JP2005211763A - Deodorizing device of garbage treatment machine and deodorizing method using the same - Google Patents

Deodorizing device of garbage treatment machine and deodorizing method using the same Download PDF

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JP2005211763A
JP2005211763A JP2004020196A JP2004020196A JP2005211763A JP 2005211763 A JP2005211763 A JP 2005211763A JP 2004020196 A JP2004020196 A JP 2004020196A JP 2004020196 A JP2004020196 A JP 2004020196A JP 2005211763 A JP2005211763 A JP 2005211763A
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deodorizing
gas
garbage
plasma
plasma decomposition
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Yuji Hayashi
佑二 林
Takeshi Matsumoto
松本猛史
Ichiji Kotari
小足一司
Katsuya Tokumura
徳村勝也
Akira Maruyama
昭 丸山
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E-NIIT CO
I M PACT WORLD KK
I Mpact World
I'M PACT WORLD KK
NIIT CO E
Yutaka Electric Co Ltd
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E-NIIT CO
I M PACT WORLD KK
I Mpact World
I'M PACT WORLD KK
NIIT CO E
Yutaka Electric Co Ltd
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    • 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
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Abstract

<P>PROBLEM TO BE SOLVED: To provide a malodor removing method capable of deodorizing, decomposing and detoxifying a complicated mixed gas at the same time in the deodorizing means of a garbage treatment machine due to plasma decomposition, and a deodorizing device therefor. <P>SOLUTION: The deodorizing device of the garbage treatment machine is constituted so that an adsorbing member for moisture, hydrogen sulfide, ammonia, and the like, is arranged to the front stage of a plasma decomposition device to suppress the occurrence of a reaction byproduct at the time of plasma decomposition and a plurality of kinds of harmful chemical substances are simultaneously and properly deodorized and detoxified using a catalytic metal as the electrode of a plasma decomposition device. An adsorbing member such as activated carbon is arranged to the rear stage of the plasma decomposition device to treat a byproduct such as ozone or sulfur discharged from the plasma decomposition device. Further, moisture, hydrogen sulfide and ammonia are subjected to time lag desorption by heaters individually attached to the respective adsorbing members of the front stage to efficiently treat not only an organic gas but also hydrogen sulfide or ammonia while avoiding an increase in humidity at the time of plasma decomposition. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、生ごみ処理機の臭気除去のための装置及びその方法に係り、特に厨房における生ごみ処理機から発生する高温多湿の悪臭成分を分解脱臭し有害物質を除去することができる生ごみ処理機の脱臭装置及びその方法に関するものである。   The present invention relates to an apparatus and method for removing odors from a garbage disposal machine, and more particularly, garbage capable of decomposing and deodorizing high-temperature and high-humidity odor components generated from a garbage disposal apparatus in a kitchen to remove harmful substances. The present invention relates to a deodorizing apparatus for a processing machine and a method thereof.

生ごみ処理機では悪臭が発生するため、その臭気を脱臭除去する必要がある。従来の脱臭装置としては、微生物や化学触媒を用いたり或いはプラズマにより分解処理する装置などがある。   Since a bad odor is generated in a garbage disposal machine, it is necessary to deodorize and remove the odor. As a conventional deodorizing apparatus, there are an apparatus that uses microorganisms, chemical catalysts, or decomposes by plasma.

従来の微生物による生ごみ処理機は、生ごみをオガクズ等の水分調整材とともに発酵槽内に入れ、これらをゆっくり撹拌して十分な酸素を供給し、水分調整材に生息する微生物により生ごみを発酵分解して堆肥化するものである。しかし微生物の酸化還元処理能力は小さく、大量の悪臭を短時間に処理するには不向きである。また、微生物は供給される生ゴミを栄養源とできるものだけが増殖するが、条件が悪くなると微生物が死滅して全く消臭機能がなくなってしまう。   A conventional garbage processing machine using microorganisms puts garbage in a fermenter together with moisture adjusting materials such as sawdust, supplies them with sufficient oxygen, and removes garbage by microorganisms that live in the moisture adjusting materials. It is fermented and decomposed into compost. However, the ability of microorganisms to undergo redox treatment is small, and is unsuitable for treating a large amount of malodor in a short time. In addition, microorganisms grow only those that can use the raw garbage supplied as nutrients, but if the conditions worsen, the microorganisms die and the deodorizing function is completely lost.

化学触媒を利用する脱臭装置は、その性質上あらゆる悪臭因子の全てに対して触媒機能を発揮するというわけにはいかず、悪臭の原因物質が多岐にわたる場合には一部の悪臭が残存してしまうという欠点があった。   Deodorizers that use chemical catalysts are not capable of exerting catalytic functions for all offensive odor factors due to their properties, and some offensive odors remain if there are a wide variety of odor-causing substances. There was a drawback.

また、臭気を吸着して除去する脱臭装置では、吸着材が飽和するとその都度交換する必要があり、メンテナンス性がよくなかった。一方、臭気ガスを分解する装置では、光触媒や白金(Pt)燃焼触媒を利用するものがあるが、紫外線ランプやヒーターが必要となり装置が高価である。いずれの場合も初期段階では性能がよくても、時間が経過するにつれ触媒の劣化が進んでしまうという難点がある。また、これらの装置では脱臭と分解無害化を同時に行うことができない。   In addition, the deodorizing apparatus that adsorbs and removes odors needs to be replaced each time the adsorbent is saturated, and the maintainability is not good. On the other hand, some apparatuses that decompose odor gas use a photocatalyst or a platinum (Pt) combustion catalyst, but an ultraviolet lamp or a heater is required, and the apparatus is expensive. In either case, even if the performance is good in the initial stage, there is a problem that the deterioration of the catalyst proceeds as time passes. Also, these devices cannot perform deodorization and detoxification simultaneously.

これに対し、生ごみ処理機においてプラズマを発生させて臭気を分解除去する脱臭装置(特許文献1)が開発されている。このシステムは単一の原因化合物に対しては非常に有効であるが、バイオマスにおける複雑混合ガス系では有害物質を生成する危険性がある。これは、生ごみ処理機やバイオトイレ内の湿度が高いことによるプラズマ効率の劣化や、悪臭成分内に存在する硫化水素(H2S)、アンモニア(NH3)、メチルメルカプタン(MMK)の同時処理による有害物質の副生成が原因であると考えられている。実際、プラズマ分解装置を用いたバイオトイレでは、脱臭はできても硫酸アンモニウムや硝酸アンミニウムを生成してしまうという事例報告がある。また、H2Sの単独処理過程で硫酸が生成される危険性も指摘されている。 On the other hand, a deodorizing apparatus (Patent Document 1) that generates plasma in a garbage disposal machine to decompose and remove odors has been developed. While this system is very effective for single causative compounds, there is a risk of producing harmful substances in complex gas mixtures in biomass. This is due to the deterioration of plasma efficiency due to the high humidity in the garbage processing machine and biotoilet, and the simultaneous use of hydrogen sulfide (H 2 S), ammonia (NH 3 ), and methyl mercaptan (MMK) present in malodorous components. It is thought to be caused by the by-production of harmful substances by treatment. In fact, there is a case report that a biotoilet using a plasma decomposition apparatus produces ammonium sulfate or ammonium nitrate even if it can be deodorized. In addition, it has been pointed out that there is a risk that sulfuric acid is generated during the single treatment of H 2 S.

特開2001−079343号公報Japanese Patent Application Laid-Open No. 2001-078343 特開2001−300297号公報JP 2001-300247 A

本発明は、生ごみ処理機の臭気除去におけるプラズマ分解による上記の問題点を解決するためになされたもので、生ごみ処理機やバイオトイレ等から発生する高湿度空気、発酵ガス、臭気ガスを含んだ複雑混合ガス系の脱臭及び分解無害化を同時に行うことができる脱臭装置及び脱臭方法を提供するものである。   The present invention was made in order to solve the above-mentioned problems caused by plasma decomposition in the removal of odors from garbage processing machines. The present invention relates to high-humidity air, fermentation gas, and odor gas generated from garbage processing machines and biotoilets. It is an object of the present invention to provide a deodorizing apparatus and a deodorizing method capable of simultaneously performing deodorization and detoxification of a complex gas mixture system.

本発明は、微生物を用いた発酵分解処理により生ごみを処理する場合などに発生する悪臭を伴う複合ガスに対応できるように、触媒による吸着除去及び脱着機能とプラズマによる成分別分解無害化の機能を持たせた。投入口14より投入された生ごみは、微生物を含んだ発酵槽18に導入され、該発酵槽18内で堆肥化を行い、その堆肥をカセットトレー13に移す。以下、堆肥化の際に発生する臭気ガスの脱臭及び分解無害化過程に沿って説明する。   The present invention is capable of adsorbing and desorbing with a catalyst and decomposing and detoxifying by component with plasma so that it can cope with a complex gas with bad odor generated when treating garbage by fermentation and decomposition using microorganisms. Was held. The garbage input from the input port 14 is introduced into a fermenter 18 containing microorganisms, composted in the fermenter 18, and the compost is transferred to the cassette tray 13. Hereinafter, the process of deodorizing and detoxifying odor gas generated during composting will be described.

まず、臭気ガス内のH2S、NH3等のプラズマ分解による硫酸アンモニウムの生成を防ぐため、プラズマ分解の前段で悪臭ガスの選択吸着除去を行う。また、高湿度では触媒機能やプラズマ効率の劣化を引き起こすため、水分も除去する必要がある。前段処理部には、水分吸着部1、H2S吸着部2、NH3吸着部3を設け、そこに臭気ガス10を導入する。吸着材によっては高温で反応するものがあるため、必要に応じてヒーター4を付加することによって吸着性能を高めることができる。また、ヒーター4を各吸着部に個別に設置すれば、加熱時間のタイミングを変えることによってガスの時間差脱着が可能になる。 First, in order to prevent generation of ammonium sulfate due to plasma decomposition of H 2 S, NH 3 and the like in odor gas, selective adsorption removal of malodorous gas is performed before the plasma decomposition. Moreover, since the catalytic function and the plasma efficiency are deteriorated at high humidity, it is necessary to remove moisture. The pre-treatment unit is provided with a moisture adsorption unit 1, an H 2 S adsorption unit 2, and an NH 3 adsorption unit 3, and an odor gas 10 is introduced therein. Since some adsorbents react at high temperatures, the adsorption performance can be enhanced by adding a heater 4 as necessary. In addition, if the heaters 4 are individually installed in the respective adsorption units, the time difference of the gas can be desorbed by changing the timing of the heating time.

前段処理部で吸着されなかった有機ガスを、プラズマ分解装置に導入する。本発明では、プラズマ分解装置として、これまで生ごみ処理機に用いられていなかったPACT装置5(特許文献2)を採用した。PACT装置5は、プラズマ発生電極に触媒金属を用いたもので、従来のプラズマ分解装置に比べて分解効率が格段に高く小型化も容易である。このコンパクトで簡易なPACT装置5を用いることにより、複数種の有害化学物質を適切にその場で無害化処理することができる。PACT装置5による分解後に発生するオゾンや硫黄などの副生成物は、活性炭6を含む後段処理部をオプションとして設置することにより処理することができる。   Organic gas that has not been adsorbed by the pre-treatment unit is introduced into the plasma decomposition apparatus. In the present invention, a PACT apparatus 5 (Patent Document 2) that has not been used in a garbage disposal machine so far is employed as a plasma decomposition apparatus. The PACT device 5 uses a catalytic metal as a plasma generating electrode, and has a resolving efficiency much higher than that of a conventional plasma decomposing device, and can be easily downsized. By using this compact and simple PACT device 5, it is possible to appropriately detoxify a plurality of types of harmful chemical substances on the spot. By-products such as ozone and sulfur generated after decomposition by the PACT device 5 can be processed by installing a post-processing unit including activated carbon 6 as an option.

本発明は、プラズマ分解の前段で悪臭ガスを選択的に吸着除去するようにしたので、臭気ガス内のH2S、NH3等がプラズマ分解によって硫酸アンモニウム等の反応副生成物が発生するのを抑制することができる。また、同プラズマ分解の前段に水分吸着部を設けたので、高湿度による触媒機能の劣化やプラズマ効率の低下を防ぐことができる。 In the present invention, the malodorous gas is selectively adsorbed and removed before the plasma decomposition, so that H 2 S, NH 3 and the like in the odor gas generate reaction by-products such as ammonium sulfate by the plasma decomposition. Can be suppressed. In addition, since the moisture adsorbing portion is provided in the previous stage of the plasma decomposition, it is possible to prevent deterioration of the catalyst function and plasma efficiency due to high humidity.

また、臭気ガス吸着装置及び水分吸着部に必要に応じてヒーターを設けることにより、ガスや水分の吸着性能を高めることができる。このヒーターを水分、H2S、NH3の各吸着部に個別に設置することにより、加熱時間のタイミングを変え、ガスの時間差脱着を可能にすることができる。また、各吸着部に個別設置されたヒーターを利用して、水分、H2S、NH3の吸脱着のタイミングを変えることにより、PACT装置による分解時の高湿度化を避けながら、有機ガスだけでなくH2S及びNH3も処理することができ、吸着材の交換などの余分なメンテナンスを極力少なくすることができる。 Moreover, the adsorption | suction performance of gas and a water | moisture content can be improved by providing a heater as needed in an odor gas adsorption | suction apparatus and a water | moisture-content adsorption | suction part. By separately installing this heater in each of the moisture, H 2 S, and NH 3 adsorption sections, it is possible to change the timing of the heating time and enable the time difference desorption of gas. In addition, by using heaters installed individually in each adsorption section, changing the timing of moisture adsorption, desorption and desorption of H 2 S, NH 3 , while avoiding high humidity during decomposition by the PACT device, only organic gas In addition, H 2 S and NH 3 can be processed, and extra maintenance such as replacement of the adsorbent can be minimized.

さらに、プラズマ分解装置としてコンパクトで簡易なPACT装置を用いることにより、複数種の有害化学物質を適切にその場で無害化処理することができる。プラズマ分解装置の後段に活性炭などの後段処理部を設置することにより、分解後に発生するオゾンや硫黄などの副生成物の処理を行うことができる。このように吸着部材を配置したPACT装置によるプラズマ分解により、生ごみ処理機における複雑混合ガス系の脱臭及び分解無害化を同時に行うことができる。   Furthermore, by using a compact and simple PACT apparatus as the plasma decomposing apparatus, it is possible to appropriately detoxify a plurality of types of harmful chemical substances on the spot. By installing a post-processing unit such as activated carbon in the subsequent stage of the plasma decomposition apparatus, it is possible to process by-products such as ozone and sulfur generated after the decomposition. As described above, by the plasma decomposition by the PACT device in which the adsorbing member is arranged, it is possible to simultaneously perform deodorization and detoxification of the complex mixed gas system in the garbage processing machine.

以下に、本発明に係る生ゴミ処理機の脱臭装置及び脱臭方法の実施形態を図1に基づいて説明する。まず、投入口14に投入された生ごみを、微生物を含んだ発酵槽18に導入する。発酵槽18には微生物の生息環境であるバイオチップ12に微生物を装填しておき、生ごみと容易に接触できるようにする。また、発酵槽18内に設置されたミキシングフィン16により、バイオチップ12を撹拌して分解を促進させる。微生物は一般に30℃〜50℃で活発に活動するので、バイオチップ12が30℃以下になると温度調節ヒーター17が自動的に加温し、外気温が−5℃以下になっても分解性能を落とすことなく分解が可能である。また、水分センサー15によってバイオチップ12の温度、湿度をチェックし、高湿度の際には点滅して使用者に注意を促す。   Below, embodiment of the deodorizing apparatus and the deodorizing method of the garbage processing machine which concerns on this invention is described based on FIG. First, the garbage thrown into the inlet 14 is introduced into the fermenter 18 containing microorganisms. The fermenter 18 is loaded with microorganisms on the biochip 12, which is a habitat for microorganisms, so that it can be easily brought into contact with garbage. Further, the biochip 12 is stirred by the mixing fins 16 installed in the fermenter 18 to promote decomposition. In general, microorganisms are actively active at 30 ° C. to 50 ° C. Therefore, when the biochip 12 becomes 30 ° C. or less, the temperature control heater 17 automatically heats, and even if the outside air temperature becomes −5 ° C. or less, the degradation performance is improved. Disassembly is possible without dropping. In addition, the temperature and humidity of the biochip 12 are checked by the moisture sensor 15 and flashes to alert the user when the humidity is high.

発酵槽18内で微生物により分解された生ごみは、堆肥としてカセットトレー13に蓄えられる。また、液体として取り出せる水分は、ドリップドレイン19に流される。一方、微生物による分解の過程で発生した臭気ガス10は、脱臭装置の前段処理部に導入される。まず、ガス導入口7より入った臭気ガス10を水分吸着材1に通し、ガス中に含まれる水分を除去する。これは、プラズマ分解時に水分が残っていると、空気中の窒素、酸素と結合して有害な窒素酸化物を生成する危険があるのを防止するためである。   Garbage decomposed by microorganisms in the fermenter 18 is stored in the cassette tray 13 as compost. Further, the water that can be taken out as a liquid flows into the drip drain 19. On the other hand, the odor gas 10 generated in the process of decomposition by microorganisms is introduced into the pre-treatment unit of the deodorization apparatus. First, the odor gas 10 entered from the gas inlet 7 is passed through the moisture adsorbent 1 to remove moisture contained in the gas. This is to prevent the danger of generating harmful nitrogen oxides by combining with nitrogen and oxygen in the air if moisture remains during plasma decomposition.

水分を除去された臭気ガス10は、H2S吸着部2及びNH3吸着部3に導入される。このように構成することによってプラズマ分解時にH2SとNH3が反応して硝酸や硫酸が生成されるのを防ぐことができる。PACT装置によるプラズマ分解と連動させて処理を行いたい場合には、ヒーター4を各吸着材に個別に付加し、加熱時間を変化させてガスの吸脱着を行うことにより、プラズマ分解の効率を上げることができる。なお、H2S吸着部2及びNH3吸着部3の順序は発生ガスに応じて変更が可能である。 The odor gas 10 from which moisture has been removed is introduced into the H 2 S adsorption unit 2 and the NH 3 adsorption unit 3. With this configuration, it is possible to prevent H 2 S and NH 3 from reacting during plasma decomposition to generate nitric acid or sulfuric acid. When processing is performed in conjunction with plasma decomposition by a PACT device, the efficiency of plasma decomposition is increased by adding a heater 4 to each adsorbent individually and changing the heating time to perform gas adsorption / desorption. be able to. Note that the order of the H 2 S adsorption unit 2 and the NH 3 adsorption unit 3 can be changed according to the generated gas.

プラズマ分解時に悪影響を及ぼす物質を前段処理部で吸着後、臭気ガス10はファン型PACT装置5に導入され、プラズマによる有機ガスの分解を行う(図2)。ファン型PACT装置5では外部電極22及びファン型電極23として触媒金属でできた分割電極を並列配置して電極間にプラズマ24を発生させ、ガス入口20から流入した複数種の有機ガスを高効率でCO2とH2Oに分解してガス出口21から放出する。分解完了後は反応生成物が再結合しないようにコントロールし、不要な反応を抑制する機能を備えている。また、ファン型PACT装置5は商用電源を用いたインバータ9で動作することができる。 After adsorbing substances that have an adverse effect on plasma decomposition in the pre-treatment unit, the odor gas 10 is introduced into the fan-type PACT device 5 to decompose the organic gas by plasma (FIG. 2). In the fan-type PACT device 5, split electrodes made of catalytic metal are arranged in parallel as the external electrode 22 and the fan-type electrode 23 to generate a plasma 24 between the electrodes, and a plurality of types of organic gases flowing from the gas inlet 20 are highly efficient. Is decomposed into CO 2 and H 2 O and discharged from the gas outlet 21. After the completion of decomposition, the reaction product is controlled so as not to recombine, and has a function of suppressing unnecessary reactions. The fan-type PACT device 5 can be operated by an inverter 9 using a commercial power source.

PACT装置5によるプラズマ分解時に発生するオゾンや硫黄の成分は、後段に配置した活性炭6によって吸着除去することができる。そして分解ガスはCO2やH2Oなどのクリーンガス11となって排気口8より排気される。以上のような装置全体の構成図を図1に示す。 Ozone and sulfur components generated at the time of plasma decomposition by the PACT device 5 can be adsorbed and removed by the activated carbon 6 disposed in the subsequent stage. The cracked gas becomes a clean gas 11 such as CO 2 or H 2 O and is exhausted from the exhaust port 8. A configuration diagram of the entire apparatus as described above is shown in FIG.

本発明の脱臭装置及び方法について、ヒーター4を用いない例を以下に記述する。水分吸着材には塩化カルシウムを、H2S及びNH3吸着材にはネオコール(登録商標)を用いた。ネオコールは、長時間使用してもH2S及びNH3の除去率がほとんど低下しないという優れた性質を持っている。塩化カルシウムやネオコールは約1年間その性能を維持することができるので、1年ごとに取り替えるだけでよい。 About the deodorizing apparatus and method of this invention, the example which does not use the heater 4 is described below. Calcium chloride was used as the moisture adsorbent, and Neocor (registered trademark) was used as the H 2 S and NH 3 adsorbent. Neocor has an excellent property that the removal rate of H 2 S and NH 3 hardly decreases even when used for a long time. Since calcium chloride and neocor can maintain their performance for about one year, they only need to be replaced every year.

前段処理を通過した臭気ガスには有機ガスが多く含まれているので、この有機ガスをファン型PACT装置5のプラズマによって分解した。このさい発酵槽内のミキシングフィン16によって30分ごとに撹拌を行い、PACT装置5を3分程度稼動させるだけで十分に悪臭成分を減少させることができた。PACT装置5の後段に活性炭6を設置することにより、PACT装置5による分解副生成物は除去され最終的に無臭かつ無害なクリーンガス11となることが確認された。   Since the odor gas that has passed through the previous stage treatment contains a large amount of organic gas, the organic gas was decomposed by the plasma of the fan-type PACT device 5. At this time, the mixing fins 16 in the fermenter were stirred every 30 minutes and the PACT apparatus 5 was operated for about 3 minutes. It was confirmed that by installing the activated carbon 6 in the subsequent stage of the PACT device 5, the decomposition by-products by the PACT device 5 are removed and finally the odorless and harmless clean gas 11 is obtained.

本発明の脱臭装置及び方法について、ヒーター4を用いる例を以下に記述する。水分吸着材にはゼオライトを、H2S 及びNH3吸着材には活性炭を主体としたH2S及びNH3をそれぞれ選択的に吸脱着する材料を用いた。ヒーター4を用いる場合には、ヒーター4の加熱時間及びファン型PACT装置5の稼動時間を適宜調節することによって、臭気ガスに含まれる成分に応じて吸脱着を行うことができ、また触媒の劣化を防ぎPACT装置5によるプラズマ分解の効率を高めることができる。加熱時間のタイムチャートの一例を図3に示す。 About the deodorizing apparatus and method of this invention, the example using the heater 4 is described below. The zeolite in the moisture adsorbent, the H 2 S and NH 3 adsorbent using a material selectively adsorbing and desorbing H 2 S and NH 3 consisting mainly of activated carbon, respectively. In the case of using the heater 4, by appropriately adjusting the heating time of the heater 4 and the operation time of the fan-type PACT device 5, adsorption / desorption can be performed according to the components contained in the odor gas, and the catalyst is deteriorated. And the efficiency of plasma decomposition by the PACT device 5 can be increased. An example of a time chart of the heating time is shown in FIG.

まず、発酵槽18内のミキシングフィン16によりバイオチップ12の撹拌を行い、生ごみの分解を促進させて臭気ガス10を発生させる。臭気ガス10に含まれる水分、H2S、NH3はそれぞれの吸着部で吸着される。この時点ではファン型PACT装置5は稼動しておらず、前段処理部のみが稼動している。次に、H2S吸着部2に付属のヒーターを加熱してH2Sを脱着すると同時にPACT装置5を稼動させ、H2SをH2とSに分解する。Sは後段処理部の活性炭6により除去される。さらに、NH3吸着部3に付属のヒーターを加熱してNH3を脱着し、PACT装置5によるプラズマによりNH3をN2とH2に分解させる。最後に、PACT装置5の停止後に水分吸着部1に付属のヒーターを加熱してH2Oを脱着して排出する。以上により、PACT装置5によるプラズマ分解時の高湿度化を避けながら、有機ガスだけでなく、H2S及びNH3も無害化することができた。 First, the biochip 12 is agitated by the mixing fins 16 in the fermenter 18 to promote decomposition of garbage and generate odor gas 10. Moisture, H 2 S, and NH 3 contained in the odor gas 10 are adsorbed at the respective adsorption portions. At this time, the fan-type PACT device 5 is not operating, and only the pre-processing unit is operating. Next, the heater attached to the H 2 S adsorption unit 2 is heated to desorb H 2 S, and at the same time, the PACT device 5 is operated to decompose H 2 S into H 2 and S. S is removed by the activated carbon 6 in the subsequent processing section. Further, the NH 3 desorbed by heating the heater supplied with the adsorbed NH 3 part 3, to decompose NH 3 into N 2 and H 2 by the plasma by PACT device 5. Finally, after the PACT device 5 is stopped, the heater attached to the moisture adsorption unit 1 is heated to desorb and discharge H 2 O. As described above, not only the organic gas but also H 2 S and NH 3 could be made harmless while avoiding high humidity during plasma decomposition by the PACT device 5.

なお、本発明は上記の実施形態及び実施例における脱臭処理に限定されるものではなく、特許請求の範囲の請求項に記載する内容の範囲内でさまざまな変形が可能であり、本発明はこれら全てを含むものである。   Note that the present invention is not limited to the deodorization treatment in the above-described embodiments and examples, and various modifications are possible within the scope of the contents described in the claims. It includes everything.

本発明は、低温発酵だけでなく高温発酵による生ごみ処理機にも応用が可能である。また、本発明は、主として生ごみ処理機における臭気の除去を目的として記述したが、厨房用生ごみの脱臭のみならず一般ごみ廃棄場、畜舎、バイオトイレ等から発生する高湿度空気、発酵ガス、臭気ガスを含んだ複雑混合ガスの脱臭及び分解無害化を行うことができ、廃棄物処理場、農耕畜産場、衛生下水処理場等様々な分野に応用することが可能である。   The present invention can be applied not only to low-temperature fermentation but also to garbage processing machines using high-temperature fermentation. In addition, although the present invention has been described mainly for the purpose of removing odors in garbage processing machines, not only deodorization of kitchen garbage, but also high-humidity air and fermentation gas generated from general waste disposal sites, barns, biotoilets, etc. It is possible to deodorize and decompose and detoxify complex mixed gas containing odor gas, and it can be applied to various fields such as waste treatment plant, agricultural and livestock farm, sanitary sewage treatment plant.

本発明の生ごみ処理機の脱臭装置の断面図である。It is sectional drawing of the deodorizing apparatus of the garbage processing machine of this invention. ファン型PACT装置の構成図を示す。The block diagram of a fan type PACT apparatus is shown. 実施例2における脱臭装置の加熱時間のタイムチャートを示す。The time chart of the heating time of the deodorizing apparatus in Example 2 is shown.

符号の説明Explanation of symbols

1 水分吸着部
2 H2S吸着部
3 NH3吸着部
4 ヒーター
5 ファン型PACT装置
6 活性炭
7 ガス導入口
8 排気口
9 インバータ
10 臭気ガス
11 クリーンガス
12 バイオチップ
13 カセットトレー
14 投入口
15 水分センサー
16 ミキシングフィン
17 温度調節ヒーター
18 発酵槽
19 ドリップドレイン
20 ガス入口
21 ガス出口
22 外部電極
23 ファン型電極
24 プラズマ


NH 1 moisture adsorption portion 2 H 2 S adsorbent 3 3 adsorption unit 4 Heater 5-fan PACT device 6 charcoal 7 gas inlet 8 outlet 9 inverter 10 odorous gases 11 clean gas 12 biochip 13 cassette tray 14 inlet 15 water Sensor 16 Mixing fin 17 Temperature control heater 18 Fermenter 19 Drip drain 20 Gas inlet 21 Gas outlet 22 External electrode 23 Fan-type electrode 24 Plasma


Claims (12)

生ごみ処理機の臭気除去装置において、臭気ガスを処理するプラズマ分解装置と、その前段部に水分及びガスを別個に吸脱着する吸着部を設けたことを特徴とする生ごみ処理機の脱臭装置。   Deodorizing apparatus for garbage processing machine, characterized in that in the odor removing apparatus for garbage processing machine, a plasma decomposing apparatus for treating odor gas and an adsorbing part for separately adsorbing and desorbing moisture and gas are provided in the front part thereof. . 前記吸着部は、H2O、H2S、NH3を各々個別に吸脱着するものであることを特徴とする請求項1に記載の生ごみ処理機の脱臭装置。 2. The deodorizing apparatus for a garbage disposal machine according to claim 1, wherein the adsorbing unit adsorbs and desorbs H 2 O, H 2 S, and NH 3 individually. 前記吸着部ごとに加熱制御装置を設けたことを特徴とする請求項1又は2に記載の生ごみ処理機の脱臭装置。   The deodorizing apparatus for a garbage disposal machine according to claim 1 or 2, wherein a heating control device is provided for each of the adsorption sections. 前記個々の吸着部及び加熱制御装置は、各々の吸着成分に対応して時間差脱着を行うものであることを特徴とする請求項3に記載の生ごみ処理機の脱臭装置。   The deodorizing apparatus for a garbage processing machine according to claim 3, wherein each of the individual adsorbing units and the heating control apparatus performs time-desorption according to each adsorbing component. 前記プラズマ分解装置の後段部に、活性炭等の吸着部を設けたことを特徴とする請求項1ないし4のいずれかに記載の生ごみ処理機の脱臭装置。   The deodorizing apparatus for a garbage processing machine according to any one of claims 1 to 4, wherein an adsorption part such as activated carbon is provided at a subsequent stage of the plasma decomposition apparatus. 前記プラズマ分解装置の電極は、触媒金属電極であることを特徴とする請求項1ないし4のいずれかに記載の生ごみ処理機の脱臭装置。   The deodorizing apparatus for a garbage disposal machine according to any one of claims 1 to 4, wherein the electrode of the plasma decomposition apparatus is a catalytic metal electrode. 生ごみ処理機の臭気ガスを除去する手段として、臭気ガスをプラズマにより分解させ、その前段で水分及びガスを吸着させることを特徴とする生ごみ処理機の脱臭方法。   A method for deodorizing a garbage treatment machine, characterized in that the odor gas is decomposed by plasma and moisture and gas are adsorbed before the odor gas as means for removing the odor gas of the garbage treatment machine. 前記吸着は、プラズマ分解の前段においてH2O、H2S、NH3を各々個別に吸脱着するものであることを特徴とする請求項7に記載の生ごみ処理機の脱臭方法。 8. The deodorizing method for a garbage disposal machine according to claim 7, wherein the adsorption is performed by individually adsorbing and desorbing H 2 O, H 2 S, and NH 3 before the plasma decomposition. 前記H2O、H2S、NH3の吸脱着は、各々個別に温度制御することを特徴とする請求項7又は8のいずれかに記載の生ごみ処理機の脱臭方法。 The deodorizing method for a garbage disposal machine according to claim 7 or 8, wherein the adsorption / desorption of the H 2 O, H 2 S, and NH 3 is individually controlled in temperature. 前記H2O、H2S、NH3の吸着成分に対応して各々温度制御をしながら時間差脱着を行うことを特徴とする請求項7ないし9のいずれかに記載の生ごみ処理機の脱臭方法。 The deodorization of a garbage disposal machine according to any one of claims 7 to 9, wherein time-desorption is performed while controlling the temperature corresponding to the adsorbed components of H 2 O, H 2 S, and NH 3 respectively. Method. 前記プラズマ分解の後段において、活性炭等によりガス等を吸着除去することを特徴とする請求項7ないし10のいずれかに記載の生ごみ処理機の脱臭方法。   The deodorization method for a garbage disposal machine according to any one of claims 7 to 10, wherein gas or the like is adsorbed and removed by activated carbon or the like in a subsequent stage of the plasma decomposition. 前記プラズマを発生させる電極として、触媒金属を用いて臭気ガスを分解することを特徴とする請求項7ないし10のいずれかに記載の生ごみ処理機の脱臭方法。
The deodorization method for a garbage disposal machine according to any one of claims 7 to 10, wherein an odor gas is decomposed using a catalytic metal as an electrode for generating the plasma.
JP2004020196A 2004-01-28 2004-01-28 Deodorizing device of garbage treatment machine and deodorizing method using the same Pending JP2005211763A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108479344A (en) * 2018-04-08 2018-09-04 中冶长天国际工程有限责任公司 A kind of desulphurization denitration removes ammonia system
CN108662587A (en) * 2018-06-07 2018-10-16 广西凯泉环保工程有限公司 A kind of biological deodorizing and pyrolysis rubbish processing to be harmless system
KR101949148B1 (en) * 2018-04-05 2019-02-19 (주)오클린테크 Compost manufacture apparatus using microorganism

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101949148B1 (en) * 2018-04-05 2019-02-19 (주)오클린테크 Compost manufacture apparatus using microorganism
CN108479344A (en) * 2018-04-08 2018-09-04 中冶长天国际工程有限责任公司 A kind of desulphurization denitration removes ammonia system
CN108479344B (en) * 2018-04-08 2021-01-19 中冶长天国际工程有限责任公司 Desulfurization, denitrification and ammonia removal system
CN108662587A (en) * 2018-06-07 2018-10-16 广西凯泉环保工程有限公司 A kind of biological deodorizing and pyrolysis rubbish processing to be harmless system

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