JPH0731964A - Garbage processor - Google Patents
Garbage processorInfo
- Publication number
- JPH0731964A JPH0731964A JP5182758A JP18275893A JPH0731964A JP H0731964 A JPH0731964 A JP H0731964A JP 5182758 A JP5182758 A JP 5182758A JP 18275893 A JP18275893 A JP 18275893A JP H0731964 A JPH0731964 A JP H0731964A
- Authority
- JP
- Japan
- Prior art keywords
- drying
- air
- drying container
- food waste
- heat exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- 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
Landscapes
- Drying Of Solid Materials (AREA)
- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
(57)【要約】
【目的】乾燥容器及びホッパー内を負圧にすることによ
り、運転中における生ごみの追加投入を可能にすると共
に、脱臭炉におけるバーナへの空気を確保し、かつ、乾
燥容器内への熱風量を増大させる。
【構成】生ごみを乾燥させる乾燥容器3と、バーナ6を
有する脱臭炉7と、脱臭炉7の周囲に形成される第1の
熱交換器8と、第1の熱交換器8に空気を供給する乾燥
用空気供給管23と、乾燥容器3と第1の熱交換器8を
接続する熱風供給管19と、脱臭炉7の排気と乾燥容器
3の排気とを熱交換させる第2の熱交換器9と、乾燥容
器3の排気を前記第2の熱交換器9を経て脱臭炉7に供
給する乾燥用空気排出管20と、乾燥用空気排出管20
に配設され、乾燥容器3の排気の一部をバーナ6に供給
する送風ファンとを備える。
(57) [Summary] [Purpose] Negative pressure inside the drying container and hopper allows additional input of food waste during operation, while ensuring air to the burner in the deodorizing furnace and drying. Increase the amount of hot air into the container. [Structure] A drying container 3 for drying food waste, a deodorizing furnace 7 having a burner 6, a first heat exchanger 8 formed around the deodorizing furnace 7, and air to the first heat exchanger 8. A drying air supply pipe 23 for supplying, a hot air supply pipe 19 for connecting the drying container 3 and the first heat exchanger 8, and a second heat for exchanging heat between the exhaust gas of the deodorizing furnace 7 and the exhaust gas of the drying container 3. An exchanger 9, a drying air discharge pipe 20 for supplying the exhaust air of the drying container 3 to the deodorizing furnace 7 through the second heat exchanger 9, and a drying air discharge pipe 20.
And a blower fan for supplying a part of the exhaust gas of the drying container 3 to the burner 6.
Description
【0001】[0001]
【産業上の利用分野】本発明は、食品工場、ホテル、飲
食店、社員食堂、集合住宅等から出る残飯等の生ごみの
減容化、減量化を図るとともに生ごみの腐敗を防止し、
また、生ごみを肥料、飼料等の原料に再利用可能にする
ための生ごみ処理装置に関する。[Field of Industrial Application] The present invention is intended to reduce the volume and weight of food waste such as leftover food from food factories, hotels, restaurants, employee cafeterias, apartments, etc., and prevent the decay of food waste.
Further, the present invention relates to a food waste processing device for reusing food waste as a raw material such as fertilizer and feed.
【0002】[0002]
【従来の技術】近年、上記残飯等の生ごみは、ユーザ側
においては、腐敗の発生、ごみ置き場面積の増加或いは
処理業者の引き取り手数料の増加等の問題を有し、処理
業者側においては、収集、運搬コストの増大、人手不足
等の問題を有し、さらに、自治体側においては、焼却炉
及び埋立地対策等の問題を有し、生ごみの減容化、減量
化が大きな課題となっている。2. Description of the Related Art In recent years, food waste such as leftover foods has problems such as occurrence of decay on the user side, increase of garbage storage area, and increase of collection fee of a processing company. There are problems such as increase in collection and transportation costs, labor shortage, etc. Furthermore, local governments also have problems such as incinerator and landfill countermeasures, and the reduction of volume and reduction of garbage becomes a major issue. ing.
【0003】従来の生ごみ処理装置を図3により説明す
ると、生ごみ処理装置は、概略、生ごみ投入用のホッパ
ー51、生ごみ供給装置52、乾燥容器53、バーナ5
4を有する脱臭炉55、第1の熱交換器56、第2の熱
交換器57、送風用ファン58からなる。ホッパー51
は開閉蓋59を備え、乾燥容器53内には、図示しない
電動モータにより駆動される回転軸60と回転軸60に
設けられる攪拌部材61とを備えている。乾燥容器53
の下部には、ごみ収納容器62が取付けられ、開閉蓋6
3が配設されている。A conventional food waste processing apparatus will be described with reference to FIG. 3. The food waste processing apparatus is roughly composed of a hopper 51 for inputting food waste, a food waste supply device 52, a drying container 53, and a burner 5.
4, a deodorizing furnace 55, a first heat exchanger 56, a second heat exchanger 57, and a blower fan 58. Hopper 51
The opening / closing lid 59 is provided, and the drying container 53 is provided with a rotating shaft 60 driven by an electric motor (not shown) and a stirring member 61 provided on the rotating shaft 60. Drying container 53
A waste container 62 is attached to the lower part of the
3 are provided.
【0004】バーナー54及び送風用ファン58を運転
すると、外気は第1の熱交換器56において排気管64
を通る空気により加熱され、熱風供給管65を通って乾
燥容器53内に供給されると共に、バーナ54に燃焼用
空気供給管67を通って1次空気として供給される。熱
風は乾燥容器53内で生ごみと接触することにより断熱
冷却され、生ごみの水分を吸収した湿り空気は、乾燥用
空気排出管66を経て第2の熱交換器57に送られ、こ
こで、排気管64を通る排気により加熱された後、バー
ナー54に2次空気として送られる。この2次空気は、
脱臭炉55において、燃焼用空気として用いられると共
に、2次空気に含まれる臭気が加熱分解されて外部に排
気される。一方、生ごみは、ホッパー51に投入され生
ごみ供給装置52にて破砕脱水され、次に、生ごみは乾
燥容器53内に送られ、乾燥容器53内で攪拌部材61
により攪拌され、乾燥容器53内で乾燥された生ごみ
は、開閉蓋63を開くことによりごみ収納容器62内に
収納される。When the burner 54 and the blower fan 58 are operated, outside air is exhausted from the exhaust pipe 64 in the first heat exchanger 56.
It is heated by the air passing therethrough, is supplied into the drying container 53 through the hot air supply pipe 65, and is supplied as primary air to the burner 54 through the combustion air supply pipe 67. The hot air is adiabatically cooled by coming into contact with the food waste in the drying container 53, and the moist air that has absorbed the water content of the food waste is sent to the second heat exchanger 57 via the drying air discharge pipe 66, where After being heated by the exhaust gas passing through the exhaust pipe 64, the secondary air is sent to the burner 54. This secondary air is
In the deodorization furnace 55, the odor contained in the secondary air is decomposed by heating and used as combustion air, and is exhausted to the outside. On the other hand, the food waste is put into the hopper 51, crushed and dehydrated by the food waste supply device 52, and then the food waste is sent into the drying container 53, and the stirring member 61 is placed in the drying container 53.
The food waste that has been stirred by and dried in the drying container 53 is stored in the garbage storage container 62 by opening the opening / closing lid 63.
【0005】ところで、生ごみは各種食品の混合物であ
り、その腐敗、臭気発生の要因は、各食品毎の水分活性
aw により異なる。ここで水分活性aw は、 aw =食品の示す水蒸気圧/空気の飽和水蒸気圧 である。この水分活性aw を0.2〜0.6程度にする
ように乾燥するのがよいとされている。水分活性が少な
すぎると脂質の酸化により変質が促進されるからであ
る。従って、水分活性をある所定値となるように乾燥す
る必要がある。そのために、乾燥容器53の入口温度T
INが一定になるように脱臭炉55の燃焼量を制御し、乾
燥容器53の出口温度TOUT で乾燥状態を把握するよう
にしている。By the way, the food waste is a mixture of various foods, and the factors of spoilage and odor generation thereof differ depending on the water activity aw of each food. Here, the water activity aw is aw = steam pressure of food / saturated steam pressure of air. It is said that it is preferable to dry so that the water activity aw becomes about 0.2 to 0.6. This is because if the water activity is too low, the deterioration of the lipid is promoted by the oxidation of the lipid. Therefore, it is necessary to dry so that the water activity becomes a predetermined value. Therefore, the inlet temperature T of the drying container 53
The combustion amount of the deodorizing furnace 55 is controlled so that IN becomes constant, and the dry state is grasped by the outlet temperature T OUT of the drying container 53.
【0006】これを図4により説明する。図4は湿り空
気線図を示し、tは乾球温度(℃)、Xは絶対湿度(x
g/kgAir)、ψは相対湿度(%)を示している。
例えば、生ごみの水分活性を0.3まで乾燥するのであ
れば、乾燥容器53の出口の湿り空気の相対湿度を30
%にすればよい。また、外気の温度が30℃、相対湿度
が80%(図のA点)とすれば、これを第1の熱交換器
56で等絶対湿度線Bに沿って120℃まで加熱し(図
のC点)、乾燥容器53内では、断熱冷却線Dにそって
冷却され定常状態では40℃のE点で飽和空気となる。
生ごみの乾燥が進み水分活性が低下すると、出口空気温
度は上昇し相対湿度が30%と交わる点Fの温度65℃
が、乾燥容器53の出口温度となる。すなわち、生ごみ
の水分活性を0.3とするには、乾燥容器53の出口温
度がF点の温度となった時点で乾燥を終了させればよ
い。This will be described with reference to FIG. FIG. 4 shows a moist air diagram, where t is the dry-bulb temperature (° C.), X is the absolute humidity (x
g / kg Air), ψ indicates relative humidity (%).
For example, if the water activity of food waste is dried to 0.3, the relative humidity of the humid air at the outlet of the drying container 53 is set to 30.
You can set it to%. If the outside air temperature is 30 ° C. and the relative humidity is 80% (point A in the figure), this is heated to 120 ° C. along the iso-absolute humidity line B by the first heat exchanger 56 (see the figure). (Point C), inside the drying container 53, the air is cooled along the adiabatic cooling line D and becomes saturated air at point E at 40 ° C. in a steady state.
When the garbage is dried and the water activity decreases, the outlet air temperature rises and the relative humidity crosses 30%.
Becomes the outlet temperature of the drying container 53. That is, in order to set the water activity of raw garbage to 0.3, the drying may be terminated when the outlet temperature of the drying container 53 reaches the temperature of point F.
【0007】[0007]
【発明が解決しようとする課題】しかしながら、上記従
来の生ごみ処理装置においては、送風ファン58が乾燥
容器53の上流側に配設されており、乾燥容器及びホッ
パー内は加圧状態のため、運転中に開閉蓋59を開ける
と、熱風供給管65から乾燥容器53内に供給される熱
風がホッパー51から外部に流れて臭気が漏れてしまう
という問題を有している。また、燃焼用空気供給管67
へ流れる空気が減少するため、脱臭炉55におけるバー
ナ54の燃焼が悪化し、臭気やスス等が発生してしまう
という問題を有している。その結果、運転中に開閉蓋5
9を開けて生ごみを追加投入することができなかった。However, in the above-mentioned conventional food waste processing apparatus, the blower fan 58 is disposed on the upstream side of the drying container 53, and since the inside of the drying container and the hopper are in a pressurized state, If the opening / closing lid 59 is opened during the operation, there is a problem that the hot air supplied from the hot air supply pipe 65 into the drying container 53 flows from the hopper 51 to the outside and the odor leaks. In addition, the combustion air supply pipe 67
Since the amount of air flowing into the burner 54 decreases, the combustion of the burner 54 in the deodorizing furnace 55 deteriorates, and there is a problem that odors, soot, and the like are generated. As a result, the lid 5 can be opened and closed during operation.
It was not possible to open 9 and add additional garbage.
【0008】本発明は上記問題を解決するものであっ
て、乾燥容器及びホッパー内を負圧にすることにより、
運転中における生ごみの追加投入を可能にすると共に、
脱臭炉におけるバーナへの空気を確保し、かつ、乾燥容
器内への熱風量を増大させることができる生ごみ処理装
置を提供することを目的とする。The present invention is to solve the above-mentioned problems, and by making the inside of the drying container and the hopper a negative pressure,
In addition to enabling the addition of food waste during operation,
It is an object of the present invention to provide a food waste processing device which can secure air to a burner in a deodorizing furnace and can increase the amount of hot air into the drying container.
【0009】[0009]
【課題を解決するための手段】そのために本発明の生ご
み処理装置は、生ごみを乾燥させる乾燥容器3と、バー
ナ6を有する脱臭炉7と、脱臭炉7の周囲に形成される
第1の熱交換器8と、第1の熱交換器8に空気を供給す
る乾燥用空気供給管23と、乾燥容器3と第1の熱交換
器8を接続する熱風供給管19と、脱臭炉7の排気と乾
燥容器3の排気とを熱交換させる第2の熱交換器9と、
乾燥容器3の排気を前記第2の熱交換器9を経て脱臭炉
7に供給する乾燥用空気排出管20と、乾燥用空気排出
管20に配設され、乾燥容器3の排気の一部をバーナ6
に供給する送風ファンとを備えることを特徴とする。な
お、上記構成に付加した番号は、本発明の理解を容易に
するために図面と対比させるためのもので、これにより
本発明の構成が何ら限定されるものではない。For this purpose, the apparatus for treating food waste according to the present invention comprises a drying container 3 for drying food waste, a deodorizing furnace 7 having a burner 6, and a first device formed around the deodorizing furnace 7. Heat exchanger 8, a drying air supply pipe 23 that supplies air to the first heat exchanger 8, a hot air supply pipe 19 that connects the drying container 3 and the first heat exchanger 8, and a deodorizing furnace 7 A second heat exchanger 9 for exchanging heat between the exhaust of the air and the exhaust of the drying container 3,
The drying air exhaust pipe 20 for supplying the exhaust air of the drying container 3 to the deodorizing furnace 7 via the second heat exchanger 9 and the drying air exhaust pipe 20 are arranged so that a part of the exhaust gas of the drying container 3 is exhausted. Burner 6
And a blower fan for supplying to the. It should be noted that the numbers added to the above-mentioned configurations are for comparison with the drawings in order to facilitate understanding of the present invention, and the configurations of the present invention are not limited thereby.
【0010】[0010]
【作用】本発明においては、例えば図1に示すように、
送風ファン10が乾燥容器3の下流側に設けられている
ため、運転中は、ホッパー1及び乾燥容器3内は負圧と
なり、ホッパー1内に乾燥容器3内の熱風が吹き出すこ
とがなく、運転中における生ごみの追加投入が可能にな
る。また、脱臭炉7おけるバーナ6への空気を確保し、
かつ、乾燥容器3内への熱風量を増大させることができ
る。In the present invention, for example, as shown in FIG.
Since the blower fan 10 is provided on the downstream side of the drying container 3, a negative pressure is generated in the hopper 1 and the drying container 3 during operation, and the hot air in the drying container 3 does not blow into the hopper 1 and the operation is performed. It is possible to add additional garbage inside. Also, secure air to the burner 6 in the deodorization furnace 7,
Moreover, the amount of hot air flowing into the drying container 3 can be increased.
【0011】[0011]
【実施例】以下、本発明の実施例を図面を参照しつつ説
明する。図1は、本発明における生ごみ処理装置の1実
施例を示す構成図である。本発明の生ごみ処理装置は、
概略、生ごみ投入用のホッパー1、生ごみ供給装置2、
乾燥容器3、フィルタ4、生ごみ収納容器5、バーナ6
を有する脱臭炉7、脱臭炉7の周囲に形成される第1の
熱交換器8、第2の熱交換器9、送風用ファン10、燃
料タンク11、燃料ポンプ12、点火装置13、制御装
置14からなる。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a block diagram showing an embodiment of a food waste processing device according to the present invention. The garbage processing device of the present invention,
Outline, hopper 1 for inputting food waste, food waste supply device 2,
Drying container 3, filter 4, food waste container 5, burner 6
Deodorizing furnace 7 having a heater, a first heat exchanger 8 formed around the deodorizing furnace 7, a second heat exchanger 9, a blower fan 10, a fuel tank 11, a fuel pump 12, an ignition device 13, and a controller. It consists of 14.
【0012】生ごみ投入用のホッパー1は開閉蓋15を
備える。ホッパー1の下部には生ごみ供給装置2が装着
され、生ごみ供給装置2の下部は排水弁18に接続され
ている。生ごみ供給装置2は、乾燥容器3の下部側面の
開口3aに接続されており電動モータM1により駆動さ
れ、ホッパー1からの生ごみを乾燥容器3内へ搬送す
る。乾燥容器3内には、電動モータM2により駆動され
る攪拌部材16が設けられる。乾燥容器3の下部には、
生ごみ排出用開閉蓋17が設けられ、乾燥された生ごみ
を収納容器5に排出可能にしている。The hopper 1 for throwing in garbage has an opening / closing lid 15. A raw garbage supply device 2 is attached to a lower portion of the hopper 1, and a lower portion of the raw garbage supply device 2 is connected to a drain valve 18. The raw garbage supply device 2 is connected to the opening 3a on the lower side surface of the drying container 3 and is driven by the electric motor M1 to convey the raw garbage from the hopper 1 into the drying container 3. A stirring member 16 driven by an electric motor M2 is provided in the drying container 3. At the bottom of the drying container 3,
An open / close lid 17 for discharging raw garbage is provided so that dried raw garbage can be discharged into the storage container 5.
【0013】乾燥容器3の上部には、熱風供給管19が
接続され、乾燥空気供給管23、第1の熱交換器8を経
て乾燥容器3内に熱風が供給される。乾燥容器3の上部
の熱風供給管19に対向する位置には、フィルタ4及び
乾燥空気排出管20が接続され、フィルタ4の下流側に
送風ファン10が配設されている。この送風ファン10
により、乾燥空気の一部は、第2の熱交換器9におい
て、脱臭炉7からの排気管21の排気により加熱された
後、脱臭炉7内に燃焼用2次空気として供給され、乾燥
空気の一部は、燃焼用空気供給管22を通ってバーナ6
に1次空気として供給される。バーナ6には、燃料ポン
プ12により燃料タンク11から燃料が供給される。第
1及び第2の熱交換器8、9、熱風供給管19等は、保
温材27で被覆されている。脱臭炉7内には火炎検知セ
ンサ24が設けられ、乾燥容器3の入口側と出口側に
は、それぞれ温度センサTIN、TOUT が配設され、それ
ぞれ制御装置14に接続されている。A hot air supply pipe 19 is connected to the upper part of the drying container 3, and hot air is supplied into the drying container 3 through the dry air supply pipe 23 and the first heat exchanger 8. The filter 4 and the dry air discharge pipe 20 are connected to a position facing the hot air supply pipe 19 in the upper part of the drying container 3, and the blower fan 10 is arranged on the downstream side of the filter 4. This blower fan 10
As a result, a part of the dry air is heated in the second heat exchanger 9 by the exhaust gas from the exhaust pipe 21 from the deodorizing furnace 7, and then supplied as the secondary air for combustion into the deodorizing furnace 7 to obtain the dry air. Part of the burner 6 passes through the combustion air supply pipe 22.
Is supplied as primary air. Fuel is supplied to the burner 6 from a fuel tank 11 by a fuel pump 12. The first and second heat exchangers 8 and 9, the hot air supply pipe 19 and the like are covered with a heat insulating material 27. A flame detection sensor 24 is provided in the deodorizing furnace 7, and temperature sensors T IN and T OUT are provided on the inlet side and the outlet side of the drying container 3, respectively, and are connected to the controller 14.
【0014】図2は、図1における生ごみ処理装置の具
体的構成の1例を示し、図2(A)は内部を示す正面
図、図2(B)、図2(C)は、それぞれ図2(A)の
B方向及びC方向から見た図である。なお、図1と同一
の構成については同一番号を付して説明を省略する。図
中、30はハウジング、31は電動モータM2用の減速
機、32は電動モータM1の動力を生ごみ供給装置2に
伝達させるための伝動ベルト又はチェーンである。FIG. 2 shows an example of a specific structure of the food waste processing apparatus in FIG. 1. FIG. 2 (A) is a front view showing the inside, and FIGS. 2 (B) and 2 (C) are respectively, It is the figure seen from the B direction and C direction of FIG. 2 (A). The same components as those in FIG. 1 are designated by the same reference numerals and the description thereof will be omitted. In the figure, 30 is a housing, 31 is a speed reducer for the electric motor M2, and 32 is a transmission belt or chain for transmitting the power of the electric motor M1 to the food waste feeder 2.
【0015】次に、上記構成からなる本発明における生
ごみ処理方法について説明する。バーナ6及び送風用フ
ァン10を運転すると、外気は、乾燥用空気供給管23
から第1の熱交換器8において脱臭炉7の熱により加熱
され、熱風供給管19を経て乾燥容器3内に吸引され
る。この高温空気は、乾燥容器3内で生ごみと接触する
ことにより断熱冷却され、生ごみの水分を吸収した湿り
空気は、乾燥空気排出管20を経て第2の熱交換器9に
送られ、ここで、排気管21を通る排気により加熱され
た後、脱臭炉7に2次空気として送られる。この2次空
気は、脱臭炉7において、燃焼用空気として用いられる
と共に、排出空気に含まれる臭気は加熱分解されて外部
に排気される。Next, the method of treating food waste according to the present invention having the above-mentioned structure will be described. When the burner 6 and the blower fan 10 are operated, outside air is supplied to the drying air supply pipe 23.
Is heated by the heat of the deodorizing furnace 7 in the first heat exchanger 8 and is sucked into the drying container 3 through the hot air supply pipe 19. This high temperature air is adiabatically cooled by coming into contact with food waste in the drying container 3, and the moist air that has absorbed the water content of the food waste is sent to the second heat exchanger 9 via the dry air discharge pipe 20. Here, after being heated by the exhaust gas passing through the exhaust pipe 21, it is sent to the deodorizing furnace 7 as secondary air. This secondary air is used as combustion air in the deodorizing furnace 7, and the odor contained in the exhaust air is thermally decomposed and exhausted to the outside.
【0016】一方、生ごみは、ホッパー1に投入され、
電動モータM1により駆動される生ごみ供給装置2によ
り搬送されて開口3aから乾燥容器3内に供給される。
次いで、生ごみは、乾燥容器3内で電動モータM2によ
り駆動される攪拌部材16により破砕、攪拌し、乾燥さ
れる。乾燥が終了した生ごみは、排出用開閉蓋17を開
くことにより、ごみ収納容器5内に収納される。本発明
によれば、送風ファン10が乾燥容器3の下流側に設け
られているため、運転中は、ホッパー1及び乾燥容器3
内は負圧となり、ホッパー1内に乾燥容器3内の熱風が
吹き出すことがなく、運転中における生ごみの追加投入
が可能になる。また、脱臭炉7おけるバーナ6への空気
を確保し、かつ、乾燥容器3内への熱風量を増大させる
ことができ、乾燥処理速度を従来と比較して20〜30
%程度向上させることができる。On the other hand, food waste is thrown into the hopper 1,
The food waste is fed by the food waste feeding device 2 driven by the electric motor M1 and fed into the drying container 3 through the opening 3a.
Next, the food waste is crushed and stirred by the stirring member 16 driven by the electric motor M2 in the drying container 3, and dried. The dried garbage is stored in the garbage container 5 by opening the discharge opening / closing lid 17. According to the present invention, since the blower fan 10 is provided on the downstream side of the drying container 3, the hopper 1 and the drying container 3 are in operation during operation.
The inside becomes a negative pressure, and the hot air in the drying container 3 does not blow out into the hopper 1, so that it is possible to add additional food waste during operation. Further, it is possible to secure the air to the burner 6 in the deodorization furnace 7 and increase the amount of hot air into the drying container 3, and the drying processing speed is 20 to 30 compared with the conventional one.
% Can be improved.
【0017】[0017]
【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、乾燥容器及びホッパー内を負圧にすることによ
り、運転中における生ごみの追加投入を可能にすると共
に、脱臭炉におけるバーナへの空気を確保し、かつ、乾
燥容器内への熱風量を増大させることができる。As is apparent from the above description, according to the present invention, by adding negative pressure to the inside of the drying container and the hopper, it is possible to add raw garbage during operation and to burner in the deodorizing furnace. It is possible to secure air to the drying container and increase the amount of hot air into the drying container.
【図1】本発明の生ごみ処理装置の1実施例を示す構成
図である。FIG. 1 is a configuration diagram showing one embodiment of a food waste processing device of the present invention.
【図2】図1における生ごみ処理装置の具体的構成の1
例を示し、図2(A)は内部を示す正面図、図2
(B)、図2(C)は、それぞれ図2(A)のB方向及
びC方向から見た図である。FIG. 2 is a specific configuration 1 of the food waste processing device in FIG.
FIG. 2A shows an example, and FIG.
2B and FIG. 2C are views respectively viewed from the B direction and the C direction in FIG. 2A.
【図3】従来の生ごみ処理装置を示す構成図である。FIG. 3 is a configuration diagram showing a conventional food waste processing device.
【図4】生ごみ処理方法を説明するための湿り空気線図
である。FIG. 4 is a moist air diagram for explaining the method of treating food waste.
1…生ごみ投入用のホッパー、2…生ごみ供給装置、3
…乾燥容器 5…生ごみ収納容器、6…バーナ、7…脱臭炉、8…第
1の熱交換器 9…第2の熱交換器、10…送風用ファン、16…攪拌
部材 19…熱風供給管、20…乾燥空気排出管、21…排気
管 22…燃焼用空気供給管、23…乾燥用空気供給管1 ... Hopper for inputting garbage, 2 ... Garbage feeding device, 3
... Drying container 5 ... Raw food storage container, 6 ... Burner, 7 ... Deodorizing furnace, 8 ... First heat exchanger 9 ... Second heat exchanger, 10 ... Blower fan, 16 ... Stirring member 19 ... Hot air supply Pipe, 20 ... Dry air discharge pipe, 21 ... Exhaust pipe 22 ... Combustion air supply pipe, 23 ... Drying air supply pipe
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F26B 21/00 M 9140−3L (72)発明者 山根昭寛 埼玉県入間郡大井町西鶴ケ岡一丁目3番1 号 東燃株式会社総合研究所内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Internal reference number FI Technical display location F26B 21/00 M 9140-3L (72) Inventor Akihiro Yamane Nishitsurugaoka 1-chome, Oi-cho, Iruma-gun, Saitama Prefecture No. 3 No. 1 within Tonen Corporation Research Institute
Claims (1)
有する脱臭炉と、該脱臭炉の周囲に形成される第1の熱
交換器と、該第1の熱交換器に空気を供給する乾燥用空
気供給管と、前記乾燥容器と第1の熱交換器を接続する
熱風供給管と、前記脱臭炉の排気と乾燥容器の排気とを
熱交換させる第2の熱交換器と、前記乾燥容器の排気を
前記第2の熱交換器を経て脱臭炉に供給する乾燥用空気
排出管と、該乾燥用空気排出管に配設され、乾燥容器の
排気の一部を前記バーナに供給する送風ファンとを備え
ることを特徴とする生ごみ処理装置。1. A drying container for drying food waste, a deodorizing furnace having a burner, a first heat exchanger formed around the deodorizing furnace, and air is supplied to the first heat exchanger. A drying air supply pipe, a hot air supply pipe connecting the drying container and the first heat exchanger, a second heat exchanger for exchanging heat between the exhaust of the deodorizing furnace and the exhaust of the drying container, and the drying A drying air exhaust pipe for supplying the exhaust air of the container to the deodorizing furnace through the second heat exchanger, and a blower provided for the drying air exhaust pipe and supplying a part of the exhaust gas of the drying container to the burner. A food waste processing device comprising a fan.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5182758A JPH0731964A (en) | 1993-07-23 | 1993-07-23 | Garbage processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5182758A JPH0731964A (en) | 1993-07-23 | 1993-07-23 | Garbage processor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0731964A true JPH0731964A (en) | 1995-02-03 |
Family
ID=16123923
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5182758A Pending JPH0731964A (en) | 1993-07-23 | 1993-07-23 | Garbage processor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0731964A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003004376A (en) * | 2001-06-25 | 2003-01-08 | Azusaa:Kk | Drying apparatus and method for producing fertilizer using the drying apparatus |
-
1993
- 1993-07-23 JP JP5182758A patent/JPH0731964A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003004376A (en) * | 2001-06-25 | 2003-01-08 | Azusaa:Kk | Drying apparatus and method for producing fertilizer using the drying apparatus |
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