JPH0743106B2 - Equipment for drying and incinerating livestock manure - Google Patents
Equipment for drying and incinerating livestock manureInfo
- Publication number
- JPH0743106B2 JPH0743106B2 JP3353412A JP35341291A JPH0743106B2 JP H0743106 B2 JPH0743106 B2 JP H0743106B2 JP 3353412 A JP3353412 A JP 3353412A JP 35341291 A JP35341291 A JP 35341291A JP H0743106 B2 JPH0743106 B2 JP H0743106B2
- Authority
- JP
- Japan
- Prior art keywords
- drying
- exhaust gas
- heat
- dryer
- self
- 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
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、畜産農場から排出され
る家畜糞、下水処理場で発生するし尿処理汚泥等のりん
含有率が高い高湿分廃棄処理物を乾燥・焼却処理して焼
却灰を資源回収するとともに熱損失を極力抑えた処理工
程レイアウトおよび機器系統を有した、家畜糞等の乾燥
・焼却処理装置に関する。[Field of Industrial Application] The present invention is to incinerate animal dung discharged from livestock farms, high-humidity waste products with high phosphorus content such as human sewage treatment sludge generated at sewage treatment plants by drying and incineration. Drying of livestock manure, etc. , which has a treatment process layout and equipment system that minimizes heat loss while recovering ash resources
-Regarding incineration treatment equipment .
【0002】[0002]
【従来の技術】従来より、畜産農場から排出される家畜
糞は、一部を肥料として畑地に還元してきたが、残りの
大部分とそのままでは肥料として適しないものは、乾燥
・堆積発酵等により処理するか、最終処分場へ投棄して
きた。2. Description of the Related Art Conventionally, livestock manure discharged from livestock farms has been partially returned to the field as fertilizer, but most of the rest and those that are not suitable as fertilizer as they are, are dried or deposited by fermentation. Either processed or dumped at the final disposal site.
【0003】また、下水処理場で発生するし尿処理汚泥
については、加工して肥料化される場合もあるが、大部
分焼却処理されてきた。これらに代表される高湿分の汚
泥を乾燥・焼却処理する技術として、乾燥機と焼却炉を
組み合わせた乾燥・焼却システムが知られている。この
場合、焼却炉としては、多段焼却炉、流動床式、固定床
式あるいは回転床式焼却炉等種々のものがあり、乾燥機
あるいは乾燥炉についても同様であった。Further, the sludge treated with human waste generated at the sewage treatment plant may be processed into fertilizer, but most of it has been incinerated. As a technique for drying and incinerating high-humidity sludge typified by these, a drying and incineration system that combines a dryer and an incinerator is known. In this case, there are various incinerators such as a multi-stage incinerator, a fluidized bed type, a fixed bed type or a rotary bed type incinerator, and the same applies to a dryer or a drying oven.
【0004】上記の乾燥・焼却システムにおいてなされ
てきた技術開発は、各炉の発明を含む熱回収技術の改善
による熱効率の向上、処理工程レイアウトの変更による
処理能力の向上および飛散量の低減等を主題とするもの
であった。The technical developments made in the above drying / incineration system are to improve the heat efficiency by improving the heat recovery technology including the invention of each furnace, improve the processing capacity by changing the processing process layout, and reduce the scattering amount. It was the subject.
【0005】[0005]
【発明が解決しようとする課題】しかし、これらの処理
技術のうち、とくに家畜糞等を専らに扱う乾燥・処理装
置として、処理物の安全化、安定化、および減量化を図
り、残渣である焼却灰を資源回収するところまでをフロ
ーシートとして開示したものは見当たらなかった。However, among these treatment techniques, especially as a drying / treatment device that exclusively treats livestock manure and the like , the treated product is safe, stabilized, and reduced in amount, and is a residue. I couldn't find any disclosure of flow sheets up to the point of recovering incinerated ash as a resource.
【0006】本発明は、このような事情に鑑みなされた
ものであって、熱回収による省エネルギタイプであり、
かつ、処理物の安全化、安定化、および減量化を図り、
残渣である処理物焼却灰を資源回収する新たな家畜糞等
の乾燥・焼却処理装置を提供することを目的とするもの
である。The present invention has been made in view of such circumstances, and is an energy saving type by heat recovery,
At the same time, we aim to make the processed materials safer, more stable, and less wasteful.
New livestock manure, etc. that recovers the treated incineration ash that is the residue as a resource
It is an object of the present invention to provide a drying / incineration treatment device for
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に本発明は、家畜糞等の乾燥・焼却処理装置であって、
原料フィーダからコンベア移送により投入ホッパへ供給
された被処理物を自燃可能な水分まで予備乾燥する乾燥
機と、乾燥排ガスが配管導入され乾品コンベアにより投
入スクリュに移送・供給された生成乾品を自燃させる補
助バーナおよび脱臭バーナを備えた焼却炉とを配設し、
乾燥排ガスを焼却炉に導き予備乾燥後の被処理物を自燃
させるための熱量補給に消費し、脱臭後の燃焼排ガスを
乾燥機のジャケット部に導入し新たに受け入れた被処理
物の乾燥熱源として伝熱消費し、 ジャケット部通過後の
燃焼排ガスを集塵サイクロンを経由して熱交換器に導き
外気の予熱に消費し、予熱外気を乾燥機の内筒へ送給す
る循環系統からなる熱回収機構を具備したことを特徴と
するものである。In order to achieve the above object, the present invention provides a drying and incineration treatment apparatus for livestock manure, etc.
A dryer that pre-drys the object to be processed that is supplied from the raw material feeder to the input hopper by conveyor transfer to a moisture content that can burn itself, and the dry exhaust gas that is introduced into the pipe and the product dry product that is transferred and supplied to the input screw by the dry product conveyor. An incinerator equipped with a self-burning auxiliary burner and a deodorizing burner is installed ,
Direct the dried exhaust gas to the incinerator and self-burn the object to be treated after preliminary drying.
It is consumed to replenish the amount of heat for
Introduced in the jacket of the dryer and newly accepted
Heat is consumed as a heat source for drying the product, and after passing through the jacket
The combustion exhaust gas is guided to the heat exchanger via the dust collection cyclone.
It is consumed for preheating the outside air and sends the preheated outside air to the inner cylinder of the dryer.
It is characterized by being equipped with a heat recovery mechanism consisting of a circulating system .
【0008】[0008]
【作用】上述した本発明の乾燥・焼却装置は、乾燥機に
より、高湿分廃棄処理物が自燃可能な水分まで乾燥さ
せ、焼却炉へ投入後、この乾燥排ガスの配管導入ととも
に、点火のみをおこない自燃させる。ここで、点火をお
こなう補助バーナは、焼却中の発熱量の変動に対応する
ものである。また、乾燥排ガスは悪臭ガスでもあり、こ
れを脱臭バーナにより高温燃焼させ、悪臭を分解する。
次いで、燃焼排ガスを乾燥機のジャケット部へ導き、熱
回収するとともに、さらに、集塵サイクロンを介して熱
交換し、予熱された外気を乾燥熱源として乾燥機内筒へ
送出・供給する。この高湿分廃棄処理物の乾燥・自燃化
焼却と燃焼排ガスの循環供給による熱回収を機器系統に
組み込むことにより省エネルギを可能とする。In the above-described drying / incineration apparatus of the present invention, the high-humidity waste treatment product is dried to a moisture content that can be self-combusted by the dryer, and after being put into the incinerator, the piping of this dry exhaust gas is introduced and only ignition is performed. Do it by yourself. Here, the auxiliary burner for igniting corresponds to the fluctuation of the calorific value during incineration. The dry exhaust gas is also a malodorous gas, which is burned at a high temperature by a deodorizing burner to decompose the malodorous substance.
Next, the combustion exhaust gas is guided to the jacket of the dryer to recover heat, and further, heat is exchanged via the dust collecting cyclone, and preheated outside air is delivered / supplied to the dryer inner cylinder as a heat source for drying. Energy can be saved by incorporating heat recovery by drying / self-combustion incineration of this high-humidity waste treatment and circulation supply of combustion exhaust gas into the equipment system.
【0009】[0009]
【実施例】本発明の最適な実施例について添付図面を参
照して以下説明する。図1は、家畜糞等の乾燥・焼却処
理置のフローシートの例を示したものである。最適な利
用先は、鶏糞の乾燥・焼却処理装置としてであって、被
処理物(鶏糞)の無公害化処理と炭化物を含む処理物焼
却灰の資源回収を図ったものである。 DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An optimum embodiment of the present invention will be described below with reference to the accompanying drawings. Figure 1 shows the drying and incineration facility for livestock manure .
It is an example of a flow sheet of the abduction . Optimal profit
The place of use was as a device for drying and incinerating chicken manure.
Pollution-free treatment of treated material (chicken dung) and treatment of charcoal-containing material
This is an attempt to recover the ash resources.
【0010】図において、原料となる家畜糞等(以下、
原料汚泥という。)を原料フィーダ(1)に貯留する。
この原料汚泥を原料フィーダ(1)から原料コンベア
(2)により乾燥機(4)の投入ホッパ(3)へ移送す
る。ここで、原料フィーダ(1)は、可変モータ付きス
クリュによって供給量が任意に選択できるようにしたも
のとされ、目標供給量を設定することができる。In the figure, livestock manure etc. as raw materials (hereinafter,
It is called raw material sludge. ) Is stored in the raw material feeder (1).
This raw material sludge is transferred from the raw material feeder (1) to the input hopper (3) of the dryer (4) by the raw material conveyor (2). Here, the raw material feeder (1) is configured such that the supply amount can be arbitrarily selected by a screw with a variable motor, and a target supply amount can be set.
【0011】投入された原料汚泥は、約70〜85パーセン
トの高湿分から、20〜30パーセント程度にまで、すなわ
ち自燃可能な水分量まで乾燥され、乾品コンベア(6)
に排出される。ここで、乾燥は、後述する燃焼排ガスの
熱回収によりなされるので、外部から熱量供給は不要で
ある。The input raw material sludge is dried from high humidity of about 70 to 85% to about 20 to 30%, that is, to a moisture content capable of self-combustion, and a dry product conveyor (6).
Is discharged to. Here, since the drying is performed by recovering the heat of the combustion exhaust gas described later, it is not necessary to supply the amount of heat from the outside.
【0012】予備乾燥された原料汚泥は、乾品コンベア
(6)によって投入スクリュ(7)に移送され、焼却炉
(8)へ投入される。焼却炉では、原料汚泥が自燃する
ために点火時のみ燃料を消費するだけでよいが、この点
火と発熱量の変動に対応するための補助バーナ(9)
と、脱臭温度を確保するための脱臭バーナ(10)とが設
けられている。The pre-dried raw material sludge is transferred to the input screw (7) by the dry product conveyor (6) and is input to the incinerator (8). In the incinerator, since the raw material sludge self-combusts, it suffices to consume the fuel only at the time of ignition, but the auxiliary burner (9) for coping with this ignition and the fluctuation of the calorific value.
And a deodorizing burner (10) for ensuring the deodorizing temperature.
【0013】焼却灰は、焼却灰排出スクリュ(11)によ
って灰ホッパに一時貯留し、定期的に外部へ取り出され
る。The incinerated ash is temporarily stored in the ash hopper by the incinerated ash discharge screw (11) and is regularly taken out to the outside.
【0014】一方、乾燥排ガス(悪臭ガス)は、排気フ
ァン(15)を経由して焼却炉(8)へ配管導入され、炉
中、高温下で脱臭される。次いで、炉内燃焼排ガスが排
気口(12)から配管により乾燥機(4)のジャケット部
(5)に導入され、熱回収されるとともに、集塵サイク
ロン(13)へ導かれ、さらに熱交換器(14)を介して押
込みファン(16)により予熱された外気となって乾燥熱
源として乾燥機(4)内筒へ送出・供給される。上記熱
交換器(14)で熱回収済の燃焼排ガスは、別途排気ファ
ン(15)を介して煙突(17)から大気放出される。On the other hand, dry exhaust gas (malodorous gas) is introduced into the incinerator (8) through an exhaust fan (15) and is deodorized at high temperature in the furnace. Next, the combustion exhaust gas in the furnace is introduced from the exhaust port (12) into the jacket section (5) of the dryer (4) through a pipe to recover heat, and is also guided to the dust collecting cyclone (13) and further to the heat exchanger. The air is preheated by the pushing fan (16) via the (14) and is sent out and supplied to the inner cylinder of the dryer (4) as a drying heat source. The combustion exhaust gas from which the heat has been recovered in the heat exchanger (14) is separately discharged to the atmosphere from the chimney (17) via the exhaust fan (15).
【0015】なお、燃焼排ガスは、乾燥機(4)の運転
停止の際には、排気口(12)から乾燥機(4)のジャケ
ット部(5)への経路をダンパにより遮断し、直接大気
放出することができる。It should be noted that, when the dryer (4) is stopped, the combustion exhaust gas is cut off from the exhaust port (12) to the jacket section (5) of the dryer (4) by a damper so as to be directly exposed to the atmosphere. Can be released.
【0016】以上本発明の1実施例について説明した
が、本発明はこれに限定されることなく、本発明が保護
される範囲内において種々の改変を施すことができるも
のである。Although one embodiment of the present invention has been described above, the present invention is not limited to this, and various modifications can be made within the scope of protection of the present invention.
【0017】[0017]
【発明の効果】本発明は、以上の構成よりなるものであ
り、これによれば原料汚泥として家畜糞等を専らに扱う
乾燥・焼却処理レイアウトが、熱回収機構について、乾
燥排ガス及び燃焼排ガスの循環供給による多段的な熱利
用(熱回収)と脱臭及び除塵による大気放出を機器系統
に組み込んだものとされているので、熱損失を極力抑え
た省エネルギタイプの無公害化焼却処理を図ることがで
きる。According to the present invention, more than are those composed of configuration, <br/> drying and incineration layout treat exclusively livestock manure and the like as the material sludge According to this, the heat recovery mechanism, dry
Multi- stage heat utilization by circulating supply of dry exhaust gas and combustion exhaust gas
Because it is said that the equipment system incorporates the use (heat recovery) and the atmospheric release due to deodorization and dust removal, it is possible to achieve an energy-saving, pollution-free incineration process that minimizes heat loss.
【0018】また、家畜糞等りん含有率の高い原料汚泥
を自燃させるので、上記省エネルギに相乗して高い経済
性を有するとともに、焼却灰中にりん分の資源回収を図
ることができ、しかも、過剰な廃棄物の減量化に寄与す
ること等、産業上の利用において極めて価値の高いもの
である。Further, since the raw material sludge having a high phosphorus content such as livestock manure is self-combusted, it has a high economic efficiency in synergy with the above energy saving, and at the same time, the resource recovery of the phosphorus content in the incineration ash is intended. In addition, it contributes to the reduction of excess waste, and is extremely valuable in industrial use.
【図面の簡単な説明】[Brief description of drawings]
【図1】本発明の1実施例装置のフローシートである。FIG. 1 is a flow sheet of an apparatus according to an embodiment of the present invention.
1 原料フィーダ 2 原料コンベア 3 投入ホッパ 4 乾燥機 5 ジャケット部 6 乾品コンベア 7 投入スクリュ 8 焼却炉 9 補助バーナ 10 脱臭バーナ 11 排出スクリュ 12 排気口 13 集塵サイクロン 14 熱交換器 15 排気ファン 16 押込ファン 17 煙突 1 Raw material feeder 2 Raw material conveyor 3 Input hopper 4 Dryer 5 Jacket part 6 Dry product conveyor 7 Input screw 8 Incinerator 9 Auxiliary burner 10 Deodorizing burner 11 Exhaust screw 12 Exhaust port 13 Dust collection cyclone 14 Heat exchanger 15 Exhaust fan 16 Push-in Fan 17 chimney
───────────────────────────────────────────────────── 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 F23G 7/00 C 8409−3K ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location F23G 7/00 C 8409-3K
Claims (1)
処理物の乾燥・焼却処理装置において、原料フィーダか
らコンベア移送により投入ホッパへ供給された被処理物
を自燃可能な水分まで予備乾燥する乾燥機と、乾燥排ガ
スが配管導入され乾品コンベアにより投入スクリュに移
送・供給された生成乾品を自燃させる補助バーナおよび
脱臭バーナを備えた焼却炉とを配設し、乾燥排ガスを焼
却炉に導き予備乾燥後の被処理物を自燃させるための熱
量補給に消費し、脱臭後の燃焼排ガスを乾燥機のジャケ
ット部に導入し新たに受け入れた被処理物の乾燥熱源と
して伝熱消費し、ジャケット部通過後の燃焼排ガスを集
塵サイクロンを経由して熱交換器に導き外気の予熱に消
費し、予熱外気を乾燥機の内筒へ送給する循環系統から
なる熱回収機構を具備したことを特徴とする家畜糞等の
乾燥・焼却処理装置。 1. An apparatus for drying and incinerating a high-humidity waste treatment product having a high phosphorus content such as livestock manure reserves up to self-combustible water for a substance to be treated supplied from a raw material feeder to a feeding hopper by conveyor transfer. A dryer for drying and an incinerator equipped with an auxiliary burner and a deodorizing burner for self-burning the produced dry product that is introduced into the screw by the dry product exhaust gas and transferred to the feeding screw by the dry product conveyor are installed to burn the dry exhaust gas.
Heat to guide the incinerator to self-burn the object to be treated after preliminary drying
The exhaust gas exhausted after deodorizing is consumed for replenishing
And a new heat source for the processed material
And heat transfer to consume the exhaust gas after passing through the jacket.
It is led to the heat exchanger via the dust cyclone and extinguished to preheat the outside air.
From the circulation system that costs and sends the preheated outside air to the inner cylinder of the dryer
Of a livestock dung etc. characterized by having a heat recovery mechanism
Drying / incineration processing equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3353412A JPH0743106B2 (en) | 1991-12-16 | 1991-12-16 | Equipment for drying and incinerating livestock manure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3353412A JPH0743106B2 (en) | 1991-12-16 | 1991-12-16 | Equipment for drying and incinerating livestock manure |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05164314A JPH05164314A (en) | 1993-06-29 |
| JPH0743106B2 true JPH0743106B2 (en) | 1995-05-15 |
Family
ID=18430666
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3353412A Expired - Fee Related JPH0743106B2 (en) | 1991-12-16 | 1991-12-16 | Equipment for drying and incinerating livestock manure |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0743106B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10226538A1 (en) * | 2002-06-14 | 2004-01-08 | Schäch, Josef | Horse droppings held in two-part heated storage system for use as boiler fuel |
| CN107044647B (en) * | 2017-05-10 | 2018-10-30 | 山东鑫合新材料科技有限公司 | A kind of pre- roller coating aluminium volume production line emission-control equipment |
| JP6932089B2 (en) * | 2018-01-29 | 2021-09-08 | Jfeエンジニアリング株式会社 | Diaper drying equipment and methods, fuel manufacturing equipment and methods |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS558571A (en) * | 1978-07-05 | 1980-01-22 | Yoshida Masayoshi | Apparatus for combustion treatment of sludge or the like |
| JPS5543368A (en) * | 1978-09-22 | 1980-03-27 | Ishigaki Kiko Kk | Incinerator for high-water-content waste |
-
1991
- 1991-12-16 JP JP3353412A patent/JPH0743106B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05164314A (en) | 1993-06-29 |
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