JPS6149981A - Method of recovering waste heat from drying furnace for hydro-extraction - Google Patents
Method of recovering waste heat from drying furnace for hydro-extractionInfo
- Publication number
- JPS6149981A JPS6149981A JP59171556A JP17155684A JPS6149981A JP S6149981 A JPS6149981 A JP S6149981A JP 59171556 A JP59171556 A JP 59171556A JP 17155684 A JP17155684 A JP 17155684A JP S6149981 A JPS6149981 A JP S6149981A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- air
- exhaust
- air conditioner
- path
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
■1発明の目的
[産業上の利用分野]
本発明は、水切り用乾燥炉の排ガスの利用方法に関する
。DETAILED DESCRIPTION OF THE INVENTION (1) Object of the Invention [Field of Industrial Application] The present invention relates to a method of utilizing exhaust gas from a draining drying oven.
[従来の技術]
水切り用乾燥炉に限らず直燃式の一般の乾燥炉にあって
は、燃焼に必要な新鮮な空気を取入れなければならない
ため、炉内の暖気の一部を排気して給排気バランスを保
っている。[Prior art] Not only draining drying ovens but also direct combustion type drying ovens require the intake of fresh air necessary for combustion, so it is necessary to exhaust some of the warm air inside the oven. Maintains supply and exhaust balance.
ところで、このような乾燥炉hs rらの1ノ1ガスは
140〜150°C程度の高温であるから単に放出する
には熱エネルギの損失が多いため、従来は熱交換器を使
用して新鮮空気の予熱に利用していた。By the way, the high temperature of such drying oven HSR etc. gas is around 140-150°C, so there is a lot of loss of thermal energy if it is simply released. It was used to preheat the air.
しかしながら熱交換器によって排ガスの熱を回収利用し
たとしても熱の回収率は7!110%程度であり、排ガ
スの利用としては未だ不十分であった。However, even if the heat of the exhaust gas is recovered and utilized by a heat exchanger, the heat recovery rate is about 7.110%, which is still insufficient for the utilization of the exhaust gas.
一方、作業場の暖房を目的とした空調装置は、外気を吸
入しこれを加熱して送気ターるようになっているが、従
来にあっては吸入した外気をそのまま高温のスチームや
ガスバーナ或いは電気ヒータなどで加熱していた。On the other hand, air conditioners for the purpose of heating workplaces suck in outside air, heat it, and then send it to the air. It was heated with a heater.
[発明が解決しようとする問題点]
このため乾燥炉を身近に有する建屋においては、乾燥炉
からの排ガスの排熱を無駄にする一方、空調装置では夛
量搏燃料を使用して外気を所定の一定温度に加熱してい
るという不合理があった。[Problems to be solved by the invention] For this reason, in buildings that have drying ovens nearby, exhaust heat from the exhaust gas from the drying oven is wasted, while air conditioners use a large amount of fuel to supply outside air to a specified level. There was an absurdity in heating to a constant temperature.
そこで特に水切り用乾燥炉に着目すると、塗装乾燥炉の
ようにその排ガス中に有毒な溶剤力などは含まれておら
ず、燃焼開始直後の未燃焼ガスを除けばその排ガスが直
接人体に悪影響を及ばずこともない。Therefore, when we focus on draining drying ovens in particular, unlike paint drying ovens, their exhaust gas does not contain toxic solvents, and apart from the unburned gas immediately after combustion starts, the exhaust gases directly have a negative impact on the human body. I'm not even close.
本発明は上記事情に鑑みてなされたもので、省エネルギ
ーの現点から水切り用乾燥炉の77ガスからの排熱を有
効に回収する方法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 the above circumstances, and an object of the present invention is to provide a method for effectively recovering exhaust heat from 77 gas of a draining drying furnace from the point of view of energy saving.
■2発明の構成
[問題を力?決するための手段]
斯かる目的を達成するため、本発明の水切り周転)♀炉
からの排熱回収方法は、燃焼窄と炉内を循環する水切り
用乾燥炉の排ガスの一部を系外排気路及びこれに連通ず
る導入路を経て空調装置に導入し、この空調装置に導入
される外気を前記排ガスで予熱するようにして省エネル
ギーの要請を達成するものである。■2 Structure of the invention [Is the problem a force? In order to achieve such an objective, the method for recovering exhaust heat from a draining rotary furnace of the present invention removes a portion of the exhaust gas from the draining drying oven that circulates through combustion and the furnace to outside the system. The exhaust gas is introduced into an air conditioner through an exhaust path and an inlet path communicating with the exhaust gas, and the outside air introduced into the air conditioner is preheated by the exhaust gas, thereby achieving energy saving requirements.
F実施例コ 以下本発明の実M例を図面を参照しながら説明する。F Example An actual example of the present invention will be described below with reference to the drawings.
第1図は本発明の方法を実施するためのシステム構成ブ
ロック図である。本システムは、水切り用乾燥′P1か
らJノ)気される比較的高温であって水分を含んだ高エ
ンタルピー状態の排ガスの一部を導入路A+ 、A2を
経て空調装置2に導入し、この空調′1AVll 2に
導入される外気を上記排ガスで予熱し、予熱された外気
と共に上記排ガスを浄化し、かつ加熱することによって
作′2場の暖房に適した一定温湿度の清浄空気として例
えば塗装ブースへ送気するものである。FIG. 1 is a block diagram of a system configuration for implementing the method of the present invention. This system introduces a portion of relatively high-temperature, moisture-containing, and high-enthalpy exhaust gas that is aired for draining (from P1 to J) into the air conditioner 2 through introduction paths A+ and A2. By preheating the outside air introduced into the air conditioner AVll 2 with the exhaust gas, purifying the exhaust gas together with the preheated outside air, and heating it, it can be painted, for example, as clean air at a constant temperature and humidity suitable for heating the workplace. This is to supply air to the booth.
上記水切り用乾燥炉1は、排ガスをバーナ3、フィルタ
4及び送気用のファン5の順に帰還路B+ 、B2.8
3 、B4 、B5を介して循環させる構造である。尚
排ガスの循環の際には系外よりある程度の新鮮空気を吸
入することは言うまでもない。本システムにおいては、
帰還路8+ 、B2の中途部に上記導入路Δ丁が接続さ
れ、排ガスの一部を空調装置2に供給できるようになっ
ている。The draining drying oven 1 passes the exhaust gas through the burner 3, filter 4, and air supply fan 5 in this order through return paths B+ and B2.8.
3, B4, and B5. Needless to say, when circulating the exhaust gas, a certain amount of fresh air is taken in from outside the system. In this system,
The introduction path ΔT is connected to a midway portion of the return path 8+ and B2, so that a portion of the exhaust gas can be supplied to the air conditioner 2.
またバーナ3の着火時にはプレパージを行うため未燃焼
ガスが発生するので、これを系外へ排出するため系外排
気路C1が上記導入路A+ 、A2の中間部から分岐形
成されている。Further, when the burner 3 is ignited, unburned gas is generated due to pre-purging, and in order to discharge this gas to the outside of the system, an outside exhaust passage C1 is formed as a branch from the intermediate portion of the introduction passages A+ and A2.
上記未燃焼ガスはこれをそのまま空調装置2に導入する
と建屋内の雰囲気的環境を汚染し人体に有害となるので
、未燃焼ガスが空調装置2内に導入されてしまうことを
阻止し、かつ完全燃焼の排ガスを極力系外へ逃さないよ
うにするため、排ガスの流路を規制するダンパが設けら
れている。ずなわち、第1のダンパ6が導入路A1の中
間部に、第2のダンパ7が導入路A2の中間部に、そし
て第3のダンパ8が系外排気路C1の中間部に設けられ
ている。If the unburned gas mentioned above is directly introduced into the air conditioner 2, it will pollute the atmospheric environment inside the building and become harmful to the human body. In order to prevent the combustion exhaust gas from escaping out of the system as much as possible, a damper is provided to regulate the flow path of the exhaust gas. That is, the first damper 6 is provided in the middle of the introduction path A1, the second damper 7 is provided in the middle of the introduction path A2, and the third damper 8 is provided in the middle of the external exhaust path C1. ing.
排ガスを一空調装置2に導入する場合には、先ず第1及
び第3のダンパ6.8を開にり゛ると共に第2のダンパ
7を開にして未燃焼ガスを系外へ排気し、そのm ’j
41及び第2のダンパ6.7を間にすると共に第3のダ
ンパ8を開にして排ガスを空調装置2に導入する。した
がって未燃焼ガスが空調t!置に導入されることはなく
、かつ完全燃焼の排ガスは無駄に系外へJJI出される
ことなく空調装置2に導入することができる。When introducing exhaust gas into one air conditioner 2, first open the first and third dampers 6.8 and open the second damper 7 to exhaust unburned gas out of the system. That m'j
41 and the second damper 6.7, and open the third damper 8 to introduce the exhaust gas into the air conditioner 2. Therefore, unburned gas is used for air conditioning! In addition, completely combusted exhaust gas can be introduced into the air conditioner 2 without being wastefully discharged outside the system.
上記空調装置2は、成人外気を0化づ−ると共に所定の
64湿度に調整し、作業環境に適した空気にしてから塗
装ブースなどの建屋内に送気するものである。この種の
空調装置2は、例えば第2図に示すように、筐体10の
正面側吸気口に張設された防虫網11、粗大な塵埃を取
り除くロールマットフィルタ12、微細な悪疾を取り除
くと共に加湿するキャピラリーフィルタ13及びシャワ
ー14、水滴を取り除くエリミネータ15、加熱するた
めのエロフィンヒータ16、及び筐体10内の所定温湿
度の清浄空気を送気する送気ファン171)r r34
14成されている。The air conditioner 2 converts adult outdoor air to zero and adjusts it to a predetermined humidity level of 64°C to make the air suitable for the working environment before sending it into a building such as a painting booth. For example, as shown in FIG. 2, this type of air conditioner 2 includes an insect screen 11 stretched over the front intake port of a housing 10, a roll mat filter 12 that removes coarse dust, and a roll mat filter 12 that removes fine particles. At the same time, a capillary filter 13 and a shower 14 that humidify, an eliminator 15 that removes water droplets, an Erofin heater 16 that heats, and an air supply fan 171) that supplies clean air at a predetermined temperature and humidity inside the housing 10
14 have been completed.
本システムにおける空調装置2は、ロールマットフィル
タ12の前段にJプいて上記導入路A2と接続されてい
る。したがって、この空調装置2に外気が吸入されたと
き、高エンタルピー状態の排ガスが成人外気に合流、4
況合し、この外気が余熱されることにより吸入前よりも
高エンタルピー状fgすなわち高い熱■を有する状態と
なる。The air conditioner 2 in this system is connected to the introduction path A2 before the roll mat filter 12. Therefore, when outside air is taken into this air conditioner 2, the exhaust gas in a high enthalpy state joins the adult outside air.
Under the circumstances, this outside air is preheated, resulting in a state in which it has a higher enthalpy fg, that is, a higher heat (2) than before inhalation.
このようにして余熱された成人外気及び排ガスは、ロー
ルマットフィルタ12及び水シヤワー14を通過するこ
とによって浄化され、かつエリミネータ15を通過する
ことによって水滴が取り除かれる。次いでエロフィンヒ
ータ16にて所定湿度に加熱されることになるが、上)
ホのどと(吸入外気は余熱されていて高エンタルピー状
態が達成されているので、所定温度まで上昇させるため
に使用ブるエネルギーは少なくて済む。The thus preheated adult outside air and exhaust gas are purified by passing through the roll mat filter 12 and the water shower 14, and water droplets are removed by passing through the eliminator 15. Next, it is heated to a predetermined humidity using the Erofin heater 16 (above).
Since the inhaled outside air has been preheated and has achieved a high enthalpy state, less energy is required to raise it to a predetermined temperature.
そして、所定温度に上昇された外気及び排ガスは暖房用
暖気として上記送気ファン17で建屋内に送気される。The outside air and exhaust gas, which have been raised to a predetermined temperature, are then sent into the building by the air sending fan 17 as warm air for heating.
送気された暖気中には、未燃焼ガスや溶剤分は含まれて
おらず、建屋内の雰囲気を悪化させることはない、vr
に水切り用乾燥炉1から導入される排ガス中には水分を
含んでいるので、空:J、’l装置2内での加湿工程を
不要にすることができる。The supplied warm air does not contain unburned gas or solvent, and will not worsen the atmosphere inside the building.vr
Since the exhaust gas introduced from the draining drying furnace 1 contains moisture, a humidification step within the drying device 2 can be made unnecessary.
なお上記実施例は一例であり本発明の要旨の範囲内にお
いて種々の変形実施が可能である。例えば導入路Al、
A2は第3図に示ずように帰還路B+ 、・・・、B5
とは分離した別系統とすることも可能である。また未
燃焼ガスの系外排気は空調装置からの送気系の途中で行
うようにしてもよい。Note that the above-mentioned embodiment is merely an example, and various modifications can be made within the scope of the gist of the present invention. For example, the introduction path Al,
A2 is the return path B+,...,B5 as shown in FIG.
It is also possible to create a separate system separate from the . Further, unburned gas may be exhausted to the outside of the system in the middle of the air supply system from the air conditioner.
■0発明のりJ采
以上の説明から明らかなように、本発明は、燃焼室と炉
内を循環する水切り用乾燥炉の排ガスの一部を系外排気
路及びこれに3@通ずる導入路を経て空調装置に導入し
、この空調装置に導入される外気を前記排ガスで予熱す
るので、省エネルギーの四点から水切り用乾燥炉の排ガ
スからの排熱を荷動に回収することができるという効果
を有するものである。■0 Invention Glue J As is clear from the above description, the present invention provides an external exhaust path and an inlet path leading to this for a part of the exhaust gas of the draining drying oven that circulates between the combustion chamber and the furnace. The exhaust gas is then introduced into the air conditioner, and the outside air introduced into the air conditioner is preheated by the exhaust gas, which has the effect of being able to recover the exhaust heat from the exhaust gas from the drying oven for energy saving purposes. It is something that you have.
第1図は本発明方法を実施するための一例を示すシステ
ム構成ブロック図、第2図は空調装置の一例を示ず概略
31明図、第3図は本発明方法を実施するための他のシ
ステム構成ブロック図である。
1・・・水切り用乾燥炉、 2・・・空調装置、△1.
A2・・・導入路、 C1・・・系外排気路。FIG. 1 is a system configuration block diagram showing an example of implementing the method of the present invention, FIG. 2 is a schematic 31-dimensional diagram without showing an example of an air conditioner, and FIG. 3 is a system configuration block diagram showing an example of implementing the method of the present invention. It is a system configuration block diagram. 1...Drying oven for draining, 2...Air conditioner, △1.
A2...Inlet path, C1...Exhaust path outside the system.
Claims (1)
を系外排気路及びこれに連通する導入路を経て空調装置
に導入し、この空調装置に導入される外気を前記排ガス
で予熱することを特徴とする水切り用乾燥炉からの排熱
回収方法。A part of the exhaust gas from the draining drying furnace that circulates in the combustion chamber and the furnace is introduced into the air conditioner through an external exhaust path and an introduction path that communicates with this, and the outside air introduced into the air conditioner is preheated with the exhaust gas. A method for recovering exhaust heat from a draining drying oven, characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59171556A JPS6149981A (en) | 1984-08-20 | 1984-08-20 | Method of recovering waste heat from drying furnace for hydro-extraction |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59171556A JPS6149981A (en) | 1984-08-20 | 1984-08-20 | Method of recovering waste heat from drying furnace for hydro-extraction |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6149981A true JPS6149981A (en) | 1986-03-12 |
Family
ID=15925317
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59171556A Pending JPS6149981A (en) | 1984-08-20 | 1984-08-20 | Method of recovering waste heat from drying furnace for hydro-extraction |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6149981A (en) |
-
1984
- 1984-08-20 JP JP59171556A patent/JPS6149981A/en active Pending
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