air generating furnace 3 of the dryer 2 by the circulation fan 8 and the rest is blown into the combustion furnace 6. Also, the combustion furnace 6
Is equipped with a combustion air fan 9 and a heavy oil burner 10 to control the furnace temperature to 800 ° C.

【0012】燃焼炉6での乾燥廃棄麺の燃焼は、乾燥廃
棄麺が燃焼炉6に投入されるまでに細切れ状となってい
ることから、空気ファン9及び循環ファン8による炉内
への噴出撹乱によって良好に燃焼されるのである。した
がって、乾燥廃棄麺が焼却され灰となってロストルから
下に落ち、冷却コンベア11から送りコンベア12、バ
ンカー13を介して搬出されるのである。
Combustion of the dry waste noodles in the combustion furnace 6 is in a chopped shape before the dry waste noodles are charged into the combustion furnace 6, and therefore the air fan 9 and the circulation fan 8 eject the dry waste noodles into the furnace. It is burned well by the disturbance. Therefore, the dried waste noodles are incinerated and turned into ash and fall down from the grate, and are carried out from the cooling conveyor 11 via the feeding conveyor 12 and the bunker 13.

【0013】一方、食塩の分解によって発生した塩酸ガ
スは、燃焼炉6の発生ガスと共に二次燃焼室14に導か
れ、空気送入ファン15と重油バーナー16にてカーボ
ンが燃焼し炭酸ガスとなる。二次燃焼室14には内面を
耐火煉瓦で内張りした接触分解室17が連設され、内部
に脱塩素触媒18が充填してある。脱塩素触媒18は、
酸化鉄粉と粉砕したゼオライトを同量混合して約25mm
の球状に成形し、1000〜1200゜Cで焼成したもので、表
面に空隙の多い素焼きの混合触媒である。なお、接触分
解室17は、径300mmで高さ1500mmであり、その温度を
バーナー16によって約400゜Cに保っている。
On the other hand, the hydrochloric acid gas generated by the decomposition of sodium chloride is introduced into the secondary combustion chamber 14 together with the gas generated in the combustion furnace 6, and carbon is burned by the air feeding fan 15 and the heavy oil burner 16 to become carbon dioxide gas. .. In the secondary combustion chamber 14, a catalytic cracking chamber 17 having an inner surface lined with refractory bricks is continuously provided, and a dechlorination catalyst 18 is filled inside. The dechlorination catalyst 18 is
Approximately 25 mm by mixing equal amounts of iron oxide powder and crushed zeolite
This is a bismuth-mixed catalyst that has a large number of voids on the surface and is formed into a spherical shape and baked at 1000 to 1200 ° C. The catalytic decomposition chamber 17 has a diameter of 300 mm and a height of 1500 mm, and its temperature is kept at about 400 ° C. by the burner 16.

【0014】塩酸ガスは脱塩素触媒18の接触通過によ
り分解して塩素がイオン交換によって触媒18に固定さ
れる。したがって、接触分解室17からの排気ガスは無
煙無公害となるのである。このため、大量の空気にて混
合冷却し大気中に放散してもよいが、本例では、排気ガ
スをウオータージェットスクラバー19にて減圧状態と
した水タンク20に吸引し、循環ポンプ21で循環して
いる水で水洗して放出筒22から大気中に放散するので
ある。
Hydrochloric acid gas is decomposed by passing through the dechlorination catalyst 18, and chlorine is fixed to the catalyst 18 by ion exchange. Therefore, the exhaust gas from the catalytic cracking chamber 17 becomes smokeless and pollution-free. For this reason, a large amount of air may be mixed and cooled and diffused into the atmosphere, but in this example, the exhaust gas is sucked into the water tank 20 whose pressure has been reduced by the water jet scrubber 19 and circulated by the circulation pump 21. It is washed with water and then diffused from the discharge cylinder 22 into the atmosphere.

【0015】なお、熱風乾燥機2からの排気ガスの集塵
機7及び接触分解室17からの排気ガスの集塵機23で
採取された塵体は送りコンベア12に集められ、バンカ
ー13を介して搬出されるのである。
The dust collected by the exhaust gas dust collector 7 from the hot air dryer 2 and the exhaust gas dust collector 23 from the catalytic cracking chamber 17 is collected on the feed conveyor 12 and carried out through the bunker 13. Of.

【0016】ダスト等の含有物質の計量結果を表1に、
ダスト濃度測定結果を表2に、接触分解室17からの排
出ガスの組成量の結果を表3に示す。これらから、いず
れも正常な結果が得られたのである。
Table 1 shows the measurement results of the contained substances such as dust.
The results of dust concentration measurement are shown in Table 2, and the results of the composition amount of the exhaust gas from the catalytic cracking chamber 17 are shown in Table 3. From these, normal results were obtained.

【0017】[0017]

【表1】 [Table 1]

【0018】[0018]

【表2】 [Table 2]

【0019】[0019]

【表3】 [Table 3]

【0020】このように本例方法によると、澱粉を含ん
で湿潤状態の麺類が、熱風乾燥によって焼却に適する状
態に乾燥され、乾燥によって細切れ状となって有効に焼
却されるのである。そして、含有する食塩の燃焼によっ
て生じる塩素ガスは脱塩素触媒18によって塩素を除か
れ、カーボンも二次燃焼で炭酸ガスとなるのである。
As described above, according to the method of this example, the noodles in a wet state containing starch are dried by hot air drying to a state suitable for incineration, and the dried noodles are shredded to be effectively incinerated. Then, chlorine gas generated by combustion of the contained salt is dechlorinated by the dechlorination catalyst 18, and carbon also becomes carbon dioxide gas by secondary combustion.

【0021】本例方法は上記のように構成したが、本発
明方法においてはこれに限定されない。例えば、含塩廃
棄食品はうどん類、ラーメン類等の他、スパゲッティや
マカロニ等の麺類の他、小麦粉を主原料とするクレープ
やお好み焼等が最適であるが、含塩分の多い漬物等の各
種廃棄食品を焼却できるのである。
Although the method of the present example is configured as described above, the method of the present invention is not limited to this. For example, salt-containing waste foods include udon noodles, ramen noodles, noodles such as spaghetti and macaroni, and crepes and okonomiyaki that use wheat flour as the main raw material are most suitable, but salt-containing pickles, etc. It is possible to incinerate various waste foods.

【0022】また、熱風乾燥工程において、廃棄食品を
予め細切れにしてもよい。さらに、脱塩素触媒の混合割
合も限定されないが、ゼオライト50容積%に対して銅
及び/或いは鉄を単体、混合共50容積%とするのが適
当である。
In the hot air drying step, the waste food may be cut into pieces beforehand. Further, although the mixing ratio of the dechlorination catalyst is not limited, it is appropriate to use 50% by volume of zeolite and 50% by volume of copper and / or iron alone as a simple substance.

【0023】[0023]

【発明の効果】本発明によると、含塩廃棄食品の澱粉質
が熱風乾燥によって粘着性を解かれるためその焼却が容
易となると共に、含有する食塩の燃焼によって生じる塩
素ガスは脱塩素触媒によって塩素を除かれ、カーボンも
二次燃焼で炭酸ガスとなって無公害排気ガスとなるので
ある。請求項2では、含塩廃棄食品の燃焼及び触媒によ
る脱塩素効果が良好となり、請求項3では、排気ガスを
一層無公害化できるのである。
EFFECTS OF THE INVENTION According to the present invention, since the starch content of salt-containing waste foods is decompressed by hot air drying, it is easy to incinerate the same, and chlorine gas generated by the burning of the contained salt is chlorinated by a dechlorination catalyst. After that, carbon also becomes carbon dioxide gas in the secondary combustion and becomes pollution-free exhaust gas. According to the second aspect, the combustion effect of the salt-containing waste food and the dechlorination effect by the catalyst are improved, and in the third aspect, the exhaust gas can be made more pollution-free.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明方法を説明する焼却システムの概略図で
ある。
FIG. 1 is a schematic diagram of an incineration system illustrating the method of the present invention.

【符号の説明】[Explanation of symbols]

1 ストックフィダー 2 熱風乾燥機 3 熱風発生炉 4 コンベア 6 一次燃焼炉 7,23 集塵機 9 燃焼用空気ファン 10,16 重油バーナー 11 冷却コンベア 14 二次燃焼室 17 接触分解室 18 脱塩素触媒 19 ウオータージェットスクラバー 20 水タンク 22 放出筒 1 stock feeder 2 hot air dryer 3 hot air generating furnace 4 conveyor 6 primary combustion furnace 7,23 dust collector 9 combustion air fan 10,16 heavy oil burner 11 cooling conveyor 14 secondary combustion chamber 17 catalytic cracking chamber 18 dechlorination catalyst 19 water jet Scrubber 20 Water tank 22 Discharge cylinder

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 含塩廃棄食品を熱風で乾燥し、その乾燥
された廃棄食品を、その熱風排気ガスの一部が送られる
一次燃焼炉で燃焼してその焼却灰を取り出し、一次燃焼
の塩素ガス及びカーボンを含んだ排ガスを二次燃焼して
カーボンを炭酸ガスとすると共に、銅及び/或いは鉄
を、ゼオライトに混合させて素焼きして成る脱塩素触媒
に通過させることで塩素を固定除去して排気することを
特徴とする含塩廃棄食品の焼却方法。
1. A salt-containing waste food is dried with hot air, the dried waste food is burned in a primary combustion furnace to which a part of the hot air exhaust gas is sent, and the incinerated ash is taken out. Secondary combustion of exhaust gas containing gas and carbon turns carbon into carbon dioxide, and copper and / or iron is mixed with zeolite and passed through a dechlorination catalyst that is calcinated to fix and remove chlorine. A method for incinerating salt-containing waste food, characterized by exhausting air.
【請求項2】 一次燃焼炉の温度を700〜900゜Cに保持
し、脱塩素触媒の設置部を300〜500゜Cに保持した請求
項1の焼却方法。
2. The incineration method according to claim 1, wherein the temperature of the primary combustion furnace is maintained at 700 to 900 ° C., and the installation portion of the dechlorination catalyst is maintained at 300 to 500 ° C.
【請求項3】 脱塩素触媒を通過した二次燃焼排気ガス
を、上水にて水洗した後、大気中に放散する請求項1又
は請求項2の焼却方法。
3. The incineration method according to claim 1, wherein the secondary combustion exhaust gas that has passed through the dechlorination catalyst is washed with clean water and then diffused into the atmosphere.
JP4163564A 1992-05-29 1992-05-29 Method of igniting waste food containing salt Pending JPH05332522A (en)

Priority Applications (1)

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JP4163564A JPH05332522A (en) 1992-05-29 1992-05-29 Method of igniting waste food containing salt

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Application Number Priority Date Filing Date Title
JP4163564A JPH05332522A (en) 1992-05-29 1992-05-29 Method of igniting waste food containing salt

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JPH05332522A true JPH05332522A (en) 1993-12-14

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JP4163564A Pending JPH05332522A (en) 1992-05-29 1992-05-29 Method of igniting waste food containing salt

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS527370A (en) * 1975-07-01 1977-01-20 Asahi Glass Co Ltd Process for decomposing organic compounds containing halogens
JPS52146769A (en) * 1976-06-01 1977-12-06 Jgc Corp Treatment of exhaust gas containing chlorine compounds
JPH0335578A (en) * 1989-06-30 1991-02-15 Mitsubishi Electric Corp Laser device
JPH03236508A (en) * 1990-02-10 1991-10-22 Koyo Eng:Kk Waste incinerator

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS527370A (en) * 1975-07-01 1977-01-20 Asahi Glass Co Ltd Process for decomposing organic compounds containing halogens
JPS52146769A (en) * 1976-06-01 1977-12-06 Jgc Corp Treatment of exhaust gas containing chlorine compounds
JPH0335578A (en) * 1989-06-30 1991-02-15 Mitsubishi Electric Corp Laser device
JPH03236508A (en) * 1990-02-10 1991-10-22 Koyo Eng:Kk Waste incinerator

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