JPS5836280B2 - Water treatment method for heat exchanger for sintering exhaust gas treatment - Google Patents
Water treatment method for heat exchanger for sintering exhaust gas treatmentInfo
- Publication number
- JPS5836280B2 JPS5836280B2 JP51133216A JP13321676A JPS5836280B2 JP S5836280 B2 JPS5836280 B2 JP S5836280B2 JP 51133216 A JP51133216 A JP 51133216A JP 13321676 A JP13321676 A JP 13321676A JP S5836280 B2 JPS5836280 B2 JP S5836280B2
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- water
- exhaust gas
- dust
- temperature
- 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 title claims description 34
- 238000000034 method Methods 0.000 title claims description 4
- 238000005245 sintering Methods 0.000 title description 7
- 239000000428 dust Substances 0.000 claims description 30
- 238000006477 desulfuration reaction Methods 0.000 claims description 11
- 230000023556 desulfurization Effects 0.000 claims description 11
- 239000002562 thickening agent Substances 0.000 claims description 8
- 238000005406 washing Methods 0.000 claims description 7
- 239000006228 supernatant Substances 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 2
- 238000010586 diagram Methods 0.000 description 4
- 238000007789 sealing Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 241001653678 Russula emetica Species 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
Landscapes
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
【発明の詳細な説明】
この発明は、焼結機等からの排ガスを処理する装置にお
ける熱交換器の水処理方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water treatment method for a heat exchanger in an apparatus for treating exhaust gas from a sintering machine or the like.
焼結機から発生する焼結排ガスは、100万Nrn’/
Hr以上の大量で、この排ガス中のダストは5 0 〜
2 0 0m9/ Nm”の多量であり、しかも、排ガ
ス中には10〜12%の水分が含壕れている。The sintering exhaust gas generated from the sintering machine is 1 million Nrn'/
In a large amount of Hr or more, the dust in this exhaust gas is 50 ~
200 m9/Nm'', and furthermore, the exhaust gas contains 10 to 12% moisture.
このような焼結排ガスを大気中に排棄(放散)するに際
しては、公害発生防止等の関係から無害化する必要があ
り、このため前記排気ガスは、脱硫装置により脱硫する
と共に、集塵機により除塵してから、煙突を介して大気
中に放散しているが、前記排ガスの温度は通常約150
℃程度の高温なので、その1寸脱硫装置に導入すると反
応温度が高すぎて脱硫効率が悪化するとともに装置の損
傷のおそれもでてくる等の問題がある。When discharging (dispersing) such sintering exhaust gas into the atmosphere, it is necessary to make it harmless in order to prevent pollution, etc. Therefore, the exhaust gas is desulfurized by a desulfurization device and dust is removed by a dust collector. After that, it is released into the atmosphere through the chimney, but the temperature of the exhaust gas is usually about 150℃.
Since the temperature is as high as 0.degree. C., there are problems such as the reaction temperature being too high when introduced into the 1-inch desulfurization device, which deteriorates the desulfurization efficiency and may damage the device.
したがって、従来は、第1図に排ガスの脱硫除塵処理装
置の概略図で示されるように、熱交換器1を使用し、こ
の熱交換器1に降温用ガスとして焼結機等からの未処理
排ガスを導き、前記未処理排ガスを、前記熱交換器1に
お・いてその温度をたとえば150℃から90℃に降温
させてから、(湿式)脱硫装置2に導いて脱硫処理し、
ついで脱硫処理後の温度が50℃程度に下がった排ガス
を、集塵機3に導いて除塵し、ついで除塵処理後の排ガ
スを、ブロア4を介して、昇温用ガスとして前記熱交換
器1を通過させて、その温度を50℃から110’C程
度に昇温させ、ついで前記110℃程度の処理排ガスを
、大気放散に適する120℃程度に昇温させるべ〈再カ
ロ熱炉5を通過させて煙突6に導き大気中に放散させて
いた。Therefore, conventionally, as shown in the schematic diagram of an exhaust gas desulfurization and dust removal treatment device in FIG. The untreated exhaust gas is passed through the heat exchanger 1 to lower its temperature from, for example, 150°C to 90°C, and then led to the (wet type) desulfurization device 2 for desulfurization treatment;
Next, the exhaust gas whose temperature has dropped to about 50° C. after the desulfurization treatment is guided to a dust collector 3 to remove dust, and then the exhaust gas after the dust removal treatment is passed through the heat exchanger 1 as a heating gas via a blower 4. The temperature should be raised from 50°C to about 110'C, and then the treated exhaust gas at about 110°C should be heated to about 120°C, which is suitable for dissipation into the atmosphere. It was led to chimney 6 and dissipated into the atmosphere.
しかしながら、前記熱交換器1の伝熱エレメントには夕
“ストを多量に含んだ未処理排ガスが通過するので、時
間の経過とともに、ダストが付着し、この結果、前記熱
交換器1は、熱交換効率が悪化すると共に、いわゆるつ
1りが生じるという問題があり、しかも回転式熱交換器
の場合には伝熱エレメントが回転し、付着したダストが
昇温用ガス中にその通過の際に混入することによって大
気中にダストが放散されるという問題があった。However, since untreated exhaust gas containing a large amount of dust passes through the heat transfer element of the heat exchanger 1, dust adheres to it over time, and as a result, the heat exchanger 1 loses heat. There is a problem that the exchange efficiency deteriorates and so-called sagging occurs.Moreover, in the case of a rotary heat exchanger, the heat transfer element rotates, and the attached dust is absorbed into the heating gas as it passes through. There was a problem in that dust was dispersed into the atmosphere due to the mixing.
そこでこの発明は以上のような問題を解決し、熱交換器
の熱交換効率を良好に保持すると共につ筐りをなくし、
しかもターストが脱硫除塵処理後のガスに混入するのを
防止した焼結排ガス処理用熱交換器の水処理方法を提供
するもので、降温用ガスとして焼結未処理排ガスを通過
させると共に、昇温用ガスとして脱硫除塵処理後の焼結
排ガスを通過させるための熱交換器において、前記熱交
換器をその上部から散水することによって水洗滌し、前
記熱交換器からの洗滌水を、前記熱交換器の下部からシ
ツクナーに導き、前記シツクナーの上澄水を、前記熱交
換器の洗滌水として循環使用することに特徴を有する。Therefore, this invention solves the above problems, maintains the heat exchange efficiency of the heat exchanger well, and eliminates the need for a casing.
Moreover, it provides a water treatment method for a heat exchanger for sintering exhaust gas treatment that prevents tarst from being mixed into the gas after desulfurization and dust removal treatment. In a heat exchanger for passing sintering exhaust gas after desulfurization and dust removal treatment as a cleaning gas, the heat exchanger is washed with water by spraying water from above, and the washing water from the heat exchanger is used to pass through the heat exchanger. It is characterized in that it is led to a thickener from the lower part of the vessel, and the supernatant water of the thickener is circulated and used as washing water for the heat exchanger.
以下この発明を、実施例により図面とともに説明する。The present invention will be explained below with reference to examples and drawings.
第2図はこの発明を回転式熱交換器に適用した場合の概
略図であって、7は回転式熱交換器(以下熱交換器とい
う)、8は前記熱交換器7の下部に気密に取付けたダス
トホツパー、9は前記熱交換器7の上部に取付けた散水
管であり、前記散水管9から散水された洗滌水は前記熱
交換器7の伝熱エレメントを洗滌した後、前記ダストホ
ッパー8に導かれるようになっている。FIG. 2 is a schematic diagram of the case where the present invention is applied to a rotary heat exchanger, in which 7 is a rotary heat exchanger (hereinafter referred to as a heat exchanger), and 8 is an airtight structure installed at the bottom of the heat exchanger 7. The installed dust hopper 9 is a water sprinkling pipe installed on the upper part of the heat exchanger 7, and the cleaning water sprayed from the water sprinkling pipe 9 washes the heat transfer element of the heat exchanger 7, and then flows into the dust hopper 8. It is designed to be guided by
10は前記ダストホッパ−8の下部を水封するための水
封槽であり、前記水封槽10からの水は、ポンプ11を
介してシツクナー12に導かれるようになっている。10 is a water sealing tank for sealing the lower part of the dust hopper 8 with water, and water from the water sealing tank 10 is led to a thickener 12 via a pump 11.
前記シツクナー12の上澄水は、ポンプ13を介して必
要に応じて前記散水管9に導かれるようになっていて、
前記シツクナー12の底部の夕゛ストを含んだ沈殿液は
、ポンプ14を介してダスト分離器15に導かれ、この
ダスト分離器15において、ダストが除去され、ダスト
除去後の水がシツクナー12に戻されるようになってい
る。The supernatant water of the thickener 12 is guided to the water sprinkling pipe 9 via a pump 13 as needed,
The precipitate containing dust at the bottom of the thickener 12 is led to the dust separator 15 via the pump 14, where the dust is removed and the water after the dust removal is sent to the thickener 12. It is set to be returned.
16は熱交換器7の降温用ガスのダクト、17は昇温用
ガスのダクトであって、熱交換器7の上部に取付げたダ
クN6,17内に散水管9が位置している。16 is a duct for the temperature-lowering gas of the heat exchanger 7, 17 is a duct for the temperature-raising gas, and the water sprinkler pipe 9 is located in the duct N6, 17 attached to the upper part of the heat exchanger 7.
このような構成によって、必要に応じて散水管9から水
を散水すれば、熱交換器7の伝熱エレメントは洗滌され
、ダストが付着していた場合にはこれが洗い落とされ、
ダストホッパ−8を介してシツクナ−12に至り、夕゛
スト分離器15によって回収される一方、夕゛ストが除
去された水は再び散水管9に送られて洗滌水として使用
される。With such a configuration, the heat transfer element of the heat exchanger 7 is cleaned by sprinkling water from the water sprinkler pipe 9 as necessary, and if dust is attached, it is washed off.
The water reaches the dust tanker 12 via the dust hopper 8 and is recovered by the dust separator 15, while the water from which the dust has been removed is again sent to the sprinkler pipe 9 and used as washing water.
以上説明したように、.この発明においては、洗滌水に
よって適宜伝熱エレメントが洗滌されるので、熱交換効
率が下がることがなく、壕たダストが大気中に放散され
るおそれもなく、しかも水は循環使用によって有効利用
することができる。As explained above,. In this invention, since the heat transfer element is appropriately washed with washing water, the heat exchange efficiency does not decrease and there is no fear that trapped dust will be dissipated into the atmosphere, and water can be used effectively by being recycled. be able to.
第1図は排ガスの脱硫除塵処理装置の概略図、第2図は
この発明を回転式熱交換器に適用した状態の概略図であ
る。
1,7・・・熱交換器、2・・・脱硫装置、3・・・集
塵機、4・・・ブロア、5・・・再加熱炉、6・−・煙
突、8・・・夕゛ストホッパ− 9・・・散水管、10
・・・水封槽、11,13.14・・・ポンプ、12・
・・シツクナー、15・・・ダスト分離器、16.17
・・・ダクト。FIG. 1 is a schematic diagram of an exhaust gas desulfurization and dust removal treatment apparatus, and FIG. 2 is a schematic diagram of the present invention applied to a rotary heat exchanger. 1, 7... Heat exchanger, 2... Desulfurizer, 3... Dust collector, 4... Blower, 5... Reheating furnace, 6... Chimney, 8... Storm hopper - 9... Water pipe, 10
...Water seal tank, 11,13.14...Pump, 12.
...Sickener, 15...Dust separator, 16.17
···duct.
Claims (1)
共に、昇温用ガスとして脱硫除塵処理後の焼結排ガスを
通過させ、高温の前記焼結未処理排ガスを所定温度に降
温させるための熱交換器において、 前記熱交換器内をその上部から散水することによって水
洗滌し、前記熱交換器内を洗滌した後の洗滌水を、前記
熱交換器の下部からシツクナーに導き、前記シツクナー
の上澄水を、前記熱交換器の洗滌水として循環使用する
ことを特徴とする焼結排ガス処理用熱交換器の水処理方
法。[Scope of Claims] 1. The untreated sintered exhaust gas is passed through as a temperature-lowering gas, and the sintered exhaust gas after desulfurization and dust removal treatment is passed through as a temperature-raising gas, and the high-temperature untreated sintered exhaust gas is brought to a predetermined temperature. In a heat exchanger for lowering the temperature, the inside of the heat exchanger is washed with water by spraying water from the upper part thereof, and the washing water after washing the inside of the heat exchanger is led to a thickener from the lower part of the heat exchanger. . A water treatment method for a heat exchanger for treating sintered exhaust gas, characterized in that the supernatant water of the thickener is recycled as washing water for the heat exchanger.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP51133216A JPS5836280B2 (en) | 1976-11-08 | 1976-11-08 | Water treatment method for heat exchanger for sintering exhaust gas treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP51133216A JPS5836280B2 (en) | 1976-11-08 | 1976-11-08 | Water treatment method for heat exchanger for sintering exhaust gas treatment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5358408A JPS5358408A (en) | 1978-05-26 |
JPS5836280B2 true JPS5836280B2 (en) | 1983-08-08 |
Family
ID=15099431
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP51133216A Expired JPS5836280B2 (en) | 1976-11-08 | 1976-11-08 | Water treatment method for heat exchanger for sintering exhaust gas treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5836280B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11524935B2 (en) | 2009-11-06 | 2022-12-13 | Sk Biopharmaceuticals Co., Ltd. | Methods for treating attention-deficit/hyperactivity disorder |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5838315Y2 (en) * | 1978-10-13 | 1983-08-30 | 三菱化学株式会社 | Heat exchanger |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4981949A (en) * | 1972-12-12 | 1974-08-07 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5329538Y2 (en) * | 1974-07-17 | 1978-07-24 |
-
1976
- 1976-11-08 JP JP51133216A patent/JPS5836280B2/en not_active Expired
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4981949A (en) * | 1972-12-12 | 1974-08-07 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11524935B2 (en) | 2009-11-06 | 2022-12-13 | Sk Biopharmaceuticals Co., Ltd. | Methods for treating attention-deficit/hyperactivity disorder |
Also Published As
Publication number | Publication date |
---|---|
JPS5358408A (en) | 1978-05-26 |
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