JPS6354439B2 - - Google Patents

Info

Publication number
JPS6354439B2
JPS6354439B2 JP23413382A JP23413382A JPS6354439B2 JP S6354439 B2 JPS6354439 B2 JP S6354439B2 JP 23413382 A JP23413382 A JP 23413382A JP 23413382 A JP23413382 A JP 23413382A JP S6354439 B2 JPS6354439 B2 JP S6354439B2
Authority
JP
Japan
Prior art keywords
drain water
oil
liquid reservoir
water inlet
neutralization
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
Application number
JP23413382A
Other languages
Japanese (ja)
Other versions
JPS59123594A (en
Inventor
Shigeo Suzuki
Kenya Okamoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KOGATA GASU REIBO GIJUTSU KENKYU KUMIAI
Original Assignee
KOGATA GASU REIBO GIJUTSU KENKYU KUMIAI
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by KOGATA GASU REIBO GIJUTSU KENKYU KUMIAI filed Critical KOGATA GASU REIBO GIJUTSU KENKYU KUMIAI
Priority to JP23413382A priority Critical patent/JPS59123594A/en
Publication of JPS59123594A publication Critical patent/JPS59123594A/en
Publication of JPS6354439B2 publication Critical patent/JPS6354439B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、排気ガスからの熱回収装置に利用さ
れる中和処理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a neutralization treatment device used in a heat recovery device from exhaust gas.

従来例の構成とその問題点 近年、省エネルギー化、機器の高効率化に伴
い、排気ガス中の潜熱分をも有効に回収し、その
高効率化を計ろうとする傾向にあり、その際に生
じる高酸性ドレン水の中和処理が問題となつてい
る。
Conventional configuration and its problems In recent years, with energy saving and equipment becoming more efficient, there is a tendency to effectively recover the latent heat in exhaust gas and increase its efficiency. Neutralization of highly acidic drain water has become a problem.

第1図、第2図は従来の排気ガス熱回収装置に
設けられたドレン水中和処理装置の実施例を示す
ものである。第1図において1は、熱回収装置か
らのドレン水の入口であり、2はマグネシウム、
アルミニウム等の金属塊などの固形中和物質で、
ドレン水がこの物質表面と接触し、ドレン水流路
3を通過し、排出口4に達するまでの間に高酸性
ドレン水を中性に変えるものである。また第2図
において5はドレン水の入口、6は上記固形中和
物質7を封入した容器であり、入口5より滴下し
たドレン水が、7の中和物質と接触して排出口8
に達するまでの間に中和されるものである。
FIG. 1 and FIG. 2 show an embodiment of a drain water hydration treatment device installed in a conventional exhaust gas heat recovery device. In Fig. 1, 1 is the inlet of drain water from the heat recovery device, 2 is magnesium,
With solid neutralizing substances such as metal lumps such as aluminum,
The highly acidic drain water is changed into neutral water while the drain water comes into contact with the surface of the substance, passes through the drain water channel 3, and reaches the outlet 4. Further, in FIG. 2, 5 is an inlet of drain water, and 6 is a container in which the solid neutralizing substance 7 is sealed, and the drain water dripped from the inlet 5 comes into contact with the neutralizing substance 7, and is discharged to the outlet 8.
It is neutralized by the time it reaches .

以上のように構成された中和処理装置は、主と
してガス湯沸器などに用いられているものであ
り、熱交換器での凝縮水をそのまま上記中和処理
装置に直接導き、高酸性ドレン水を中性に変える
が、一般のガス湯沸器などに於いては、排気ガス
中成分は比較的清浄であり、油などの不純物質を
含まない。それ故凝縮水も清浄であり、中和物質
表面の汚れ、すなわち中和物質表面への油膜の生
成、堆積などがなく、常にその効果は保たれる事
ができる。しかしながら、熱源として内燃機関な
どを用い、その排気ガスの排熱を回収するような
場合、特に2サイクルエンジンで、潤滑油をも同
時に燃料として燃焼させるような場合には、排気
ガス中に油分が存在し、それ故ドレン水中にも、
油分あるいは、油の分解生成物が存在する。この
ような場合、上記のような構成ではこのドレン水
を直接中和物質に接触させると、その表面にこれ
らの物質が堆積したり、油膜を形成し、中和効果
が薄れてしまう欠点を有していた。
The neutralization treatment device configured as described above is mainly used in gas water heaters, etc., and the condensed water from the heat exchanger is directly guided to the neutralization treatment device, and highly acidic drain water is However, in general gas water heaters, the components in the exhaust gas are relatively clean and do not contain impurities such as oil. Therefore, the condensed water is also clean, and there is no dirt on the surface of the neutralized material, that is, no oil film formation or accumulation on the surface of the neutralized material, and the effect can be maintained at all times. However, when using an internal combustion engine as a heat source and recovering the exhaust heat from the exhaust gas, especially when using a two-stroke engine that also burns lubricating oil as fuel, oil content may be present in the exhaust gas. exist, therefore also in drain water,
Oil or oil decomposition products are present. In such cases, the above configuration has the disadvantage that if this drain water is brought into direct contact with neutralizing substances, these substances will accumulate on the surface or form an oil film, reducing the neutralizing effect. Was.

発明の目的 そこで本発明は上記欠点に鑑み、排気ガス中に
油分などの水に対して親和性のない物質を含む熱
回収装置に於いて、熱回収の際に生じる高酸性ド
レン水の中和処理を効率良く、長期に亘つて行な
うことを目的とする。
Purpose of the Invention In view of the above-mentioned drawbacks, the present invention aims to neutralize highly acidic drain water generated during heat recovery in a heat recovery device containing substances that have no affinity for water such as oil in the exhaust gas. The purpose is to carry out treatment efficiently and over a long period of time.

発明の構成 本発明は、マグネシウムなどの中和物質にドレ
ン水が入る前に、2室の液溜め室を設けて、それ
らの下部を連通させ、片方の液溜め室に開口する
中和物質へのドレン水流入口を、もう片方の液溜
め室に開口する油流出口よりも低位置に設けた構
成の油分離装置を具備した中和処理装置である。
Structure of the Invention The present invention provides two liquid reservoir chambers before drain water enters a neutralizing substance such as magnesium, communicates the lower parts of the chambers, and connects the neutralizing substance with an opening to one of the liquid reservoir chambers. This is a neutralization treatment device equipped with an oil separation device having a drain water inlet located at a lower position than an oil outlet opening into the other liquid storage chamber.

実施例の説明 以下本発明の一実施例について、図面を参照し
ながら説明する。第3図は本発明の実施例におけ
る中和処理装置を用いた熱回収装置の概略を示す
ものである。第3図において、9は熱源機であ
り、本実施例では動力装置としての2サイクルエ
ンジンである。10はそのエンジン動力を利用す
る機械装置、11はエンジン9の排気ガスを熱回
収する熱交換器、12は排気ガスの排出口であ
る。13は熱交換器11で熱回収される際に生じ
るドレン水の排出口であり、14の中和処理装置
に接続される。
DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 3 schematically shows a heat recovery device using a neutralization treatment device in an embodiment of the present invention. In FIG. 3, 9 is a heat source device, which in this embodiment is a two-stroke engine as a power device. 10 is a mechanical device that utilizes the engine power; 11 is a heat exchanger that recovers heat from exhaust gas from the engine 9; and 12 is an exhaust gas outlet. Reference numeral 13 designates an outlet for drain water produced when heat is recovered by the heat exchanger 11, and is connected to the neutralization processing device 14.

第4図は本発明の一実施例の中和処理装置の詳
細を示した図である。15は中和処理装置へのド
レン水導入口、16はドレン水中に含まれる油な
どの排出口、17は液溜め室A、18は液溜め室
Bであり、液溜め室Aと液溜め室Bとは底部が液
溜め室Aと液溜め室Bを連通させた仕切板19で
区分けされている。20は液溜め室Bに設けられ
中和物質21へのドレン水流入口であり、ドレン
水流入口20は油排出口16よりも距離Hだけ低
部に位置している。また21は中和物質で、22
はドレン水の流路である。23はドレン水排出口
である。
FIG. 4 is a diagram showing details of a neutralization processing apparatus according to an embodiment of the present invention. 15 is a drain water inlet to the neutralization processing device, 16 is an outlet for discharging oil contained in the drain water, 17 is a liquid reservoir chamber A, and 18 is a liquid reservoir chamber B. B is separated at the bottom by a partition plate 19 that communicates the liquid reservoir chamber A and the liquid reservoir chamber B. Reference numeral 20 denotes a drain water inlet port provided in the liquid reservoir B to the neutralizing substance 21, and the drain water inlet port 20 is located lower than the oil discharge port 16 by a distance H. Also, 21 is a neutralizing substance, and 22
is the drain water flow path. 23 is a drain water outlet.

以下その動作を説明する。まず、初期の状態に
於て、第4図の液溜め室A17と液溜め室B18
にドレン水流入口20と同レベルまで水を溜めて
おく。しかる後、第3図の熱交換器11にて発生
したドレン水導入口15より液溜め室A17に落
下させる。この時、液溜め室A17,B18には
ドレン水流入口20と同レベルまで水を溜めてい
るので、落下したドレン水分の水量はドレン水流
入口20より中和物質21に流れ、ドレン水の流
路22を通過しながら中和物質21と接触し、高
酸性のドレン水が中性となつてドレン水排出口2
3より排出される。この時、液溜め室A17にド
レン水と共に落下した油分は、水よりも比重が小
さいために、第4図に示すようにドレン水のレベ
ルより上部に浮遊する。そこで、ドレン水流入口
より少し高めのレベルに設けられた油排出口16
より中和処理装置14の外部に排出される。
The operation will be explained below. First, in the initial state, the liquid reservoir chamber A17 and the liquid reservoir chamber B18 in FIG.
Water is stored at the same level as the drain water inlet 20. Thereafter, the drain water generated in the heat exchanger 11 in FIG. 3 is dropped into the liquid storage chamber A17 from the inlet 15. At this time, since water is stored in the liquid storage chambers A17 and B18 to the same level as the drain water inlet 20, the amount of the drain water that has fallen flows from the drain water inlet 20 to the neutralizing substance 21, and the drain water flow path While passing through the drain water outlet 22, the highly acidic drain water comes into contact with the neutralizing substance 21 and becomes neutral.
It is discharged from 3. At this time, the oil that has fallen into the liquid storage chamber A17 together with the drain water has a lower specific gravity than water, so it floats above the level of the drain water as shown in FIG. Therefore, the oil drain port 16 is installed at a slightly higher level than the drain water inlet.
It is discharged to the outside of the neutralization treatment device 14.

以上のように本実施例によれば、2室の液溜め
室A17,B18を設け、中和物質21へのドレ
ン水流入口20よりも、上部位置に油排出口16
を設ける事により、ドレン水中に混在せる水より
も比重の小さい油分を浮かせ、油排出口16よ
り、中和処理装置の外部に排出せる事ができ、中
和物質21への油の流込みがなくなり、中和物質
表面への油付着などがなくなり、中和処理を効率
良く行なえる。また液溜め室A17,B18は仕
切板19により、下部を連通せしめて仕切つてい
るので液溜め室A,Bの水位が低下しても、液溜
め室B18に油が入らず、常に油排出口16のあ
る液溜め室A17に浮遊する事になり中和物質へ
の油の流入が防げる。
As described above, according to this embodiment, two liquid reservoir chambers A17 and B18 are provided, and the oil outlet 16 is located above the drain water inlet 20 to the neutralizing substance 21.
By providing this, oil having a specific gravity lower than water mixed in the drain water can be floated and discharged from the oil outlet 16 to the outside of the neutralization treatment equipment, thereby preventing the oil from flowing into the neutralization substance 21. This eliminates oil adhesion to the surface of the neutralized substance, allowing efficient neutralization. In addition, the liquid reservoir chambers A17 and B18 are partitioned by a partition plate 19 with their lower parts communicating with each other, so even if the water level in the liquid reservoir chambers A and B decreases, oil will not enter the liquid reservoir chamber B18 and there will always be an oil outlet. Since the oil is suspended in the liquid reservoir A17 where the neutralizing substance is located, the oil is prevented from flowing into the neutralizing substance.

発明の効果 中和物質への油の流れ込みを防止し、中和処理
が効率良く長期に亘つて行う事ができる。
Effects of the invention It is possible to prevent oil from flowing into the neutralizing substance, and neutralization processing can be carried out efficiently over a long period of time.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図および第2図は従来の異なる実施例の中
和処理装置の断面図、第3図は本発明の一実施例
の中和処理装置を具備した熱回収装置の概略図、
第4図は本発明の一実施例の中和処理装置の断面
図である。 16……油排出口、17,18……液溜め室、
19……仕切板、20……ドレン水流入口、21
……中和物質、22……ドレン水流路、23……
ドレン水排出口。
1 and 2 are cross-sectional views of conventional neutralization processing equipment according to different embodiments, and FIG. 3 is a schematic diagram of a heat recovery equipment equipped with a neutralization processing equipment according to an embodiment of the present invention.
FIG. 4 is a sectional view of a neutralization treatment apparatus according to an embodiment of the present invention. 16...Oil discharge port, 17,18...Liquid reservoir chamber,
19... Partition plate, 20... Drain water inlet, 21
... Neutralizing substance, 22 ... Drain water flow path, 23 ...
Drain water outlet.

Claims (1)

【特許請求の範囲】[Claims] 1 液溜室を、その下部を連通させた状態で仕切
り、一方の液溜室の上部に熱回収部からのドレン
水導入口と油流出口を設け、他方の液溜室に中和
物質部へのドレン水流入口を設け、前記油流出口
を前記ドレン水流入口より高い位置に設けた中和
処理装置。
1 The liquid storage chamber is partitioned with its lower part communicating with each other, and the upper part of one liquid storage chamber is provided with a drain water inlet from the heat recovery section and the oil outlet, and the other liquid storage chamber is provided with a neutralizing substance section. A neutralization treatment device, wherein a drain water inlet is provided, and the oil outlet is provided at a higher position than the drain water inlet.
JP23413382A 1982-12-29 1982-12-29 Neutralization apparatus Granted JPS59123594A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23413382A JPS59123594A (en) 1982-12-29 1982-12-29 Neutralization apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23413382A JPS59123594A (en) 1982-12-29 1982-12-29 Neutralization apparatus

Publications (2)

Publication Number Publication Date
JPS59123594A JPS59123594A (en) 1984-07-17
JPS6354439B2 true JPS6354439B2 (en) 1988-10-27

Family

ID=16966150

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23413382A Granted JPS59123594A (en) 1982-12-29 1982-12-29 Neutralization apparatus

Country Status (1)

Country Link
JP (1) JPS59123594A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2502501B2 (en) * 1985-03-16 1996-05-29 日立マクセル株式会社 Information recording system
JP4604635B2 (en) * 2004-10-04 2011-01-05 株式会社ノーリツ Hot water supply device equipped with a drain treatment device
JP2009172535A (en) * 2008-01-25 2009-08-06 Gastar Corp Neutralization device and combustion apparatus equipped with the same
JP5758319B2 (en) * 2012-02-13 2015-08-05 株式会社コロナ Neutralizer and hot water supply apparatus having the same

Also Published As

Publication number Publication date
JPS59123594A (en) 1984-07-17

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