JPS6220876B2 - - Google Patents
Info
- Publication number
- JPS6220876B2 JPS6220876B2 JP1391582A JP1391582A JPS6220876B2 JP S6220876 B2 JPS6220876 B2 JP S6220876B2 JP 1391582 A JP1391582 A JP 1391582A JP 1391582 A JP1391582 A JP 1391582A JP S6220876 B2 JPS6220876 B2 JP S6220876B2
- Authority
- JP
- Japan
- Prior art keywords
- main body
- acidic
- condensed water
- outlet
- inlet
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 230000002378 acidificating effect Effects 0.000 claims description 31
- 239000000126 substance Substances 0.000 claims description 7
- 238000009833 condensation Methods 0.000 description 14
- 230000005494 condensation Effects 0.000 description 14
- 230000003472 neutralizing effect Effects 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 10
- 238000002485 combustion reaction Methods 0.000 description 8
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000000567 combustion gas Substances 0.000 description 4
- 238000006386 neutralization reaction Methods 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
Description
【発明の詳細な説明】
本発明は石油燃焼機、ガス湯沸器等に用いられ
る潜熱型熱交換器で生じる酸性結露水の処理装置
に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for treating acidic condensation water generated in latent heat type heat exchangers used in oil combustion machines, gas water heaters, and the like.
従来の石油燃焼機やガス湯沸器においては、一
次熱交換器で全燃焼熱の80%を利用していたが、
省エネルギーの観点から潜熱型熱交換器を用いて
90%以上の熱効率を有する燃焼器具が開発されて
きた。 In conventional oil-burning machines and gas water heaters, 80% of the total combustion heat is used in the primary heat exchanger.
Using a latent heat exchanger from the perspective of energy saving
Combustion appliances have been developed that have thermal efficiencies of over 90%.
熱交換を一次熱交換器のみで行う場合には、燃
焼ガス中に含まれる窒素酸化物や、二酸化炭素が
そのまま大気中に排出されるが、潜熱型熱交換器
を用いて熱交換を行うことにより、排出される燃
焼ガスの温度が著しく低下して50〜60℃となる。
従つて燃焼ガス中に含まれる水分が結露し、この
結露水に窒素酸化物や二酸化炭素が溶解して酸性
結露水となる。 When heat exchange is performed only with a primary heat exchanger, nitrogen oxides and carbon dioxide contained in the combustion gas are emitted as they are into the atmosphere, but heat exchange can be performed using a latent heat exchanger. As a result, the temperature of the emitted combustion gas drops significantly to 50-60°C.
Therefore, the moisture contained in the combustion gas condenses, and nitrogen oxides and carbon dioxide are dissolved in this condensed water to become acidic condensed water.
この酸性結露水は排水管を腐食したり、また外
部へ排出するとコンクリートを溶かす等の弊害が
生じる。この対策として流入口と流出口とを有す
る容器に塩基性物質からなる中和剤を充填し、こ
の容器中に酸性結露水を流入して中和処理を行つ
ていた。その従来例を第2図にもとづいて説明す
る。 This acidic condensation water corrodes drain pipes, and when discharged to the outside, it causes problems such as melting concrete. As a countermeasure to this problem, a neutralizing agent made of a basic substance is filled in a container having an inlet and an outlet, and acidic condensed water is flowed into the container to effect neutralization. The conventional example will be explained based on FIG. 2.
第2図において1は酸性結露水の中和処理装置
の本体で、上部に流入口2、下部に流出口3が設
けられている。21は本体1内に設けられた酸性
結露水の流路で、この流路21には塩基性物質か
らなる中和剤6が設けられている。22は本体1
内に設けられた酸性結露水のバイパス流路であ
る。 In FIG. 2, reference numeral 1 denotes the main body of the apparatus for neutralizing acidic condensed water, which has an inlet 2 in the upper part and an outlet 3 in the lower part. Reference numeral 21 denotes a flow path for acidic condensed water provided in the main body 1, and a neutralizing agent 6 made of a basic substance is provided in this flow path 21. 22 is main body 1
This is a bypass flow path for acidic condensed water provided inside.
このように構成された酸性結露水の処理装置に
おいて、燃焼器具の燃焼量を変化させる当然酸性
結露水の生じる量が変化するため、流出口3から
排出される酸性結露水の酸性度(水素イオン濃度
指数:PH)が変化する。 In the acidic condensation water treatment device configured in this way, since the amount of acidic condensed water produced naturally changes, which changes the combustion amount of the combustion appliance, the acidity (hydrogen ion Concentration index (PH) changes.
また中和剤6は流入口2側から劣化していくた
め、所定量の酸性結露水を処理するには、相当量
以上の中和剤6を設ける必要があり、従つて本体
1が必要以上に大きくなるという欠点があつた。 In addition, since the neutralizing agent 6 deteriorates from the inlet 2 side, in order to treat a predetermined amount of acidic condensed water, it is necessary to provide a considerable amount or more of the neutralizing agent 6. It had the disadvantage of becoming larger.
本発明は流入口を有する本体と、この本体に設
けられた高さの異なる複数の流出口と、前記本体
内に設けられた所定量の管状体からなる塩基性物
質とで酸性結露水の処理装置を構成することによ
り、上記従来の欠点を解消するものである。 The present invention processes acidic condensed water using a main body having an inlet, a plurality of outlet ports provided in the main body at different heights, and a basic substance consisting of a predetermined amount of a tubular body provided in the main body. By configuring the device, the above-mentioned conventional drawbacks are solved.
以下本発明の一実施例を第1図にもとづいて説
明する。 An embodiment of the present invention will be described below based on FIG.
なお、従来例と同じ部材については同一符号を
付して説明する。 Note that the same members as in the conventional example will be described with the same reference numerals.
第1図において1はアクリル樹脂等からなる酸
性結露水の処理装置の本体で、外径が38ミリ、内
径が24ミリ、高さが123ミリに構成され、上部に
酸性結露水の流入口2、側部には高さの異なる複
数の流出口3,4,5が設けられている。流出口
3の高さHは本体1の底面から16ミリの位置に、
流出口4の高さH′は本体1の底面から26ミリの
位置に設けられている。また流出口3の内径は2
ミリ、流出口4の内径は3ミリに構成されてい
る。6は本体1内に設けられた塩基性物質のマグ
ネシウム管からなる中和剤で、この中和剤6の重
量は23g、外径l20ミリ、内径l′12ミリ、高さ
H″90ミリに構成されている。7は本体1内に位
置して中和剤6の下部に設けられた置台で、本体
1内の酸性結露水8が中和剤6の内側へ流入しや
すくするためのものである。9は中和された結露
水を排出する排水管である。 In Figure 1, 1 is the main body of the acidic condensation water treatment device made of acrylic resin, etc., and has an outer diameter of 38 mm, an inner diameter of 24 mm, and a height of 123 mm. , a plurality of outlet ports 3, 4, and 5 having different heights are provided on the sides. The height H of the outlet 3 is 16 mm from the bottom of the main body 1.
The height H' of the outlet 4 is set at a position of 26 mm from the bottom of the main body 1. Also, the inner diameter of the outlet 3 is 2
mm, and the inner diameter of the outlet 4 is 3 mm. Reference numeral 6 is a neutralizer made of a basic magnesium tube installed inside the main body 1, and the weight of this neutralizer 6 is 23 g, the outer diameter is 20 mm, the inner diameter is 12 mm, and the height is
7 is a stand located inside the main body 1 and provided below the neutralizer 6, so that the acidic condensed water 8 inside the main body 1 flows into the inside of the neutralizer 6. 9 is a drain pipe for discharging neutralized condensed water.
このように構成された酸性結露水の処理装置に
おいて、流入口2より温度30℃、PH4の酸性結露
水を60ml/Hの割合で流入すると、本体1内に設
けられた中和剤6でPH8.5に中和された結露水が
流出口3から排出される。 In the acidic condensation water treatment device configured as described above, when acidic condensed water with a temperature of 30°C and a pH of 4 flows in from the inlet 2 at a rate of 60ml/H, the neutralizer 6 provided in the main body 1 reduces the pH to 8. The condensed water neutralized to .5 is discharged from the outlet 3.
また流入口2より温度30℃、PH3.5の酸性結露
水を180ml/Hの割合で流入すると、本体1内に設
けられた中和剤6でPH6に中和された結露水が流
出口3と4とから排出される。このPH3.5の酸性
結露水を180ml/Hの割合で流入口2から本体1内
に流入すると、5ppmの中和剤6が溶出する。従
つて23gの中和剤6が消滅するには26000時間要
し、年間の使用時間を1000時間とすれば26年間使
用することができる。 In addition, when acidic condensed water with a temperature of 30℃ and PH3.5 flows in from the inlet 2 at a rate of 180ml/H, the condensed water is neutralized to a pH of 6 by the neutralizer 6 provided in the main body 1, and the condensed water is neutralized to a pH of 6 at the outlet 3. and 4. When this acidic condensed water with a pH of 3.5 flows into the main body 1 from the inlet 2 at a rate of 180 ml/H, 5 ppm of the neutralizing agent 6 is eluted. Therefore, it takes 26,000 hours for 23g of neutralizing agent 6 to disappear, and if the annual usage time is 1,000 hours, it can be used for 26 years.
なお、この本体1の内径と中和剤6の外径l及
び内径l′との関係は、中和処理能力に大きい影響
をおよぼす要因であるため相関関係を最適に設け
る必要がある。 Note that the relationship between the inner diameter of the main body 1 and the outer diameter l and inner diameter l' of the neutralizing agent 6 is a factor that greatly influences the neutralization processing ability, so it is necessary to establish an optimal correlation.
酸性結露水の処理装置をこのように構成したこ
とにより、燃焼器具の燃焼量を変化させて燃焼ガ
スから生じる酸性結露水8の量が変化しても、酸
性結露水8と接触する中和剤6の表面積が酸性結
露水8の量とともに変化して酸性結露水8を中和
し、かつ各々高さの異つた流出口3,4から中和
された結露水が排出されるため、中和剤6の中和
能力をあまり低下することなく、ほぼ中性の状態
で排出することができる。 By configuring the acidic condensation water treatment device in this way, even if the amount of acidic condensed water 8 generated from the combustion gas changes by changing the combustion amount of the combustion appliance, the neutralizing agent that comes into contact with the acidic condensed water 8 changes. The surface area of the condensed water 6 changes with the amount of the acidic condensed water 8 to neutralize the acidic condensed water 8, and the neutralized condensed water is discharged from the outlet ports 3 and 4, which have different heights, so that the neutralization is achieved. The agent 6 can be discharged in a substantially neutral state without significantly reducing its neutralizing ability.
また酸性結露水の処理装置の本体1内に設けら
れた中和剤6を管状体としたことにより、本体1
を小型に構成することが可能となる。 In addition, by making the neutralizer 6 provided in the main body 1 of the acidic condensation water treatment device into a tubular body, the main body 1
It becomes possible to configure it in a small size.
以上の説明から明らかな如く本発明の酸性結露
水の処理装置は、所定量の管状体からなる塩基性
物質を高さの異なる複数の流出口を有する本体に
設けたことにより、燃焼量の変化に伴つて生じる
酸性結露水の量が変化しても、酸性結露水と接触
する管状体の塩基性物質の表面積が変化し、酸性
結露水を中和して本体に設けられた高さの異なる
流出口から各々排出されるため、管状体からなる
塩基性物質の中和能力の低下が少なく、しかも小
型で処理能力の優れた酸性結露水の処理装置を提
供することができる。 As is clear from the above description, the acidic condensation water treatment device of the present invention is capable of changing the amount of combustion by providing a predetermined amount of basic material consisting of a tubular body in a main body having a plurality of outlet ports at different heights. Even if the amount of acidic condensation water that occurs changes, the surface area of the basic substance in the tubular body that comes into contact with the acidic condensation water changes, and the acidic condensation water is neutralized and the Since they are each discharged from the outlet, there is little reduction in the ability of the tubular body to neutralize basic substances, and it is possible to provide a small-sized acidic condensation water treatment device with excellent processing ability.
第1図は本発明の一実施例を示す酸性結露水の
処理装置の断面図、第2図は従来例を示す酸性結
露水の処理装置の断面図である。
1……本体、2……流入口、3,4,5……流
出口、6……中和剤(塩基性物質)。
FIG. 1 is a cross-sectional view of an acidic condensation water treatment apparatus showing an embodiment of the present invention, and FIG. 2 is a cross-sectional view of an acidic condensation water treatment apparatus showing a conventional example. 1... Main body, 2... Inlet, 3, 4, 5... Outlet, 6... Neutralizing agent (basic substance).
Claims (1)
た高さの異なる複数の流出口と、前記本体内に設
けられた所定量の管状体からなる塩基性物質とで
構成した酸性結露水の処理装置。1 Treatment of acidic condensed water consisting of a main body having an inlet, a plurality of outlet ports at different heights provided in the main body, and a basic substance consisting of a predetermined amount of tubular bodies provided in the main body. Device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57013915A JPS58131194A (en) | 1982-01-29 | 1982-01-29 | Acidic condensation water treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57013915A JPS58131194A (en) | 1982-01-29 | 1982-01-29 | Acidic condensation water treatment equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58131194A JPS58131194A (en) | 1983-08-04 |
| JPS6220876B2 true JPS6220876B2 (en) | 1987-05-09 |
Family
ID=11846459
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57013915A Granted JPS58131194A (en) | 1982-01-29 | 1982-01-29 | Acidic condensation water treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58131194A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4553429B2 (en) | 1999-11-25 | 2010-09-29 | パナソニック株式会社 | Disk unit |
-
1982
- 1982-01-29 JP JP57013915A patent/JPS58131194A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58131194A (en) | 1983-08-04 |
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