JP3127212B1 - Deodorizing and harmful gas decomposing equipment for food and beverage waste processing equipment - Google Patents

Deodorizing and harmful gas decomposing equipment for food and beverage waste processing equipment

Info

Publication number
JP3127212B1
JP3127212B1 JP11245118A JP24511899A JP3127212B1 JP 3127212 B1 JP3127212 B1 JP 3127212B1 JP 11245118 A JP11245118 A JP 11245118A JP 24511899 A JP24511899 A JP 24511899A JP 3127212 B1 JP3127212 B1 JP 3127212B1
Authority
JP
Japan
Prior art keywords
reactor
exhaust gas
food
gas
deodorizing
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.)
Expired - Fee Related
Application number
JP11245118A
Other languages
Japanese (ja)
Other versions
JP2001041433A (en
Inventor
ション ヨン ヤン
Original Assignee
ション ヨン ヤン
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 ション ヨン ヤン filed Critical ション ヨン ヤン
Application granted granted Critical
Publication of JP3127212B1 publication Critical patent/JP3127212B1/en
Publication of JP2001041433A publication Critical patent/JP2001041433A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/01Deodorant compositions
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/02Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/04Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour circulating over or surrounding the materials or objects to be dried
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2200/00Drying processes and machines for solid materials characterised by the specific requirements of the drying good
    • F26B2200/04Garbage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Animal Behavior & Ethology (AREA)
  • Epidemiology (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Microbiology (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Processing Of Solid Wastes (AREA)
  • Chimneys And Flues (AREA)
  • Incineration Of Waste (AREA)

Abstract

【要約】 【課題】排気ガス中の有害成分及び悪臭を除去すると共
に脱臭効率を向上させる。 【解決手段】飲食物のゴミを、微生物が生殖される菌床
(C)と一緒に高温で発酵・消滅されるように撹拌羽根
(21)が処理槽(20)に設置され、この処理槽(2
0)の上部一側に本体(10)の外部へ連通させる排気
口(23)を形成して、飲食物のゴミの発酵・消滅過程
で発生される排気ガス中の有害成分及び悪臭を多数の段
階を経て除去する脱臭装置(30)が設置されたものに
おいて、脱臭装置(30)は、排気ガス中の有毒ガスを
高温の直熱で燃焼させて分解する熱反応機(40)と、
上記の熱反応過程を通過した湿ガスを除去する水分反応
機(50)と、上記の2段階の反応過程を経た排気ガス
中の悪臭成分を除去するように2段の触媒材を備えた低
温反応機(60)を含む構成。
An object of the present invention is to remove harmful components and odor in exhaust gas and improve deodorizing efficiency. A stirring blade (21) is provided in a processing tank (20) so that food waste can be fermented and extinguished at a high temperature together with a bacterial bed (C) in which microorganisms are reproduced. (2
An exhaust port (23) communicating with the outside of the main body (10) is formed at one side of the upper part of (0), so that a number of harmful components and odors in the exhaust gas generated during the fermentation / extinction process of food waste are removed. A deodorizer (30) for removing through a step, the deodorizer (30) includes a thermal reactor (40) that decomposes by burning toxic gas in exhaust gas by high-temperature direct heat,
A moisture reactor (50) for removing the wet gas that has passed through the thermal reaction process, and a low-temperature reactor having a two-stage catalyst material for removing malodorous components in the exhaust gas that has undergone the two-stage reaction process. A configuration including a reactor (60).

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、飲食物のゴミ処理
機の脱臭及び有害ガス分解装置、さらに詳しくは多量の
毒性と水分が含まれた飲食物のゴミを、微生物が培養さ
れる鋸屑と一緒に最適温度の処理槽内において撹拌させ
ながら発酵・消滅させる時、湿蒸気を含む排気ガスを多
数の段階の反応装置を経るようにすることによって、排
気ガス中の有毒成分及び悪臭を除去すると共に脱臭効率
を向上させることができるようにした脱臭及び有害ガス
分解装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deodorizing and harmful gas decomposing device for a food waste treatment machine, and more particularly, to a food waste containing a large amount of toxicity and water, and a sawdust on which microorganisms are cultured. When the fermentation and extinction are performed together with stirring in the processing bath at the optimum temperature, the exhaust gas containing the wet steam is passed through a multi-stage reactor to remove toxic components and odors in the exhaust gas. The present invention also relates to a deodorizing and harmful gas decomposing apparatus capable of improving the deodorizing efficiency.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】一般
に、食生活によって派生される飲食物のゴミは、減量化
の状態で埋め立てするか、又は飼料及び肥料等に再活用
する方法が普遍化されているが、埋め立ての場合には2
次的な環境汚染を誘発するようになったし、再活用の場
合にはその処理過程に多くの経済的負担を加重させる一
方、廃棄飲食物を主原料とする飼料は、その衛生的な側
面ではその有害性検証されていないので、動物の飼育時
には集団死の危険負担が常に存在する問題点があった。
2. Description of the Related Art In general, methods of reclaiming food and drink garbage derived from eating habits in a reduced state or reusing them as feed and fertilizer have been universalized. But 2 in case of landfill
In the case of re-use, this process adds to the economical burden of the process. However, since its toxicity has not been verified, there is a problem that there is always a risk of collective death when breeding animals.

【0003】近年に微生物を利用して飲食物のゴミを堆
肥化した後、肥料として土へ還元する、いわゆるリサイ
クルの方法も登場したが、この場合、都市地域では堆肥
を迅速に処理することができなくなって、また他の形態
のゴミを量産する結果を招来するようになったし、堆肥
化による微生物が好気性菌に局限されることによって、
ゴミの分解時間が遅延されたことは勿論、難分解性の物
質が残留される等、完全な分解が不可能であるという問
題点があった。
[0003] In recent years, a so-called recycling method has been introduced in which food waste is composted using microorganisms and then returned to the soil as fertilizer. In this case, in urban areas, compost can be rapidly processed. And the mass production of other forms of garbage, and by limiting composting to aerobic bacteria,
There has been a problem that complete decomposition is impossible, for example, a substance that is hardly decomposable remains, as well as a delay in decomposing the trash.

【0004】特に、飲食物のゴミを微生物が培養される
菌床と一緒に高温で撹拌させて消滅処理するようになっ
ている従来の処理は、処理過程で発生される高い湿度を
持った排気ガスを直燃法または既存の触媒法等によって
脱臭することによって、その脱臭工程において排気ガス
中の悪臭成分及び有毒成分が完全に除去されないまま大
気中へ放出され、大気汚染を加重させることは勿論、脱
臭効率が低調であるという問題点があった。
[0004] In particular, in the conventional treatment in which food waste is agitated at a high temperature together with a microbial bed on which microorganisms are cultured to extinguish the waste, a high humidity exhaust gas generated in the treatment process is used. By deodorizing the gas by the direct combustion method or the existing catalyst method, etc., in the deodorizing process, the odorous and toxic components in the exhaust gas are released to the atmosphere without being completely removed, and of course, the air pollution is increased. However, there is a problem that the deodorizing efficiency is low.

【0005】なお、上記の従来の設備は、撹拌処理槽か
ら発生された排気ガスを強制循環させるための循環装置
が上記の撹拌処理槽の内部に設置されることによって、
排気ガス中に含まれた高い湿蒸気が循環装置の回転ファ
ンの駆動部を脆弱にしながら頻繁な補修保持を誘発した
し、また排気ガスを熱分解させる燃焼脱臭装置が高温を
保持するためには電気ヒータの動作に多くの電力が消耗
される欠点もあった。
[0005] The above-mentioned conventional equipment has a circulating device for forcibly circulating the exhaust gas generated from the agitation processing tank, which is installed inside the agitation processing tank.
In order for the high humidity vapor contained in the exhaust gas to cause frequent repair and maintenance while weakening the drive of the rotating fan of the circulation device, and for the combustion deodorization device that thermally decomposes the exhaust gas to maintain high temperature There is also a disadvantage that much electric power is consumed in the operation of the electric heater.

【0006】本発明は、上記のような従来の排気ガス脱
臭装置の問題点を勘案して案出したもので、その目的
は、飲食物のゴミを撹拌処理槽において発酵・消滅させ
る時に、発生される排気湿ガスを、多数の段階の反応槽
を通過させて脱臭効率を向上させることができる飲食物
のゴミ処理機の脱臭及び有害ガス分解装置を提供するも
のである。
The present invention has been devised in consideration of the above-mentioned problems of the conventional exhaust gas deodorizing apparatus, and has as its object to produce food and drink debris when fermenting and extinguishing them in a stirring tank. It is an object of the present invention to provide a deodorizing and harmful gas decomposing apparatus for a food and drink garbage disposer capable of improving the deodorizing efficiency by passing exhausted wet gas through a multi-stage reaction tank.

【0007】なお、本発明の他の目的は、脱臭装置の稼
働に伴う運転費用を節減するとともに、機器の使用寿命
を延長することができる飲食物のゴミ処理機の脱臭及び
有害ガス分解装置を提供するのにある。
[0007] Another object of the present invention is to provide a deodorizing and harmful gas decomposing apparatus for a food and drink garbage disposer capable of reducing the operating cost associated with the operation of the deodorizing apparatus and extending the service life of the equipment. To provide.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
に、本発明は、本体(10)の内部にドア(11)を通
じて投入された飲食物のゴミを、微生物が生殖される菌
床(C)と一緒に高温で発酵・消滅されるようにモータ
(22)によって駆動される撹拌羽根(21)が処理槽
(20)に設置され、この処理槽(20)の上部一側に
本体(10)の外部へ連通させる排気口(23)を形成
して、飲食物のゴミの発酵・消滅過程で発生される排気
ガス中の有害成分及び悪臭を多数の段階を経て除去する
脱臭装置(30)が設置されたものにおいて、上記の脱
臭装置(30)は、排気ガス中の有毒ガスを高温の直熱
で燃焼させて分解する熱反応機(40)と、上記の熱反
応過程を通過した湿ガスを除去する水分反応機(50)
と、上記の2段階の反応過程を経た排気ガス中の悪臭成
分を除去するように2段の触媒材を備えた低温反応機
(60)とを備え、上記の熱反応機(40)は、沸石、
黄土、白土及びセラミック等が適正比率で混合されて反
射熱の効率と高熱に耐えるようにルツボの形態で製作さ
れ、そのルツボの側壁には電気ヒータ(41)が埋蔵設
置され、熱反応機(40)の内部空間には燃焼効率が向
上されるようにする加熱部材(42)は介入されている
ことを特徴とする。
In order to achieve the above object, the present invention provides a door (11) inside a body (10).
The food and drink garbage thrown in
Motor to be fermented and extinguished at high temperature with floor (C)
The stirring blade (21) driven by (22) is a processing tank.
(20), on one side of the upper part of this processing tank (20).
Forming an exhaust port (23) communicating with the outside of the main body (10)
Emissions generated during the fermentation and extinction of food and beverage garbage
Removes harmful components and odors in gas through multiple steps
In the case where the deodorizing device (30) is installed,
The odor device (30) converts toxic gas in exhaust gas to high-temperature direct heat.
A thermal reactor (40) that burns and decomposes in the
Moisture reactor for removing wet gas that has passed through the reaction process (50)
And offensive odor in the exhaust gas after the above two-step reaction process
Low-temperature reactor equipped with two-stage catalytic material to remove
(60), wherein the thermal reactor (40) includes a zeolite,
Loess, clay and ceramics are mixed in the proper ratio and
Manufactured in crucible form to withstand heat radiation and high heat
The electric heater (41) is buried on the side wall of the crucible.
And the internal space of the thermal reactor (40) has high combustion efficiency.
The heating element (42) to be raised is interposed .

【0009】[0009]

【発明の実施の形態】以下、本発明の飲食物のゴミ処理
機の脱臭及び有害ガス分解装置の実施の形態を図面を参
照しつつ説明する。図1は、本発明の分解装置が適用さ
れる飲食物のゴミ処理機の全体構成を示す斜視図、図2
は本発明における分解装置の1実施形態を示す正面から
見た断面図、図3は図2の側面から見た断面図、図4は
図2及び図3の分解装置の拡大断面図、図5は本発明に
おける分解装置の作動状態を示す断面図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a deodorizing and harmful gas decomposing apparatus for a food waste disposal machine according to the present invention will be described below with reference to the drawings. FIG. 1 is a perspective view showing the overall configuration of a food and beverage refuse treatment machine to which the decomposition apparatus of the present invention is applied, and FIG.
FIG. 3 is a cross-sectional view from the front showing an embodiment of the disassembling apparatus of the present invention, FIG. 3 is a cross-sectional view from the side of FIG. 2, FIG. 4 is an enlarged cross-sectional view of the disassembly apparatus of FIGS. FIG. 2 is a sectional view showing an operation state of the disassembling apparatus according to the present invention.

【0010】本体10の内部にドア11を通じて投入さ
れた飲食物のゴミと、少なくとも一種類以上の微生物が
生殖される鋸屑からなった菌床Cが収容されて、高温で
発酵・消滅されるようにする処理槽20が設置され、こ
の処理槽20の内部には各種投入物が撹拌されるように
モータ22によって駆動される撹拌羽根21が設置され
ている。
Food and drink trash introduced through the door 11 and a bed C made of sawdust from which at least one kind of microorganisms are reproduced are accommodated in the body 10 and fermented and eliminated at a high temperature. A processing tank 20 is provided. Inside the processing tank 20, a stirring blade 21 driven by a motor 22 is provided so as to stir various kinds of materials.

【0011】上記の処理槽20の内周面には、その内部
の投入物に高熱を伝導させる多数の電気ヒータ(図示せ
ず)が設置され、モータ22によって処理槽20内で駆
動される撹拌羽根21は約5分ほど駆動された後、約3
0分間停止させることが、好気性菌は勿論、嫌気性菌の
分解力を高めるのに好ましいものである。
A large number of electric heaters (not shown) are provided on the inner peripheral surface of the processing tank 20 to conduct high heat to the input material therein. After the blades 21 are driven for about 5 minutes, about 3 minutes
Stopping for 0 minutes is preferable to increase the decomposing ability of anaerobic bacteria as well as aerobic bacteria.

【0012】上記の処理槽20の上部の一側に本体10
の外部に連通される排気口23が形成され、この排気口
23の排出口には飲食物のゴミの発酵・消滅過程で発生
された排気ガスの有害成分及び悪臭を多数の段階を経て
除去する脱臭装置30が設置されている。
A main body 10 is provided on one side of the upper part of the processing tank 20.
An exhaust port 23 is formed which communicates with the outside of the vehicle, and the exhaust port of the exhaust port 23 removes harmful components and odor of exhaust gas generated during fermentation and extinction of food waste through a number of steps. A deodorizing device 30 is provided.

【0013】脱臭装置30は、排気ガス中の有毒ガスを
高温の直熱で燃焼させて分解する熱反応機40と、熱反
応の過程を通過した湿ガスを除去する水分反応機50
と、上記の2段階の反応過程を経た排気ガス中の悪臭成
分を除去した後、熱が冷えたガスを再び2段の触媒材を
備えた低温反応機60からなっている。
The deodorizer 30 includes a thermal reactor 40 for decomposing toxic gas in exhaust gas by burning it with high-temperature direct heat, and a moisture reactor 50 for removing wet gas that has passed through the thermal reaction process.
After removing the malodorous components in the exhaust gas that has undergone the above-described two-stage reaction process, the low-temperature reactor 60 is provided with the two-stage catalyst material from the cooled gas.

【0014】上記の熱反応機40は、沸石(ゼオライ
ト)、黄土、白土及びセラミック等が適正比率で混合さ
れていて反射熱による高熱効果があり、高熱に耐えるこ
とができるようにルツボの形態に製作されているが、そ
のルツボの内部には電気ヒータ41が埋蔵設置され、熱
反応機40の内部空間には燃焼効率を向上させるように
する加熱部材42が介入されている。
The above-mentioned thermal reactor 40 is formed in a crucible form in which zeolite, ocher, terra alba, ceramic and the like are mixed in an appropriate ratio, which has a high heat effect by reflected heat and can withstand high heat. Although manufactured, an electric heater 41 is embedded and installed inside the crucible, and a heating member 42 for improving combustion efficiency is interposed in the internal space of the thermal reactor 40.

【0015】水分反応機50は、黄土等の4つ以上のセ
ラミック材からなる多数のボール51を積層になるよう
に内装した構造になって、上記の熱反応機40により1
段階の脱臭過程を経た高温の排気ガスが通過されると
き、アンモニア、メタンガス及び悪臭等の有毒ガスが含
有された湿ガスを捕集吸収させる一方、高熱(約600
℃)で吸収された湿ガスのH2O成分中の酸素は燃焼を
促進させ、水素は燃焼される相互作用によって熱反射効
果の高熱(約850℃)で有害ガス及び悪臭を燃焼させ
ながら通過される排気ガスを乾燥ガスに転換されるよう
にする。
The moisture reactor 50 has a structure in which a large number of balls 51 made of four or more ceramic materials such as loess are housed in a stacked manner.
When the high-temperature exhaust gas that has passed through the deodorizing process is passed through, the humid gas containing toxic gas such as ammonia, methane gas, and odor is collected and absorbed, while the high heat (about 600
Oxygen in the H 2 O component of the wet gas absorbed at ℃ promotes combustion, and hydrogen passes while burning harmful gas and odor with high heat of heat reflection effect (about 850 ℃) due to the combustion interaction The exhaust gas is converted to dry gas.

【0016】低温反応機60には、2種類の触媒材61
が設置されて、上記の1、2段階の脱臭過程を経た乾燥
気体が各温度別に濾過反応を経ることによって、排気ガ
ス中の悪臭を再び除去するようになる(第1段階は35
0℃以上、第2段階は350℃未満)。
The low-temperature reactor 60 has two types of catalyst materials 61.
Is installed, and the dry gas that has undergone the above-described one or two-stage deodorization process undergoes a filtration reaction at each temperature, thereby removing the bad odor in the exhaust gas again (the first stage is 35).
0 ° C or higher, the second stage is lower than 350 ° C).

【0017】上記の水分反応機50の外周面にはポンプ
70によって強制的に供給された外気を熱交換させて高
温に変換されるようにする熱交換室52を備え、この熱
交換室52の一側には高温の空気を処理槽20の内部へ
供給するホース71が連結されている。
On the outer peripheral surface of the moisture reactor 50, there is provided a heat exchange chamber 52 for exchanging heat with the outside air forcibly supplied by a pump 70 so as to be converted to a high temperature. A hose 71 for supplying high-temperature air to the inside of the processing tank 20 is connected to one side.

【0018】図5に示すように、上記の処理槽20の上
側にはその内部の空気が循環されるように、区画壁81
を基点に流入口82を通じて処理槽20から空気を吸入
した後、吐出口83を通じて冷却空気を再び処理槽20
へ流入されるようにする循環ファン80が装着され、こ
の循環ファン80を駆動させるモータ84の同一の軸上
には循環ファン80を冷却させる冷却ファン85が設置
されている。
As shown in FIG. 5, a partition wall 81 is provided above the processing tank 20 so that air inside the processing tank 20 is circulated.
After the air is sucked from the processing tank 20 through the inflow port 82 at the base point, the cooling air is again
A circulating fan 80 for allowing the circulating fan 80 to flow into the cooling fan 85 is mounted. A cooling fan 85 for cooling the circulating fan 80 is provided on the same axis of a motor 84 that drives the circulating fan 80.

【0019】一方、処理槽20に投入される微生物は、
酸素を必要としながら有機物を酸化分解させてアンモニ
アと炭酸ガス及び水を生成させる好気性菌と、酸素の有
無にかかわることなく与えられた環境に親和的に対応し
て、有機物を酸化又は嫌気的に分解させる通性嫌気性菌
と、酸素がない条件下でも迅速に分解作用をして、アル
コール又は有機酸を生成させる嫌気性菌等、三種類を混
合することが好ましい。
On the other hand, the microorganisms put into the treatment tank 20 are:
Aerobic bacteria that oxidize and decompose organic matter to produce ammonia, carbon dioxide, and water while requiring oxygen, and oxidize or anaerobic organic matter in a friendly manner to the given environment with or without oxygen. It is preferable to mix three types, such as a facultative anaerobic bacterium that decomposes into water, and an anaerobic bacterium that rapidly decomposes and generates an alcohol or an organic acid even under oxygen-free conditions.

【0020】このような他種類の微生物群は、各々の特
性が組み合わされながら相互補完的に上昇作用を起こす
ようになって、飲食物のゴミの分解力を高めることによ
って、飲食物のゴミを迅速で完全に分解および消滅させ
ることができるものである。
[0020] Such other types of microbial organisms, when combined with each other's properties, have an ascending action to complement each other, thereby increasing the decomposing ability of food and drink garbage, thereby reducing food and drink garbage. It can be rapidly decomposed and completely destroyed.

【0021】従って、飲食物のゴミの主成分となる炭水
化物、蛋白質、脂肪質等は、微生物自体から生成される
酸素によって糖質、グリセリン及びアミノ酸等、微生物
が飽食しやすい低分子物質に分解された後、微生物が飽
食することによって菌が迅速に増加されながら無機質で
ある水と炭酸ガス及びアンモニアに変化され、このよう
な物質は、微生物が増殖される菌床Cの発酵熱によって
湿気を包含した気体に蒸発及び排出されることによっ
て、消滅がなされるものである。
Therefore, carbohydrates, proteins, fats, etc., which are the main components of food and drink garbage, are decomposed into low-molecular substances, such as carbohydrates, glycerin and amino acids, which are easily satiated by microorganisms by oxygen generated from the microorganisms themselves. Then, the microorganisms are rapidly increased by being saturated by the microorganisms, and are changed into inorganic water, carbon dioxide, and ammonia while being increased, and such substances include moisture due to the fermentation heat of the bacterial bed C on which the microorganisms are grown. The gas is annihilated by being evaporated and discharged.

【0022】処理槽20に投入されて微生物菌群が培養
される菌床Cは、微生物に酸素供給を十分にすると共
に、飲食物のゴミの水分や栄養分の移動を円滑にして、
微生物の成熟に適合する環境を提供するようになるが、
理想的な菌床Cとしては、水分の保有力が高くて通気性
がよいし、耐摩耗性があって水分がよく蒸発されないよ
うにしたものがよい。
The microbial bed C, which is put into the treatment tank 20 and in which the microbial group is cultured, provides a sufficient oxygen supply to the microbes and facilitates the movement of moisture and nutrients in food and drink garbage.
It will provide an environment compatible with the maturation of microorganisms,
As an ideal microbial bed C, one having high water retention and good air permeability, and having good abrasion resistance so that water is not well evaporated is preferable.

【0023】なお、菌床Cの含水率は、飲食物のゴミの
分解速度と悪臭発生に影響を及ぼすようになり、効率的
に飲食物のゴミを処理するためには最適の含水率を保持
することが好ましい。このとき、もっとも好ましい菌床
Cの含水率は、20〜40(w/w%)であり、このよ
うな含水率を保持するために菌床Cに水を加えて水分が
調整されるようにする。
The water content of the bacterial bed C has an effect on the decomposition rate of food and drink garbage and the generation of offensive odors, and maintains an optimum water content for efficient disposal of food and drink garbage. Is preferred. At this time, the most preferable moisture content of the microbial bed C is 20 to 40 (w / w%), and water is added to the microbial bed C so as to adjust the water content in order to maintain such a water content. I do.

【0024】菌床Cの含水率が20%より低い場合に
は、飲食物のゴミから菌床Cへ水分移動が円滑で処理速
度が速いように見られるが、菌床C自体と飲食物のゴミ
が乾燥されやすい結果を招来することによって微生物の
活性が弱くなって分解が不十分となる。
When the water content of the bacterial bed C is lower than 20%, it seems that the moisture transfer from the food waste to the bacterial bed C is smooth and the treatment speed is high. The result is that the debris tends to dry, which results in weak microbial activity and poor decomposition.

【0025】もし、含水率が40%を超過する場合に
は、飲食物のゴミの水分とともに過剰状態になりながら
菌床C中に酸素供給が不十分となり、これによって好気
性菌の生殖が低下される反面、嫌気性菌が活性化されて
分解力が落ちるようになるばかりではなく、酸化水素と
メタン及び有機酸等の悪臭物質が残留されて、処理効率
が落ちるようになることを、多数の重なる実験を通じて
確認することができた。
If the water content exceeds 40%, the oxygen supply becomes insufficient in the fungal bed C while being in an excess state together with the water content of food and drink garbage, thereby reducing the reproduction of aerobic bacteria. On the other hand, it is often the case that anaerobic bacteria are activated and the decomposition power is reduced, and that the odorous substances such as hydrogen oxide and methane and organic acids remain and the treatment efficiency is reduced. Could be confirmed through overlapping experiments.

【0026】従って、本発明の処理槽20に適正含水率
を備えた菌床Cを約60w%程度投入して、これに微生
物が培養されるようにした状態で適量の飲食物のゴミを
投入してモータ22を駆動(30分停止ー4分稼働)さ
せて撹拌羽根21を回転させることによって、菌床C中
に飲食物のゴミが混合されながら各種微生物の飽食が始
まる。
Therefore, about 60 w% of the bacterial bed C having an appropriate water content is put into the treatment tank 20 of the present invention, and an appropriate amount of food and drink garbage is put in the state where the microorganisms are cultured. Then, the motor 22 is driven (stop for 30 minutes-4 hours of operation) to rotate the stirring blade 21, so that various microorganisms start to get saturated while food and drink garbage are mixed in the bacterial bed C.

【0027】上記の処理過程において、処理に要する最
適温度は、45〜55℃であり、このような温度が保持
されるようにするために処理槽20に内装された電熱ヒ
ータが作動されるようにする。
In the above process, the optimum temperature required for the process is 45 to 55 ° C. In order to maintain such a temperature, the electric heater installed in the processing tank 20 is operated. To

【0028】さらに、上記の処理作動時、水分反応機5
0の外周面に備えられた熱交換室52を経由してホース
71を通じて処理槽20の内部へ高温の空気が供給され
ると共に、処理槽20の上側に装着された循環ファン8
0が稼働し、区画壁81を基点として流入口82を通じ
て処理槽20から空気を吸入した後、吐出口83を通じ
て冷却空気を再び処理槽20へ流入させることによっ
て、菌床Cで生殖される微生物に酸素を供給して好気性
菌を増加させながら、飲食物のゴミの分解力を高めると
同時に、生成された水や炭酸ガス等の無機物の排出を促
進させる役割を遂行し、処理材の撹拌によって通気性が
良好となりながら飲食物のゴミと菌床Cに生殖される微
生物の接触をよくすると共に、嫌気性菌の分解力を高め
ることができる。
Further, at the time of the above-mentioned processing operation, the water reactor 5
A high-temperature air is supplied to the inside of the processing tank 20 via a hose 71 via a heat exchange chamber 52 provided on the outer peripheral surface of the processing tank 20, and a circulation fan 8 mounted on the upper side of the processing tank 20.
0 is operated, air is sucked from the processing tank 20 through the inlet 82 with the partition wall 81 as a base point, and then the cooling air is flown into the processing tank 20 again through the outlet 83, whereby the microorganisms reproduced in the bacterial bed C are obtained. While supplying oxygen to the air to increase aerobic bacteria, it also enhances the decomposability of food and drink garbage, and at the same time, promotes the discharge of generated inorganic substances such as water and carbon dioxide, and stirs the processing materials. This makes it possible to improve the contact between the garbage of food and drink and the microorganisms regenerated in the fungal bed C while improving the air permeability, and to enhance the decomposition power of the anaerobic bacteria.

【0029】上記のように、空気を供給及び循環させる
とき、常温の外気が熱交換によって高温に変化されたま
ま処理槽20に供給されて熱損失を最小化することがで
き、空気を循環させる循環ファン80はその駆動モータ
84の同一の軸上に設置された冷却パイプ86から入る
冷たい空気が冷却ファン85によって持続的に冷却され
て、高熱による循環ファン80の破損が防止されること
によって、使用寿命を延長することができるようにな
る。
As described above, when the air is supplied and circulated, the outside air at room temperature is supplied to the processing tank 20 while being changed to a high temperature by heat exchange so that heat loss can be minimized and the air is circulated. The circulating fan 80 is continuously cooled by the cooling fan 85 from the cooling pipe 86 installed on the same shaft of the drive motor 84, thereby preventing the circulating fan 80 from being damaged by high heat, The service life can be extended.

【0030】飲食物のゴミを長期間にわたって処理する
過程で、菌床Cの性質が変化されるとき、新しい菌床C
に交替されるが、その交替時期は約2ヶ月くらいが好ま
しいし、廃棄される菌床Cは別途の工程をい通じて付加
価値が高い活性炭(発酵助燃剤)として製作して、今ま
での方法より効果的な再活用が可能である。
In the process of treating food and drink garbage over a long period of time, when the properties of the bacterial bed C are changed, a new bacterial bed C
The replacement time is preferably about 2 months, and the bacterial bed C to be discarded is manufactured as a high value-added activated carbon (fermentation assistant) through a separate process. Reuse is more effective than the method.

【0031】一方、上記のような過程を通じて飲食物の
ゴミを処理する時に発生される排気ガスは、本体10の
外部へ連通されるように処理槽20の上部一側に形成さ
れた排気口23を通じて、排気ガス中の有毒ガスを高温
の直熱で燃焼させて分解する熱反応機40と、熱反応過
程を通過した湿ガスを除去するする水分反応機50と、
上記の2段階の反応過程を経た排気ガス中の悪臭成分を
除去するように、少なくとも一つ以上の触媒材を備えた
低温反応機60からなった脱臭装置30を経るようにな
る。
On the other hand, the exhaust gas generated when the food waste is processed through the above-described process is discharged through an exhaust port 23 formed at one upper portion of the processing tank 20 so as to communicate with the outside of the main body 10. Through a thermal reactor 40 that burns and decomposes the toxic gas in the exhaust gas with high-temperature direct heat, a moisture reactor 50 that removes the wet gas that has passed through the thermal reaction process,
In order to remove the malodorous components in the exhaust gas after the two-step reaction process, the exhaust gas passes through a deodorizer 30 including a low-temperature reactor 60 having at least one catalyst material.

【0032】従って、沸石、黄土、白土及びセラミック
等を適正比率に混合して、高熱に耐えることができるよ
うにルツボの形態に製作し、そのルツボの側壁に電気ヒ
ータ41が埋設された熱反応機40と内部空間に介入さ
れた加熱部材42によって排気ガスが燃焼されて悪臭成
分が除去され、次いでセラミック材からなった多数のボ
ール51を積層されるように内装した水分反応機50を
上記の熱反応機40によって1段階の脱臭過程を経た排
気ガスが通過される過程で、アンモニア、メタンガス、
及び悪臭等の有毒ガスが含有された湿ガスを捕集吸収さ
せる一方、湿ガスのH2O成分中の酸素(O)は燃焼を
促進させる作用をしながら通過される排気ガスを乾燥ガ
スに転換されるようにする。
Therefore, a mixture of zeolite, loess, clay, ceramic and the like in an appropriate ratio is manufactured in the form of a crucible so as to withstand high heat, and a thermal reaction in which an electric heater 41 is embedded in the side wall of the crucible. The exhaust gas is combusted by the heating device 42 and the heating member 42 interposed in the internal space to remove malodorous components, and then the moisture reactor 50 having the above-described interior provided with a large number of balls 51 made of a ceramic material is laminated. In the process in which the exhaust gas that has undergone the one-stage deodorization process is passed by the thermal reactor 40, ammonia, methane gas,
Oxygen (O) in the H 2 O component of the wet gas, while collecting and absorbing the humid gas containing toxic gas such as odorous gas and odor, converts the passed exhaust gas into a dry gas while acting to promote combustion. To be converted.

【0033】また、上記の1,2段階の脱臭過程を経た
乾燥した気体ガスが、2段に構成された触媒材61を備
えた低温反応機60によって濾過反応を経ることによっ
て、排気ガス中の悪臭を再び除去するようになる。
The dried gaseous gas that has undergone the above-described one- or two-stage deodorization process is subjected to a filtration reaction by a low-temperature reactor 60 having a two-stage catalyst material 61, whereby the exhaust gas in the exhaust gas is removed. The odor is removed again.

【0034】[0034]

【発明の効果】以上の説明から明らかなように、本発明
によれば、人体に無害な微生物製剤を適正含水率が備え
られた菌床で成熟させて、これに飲食物のゴミを投入す
るが、最適の温度と適量の酸素を保持した状態下で撹拌
させることによって、飲食物のゴミを完全に分解および
消滅させるようになり、この過程で発生される排気ガス
中の有毒成分及び悪臭成分を多数の段階の脱臭装置を通
じて完全に除去して環境汚染を防止することができる効
果があって、都心の屋内のどこでも安全に使用すること
ができる。
As is apparent from the above description, according to the present invention, a microorganism preparation which is harmless to the human body is matured on a fungal bed provided with an appropriate moisture content, and food and drink garbage is poured into the maturation. However, by stirring under the condition that the optimal temperature and the appropriate amount of oxygen are held, the food waste can be completely decomposed and eliminated, and the toxic and odorous components in the exhaust gas generated in this process Can be completely removed through a multi-stage deodorizer to prevent environmental pollution, and can be used safely anywhere in the city center.

【0035】また、飲食物のゴミの消滅処理後に発生さ
れる残存物を活性炭(発酵助燃材)等に再活用して、付
加価値を向上させる一方、脱臭装置の運転費用を従来の
どんな方法に比べても50%以上を節減して、経済性を
向上させることができる。
In addition, the residue generated after the garbage of food and drink is eliminated is reused as activated carbon (fermentation aid) to improve added value, while reducing the operating cost of the deodorizing device by any conventional method. Compared with this, it is possible to save 50% or more and improve the economic efficiency.

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

【図1】本発明の分解装置が適用される飲食物のゴミ処
理機の全体構成を示す斜視図である。
FIG. 1 is a perspective view showing the overall configuration of a food and beverage refuse treatment machine to which a decomposition apparatus of the present invention is applied.

【図2】本発明における分解装置の1実施形態を示す正
面から見た断面図である。
FIG. 2 is a front sectional view showing one embodiment of the disassembling apparatus of the present invention.

【図3】図2の側面から見た断面図である。FIG. 3 is a cross-sectional view as viewed from a side surface of FIG. 2;

【図4】図2及び図3の分解装置の拡大断面図である。FIG. 4 is an enlarged sectional view of the disassembly device of FIGS. 2 and 3;

【図5】本発明における分解装置の作動状態を示す断面
図である。
FIG. 5 is a sectional view showing an operation state of the disassembling apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

20…処理槽 21…撹拌羽根 22、84…モータ 23…排気口 30…脱臭装置 40…熱反応機 41…電気ヒータ 42…加熱部材 50…水分反応機 51…ボール 52…熱交換室 60…低温反応機 61…触媒材 70…ポンプ 71…ホース 80…循環ファン 85…冷却ファン Reference Signs List 20 processing tank 21 stirring blades 22, 84 motor 23 exhaust port 30 deodorizer 40 thermal reactor 41 electric heater 42 heating member 50 moisture reactor 51 ball 52 heat exchange chamber 60 low temperature Reactor 61 ... Catalyst material 70 ... Pump 71 ... Hose 80 ... Circulation fan 85 ... Cooling fan

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F23G 7/06 B09B 3/00 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) F23G 7/06 B09B 3/00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】本体(10)の内部にドア(11)を通じ
て投入された飲食物のゴミを、微生物が生殖される菌床
(C)と一緒に高温で発酵・消滅されるようにモータ
(22)によって駆動される撹拌羽根(21)が処理槽
(20)に設置され、この処理槽(20)の上部一側に
本体(10)の外部へ連通させる排気口(23)を形成
して、飲食物のゴミの発酵・消滅過程で発生される排気
ガス中の有害成分及び悪臭を多数の段階を経て除去する
脱臭装置(30)が設置されたものにおいて、 上記の脱臭装置(30)は、排気ガス中の有毒ガスを高
温の直熱で燃焼させて分解する熱反応機(40)と、上
記の熱反応過程を通過した湿ガスを除去する水分反応機
(50)と、上記の2段階の反応過程を経た排気ガス中
の悪臭成分を除去するように2段の触媒材を備えた低温
反応機(60)とを備え、 上記の熱反応機(40)は、沸石、黄土、白土及びセラ
ミック等が適正比率で混合されて反射熱の効率と高熱に
耐えるようにルツボの形態で製作され、そのルツボの側
壁には電気ヒータ(41)が埋蔵設置され、熱反応機
(40)の内部空間には燃焼効率が向上されるようにす
る加熱部材(42)は介入されている ことを特徴とする
飲食物のゴミ処理機の脱臭及び有毒ガス分解装置。
A motor (1) is provided so that food waste introduced into the body (10) through a door (11) is fermented and eliminated at a high temperature together with a bacterial bed (C) in which microorganisms are reproduced. A stirring blade (21) driven by 22) is installed in the processing tank (20), and an exhaust port (23) for communicating with the outside of the main body (10) is formed at one upper side of the processing tank (20). A deodorizing device (30) for removing harmful components and bad odors in exhaust gas generated in the process of fermenting and extinguishing food and drink garbage through a number of steps, wherein the deodorizing device (30) is A thermal reactor (40) for combusting and decomposing toxic gas in exhaust gas by high-temperature direct heat, a moisture reactor (50) for removing wet gas passing through the thermal reaction process, To remove odorous components in exhaust gas that has undergone a three-step reaction process A low-temperature reactor (60) provided with a two-stage catalyst material , wherein the thermal reactor (40) comprises a zeolite, a loess, a clay and a clay.
Mic, etc. are mixed at an appropriate ratio to increase the efficiency of reflected heat and high heat
Made in the form of a crucible to withstand, the side of the crucible
An electric heater (41) is embedded and installed on the wall,
The internal space of (40) is designed to improve combustion efficiency.
A deodorizing and toxic gas decomposing device for a food and drink garbage disposal machine, wherein the heating member (42) is interposed .
JP11245118A 1999-07-28 1999-08-31 Deodorizing and harmful gas decomposing equipment for food and beverage waste processing equipment Expired - Fee Related JP3127212B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR30933/1999 1999-07-28
KR1019990030933A KR100302405B1 (en) 1999-07-28 1999-07-28 Deodorization and Noxiousness Resolution Apparatus for Garbage Treatment Apparatus

Publications (2)

Publication Number Publication Date
JP3127212B1 true JP3127212B1 (en) 2001-01-22
JP2001041433A JP2001041433A (en) 2001-02-13

Family

ID=19605486

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11245118A Expired - Fee Related JP3127212B1 (en) 1999-07-28 1999-08-31 Deodorizing and harmful gas decomposing equipment for food and beverage waste processing equipment

Country Status (2)

Country Link
JP (1) JP3127212B1 (en)
KR (1) KR100302405B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113639271A (en) * 2021-08-11 2021-11-12 上海泰欣环境工程有限公司 Ultra-clean emission treatment process for flue gas of waste incineration power plant

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5036938B2 (en) * 2001-07-12 2012-09-26 前澤工業株式会社 Organic waste combined treatment apparatus including combination of biogas production apparatus and biodiesel production apparatus, and organic waste treatment method using the same
KR20030061917A (en) * 2002-01-12 2003-07-23 고천일 Decomposition device of organic waste
KR20030079347A (en) * 2002-04-03 2003-10-10 주식회사 엔터프라이즈재성 a treatment method of food garbage
KR20030086085A (en) * 2002-05-03 2003-11-07 린나이코리아 주식회사 Deodorization Apparatus Of Nourishment Processor
KR20040046884A (en) * 2002-11-28 2004-06-05 고석인 Treatment apparatus for organic waste and method thereof
KR100706919B1 (en) * 2006-02-15 2007-04-12 주식회사 루펜리 Garbage dryer
KR100870519B1 (en) 2007-06-05 2008-11-26 주식회사 유성엔지니어링 A dry desulfurization machine
KR200448257Y1 (en) * 2008-02-25 2010-03-29 이비테크(주) Apparatus for sterilizing sludge using the electron beam
KR102463865B1 (en) * 2020-08-13 2022-11-04 정도테크주식회사 deodorizing apparatus for food waste treatment

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09239347A (en) * 1996-03-11 1997-09-16 Taniguchi Kogyo Kk Garbage processing device
JPH09239348A (en) * 1996-03-11 1997-09-16 Taniguchi Kogyo Kk Garbage processing device
KR970006246A (en) * 1996-11-18 1997-02-19 정재덕 Food Waste Fermenter
KR200158821Y1 (en) * 1997-03-28 1999-10-15 이창호 Disposer for refuse
KR19980085372A (en) * 1997-05-28 1998-12-05 강원석 Deodorizer of food waste processor
KR19990025758A (en) * 1997-09-13 1999-04-06 양성용 Food Waste Disposal System
KR100260505B1 (en) * 1998-03-25 2000-07-01 정재덕 A fermentation/dry apparatus of waste foods

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113639271A (en) * 2021-08-11 2021-11-12 上海泰欣环境工程有限公司 Ultra-clean emission treatment process for flue gas of waste incineration power plant

Also Published As

Publication number Publication date
KR20010011531A (en) 2001-02-15
JP2001041433A (en) 2001-02-13
KR100302405B1 (en) 2001-09-22

Similar Documents

Publication Publication Date Title
JP3127212B1 (en) Deodorizing and harmful gas decomposing equipment for food and beverage waste processing equipment
GB2348876A (en) Disposal of organic waste by bacterial decomposition
JP3657841B2 (en) Deodorization equipment in organic waste treatment equipment
KR200174353Y1 (en) Garbage disposer
CN1331783C (en) Extinction type biological treatment machine for organic garbage
KR19990039464A (en) Food waste extinction processing device using microorganisms
JP2004113911A (en) Disposal method for organic waste and treatment apparatus
KR200166139Y1 (en) Deodorization and noxiousness resolution apparatus for garbage treatment apparatus
JP2004262729A (en) Processing method and its processing system of wetting organic waste
JPH06285486A (en) Sewage treatment system
JPH07100459A (en) Polluted soil purifying method
KR20010076581A (en) Device to manage food and drink wastes with cancellation type for domestic economy
KR19990025758A (en) Food Waste Disposal System
JPH1043731A (en) Inorganic/organic waste mixture treating device
KR0159355B1 (en) Device and method for treating garbage
KR102579255B1 (en) Treatment method of organic waste using carrier
JPH08132007A (en) Disposal method of garbage
KR200372086Y1 (en) High Speed Extinction Machine for Food Waste Equipped on the Vehicle
KR101262928B1 (en) Fermentation of organic waste, using environmentally friendly construction methods and using the same processing device
KR200293326Y1 (en) Pollution prevention device of garbage fermenter
KR101207979B1 (en) Hazardous substance exclusion apparatus of garbage fermenter
KR200289676Y1 (en) Waste food decomposer with shredder and deodorize machine
JP3192408B2 (en) Garbage processing equipment
JP2000197898A (en) Method for treating sludge and the like
JP2006026491A (en) Garbage disposer

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees