JPS59123594A - Neutralization apparatus - Google Patents

Neutralization apparatus

Info

Publication number
JPS59123594A
JPS59123594A JP23413382A JP23413382A JPS59123594A JP S59123594 A JPS59123594 A JP S59123594A JP 23413382 A JP23413382 A JP 23413382A JP 23413382 A JP23413382 A JP 23413382A JP S59123594 A JPS59123594 A JP S59123594A
Authority
JP
Japan
Prior art keywords
drain water
oil
water
liquid storage
drain
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.)
Granted
Application number
JP23413382A
Other languages
Japanese (ja)
Other versions
JPS6354439B2 (en
Inventor
Shigeo Suzuki
茂夫 鈴木
Kenya Okamoto
岡本 ▲けん▼也
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 GAS REIBOU GIJUTSU KENKYU KUMIAI
Original Assignee
KOGATA GAS REIBOU 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 GAS REIBOU GIJUTSU KENKYU KUMIAI filed Critical KOGATA GAS REIBOU 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

Abstract

PURPOSE:To neutralize efficiently highly acidic drain water formed when heat is recovered by arranging a drain inflow port opened to one of the two liquid storage chambers communicated with each other at the bottom at a lower position than an oil outflow port opened to the other liquid storage chamber. CONSTITUTION:A liquid storage chamber A17 and a liquid storage chamber B18 are previously filled with water to the same level as a drain water inflow port 20. Then the drain water generated from a heat exchanger 11 is dropped 15 into the chamber A17. At this time, as the chambers A17 and B18 are filled with water to the same level as the inflow port 20, the same amt. of water as that of the dropped drain water is allowed to flow into a neutralization substance 21 such as Mg through the inflow port 20, and the acidic drain water is neutralized and discharged 23. Oil components dropped in the chamber A17 along with the drain water are floated above the drain surface and discharged to the outside of a neutralization apparatus 14 through an oil discharge port 16 arranged at a level slightly higher than the inflow port 20. Thus the inflow of oil to the substance 21 and the adhesion of oil to the surface of the substance 21 are prevented, and the neutralization is effected effectively. The 9 in the figure shows a heat generating machine.

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 the Invention 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
和処理が問題となっている。
Conventional configuration and its problems In recent years, with energy saving and equipment becoming more efficient, there is a trend to effectively recover 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。
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, and 2 is magnesium.

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に達する捷での間に高酸性ドレン水を中性に変
えるものである。捷だ第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。
With a solid neutralizing substance such as a metal lump such as aluminum, the drain water contacts the surface of this substance and passes through the drain water flow path 3,
The highly acidic drain water is changed into neutral water during the process of reaching the discharge port 4. In Figure 2, 5 is an inlet for drain water, and 6 is a container containing the solid neutralizing substance 7, and the drain water dripping from the inlet 5 comes into contact with the neutralizing substance 7 and flows to the outlet 8. It will be neutralized before reaching the target.

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
不純物質を含ま々い。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々どを用い、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
うな場合にはく排気カ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捷
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 an internal combustion engine is used as a heat source and the exhaust heat of the exhaust gas is recovered, especially when using a two-stroke engine and lubricating oil is also burned as fuel at the same time, oil content may be generated in the exhaust gas. Therefore, oil or oil decomposition products are also present in the drain water. In such cases, with the above configuration, if this drain water is brought into direct contact with neutralizing substances, these substances may accumulate on the surface or form an oil film, which weakens the neutralizing effect and causes the drain water to come into contact with neutralizing substances. It had

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、長期に亘って行なっユヒ先目6リヒ1う。
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. Treatment should be carried out 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 drain water to the neutralizing substance with an opening in 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。
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.

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。
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。16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A118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。2Q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. 16 is a drain water inlet to the neutralization treatment device;
16 is a discharge port for oil contained in drain water, 17 is a liquid storage chamber A, 118 is a liquid storage chamber B, and the bottoms of the liquid storage chamber A and liquid storage chamber B are connected to each other. They are separated by a partition plate 19 that communicates with them. 2Q is a drain water inlet provided in the liquid reservoir B, and is a drain water inlet to the neutralizing substance 21, and the drain water inlet 20 is located lower than the oil discharge port 16 by a distance H. Further, 21 is a neutralizing substance, and 22 is a flow path for drain water. 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にドレン水流人
口20と同しベル捷で水を溜めておく。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2o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
水が中性と々ってドレン水排出口23より排出される。
The operation will be explained below. First, in the initial state, water is stored in the liquid reservoir chamber A17 and the liquid reservoir chamber B18 in FIG. After that, the third
Drain water generated in the heat exchanger 11 shown in the figure is dropped into the liquid storage chamber A17 from the inlet 15. At this time, liquid reservoir chamber A17
.. Since water is stored in B18 to the same level as the drain water inlet 2o, 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 flows through the drain water flow path 22.
While passing through, the highly acidic drain water comes into contact with the neutralizing substance 21, and the highly acidic drain water becomes neutral and is discharged from the drain water outlet 23.

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
トレン水のレベルより上部に浮遊する。そこで、ドレン
水流入口よシ少し高めのレベルに設けられた油排出口1
6より中和処理装置14の外部に排出される。
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. 4. Therefore, the oil drain port 1 was installed at a slightly higher level than the drain water inlet.
6 and is discharged to the outside of the neutralization processing device 14.

以上のように本実施例によれば、2室の液溜め室A17
,81Bを設け、中和物質21へのトレン水流入口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っているの−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, the two liquid reservoir chambers A17
, 81B are provided, and the tren water inlet 20 to the neutralizing substance 21 is provided.
By providing the oil outlet 16 at the upper position, the oil, which has a specific gravity lower than the water mixed in the drain water, can be floated and discharged from the oil outlet 16 to the outside of the neutralization treatment equipment. Oil does not flow into the neutralizing substance 21, oil does not adhere to the surface of the neutralizing substance, and the neutralization process can be carried out efficiently. Also, the liquid reservoir chamber A17. B18 is the partition plate 19
Because the lower part is connected and partitioned, even if the water level in the liquid reservoir chambers A and B decreases, oil will not enter the liquid reservoir chamber B18 and will always float in the liquid reservoir chamber A17 where the oil outlet 16 is located. This prevents oil from entering 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
く長期に亘って行う事ができる。
Effects of the Invention Oil can be prevented from flowing into the neutralizing substance, and neutralization can be carried out efficiently over a long period of time.

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

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、2
2・  ドレン水流路、23 ・ドレン水排出口。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第2
FIG. 2 is a sectional view of a neutralization processing 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, 2
2. Drain water flow path, 23. Drain water outlet. Name of agent: Patent attorney Toshio Nakao and 1 other person 2nd
figure

Claims (1)

【特許請求の範囲】[Claims] 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。
The liquid storage chamber is partitioned with its lower part communicating, and the upper part of one liquid storage chamber is provided with a drain water inlet and an oil outlet from the heat recovery section, and the other liquid storage chamber is connected to the neutralizing substance section. A neutralization treatment device comprising: a drain water inlet, and an oil outlet located 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 true JPS59123594A (en) 1984-07-17
JPS6354439B2 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)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61211791A (en) * 1985-03-16 1986-09-19 Hitachi Maxell Ltd Optical recording card
JP2006102617A (en) * 2004-10-04 2006-04-20 Noritz Corp Drain treatment apparatus and hot-water supply apparatus equipped with the same
JP2009172535A (en) * 2008-01-25 2009-08-06 Gastar Corp Neutralization device and combustion apparatus equipped with the same
JP2013163167A (en) * 2012-02-13 2013-08-22 Corona Corp Neutralization apparatus and hot water supply device having the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61211791A (en) * 1985-03-16 1986-09-19 Hitachi Maxell Ltd Optical recording card
JP2006102617A (en) * 2004-10-04 2006-04-20 Noritz Corp Drain treatment apparatus and hot-water supply apparatus equipped with the same
JP2009172535A (en) * 2008-01-25 2009-08-06 Gastar Corp Neutralization device and combustion apparatus equipped with the same
JP2013163167A (en) * 2012-02-13 2013-08-22 Corona Corp Neutralization apparatus and hot water supply device having the same

Also Published As

Publication number Publication date
JPS6354439B2 (en) 1988-10-27

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