JP2601623B2 - Waste treatment method and apparatus - Google Patents
Waste treatment method and apparatusInfo
- Publication number
- JP2601623B2 JP2601623B2 JP33791493A JP33791493A JP2601623B2 JP 2601623 B2 JP2601623 B2 JP 2601623B2 JP 33791493 A JP33791493 A JP 33791493A JP 33791493 A JP33791493 A JP 33791493A JP 2601623 B2 JP2601623 B2 JP 2601623B2
- Authority
- JP
- Japan
- Prior art keywords
- waste
- fermenter
- magnetron
- fermentation
- temperature
- 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 - Lifetime
Links
- 239000002699 waste material Substances 0.000 title claims description 30
- 238000000034 method Methods 0.000 title description 9
- 238000001816 cooling Methods 0.000 claims description 15
- 238000002485 combustion reaction Methods 0.000 claims description 11
- XQVKLMRIZCRVPO-UHFFFAOYSA-N 4-[(2-arsonophenyl)diazenyl]-3-hydroxynaphthalene-2,7-disulfonic acid Chemical compound C12=CC=C(S(O)(=O)=O)C=C2C=C(S(O)(=O)=O)C(O)=C1N=NC1=CC=CC=C1[As](O)(O)=O XQVKLMRIZCRVPO-UHFFFAOYSA-N 0.000 claims 1
- 241000679125 Thoron Species 0.000 claims 1
- 238000010304 firing Methods 0.000 claims 1
- 239000000696 magnetic material Substances 0.000 claims 1
- 239000002351 wastewater Substances 0.000 claims 1
- 238000000855 fermentation Methods 0.000 description 25
- 230000004151 fermentation Effects 0.000 description 25
- 239000010815 organic waste Substances 0.000 description 25
- 235000019645 odor Nutrition 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 4
- 239000010813 municipal solid waste Substances 0.000 description 4
- 239000003337 fertilizer Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Treating Waste Gases (AREA)
- Treatment Of Sludge (AREA)
- Fertilizers (AREA)
Description
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【0001】[0001]
【産業上の利用分野】この発明は、廃棄物(塵芥物)を
効率的に処理、利用するための廃棄物処理方法及び装置
に関し、特に、有機性廃棄物を発酵させ、肥料又は、飼
料に再活用し得るようにした廃棄物処理方法及びその装
置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste treatment method and apparatus for efficiently treating and utilizing waste (garbage), and more particularly, to fermenting organic waste to produce fertilizer or feed. The present invention relates to a waste disposal method and a waste disposal apparatus which can be reused.
【0002】[0002]
【発明の背景】近代産業の発達と急速な人口増加による
塵芥排出量の増加は、環境を汚す深刻な要因として台頭
されてきた。特に、大都会に集中している人口によるお
びただしい塵芥が都市内で消化できず、外地へまで搬送
される実状にある。その中の全体塵芥の約28%を占め
る飲食物による廃棄物は有機性の廃棄物であって、腐敗
しやすい性質を有している。Background of the Invention The increase in refuse emissions due to the development of modern industry and rapid population growth has emerged as a serious factor polluting the environment. In particular, a large amount of garbage from the population concentrated in large cities cannot be digested in cities and is transported to outside areas. Food and drink waste, which accounts for about 28% of the total garbage, is organic waste and has a perishable property.
【0003】このような腐敗性廃棄物はすごい悪臭はも
とより、水分含有量の高い梅雨期や雨の降る時など下水
道を通して河川に流れ込み深刻に環境を汚してきてい
る。[0003] Such spoilage wastes, in addition to having a stench of great odor, flow into rivers through sewers during the rainy season or when rainy, which has a high water content, and seriously pollute the environment.
【0004】さらに、このような廃棄物は、収去及び搬
送処理がややこしいばかりでなく、焼却処理が難しいた
め、ほとんどを埋立てている実状にある。従って、腐敗
性廃棄物を効率的に収去処理し、環境の汚れを減らして
資源化する方案が促される実情にある。[0004] Further, such waste is not only difficult to remove and transport, but also difficult to incinerate. Therefore, there is a situation in which a method for efficiently removing and processing perishable waste, reducing environmental contamination, and recycling the waste is promoted.
【0005】[0005]
【発明の目的】従って、この発明の目的は、腐敗しやす
い有機性廃棄物を発酵させて、飼料や肥料として再活用
し得るようにした廃棄物処理方法及びその装置を提供す
ることにある。SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a waste disposal method and an apparatus therefor, in which perishable organic waste is fermented and can be reused as feed or fertilizer.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するため
のこの発明による廃棄物の処理方法は、有機性廃棄物を
加熱して発酵条件に適当な湿度を保たせる湿度調整段階
と、上記有機性廃棄物を発酵条件に適当な温度に保たせ
て発酵させる発酵段階とから成ることを特徴とする。According to the present invention, there is provided a method for treating waste, comprising the steps of: heating an organic waste to maintain a suitable humidity for fermentation conditions; A fermentation step in which sexual waste is maintained at an appropriate temperature for fermentation conditions and fermented.
【0007】また、廃棄物の処理装置は、有機性廃棄物
を蓄える発酵槽と、この発酵槽に蓄えられている有機性
廃棄物の含水率と、温度を発酵に適当に保たせて発酵さ
せる発酵手段とから構成されたことを特徴とする。[0007] Further, the waste treatment apparatus performs fermentation by keeping a fermenter for storing organic waste, a moisture content of the organic waste stored in the fermenter, and a temperature suitable for fermentation. And fermentation means.
【0008】[0008]
【実施例】以下、この発明による実施例を添付図面に沿
って詳述する。図1において、この発明の廃棄物処理装
置は、発酵しようとする有機性塵芥を蓄える発酵槽10
と、この発酵槽10に蓄えられた有機性塵芥の発酵条件
を提供する発酵手段とから構成される。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the accompanying drawings. In FIG. 1, a waste treatment apparatus according to the present invention includes a fermenter 10 for storing organic waste to be fermented.
And fermentation means for providing fermentation conditions for the organic trash stored in the fermenter 10.
【0009】上記構成中、発酵槽10内の上部には、有
機性廃棄物及び有機性廃棄物を発酵させるための菌株を
発酵槽10に投入させるための投入口12と、有機性廃
棄物の乾燥及び発酵時に生ずるガス及び臭いを発酵槽1
0の外部へ流出するための排気孔41が形成されてい
る。この投入口12にはふた12aが設けられている。
また、発酵槽10の一側には有機性廃棄物の発酵のため
の空気を発酵槽10内に吸込ませるための空気吸込口1
7が形成されている。In the above structure, an input port 12 for introducing organic waste and a strain for fermenting the organic waste into the fermenter 10 is provided at an upper portion in the fermenter 10, Gas and odor generated during drying and fermentation
An exhaust hole 41 is formed to flow out of the air outlet. The inlet 12 is provided with a lid 12a.
Further, an air inlet 1 for sucking air for fermenting organic waste into the fermenter 10 is provided on one side of the fermenter 10.
7 are formed.
【0010】上記発酵槽10内で発酵された有機性廃棄
物を外部へ排出させるための排出口15は、発酵槽10
の下部に設けられている。排気孔41には発酵槽内から
生じたガス及び臭いを除去する浄化手段が設けられてい
る。An outlet 15 for discharging the organic waste fermented in the fermenter 10 to the outside is provided in the fermenter 10.
It is provided at the lower part. The exhaust hole 41 is provided with a purifying means for removing gas and odor generated from the inside of the fermenter.
【0011】上記浄化手段は、上記発酵槽10に形成さ
れた排気孔41に流出するガス及び臭いを外部へ誘導す
る煙道40と、ヒータ46により上記煙道40に誘導さ
れるガスを燃焼させる燃焼室45と、上記ガスの燃焼を
促し、臭いを除去する触媒42a,42bと、上記にお
いて燃焼され、浄化された空気を外部へ排出させる排気
ファン43とからなる。上記混合手段は、動力を生ずる
モータ26と、このモータ26の動力により回転する軸
22と、上記軸22により回転しながら発酵槽10内の
有機性廃棄物をかき回すファン24とから構成される。The purifying means burns the gas and the odor flowing out to the exhaust hole 41 formed in the fermenter 10 to the outside, and the gas guided to the flue 40 by the heater 46. It comprises a combustion chamber 45, catalysts 42a and 42b for promoting the combustion of the gas and removing odors, and an exhaust fan 43 for discharging the burned and purified air to the outside. The mixing means includes a motor 26 for generating power, a shaft 22 rotated by the power of the motor 26, and a fan 24 for rotating the organic waste in the fermenter 10 while rotating by the shaft 22.
【0012】上記発酵手段は、上記発酵槽10内の湿度
をセンシングする湿度センサ52と、上記発酵槽10内
の温度をセンシングする温度センサ54と、上記湿度セ
ンサ52から感知された湿度と温度センサ54から感知
された温度による制御信号を出力する制御手段100
と、上記マイクロプロセッサにより制御され所定の電磁
波を生ずるマグネトロン32と、上記マグネトロン32
から生じた所定の電磁波を発酵槽に誘導する導波管34
と、上記導波管34により、誘導された所定の電磁波を
上記発酵槽内に供給する給電口36とから構成される。The fermenting means includes a humidity sensor 52 for sensing the humidity in the fermenter 10, a temperature sensor 54 for sensing the temperature in the fermenter 10, and a humidity and temperature sensor sensed by the humidity sensor 52. Control means 100 for outputting a control signal based on the temperature sensed from
A magnetron 32 controlled by the microprocessor to generate a predetermined electromagnetic wave;
Waveguide 34 for guiding a predetermined electromagnetic wave generated from
And a feed port 36 for supplying a predetermined electromagnetic wave guided by the waveguide 34 into the fermenter.
【0013】給電口36には導波管34内部への有害ガ
スの流入を防ぐための給電口ふた36aが形成され、マ
グネトロン32の一側にはこれを冷却させる冷却ファン
47が設けられ、これから放出されたのち、マグネトロ
ン32で温度の昇った空気は、ダクト48により燃焼室
45に誘導される。The power supply port 36 is provided with a power supply port lid 36a for preventing harmful gas from flowing into the waveguide 34, and a cooling fan 47 for cooling the magnetron 32 is provided on one side of the magnetron 32. After being released, the air whose temperature has risen in the magnetron 32 is guided to the combustion chamber 45 by the duct 48.
【0014】図3において、マイクロプロセッサ100
は、湿度センサ52で感知された湿度と、温度センサ5
4で、感知さた、温度によりマグネトロン駆動部10
0、モータ駆動部120、排気ファン駆動部130、冷
却ファン駆動部140、ヒータ駆動部150とを制御す
る。マグネトロン駆動部110は、所定の電磁波を生ず
るマグネトロン32を駆動させ、モータ駆動部120は
混合手段のモータ26を駆動させる。排気ファン駆動部
130と冷却ファン駆動部140は夫々浄化手段の排気
ファン43と、マグネトロン32を冷却させる冷却ファ
ン47を駆動させる。Referring to FIG. 3, a microprocessor 100
Is the humidity detected by the humidity sensor 52 and the temperature sensor 5
At 4, the magnetron driving unit 10 is detected according to the detected temperature.
0, the motor drive unit 120, the exhaust fan drive unit 130, the cooling fan drive unit 140, and the heater drive unit 150 are controlled. The magnetron drive unit 110 drives the magnetron 32 that generates a predetermined electromagnetic wave, and the motor drive unit 120 drives the motor 26 of the mixing unit. The exhaust fan driving unit 130 and the cooling fan driving unit 140 respectively drive the exhaust fan 43 of the purifying unit and the cooling fan 47 for cooling the magnetron 32.
【0015】次に、上記構成のこの発明の装置の動作に
ついて述べる。図4において、ステップS1での如く、
投入口12のふたを開けて発酵槽10内に有機性塵芥を
投入後、ステップS2の如く廃棄物処理装置を駆動させ
ると、制御手段のマイクロプロセッサ100によりマグ
ネトロン駆動部110と、モータ駆動部120、排気フ
ァン、冷却ファン駆動部130,140、ヒータ駆動部
150とが制御され、マグネトロン32、モータ26、
冷却ファン47、排気ファン43、ヒータ46が駆動す
る。Next, the operation of the apparatus of the present invention having the above configuration will be described. In FIG. 4, as in step S1,
After opening the lid of the charging port 12 and charging the organic waste into the fermenter 10, the waste disposal apparatus is driven as in step S 2. When the microprocessor 100 of the control means controls the magnetron driving unit 110 and the motor driving unit 120. , The exhaust fan, the cooling fan drive units 130 and 140, and the heater drive unit 150 are controlled, and the magnetron 32, the motor 26,
The cooling fan 47, the exhaust fan 43, and the heater 46 are driven.
【0016】マグネトロン32から生じた超高周波は、
導波管34に誘導され、給電口36を通して発酵槽10
に照射され、有機性廃棄物を加熱させる。モータ26は
軸22を回転させ、軸22に形成された混合ファン24
は発酵槽10内に投入された有機性廃棄物をかき回す。The very high frequency generated from the magnetron 32 is
The fermenter 10 is guided by the waveguide 34 and passes through the feed port 36.
To heat the organic waste. The motor 26 rotates the shaft 22, and a mixing fan 24 formed on the shaft 22.
Agitates the organic waste put into the fermenter 10.
【0017】上記冷却ファン47から生じた風は、マグ
ネトロン32を冷却させつつ温度が上り、ダクト48を
通して燃焼室45に流入される。一方、上記のごとく有
機性廃棄物をかき回しながら超高周波で加熱すると、ア
ンモニアと二酸化炭素を含んだ有害ガスか生じて水分が
蒸発し、排気ファン43により排気孔41を通り発酵槽
10の外部へ強制的に排気される。この有害ガスは煙道
40の上下に設けられた触媒42a,42bとヒータ4
6により燃焼および脱臭され、浄化された空気が放出さ
れるようになる。The temperature of the wind generated from the cooling fan 47 rises while cooling the magnetron 32, and flows into the combustion chamber 45 through the duct 48. On the other hand, when the organic waste is heated at an ultra-high frequency while being stirred as described above, a harmful gas containing ammonia and carbon dioxide is generated, and the moisture evaporates. It is forcibly exhausted. This harmful gas is supplied to catalysts 42 a and 42 b provided above and below the flue 40 and the heater 4.
The combustion and deodorization by 6 allows purified air to be released.
【0018】上記の如く、有機性廃棄物が乾燥され図4
のステップS3での如く、マイクロプロセッサ100
は、湿度センサ52により感知された廃棄物の水分含有
量が発酵に適当な湿度(菌株によってちがうが通常50
〜60%、この発明では50%とする)になっているの
かを判断する。その結果、排気物の含水量が発酵に適す
る湿度になっていない場合には、引き続きマグネトロン
駆動部110を通してマグネトロン32を駆動させ、廃
棄物の含水量が発酵に適した湿度になれば、図4のステ
ップS4での如く、マイクロプロセッサ100はマグネ
トロン駆動部100を制御してマグネトロン32の動作
を中止させる。この中止後、フザー音なり、点灯ランプ
によって有機性廃棄物の水分含有量が発酵に適している
ことをユーザーに知らせることもできる。As described above, the organic waste is dried, and FIG.
As in step S3 of FIG.
Means that the moisture content of the waste as detected by the humidity sensor 52 is suitable for fermentation (typically 50
6060%, and 50% in the present invention). As a result, if the water content of the exhaust gas does not reach the humidity suitable for fermentation, the magnetron 32 is continuously driven through the magnetron driving unit 110, and if the water content of the waste reaches the humidity suitable for fermentation, FIG. As in step S4, the microprocessor 100 controls the magnetron driving unit 100 to stop the operation of the magnetron 32. After this stoppage, the user may be notified that the water content of the organic waste is suitable for fermentation by a sound or a lighting lamp.
【0019】以後は、発酵槽10内の温度が高い状態で
あるため、所定時間中マグネトロン32の動作を中止さ
せた状態を保ち、有機性廃棄物を冷却させる。その後、
図4のステップS5の如く、温度センサ54により感知
された発酵に適する温度(菌株によりちがうが、通常5
0〜60℃あって、この発明では55℃とする)になれ
ば、ステップS6のごとく、所定量(通常、有機性廃棄
物処理量の0.4%)の菌株を投入口12に投入する。After that, since the temperature in the fermenter 10 is high, the operation of the magnetron 32 is stopped for a predetermined time, and the organic waste is cooled. afterwards,
As shown in step S5 in FIG. 4, the temperature suitable for fermentation detected by the temperature sensor 54 (differing depending on the strain, usually 5
When the temperature reaches 0 to 60 ° C. and the temperature is 55 ° C. in the present invention), a predetermined amount (usually 0.4% of the amount of organic waste treated) of the strain is introduced into the inlet 12 as in step S6. .
【0020】ここで、上記菌株は別の菌株投与手段を設
けて自動的に投与するこもでき、ブザー音や点灯ランプ
により菌株の投与時期を表示して、ユーザーが手動によ
り投入することもできる。Here, the above-mentioned strain can be administered automatically by providing another strain administration means, and the user can manually input the strain by displaying the administration time of the strain by means of a buzzer sound or a lighting lamp.
【0021】発酵槽10に菌株の投与後、マイクロプセ
ッサ100は温度センサ54を通して、発酵槽10内の
温度を感知する。マイクロプロセッサ100は、ステッ
プS7での如く、発酵槽10内の温度が発酵に適した温
度以下であれば(この発明では50℃)、ステップS8
での如く、マグネトロン駆動部100を制御し、マグネ
トロン32を動作させ、ステップS9の如く発酵に適し
た温度より高ければ(この発明では60℃)、ステップ
S10の如く、マグネトロン駆動部110を制御してマ
グネトロン32の動作を中止させた状態で保つ。After the administration of the strain into the fermenter 10, the microprocessor 100 senses the temperature in the fermenter 10 through the temperature sensor 54. If the temperature in the fermenter 10 is equal to or lower than the temperature suitable for fermentation (50 ° C. in the present invention) as in step S7, the microprocessor 100 proceeds to step S8.
As described above, the magnetron driving unit 100 is controlled to operate the magnetron 32. If the temperature is higher than the temperature suitable for fermentation (60 ° C. in the present invention) as in step S9, the magnetron driving unit 110 is controlled as in step S10. To keep the operation of the magnetron 32 stopped.
【0022】この際、発酵に要する空気は空気投入口1
7により流入される。At this time, the air required for fermentation is supplied to the air inlet 1
7 inflow.
【0023】このように、発酵過程の際には、発酵槽1
0の内部温度が発酵の最適条件である50〜60℃を保
つべくマグネトロン32の出力を調整する。上記発酵過
程の経過中、発酵槽10内から生じる有害ガスは、煙道
40内の排気ファン43により排気孔41を通して強制
的に排気される。煙道40内を通る過程において有害ガ
スは、ヒータ46と触媒42a,42bにより燃焼及び
脱臭された後、外部へ排出される。この発酵過程は、ス
テップS11での如く、湿度センサ52により感知され
た水分含有量が発酵を中断される所定値(この発明では
20%)に到達する時まで続けて進行される。Thus, during the fermentation process, the fermenter 1
The output of the magnetron 32 is adjusted so that the internal temperature of 0 is maintained at 50 to 60 ° C. which is the optimum condition for fermentation. During the course of the fermentation process, the harmful gas generated in the fermenter 10 is forcibly exhausted through the exhaust hole 41 by the exhaust fan 43 in the flue 40. During the process of passing through the flue 40, the harmful gas is burned and deodorized by the heater 46 and the catalysts 42a and 42b, and then discharged to the outside. This fermentation process is continued until the moisture content detected by the humidity sensor 52 reaches a predetermined value (20% in the present invention) at which the fermentation is interrupted, as in step S11.
【0024】上記の如き発酵過程を経て水分含有量が所
定値になると、マイクロプロセッサ100は、ステップ
S11の如く、マグネトロン駆動部110とモータ駆動
部120、排気ファンおよび冷却ファン駆動部130,
140、ヒータ駆動部150などの動作を中止させる。
この際、ブザー音なり点灯ランプを通して有機性廃棄物
の処理が終了されたのを表示することもできる。When the water content reaches a predetermined value through the fermentation process as described above, the microprocessor 100, as in step S11, sets the magnetron driving unit 110 and the motor driving unit 120, the exhaust fan and cooling fan driving units 130,
The operation of the heater 140, the heater driving unit 150, and the like is stopped.
At this time, it is also possible to display that the processing of the organic waste has been completed through a buzzer or a lighting lamp.
【0025】上記過程を経て発酵処理された有機性廃棄
物は、排出口15を通して取り出されて家畜の飼料や肥
料として再活用することができる。この発酵過程は、有
機性廃棄物の種によってやや時間差はあるが、通常20
〜40時間ぐらいあれば終了される。The organic waste fermented through the above process is taken out through the outlet 15 and can be reused as livestock feed or fertilizer. This fermentation process may take a little time depending on the type of organic waste,
It will be finished after about 40 hours.
【0026】[0026]
【発明の効果】上記の発明の有機性廃棄物処理方法及び
装置は、病院、食堂、軍部隊及び工場などの如き集団炊
事を行う場所はもとより、アパート団地の如き公共場所
から排出される有機性廃棄物を効率的に処理でき、さら
に、廃棄物を処理し、焼却廃棄して埋め立ての際、生じ
る人力と時間の浪費及び環境の汚れを減らし、非公害物
に変換させて再活用することにより、環境の汚れと廃棄
物の量を減らしうる効果を有する。また、マグネトロン
を冷却するための冷却ファンから放出されてマグネトロ
ンにおいて温度が上昇した空気を燃焼室に誘導するダク
トを設けたことにより、単に従来のような燃焼室におけ
る加熱にとどまらず、ダクトからの排熱を燃焼室に供給
することができ、発酵ガスの燃焼効率が高まるという効
果を有する。 The method and apparatus for treating organic waste according to the present invention can be applied to organic waste discharged from public places such as apartment complexes, as well as places such as hospitals, canteens, military units and factories. Waste can be treated efficiently, and furthermore, when waste is treated, incinerated and disposed of in landfills, the amount of manpower and time wasted and the pollution of the environment is reduced, and it is converted into non-polluting materials and reused. It has the effect of reducing the amount of environmental contamination and waste. Also, magnetron
Cooling fan released from the magnetro
Duct that directs the air with increased temperature into the combustion chamber
By simply installing the fuel cell, the conventional combustion chamber
Not only heating but also supplying exhaust heat from the duct to the combustion chamber
To increase the combustion efficiency of fermentation gas.
Have fruit.
【0027】この発明は、発明の範囲を逸脱せずに種々
の変形が実施できることは、明らかである。Obviously, various modifications can be made to the present invention without departing from the scope of the invention.
【図1】 この発明の廃棄物処理装置の構成を示す断面
図である。FIG. 1 is a cross-sectional view illustrating a configuration of a waste disposal apparatus according to the present invention.
【図2】 この発明の廃棄物処理装置の一部切開の右側
面図である。FIG. 2 is a right side view of a partially cut-away portion of the waste disposal apparatus according to the present invention.
【図3】 この発明の廃棄物処理装置の制御回路のブロ
ック図である。FIG. 3 is a block diagram of a control circuit of the waste disposal apparatus of the present invention.
【図4】 この発明の廃棄物処理装置の説明のための流
れ図である。FIG. 4 is a flowchart for explaining a waste disposal apparatus of the present invention.
10……発酵槽 12……投入口
12a……ふた 15……排出口 17……空気吸込口
22……軸 24……ファン 26……モータ
32……マグネトロン 34……導波管 36……給電口
40……煙道 41……排気孔 42a,42b……触媒
43……排気ファン 45……燃焼室 46……ヒータ
47……冷却ファン 48……ダクト 52……湿度センサ
54……温度センサ 100……制御手段10: Fermenter 12: Input port
12a ... lid 15 ... outlet 17 ... air inlet
22 ... shaft 24 ... fan 26 ... motor
32: magnetron 34: waveguide 36: power supply port
40 flue 41 exhaust vents 42a, 42b catalyst
43 exhaust fan 45 combustion chamber 46 heater
47 Cooling fan 48 Duct 52 Humidity sensor
54 temperature sensor 100 control means
Claims (1)
トロンによって発生した電磁波を照射し、前記発酵槽内
の温度調整を行って廃棄物を発酵させる廃棄物処理装置
において、 廃棄物から発生するガスおよび臭いを誘導して外部に排
気するように、前記発酵槽の排気孔に設けられて外方へ
延びる煙道と、 該煙道内部に設けられ、該煙道に誘導されるガスをヒー
タにより燃焼させる燃焼室と、 前記マグネトロンを空冷するための冷却ファンと、 前記マグネトロンにおいて温度の上昇した空気を前記燃
焼室に誘導するダクトとを有して構成されていることを
特徴とする廃棄物処理装置。 The waste stored in the fermenter is treated with a magnetic material.
Irradiate the electromagnetic waves generated by the thoron, and
Waste treatment equipment that adjusts the temperature of wastewater and ferments waste
In, discharge to the outside to induce gas and odor generated from the waste
As you notice, it is provided in the exhaust port of the fermenter and
An extending flue, and a gas provided inside the flue and guided to the flue.
A combustion chamber for burning the magnetron, a cooling fan for cooling the magnetron by air, and
And a duct leading to the firing chamber.
Characteristic waste treatment equipment.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019920025997A KR0141359B1 (en) | 1992-12-29 | 1992-12-29 | Organic garbage disposer |
KR199225997 | 1992-12-29 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06256080A JPH06256080A (en) | 1994-09-13 |
JP2601623B2 true JP2601623B2 (en) | 1997-04-16 |
Family
ID=19347104
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33791493A Expired - Lifetime JP2601623B2 (en) | 1992-12-29 | 1993-12-28 | Waste treatment method and apparatus |
Country Status (2)
Country | Link |
---|---|
JP (1) | JP2601623B2 (en) |
KR (1) | KR0141359B1 (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08188491A (en) * | 1995-01-10 | 1996-07-23 | Nec Corp | Treatment of garbage and its apparatus |
KR100521125B1 (en) * | 1997-11-28 | 2006-01-27 | 파로마 고교 가부시키 가이샤 | Food waste handler |
KR100244389B1 (en) * | 1997-12-31 | 2000-02-01 | 구자홍 | Microwave garbage processor |
KR100512100B1 (en) * | 1998-08-11 | 2005-11-24 | 엘지전자 주식회사 | Apparatus for disposing wet waste using microwave which has a mechanism for automatically removing disposed waste therefrom |
EP1048366B1 (en) * | 1999-04-27 | 2005-10-12 | JFE Engineering Corporation | A method for disposing a waste |
JP4732708B2 (en) * | 2004-05-19 | 2011-07-27 | 樋野 明人 | Deodorization treatment method and deodorization treatment apparatus for used paper diaper fermentation treatment |
JP5796855B2 (en) * | 2011-04-01 | 2015-10-21 | ジーエネックス株式会社 | Compost production system and compost production method |
KR101224286B1 (en) * | 2012-03-19 | 2013-01-21 | 김경아 | Fermentation machine for fordder |
KR101224252B1 (en) * | 2012-06-21 | 2013-01-22 | 김경아 | Fermentation machine for fordder |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52154775A (en) * | 1976-06-16 | 1977-12-22 | Fuji Kaki Kouji Kk | Apparatus for fermentating livestock manure |
JPS62126337U (en) * | 1985-12-11 | 1987-08-11 | ||
JPS62246892A (en) * | 1986-04-17 | 1987-10-28 | 鈴木 敏勝 | Manufacture of organic fertilizer |
JPH02257833A (en) * | 1988-12-27 | 1990-10-18 | Kawasaki Steel Corp | Method for fermentation and apparatus therefor |
-
1992
- 1992-12-29 KR KR1019920025997A patent/KR0141359B1/en not_active IP Right Cessation
-
1993
- 1993-12-28 JP JP33791493A patent/JP2601623B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
KR940013634A (en) | 1994-07-15 |
KR0141359B1 (en) | 1998-06-15 |
JPH06256080A (en) | 1994-09-13 |
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