JP2607304Y2 - Drying equipment for hydrous organic matter - Google Patents

Drying equipment for hydrous organic matter

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Publication number
JP2607304Y2
JP2607304Y2 JP1993032520U JP3252093U JP2607304Y2 JP 2607304 Y2 JP2607304 Y2 JP 2607304Y2 JP 1993032520 U JP1993032520 U JP 1993032520U JP 3252093 U JP3252093 U JP 3252093U JP 2607304 Y2 JP2607304 Y2 JP 2607304Y2
Authority
JP
Japan
Prior art keywords
heating
heat
organic matter
water
fermentation
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
JP1993032520U
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Japanese (ja)
Other versions
JPH0685100U (en
Inventor
好美 篠原
Original Assignee
篠原精機株式会社
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Application filed by 篠原精機株式会社 filed Critical 篠原精機株式会社
Priority to JP1993032520U priority Critical patent/JP2607304Y2/en
Publication of JPH0685100U publication Critical patent/JPH0685100U/en
Application granted granted Critical
Publication of JP2607304Y2 publication Critical patent/JP2607304Y2/en
Anticipated expiration legal-status Critical
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Classifications

    • 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

Landscapes

  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案は例えば余剰汚泥,畜糞,
鶏糞,パルプ及びその残渣,食品残渣等の水分を含有し
た有機物を、自身の発酵熱又は/及び酸化熱を利用して
乾燥する乾燥装置に関するものである。
[Industrial application fields] The present invention relates to, for example, excess sludge, animal dung,
The present invention relates to a drying apparatus for drying water-containing organic substances such as chicken dung, pulp and its residues, food residues, etc. using its own fermentation heat and / or oxidation heat.

【0002】[0002]

【従来の技術】従来より、汚泥、家畜糞尿等の比較的高
含水率の原料を発酵、乾燥させて堆肥(コンポジット)
化する装置に関しては、出願人は実開昭58−4214
0号、特開昭58−204893号、実公平2−304
19号等の多くの提案をなしてきた。これらの提案に係
る技術は、各々見張るべき効果を上げている。
2. Description of the Related Art Conventionally, raw materials having a relatively high water content, such as sludge and livestock manure, are fermented and dried to form a compost.
With regard to the device to be converted, the applicant has disclosed in
No. 0, JP-A-58-204893, and Jitsuho 2-304
Many proposals such as No. 19 have been made. The technologies according to these proposals have each produced significant effects.

【0003】ところで、先の提案は、汚泥、家畜糞尿等
の比較的高含水率の原料を発酵、乾燥させて堆肥化する
ことを目的としている。この堆肥化に要する時間は、最
も条件のよい時には、10時間以内という驚異的な短時
間で可能となっているが、原料の含水率の不均一による
処理時間の変動、これに伴う堆肥の処理ロット毎の不均
一性が一部に問題となっている。
[0003] The above proposal aims at composting fermented and dried raw materials having a relatively high water content, such as sludge and livestock manure. The time required for this composting can be astonishingly short, within 10 hours, under the best conditions. However, the processing time fluctuates due to the unevenness of the water content of the raw materials, and the compost processing accompanying this. The non-uniformity between lots is partly a problem.

【0004】また、汚泥、家畜糞尿等の原料の排出量の
急激な増加には、この短時間での堆肥化も追い付かない
場合もあった。この場合には、堆肥化装置の増設又は大
型化するしか解決の方法がないのが現状である。一方、
高含水率の原料の完全な堆肥化を行わずとも、高含水率
の原料の乾燥を行うことで、汚泥、家畜糞尿等の原料の
排出量の急激な増加に対応する要望もあった。
[0004] In addition, this rapid composting may not catch up with the rapid increase in the amount of raw materials such as sludge and livestock manure. In this case, the only solution is to increase the size or size of the composting device. on the other hand,
There has also been a demand for responding to a rapid increase in the discharge of raw materials such as sludge and livestock manure by drying the raw materials having a high water content without completely composting the raw materials having a high water content.

【0005】[0005]

【考案が解決しようとする課題】本考案は、水分を含有
した有機物を、自身の発酵熱又は/及び酸化熱を利用し
て乾燥する乾燥装置を得ることを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a drying apparatus for drying organic matter containing water by using its own fermentation heat and / or oxidation heat.

【0006】[0006]

【課題を解決するための手段】本考案に係る含水有機物
用乾燥装置では、余剰汚泥,畜糞,鶏糞,パルプ及びそ
の残渣,食品残渣等の水分を含有した有機物の発酵熱又
は/及び酸化熱を利用した乾燥機であって、内部に前記
有機物を気密保持して撹拌回動可能な缶体と、前記缶体
内部を加熱する加熱手段と、前記缶体内部を減圧状態に
保持する吸引手段と、前記缶体内部の減圧状態を維持し
たまま外気を前記缶体内部の有機物に供給する給気手段
と、前記缶体内部で発生した余剰熱を取出す熱交換手段
とを備えた含水有機物用乾燥装置において、前記缶体
は、内部に熱媒が流れる二重壁構造を有し、前記加熱手
段は、前記二重壁構造の内部に熱媒を供給すると共に、
該熱媒の加熱を、前記有機物中の発酵に関与する微生物
が生存可能な温度に缶体内部を加熱する低温加熱と、1
00℃以上の高温に缶体内部を加熱する高温加熱とに選
定可能なボイラーを備え、前記吸引手段及び給気手段
は、少なくとも前記加熱手段によって100℃以上の高
温に缶体内部を加熱する高温加熱を選択する際に、前記
缶体内部の減圧状態を維持したまま外気を缶体内部の有
機物に供給するものであり、前記熱媒が供給される二重
壁構造が前記熱交換手段を兼ねているものである。
SUMMARY OF THE INVENTION In the drying apparatus for water-containing organic matter according to the present invention, the heat of fermentation and / or oxidation of water-containing organic matter such as excess sludge, animal dung, chicken dung, pulp and its residue, and food residue is reduced. A drier that uses the can body, which can stir and rotate while keeping the organic substance airtight, a heating unit that heats the inside of the can body, and a suction unit that holds the inside of the can body in a reduced pressure state. A water supply means for supplying outside air to the organic matter inside the can body while maintaining the reduced pressure state inside the can body, and a heat exchange means for removing excess heat generated inside the can body, for drying water-containing organic matter. In the apparatus, the can body has a double-walled structure in which a heating medium flows, and the heating unit supplies a heating medium to the inside of the double-walled structure,
The heating of the heat medium includes low-temperature heating for heating the inside of the can body to a temperature at which microorganisms involved in fermentation in the organic matter can survive;
A boiler which can be selected for high-temperature heating for heating the inside of the can body to a high temperature of 00 ° C. or more, wherein the suction means and the air supply means are provided.
Is at least 100 ° C. or higher by the heating means.
When selecting high-temperature heating to heat the inside of the can body to the temperature,
While maintaining the reduced pressure inside the can body, open the outside air inside the can body.
The double-walled structure to which the heat medium is supplied also serves as the heat exchange means.

【0007】好ましくは、前記吸引手段に連通された脱
臭手段を備えたものを開示する。
[0007] Preferably, a device having a deodorizing means connected to the suction means is disclosed.

【0008】[0008]

【作用】本考案においては、内部に有機物を気密保持し
て攪拌回動可能な缶体と、乾燥処理初期に前記缶体を加
熱する加熱手段と、前記缶体内部を減圧状態に保持する
吸引手段と、前記缶体内部の減圧状態を維持したまま外
気を前記有機物に供給する給気手段と、前記缶体内部で
発生した余剰熱を取出す熱交換手段とを備えたものであ
るため、水分を含有した有機物を、自身の発酵熱又は/
及び酸化熱を利用して乾燥することができる。
According to the present invention, a can body which can stir and rotate while keeping an organic substance airtight therein, a heating means for heating the can body in the early stage of the drying process, and a suction for keeping the inside of the can body in a reduced pressure state. Means, an air supply means for supplying outside air to the organic matter while maintaining the reduced pressure inside the can body, and a heat exchange means for extracting excess heat generated inside the can body, The organic matter containing
And drying using heat of oxidation.

【0009】即ち、吸引手段と吸気手段とにより、減圧
状態で有機物に空気が送り込まれるため、含有された水
分が良好に蒸発する。更に加えて、加熱手段によって初
発から発酵に関与する微生物の有機物の分解(即ち、発
酵)による発酵熱や、有機物の酸素との化学的な結合
(即ち、酸化)による酸化熱を発生させるため、これが
含有された水分の蒸発のための熱となり、含水有機物を
良好に乾燥することができる。
That is, since air is sent into the organic matter under reduced pressure by the suction means and the suction means, the contained water evaporates well. In addition, in order to generate heat of fermentation by decomposing organic substances of microorganisms involved in fermentation (i.e., fermentation) and heat of oxidation by chemical bonding of organic substances with oxygen (i.e., oxidation) by the heating means, This serves as heat for evaporating the contained water, and the hydrated organic matter can be dried well.

【0010】また、発酵熱や酸化熱の余剰熱が発生した
場合には、熱交換手段により取出される。
When surplus heat such as fermentation heat or oxidation heat is generated, the heat is removed by heat exchange means.

【0011】また、加熱手段は、好ましくは発酵に関与
する微生物が生存可能な温度に加熱する低温加熱と、1
00℃以上の高温に加熱する高温加熱との選定が可能で
ある。即ち、乾燥処理初期に低温加熱すると、発酵に関
与する微生物が含水有機物を分解して、発酵熱を出して
乾燥・堆肥化を行うことができる。
The heating means preferably includes a low-temperature heating for heating microorganisms involved in fermentation to a viable temperature;
It is possible to select high-temperature heating in which heating is performed to a high temperature of 00 ° C. or more. That is, when heating at a low temperature in the early stage of the drying treatment, the microorganisms involved in the fermentation decompose the water-containing organic matter, generate heat of fermentation, and perform drying and composting.

【0012】また、乾燥処理初期に100℃以上に加熱
すると、給気手段により、有機物内に供給された酸素は
有機物と化学反応して結合(即ち、酸化)し、酸化熱を
放出して低温加熱に比べて短時間で乾燥を行うことがで
きる。
When heated to 100 ° C. or higher in the early stage of the drying process, oxygen supplied into the organic matter is chemically reacted with the organic matter and bonded (ie, oxidized) by the air supply means, and the heat of oxidation is released to lower the temperature to a low temperature. Drying can be performed in a shorter time than heating.

【0013】本装置で用いる水分を含有した有機物と
は、具体的には、余剰汚泥,畜糞,鶏糞,パルプ及びそ
の残渣,食品残渣等の比較的高い水分を含有した有機物
であるが、特に高温加熱を行うならば、表面をプラスチ
ックコートした紙類も乾燥処理可能である。
The organic matter containing water used in the present apparatus is, specifically, an organic matter containing relatively high water content such as excess sludge, animal dung, chicken dung, pulp and its residue, and food residue. If heating is performed, papers with plastic-coated surfaces can be dried.

【0014】即ち、好ましいことに、表面をプラスチッ
クコートした紙類は、攪拌されながら乾燥されるため、
プラスチックコートが紙と分離し、しかも、プラスチッ
クの粒状となって乾燥されるため、乾燥後のプラスチッ
クと紙との分離が容易に行われることとなる。
That is, preferably, papers with plastic coated surfaces are dried with stirring.
Since the plastic coat is separated from the paper and further dried in the form of plastic granules, separation of the dried plastic from the paper is facilitated.

【0015】また、缶体を加熱する加熱手段としては、
温熱ボイラー(60〜90℃),蒸気ボイラー(100
〜160℃),熱媒ボイラー(0〜130℃,0〜30
0℃)等があるが、本考案では、缶体の二重壁構造の内
部に熱媒を供給すると共に、この熱媒の加熱を、有機物
中の発酵に関与する微生物が生存可能な温度に缶体内部
を加熱する低温加熱と、100℃以上の高温に缶体内部
を加熱する高温加熱とに選定可能なボイラーとして、好
ましくは熱媒ボイラーを使用する。
The heating means for heating the can body includes:
Heated boiler (60-90 ° C), steam boiler (100
-160 ° C), heat medium boiler (0-130 ° C, 0-30
0 ° C) , but in the present invention, the double wall structure of the can
The heating medium is supplied to the part and the heating of the heating medium is
Inside the can at a temperature at which microorganisms involved in fermentation can survive
Heating the inside of the can body to low temperature heating and heating to over 100 ° C
As a boiler that can be selected for high-temperature heating
Preferably, a heating medium boiler is used.

【0016】何故なら、温熱ボイラーでは高温加熱の際
に、缶内の温度が100℃以上に上昇することが難し
く、蒸気ボイラーでは発酵熱・酸化熱による余剰熱を有
効利用する際に、別の熱交換手段を必要とするため、好
ましくは、熱媒ボイラーを用いる。これにより、高温加
熱を容易に行い、しかも余剰熱を有効利用する際の熱交
換手段の熱媒として用いることができる。
This is because it is difficult for the heat boiler to raise the temperature in the can to 100 ° C. or more during high-temperature heating, and in the steam boiler, when the excess heat due to fermentation heat and oxidation heat is used effectively, another Since a heat exchange means is required, a heat medium boiler is preferably used. Thus , high-temperature heating can be easily performed, and the excess heat can be used as a heat medium of a heat exchange unit when the heat is effectively used.

【0017】また、吸引手段に連通された脱臭手段は、
物理的・化学的脱臭法を用いて排気中の臭気を脱臭す
る。好ましくは、溶岩石脱臭や土壌脱臭等が用いられ
る。溶岩石脱臭とは、脱臭塔に溶岩石を充填し、これに
水を散布して溶岩石表層面及び気孔中に細菌を繁殖させ
て脱気するものである。この溶岩脱臭塔に塔下部から排
気と曝気とを通し上部で放出している。溶岩石には、多
数の気孔が形成されており、この溶岩石の気孔が臭気を
封じ込める。また、溶岩石は永久的に使用が可能であ
る。
Further, the deodorizing means connected to the suction means includes:
Deodorizes odors in exhaust air using physical and chemical deodorization methods. Preferably, lava rock deodorization and soil deodorization are used. Lava stone deodorization refers to filling a deodorization tower with lava stone, spraying water on the deodorization tower, and propagating bacteria on the surface of the lava stone and in pores to deaerate. The lava deodorization tower passes exhaust and aeration from the lower part of the tower and discharges it at the upper part. Lava rock has a large number of pores formed therein, and the pores of the lava contain odor. Lava stones can be used permanently.

【0018】また、土壌脱臭とは、土中に幾つもの排気
口を形成した配管を埋設し、排気口から排出される排気
が土中の細菌によって臭気を分解されるものである。
[0018] Soil deodorization refers to burying a pipe having a number of exhaust ports formed in the soil and decomposing the exhaust gas discharged from the exhaust port by bacteria in the soil.

【0019】[0019]

【実施例】図1は本考案の含水有機物用乾燥装置の一実
施例の構成を示す説明図である。図に示す通り、投入ホ
ッパ(1) から投入された有機物を内部に気密保持する缶
体(2) がある。この缶体(2) は電動機(3) とギア(4)
(4') とを介して缶体(2) 側面の下部に設けられた案内
ロール(5) 上を回動可能に設けられている。
FIG. 1 is an explanatory view showing the structure of an embodiment of a drying apparatus for a water-containing organic substance of the present invention. As shown in the figure, there is a can body (2) for keeping the organic matter supplied from the charging hopper (1) airtight. This can (2) consists of a motor (3) and a gear (4)
(4 '), and is rotatably provided on a guide roll (5) provided at the lower portion of the side surface of the can (2).

【0020】缶体(2) の側壁は二重構造になっており、
二重構造の内部には乾燥処理初期に前記缶体(2) を加熱
する熱媒ボイラー(加熱手段)(6) から缶体の一方の回
動軸のロータリージョイント(7) を介して熱媒が循環ポ
ンプ(8) によって循環されている。
The side wall of the can (2) has a double structure,
Inside the double structure, a heating medium boiler (heating means) (6), which heats the can (2) at the beginning of the drying process, passes through a rotary joint (7) of one rotating shaft of the can to heat the heating medium. Is circulated by the circulation pump (8).

【0021】他方の回動軸には、缶体(2) 内部の上部位
置で固定された吸引口(9) に連通した吸引ポンプ(吸引
手段)(10)と、缶体(2) 内部の減圧状態を維持しつつ外
気を缶体(2) 内部の下部位置で固定された有機物に供給
する給気ノズル(給気手段)(11)とが備わっている。ま
た、吸引ポンプ(10)に連通する配管(12)と給気ノズル(1
1)に連通する配管(13)とは、途中の熱交換機(14)によっ
て熱交換が行われ、缶体(2) 内部の熱を外部から入る空
気に与え、熱を有効に利用している。
The other rotary shaft has a suction pump (suction means) (10) communicating with a suction port (9) fixed at an upper position inside the can (2), and a suction pump (10) inside the can (2). An air supply nozzle (air supply means) (11) for supplying the outside air to the organic matter fixed at a lower position inside the can (2) while maintaining the reduced pressure state is provided. Also, the pipe (12) communicating with the suction pump (10) and the air supply nozzle (1
With the pipe (13) communicating with 1), heat is exchanged by the heat exchanger (14) on the way, and the heat inside the can (2) is given to the air entering from the outside, and the heat is used effectively .

【0022】この乾燥装置は、密閉できる構造の缶体
(2) の内部に、含水有機物を投入し、この含水有機物を
缶体(2) の回動で攪拌しながら乾燥処理初期では加熱
し、更に水分の発散を容易にするために吸引ポンプによ
り内部の空気及び蒸気を吸引除去して内部の空気圧を減
少させ、且つ排出空気と熱交換して暖められた空気を、
缶体内部を一定の負圧に保ったまま原料に吹き付けるよ
うに吸入する。
This drying device is a can body having a structure that can be sealed.
Into (2), water-containing organic matter is charged, and the water-containing organic matter is heated in the initial stage of the drying process while being stirred by rotating the can (2), and is further internally sucked by a suction pump to facilitate diffusion of water. Air and steam are removed by suction to reduce the internal air pressure, and heat exchanged with the exhaust air to heat the heated air,
While the inside of the can is maintained at a constant negative pressure, suction is performed so as to spray the raw material.

【0023】この乾燥装置では、乾燥処理初期に60℃
程度の低温加熱すると、発酵に関与する微生物が含水有
機物を分解して、乾燥処理後半では約90℃前後の発酵
熱を出し、乾燥・堆肥化を行う。また、乾燥処理初期に
100℃以上に加熱すると、給気手段により、有機物内
に供給された酸素は有機物と化学反応して結合(酸化)
し、乾燥処理後半では約200℃前後の酸化熱を放出
し、乾燥を行うことができる。
In this drying apparatus, 60 ° C.
When heated at a low temperature, microorganisms involved in fermentation decompose organic matter containing water, and in the latter half of the drying process, produce fermentation heat of about 90 ° C. to perform drying and composting. When heated to 100 ° C. or higher in the early stage of the drying process, oxygen supplied into the organic substance is chemically reacted with the organic substance to form a bond (oxidation) by an air supply unit.
Then, in the latter half of the drying treatment, heat of oxidation of about 200 ° C. is released, and drying can be performed.

【0024】 そのため、本実施例の乾燥装置では、乾
燥処理後半の含水有機物の発熱によって発生した余剰熱
は、缶体(2)の側壁に連通された熱媒ボイラー(6)
から取出して、他の施設に熱媒体として送り出すことも
できる。また、吸引ポンプ(10)に連通された熱交換
機(14)で行ってもよい。このため、使用燃料の節減
量と水分蒸散の熱効率は極めて高い。
Therefore, in the drying apparatus of the present embodiment, the excess heat generated by the heat generation of the water-containing organic substance in the latter half of the drying process is transferred to the heating medium boiler (6) communicated with the side wall of the can (2).
, And sent to another facility as a heat carrier. Alternatively, it may be performed by a heat exchanger (14) connected to the suction pump (10). Therefore, thermal efficiency savings <br/> amount and evaporation of water used fuel is extremely high.

【0025】熱効率は、通常直接熱風で45〜75%,
エロフィンヒータ加熱で30〜55%の熱効率で乾燥さ
れるが、本乾燥装置の熱効率は豚糞140%,鶏糞15
0%,牛糞130%,ミカンの皮150%,コーヒー粕
160%,製紙汚泥160%,余剰汚泥120%,平均
としては144%という驚異的な熱効率を有する。
Thermal efficiency is usually 45 to 75% with direct hot air,
Drying is performed at a thermal efficiency of 30 to 55% by heating the erofin heater. The thermal efficiency of this drying device is 140% for pig dung and 15 for chicken dung.
It has a remarkable thermal efficiency of 0%, cow dung 130%, mandarin peel 150%, coffee grounds 160%, papermaking sludge 160%, excess sludge 120%, and 144% on average.

【0026】また、吸引ポンプ(10)で排出される排気
は、臭気を帯びている場合が多いので、脱臭塔(脱臭手
段)(15)によって脱臭して放出されることが好ましい。
脱臭塔(15)としては、溶岩石脱臭を用いている。溶岩石
脱臭とは、脱臭塔(15)に溶岩石を充填し、塔下部から排
気と曝気とを通し、塔上部で放出している。
Since the exhaust gas discharged from the suction pump (10) often has an odor, it is preferable that the exhaust gas is discharged after being deodorized by a deodorizing tower (deodorizing means) (15).
Lava stone deodorization is used as the deodorization tower (15). Lava stone deodorization means that a deodorization tower (15) is filled with lava stone, exhausted and aerated from the lower part of the tower, and discharged at the upper part of the tower.

【0027】内部に充填された溶岩石には、多数の気孔
が形成されており、この溶岩石の気孔が臭気を封じ込め
る。また、溶岩石は永久的に使用が可能である。尚、脱
臭塔(15)には、薬注ポンプ(16)と曝気ポンプ(17)とが付
設されている。
A large number of pores are formed in the lava rock filled therein, and the pores of the lava rock contain the odor. Lava stones can be used permanently. The deodorization tower (15) is provided with a chemical injection pump (16) and an aeration pump (17).

【0028】以上のように、本乾燥装置は、食品・産業
残渣の乾燥・殺菌・滅菌・発酵と幅広い用途がある。ま
た、水分調整なしで高水分(90%以上)低水分に至る
までの乾燥ができる(余剰汚泥、畜糞まで)。また、本
装置は低温乾燥(60℃)から高温乾燥(200℃)ま
で選定ができる。更に、本装置は発酵と滅菌、殺菌、乾
燥と幅広い用途に使用でき、リサイクルの促進に役立
つ。
As described above, the present drying apparatus has a wide range of uses such as drying, sterilization, sterilization, and fermentation of food and industrial residues. In addition, it is possible to dry up to high moisture (90% or more) and low moisture without moisture adjustment (excess sludge and animal dung). This apparatus can be selected from low-temperature drying (60 ° C.) to high-temperature drying (200 ° C.). In addition, the device can be used for a wide range of applications including fermentation and sterilization, sterilization, and drying, and helps promote recycling.

【0029】[0029]

【考案の効果】本考案は以上説明したとおり、内部に前
記有機物を気密保持して撹拌回動可能な缶体と、前記缶
体内部を加熱する加熱手段と、前記缶体内部を減圧状態
に保持する吸引手段と、前記缶体内部の減圧状態を維持
したまま外気を前記缶体内部の有機物に供給する給気手
段と、前記缶体は、内部で発生した余剰熱を取出す熱交
換手段とを備え、前記缶体は、内部に熱媒が流れる二重
壁構造を有し、前記加熱手段は、前記二重壁構造の内部
に熱媒を供給すると共に、該熱媒の加熱を、前記有機物
中の発酵に関与する微生物が生存可能な温度に缶体内部
を加熱する低温加熱と、100℃以上の高温に缶体内部
を加熱する高温加熱とに選定可能なボイラーを備え、前
記熱媒が供給される二重壁構造が前記熱交換手段を兼ね
ているものであるため、水分を含有した有機物を、自身
の発酵熱又は/及び酸化熱を利用して乾燥することがで
きる。
According to the present invention, as described above , a can body capable of stirring and rotating the organic substance therein in an airtight manner,
A heating means for heating the body portion, and suction means for holding the inside of the can body in a reduced pressure state, and the air supply means for supplying outside air while maintaining the vacuum state of the can body part in organic matter of the can body part, The can body is provided with heat exchange means for extracting surplus heat generated therein, and the can body is provided with a heat medium flowing therethrough.
A wall structure, wherein the heating means is provided inside the double wall structure;
And heating the heating medium with the organic substance.
Inside the can at a temperature at which microorganisms involved in fermentation can survive
Heating the inside of the can body to low temperature heating and heating to over 100 ° C
Heating to high temperature heating and equipped with selectable boiler, before
The double wall structure to which the heat medium is supplied also serves as the heat exchange means.
Since those are the organic matter containing water, it can be dried by utilizing its heat of fermentation and / or oxidation heat.

【0030】即ち、吸引手段と吸気手段とにより、減圧
状態で有機物内に空気が送り込まれるため、含有された
水分が良好に蒸発するだけでなく、加熱手段によって初
発から発酵に関与する微生物の有機物の分解(発酵)に
よる発酵熱や、有機物の酸素との化学的な結合(酸化)
による酸化熱を発生させるため、これが含有された水分
の蒸発のための熱となり、含水有機物を良好に乾燥する
ことができる。
That is, since air is sent into the organic matter under reduced pressure by the suction means and the suction means, not only the contained water evaporates well, but also the organic matter of microorganisms involved in fermentation from the beginning by the heating means. Heat of fermentation due to decomposition (fermentation) and chemical bonding of organic matter with oxygen (oxidation)
As a result, heat is generated for evaporating the water contained therein, and the water-containing organic matter can be dried well.

【0031】また、発酵熱や酸化熱の余剰熱が発生した
場合には、熱交換手段により取出される。
When surplus heat such as fermentation heat or oxidation heat is generated, the heat is removed by heat exchange means.

【0032】また、加熱手段は、好ましくは発酵に関与
する微生物が生存可能な温度に加熱する低温加熱と、1
00℃以上の高温に加熱する高温加熱との選定が可能で
ある。即ち、乾燥処理初期に低温加熱すると、発酵に関
与する微生物が含水有機物を分解し、発酵熱を出して乾
燥・堆肥化を行うことができる。
The heating means preferably comprises a low-temperature heating for heating microorganisms involved in fermentation to a viable temperature, and
It is possible to select high-temperature heating in which heating is performed to a high temperature of 00 ° C. or more. That is, when heating at a low temperature in the early stage of the drying treatment, the microorganisms involved in the fermentation decompose the water-containing organic matter, and generate the heat of fermentation for drying and composting.

【0033】また、乾燥処理初期に100℃以上に加熱
すると、給気手段により、有機物内に供給された酸素は
有機物と化学反応して結合(酸化)し、酸化熱を放出し
て乾燥を行うことができる等の効果を有する。
When heated to 100 ° C. or higher in the early stage of the drying process, oxygen supplied into the organic matter is chemically reacted with the organic matter and combined (oxidized) by the air supply means, and the heat is released by oxidizing heat to perform drying. And the like.

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

【図1】本考案の含水有機物用乾燥装置の一実施例の構
成を示す説明図である。
FIG. 1 is an explanatory view showing a configuration of an embodiment of a drying apparatus for a water-containing organic substance of the present invention.

【符号の説明】[Explanation of symbols]

(1) …投入ホッパ、 (2) …缶体、 (3) …電動機、 (4)(4') …ギア、 (5) …案内ロール、 (6) …熱媒ボイラー(加熱手段)、 (7) …ロータリージョイント、 (8) …循環ポンプ、 (9) …吸引口、 (10)…吸引ポンプ(吸引手段)、 (11)…給気ノズル(給気手段)、 (12)…配管、 (13)…配管、 (14)…熱交換機、 (15)…脱臭塔(脱臭手段)、 (1) ... input hopper, (2) ... can body, (3) ... electric motor, (4) (4 ') ... gear, (5) ... guide roll, (6) ... heat medium boiler (heating means), ( 7) Rotary joint, (8) Circulation pump, (9) Suction port, (10) Suction pump (suction means), (11) Air supply nozzle (air supply means), (12) Piping, (13)… Piping, (14)… Heat exchanger, (15)… Deodorization tower (deodorizing means),

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 11/00 - 11/20 C05F 1/00 - 17/00 B09B 3/00 - 5/00 F26B 1/00 - 25/22 ──────────────────────────────────────────────────続 き Continuation of front page (58) Field surveyed (Int. Cl. 7 , DB name) C02F 11/00-11/20 C05F 1/00-17/00 B09B 3/00-5/00 F26B 1 / 00-25/22

Claims (2)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 余剰汚泥,畜糞,鶏糞,パルプ及びその
残渣,食品残渣等の水分を含有した有機物の発酵熱又は
/及び酸化熱を利用した乾燥機であって、 内部に前記有機物を気密保持して撹拌回動可能な缶体
と、 前記缶体内部を加熱する加熱手段と、 前記缶体内部を減圧状態に保持する吸引手段と、 前記缶体内部の減圧状態を維持したまま外気を前記缶体
内部の有機物に供給する給気手段と、 前記缶体内部で発生した余剰熱を取出す熱交換手段とを
備えた含水有機物用乾燥装置において、 前記缶体は、内部に熱媒が流れる二重壁構造を有し、 前記加熱手段は、前記二重壁構造の内部に熱媒を供給す
ると共に、該熱媒の加熱を、前記有機物中の発酵に関与
する微生物が生存可能な温度に缶体内部を加熱する低温
加熱と、100℃以上の高温に缶体内部を加熱する高温
加熱とに選定可能なボイラーを備え、前記吸引手段及び給気手段は、少なくとも前記加熱手段
によって100℃以上の高温に缶体内部を加熱する高温
加熱を選択する際に、前記缶体内部の減圧状態を維持し
たまま外気を缶体内部の有機物に供給するものであり、 前記熱媒が供給される二重壁構造が前記熱交換手段を兼
ねていることを特徴とする含水有機物用乾燥装置。
1. A dryer utilizing the heat of fermentation and / or the heat of oxidation of organic matter containing water such as excess sludge, animal dung, chicken dung, pulp and its residue, food residue, etc., in which the organic matter is kept airtight. A stirring and rotating can body, a heating means for heating the inside of the can body, a suction means for maintaining the inside of the can body in a reduced pressure state, and the outside air while maintaining the reduced pressure state inside the can body. In a drying apparatus for a water-containing organic substance, comprising: an air supply means for supplying organic matter inside the can body; and a heat exchange means for extracting excess heat generated inside the can body, wherein the can body has a heat medium flowing therein. The heating means supplies a heat medium to the inside of the double wall structure, and heats the heat medium to a temperature at which microorganisms involved in fermentation in the organic matter can survive. Low temperature heating to heat the inside of the body and high temperature of 100 ° C or more Comprising a selectable boiler and high temperature heating for heating the can body, the suction means and the air supply means, at least the heating means
High temperature that heats the inside of the can body to 100 ° C or higher
When selecting heating, maintain the reduced pressure inside the can body
A drying apparatus for a water-containing organic matter , wherein outside air is supplied to the organic matter inside the can body while the double-wall structure to which the heat medium is supplied also serves as the heat exchange means.
【請求項2】 前記吸引手段に連通された脱臭手段を備
えたことを特徴とする請求項1に記載の含水有機物用乾
燥装置。
2. The apparatus for drying a water-containing organic matter according to claim 1, further comprising a deodorizing means connected to the suction means.
JP1993032520U 1993-05-26 1993-05-26 Drying equipment for hydrous organic matter Expired - Fee Related JP2607304Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1993032520U JP2607304Y2 (en) 1993-05-26 1993-05-26 Drying equipment for hydrous organic matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1993032520U JP2607304Y2 (en) 1993-05-26 1993-05-26 Drying equipment for hydrous organic matter

Publications (2)

Publication Number Publication Date
JPH0685100U JPH0685100U (en) 1994-12-06
JP2607304Y2 true JP2607304Y2 (en) 2001-07-09

Family

ID=12361245

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1993032520U Expired - Fee Related JP2607304Y2 (en) 1993-05-26 1993-05-26 Drying equipment for hydrous organic matter

Country Status (1)

Country Link
JP (1) JP2607304Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101207598B1 (en) * 2012-03-14 2012-12-03 주식회사 마이크로웨이브테크놀로지 Sludge drying apparatus and sludge treatment system comprising the same

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JP2007176766A (en) * 2005-12-28 2007-07-12 Shinso Green:Kk Fertilizer for raising lawn and method for raising lawn
JP2017025732A (en) * 2015-07-17 2017-02-02 国立研究開発法人農業・食品産業技術総合研究機構 Power generation system and power generation method using compost fermentation heat
KR102426866B1 (en) * 2021-10-18 2022-08-01 비케이환경 주식회사 A system of a barnyard manure factory and Odor treatment prevention method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101207598B1 (en) * 2012-03-14 2012-12-03 주식회사 마이크로웨이브테크놀로지 Sludge drying apparatus and sludge treatment system comprising the same

Also Published As

Publication number Publication date
JPH0685100U (en) 1994-12-06

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