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JPH0657289B2 - Operating method of filtration dust collection type exhaust gas treatment equipment - Google Patents

Operating method of filtration dust collection type exhaust gas treatment equipment

Info

Publication number
JPH0657289B2
JPH0657289B2 JP1094090A JP9409089A JPH0657289B2 JP H0657289 B2 JPH0657289 B2 JP H0657289B2 JP 1094090 A JP1094090 A JP 1094090A JP 9409089 A JP9409089 A JP 9409089A JP H0657289 B2 JPH0657289 B2 JP H0657289B2
Authority
JP
Japan
Prior art keywords
exhaust gas
dust collection
gas treatment
air
type exhaust
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 - Lifetime
Application number
JP1094090A
Other languages
Japanese (ja)
Other versions
JPH02273508A (en
Inventor
一夫 家山
正治 斉藤
利行 新保
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP1094090A priority Critical patent/JPH0657289B2/en
Publication of JPH02273508A publication Critical patent/JPH02273508A/en
Publication of JPH0657289B2 publication Critical patent/JPH0657289B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] この発明は、逆気流ファンを備えた濾過集塵式排ガス処
理装置を用いて塩化水素ガスを含む燃焼排ガスを処理す
る方法に関し、さらに詳しくは、潮解製のCaCl
よる濾布の目詰まりを防止する新規運転方法に関する。
Description: TECHNICAL FIELD The present invention relates to a method for treating combustion exhaust gas containing hydrogen chloride gas using a filter dust collecting type exhaust gas treatment apparatus equipped with a reverse air flow fan, and more specifically, , A new operating method for preventing clogging of a filter cloth with CaCl 2 produced by Tikatsu.

[従来技術およびその問題点] 濾過集塵式排ガス処理装置たとえばバグフィルタを用い
てHClガスを含む燃焼排ガスを処理する場合、通常、
その前流側で同排ガスに脱塩剤としてCa(OH)
添加している。しかし、HClとCa(OH)の反応
によって生じたCaClは、特に低温において著しい
潮解性を示すために、CaClが低温時に濾布に付着
して濾布が目詰まりを起こすという問題がある。
[Prior art and its problems] When a combustion exhaust gas containing HCl gas is treated using a filter dust collecting type exhaust gas treatment apparatus such as a bag filter,
Ca (OH) 2 is added as a desalting agent to the exhaust gas on the upstream side. However, CaCl 2 generated by the reaction between HCl and Ca (OH) 2 exhibits remarkable deliquescent properties, especially at low temperatures, so that there is a problem that CaCl 2 adheres to the filter cloth at low temperatures and causes clogging of the filter cloth. is there.

この発明は、上記の如き実情に鑑み、CaClの潮解
を防止すことによって濾布の目詰まりをなくし、以って
排ガス処理装置を支障なく運転する方法を提供すること
を目的とする。
In view of the above situation, it is an object of the present invention to provide a method for preventing the deliquescent of CaCl 2 from clogging the filter cloth, thereby operating the exhaust gas treatment device without any trouble.

[問題点の解決手段] この発明による濾過集塵式排ガス処理装置の運転方法
は、上記目的の達成のために、逆気流ファンを備えた濾
過集塵式排ガス処理装置を用いて塩化水素ガスを含む燃
焼排ガスを処理するに当たり、同処理装置の運転停止時
ないしは準備時に逆気流ファンを利用して装置内の排ガ
スを空気置換するとともに、装置内にヒータを設置して
ヒータによる温風を循環させることによって、濾布を加
温することを特徴とする。
[Means for Solving Problems] In order to achieve the above-mentioned object, a method for operating a filtration dust collection type exhaust gas treatment apparatus of the present invention uses a filtration dust collection type exhaust gas treatment apparatus equipped with a reverse air flow fan to remove hydrogen chloride gas. When treating the combustion exhaust gas containing it, the exhaust gas in the equipment is replaced with air by using the backflow fan when the operation of the treatment equipment is stopped or during preparation, and a heater is installed in the equipment to circulate the warm air by the heater. This is characterized by heating the filter cloth.

装置内の循環温風の温度は、CaClの潮解が効果的
に防止されるように、好ましくは100〜150℃に維
持される。
The temperature of the circulating hot air in the device is preferably maintained at 100 to 150 ° C. so that the deliquescent of CaCl 2 is effectively prevented.

装置内における排ガスの空気置換および温風の循環は、
好ましくは、装置内の複数の部屋のうちの一部の部屋に
おける循環温風の流れ方向の集塵処理方向のままにして
おき、残りの部屋における循環温風の流れ方向を集塵処
理方向の逆方向に代え、誘引ファンを停止させかつ逆気
流ファンを作動させることによって行われる。また、循
環温風の流れ方向を変換するダンパーな開閉は、タイマ
ーによってまたは圧力損失などを検知することによって
制御せられる。こうして、すべての部屋において濾布の
加温および濾布に付着した粉塵の払い落としが均等に行
なわれる。
Air replacement of exhaust gas and circulation of warm air in the device
Preferably, the dust collection processing direction of the flow direction of the circulating warm air in a part of the plurality of rooms in the device is left as it is, and the flow direction of the circulating warm air in the remaining rooms is set to the dust collection processing direction. Instead of the reverse direction, the induction fan is stopped and the reverse airflow fan is operated. Also, the opening and closing of a damper that changes the flow direction of the circulating hot air is controlled by a timer or by detecting pressure loss or the like. In this way, the heating of the filter cloth and the dust adhering to the filter cloth are uniformly removed in all the rooms.

[作 用] この発明による運転方法では、排ガス処理装置の運転停
止時ないしは準備時にその逆気流ファンを利用して装置
内の排ガスを空気置換するとともに、装置内にヒータを
設置してヒータによる温風を循環させるので、濾布は循
環温風によって加温され、その結果CaClの潮解が
防止されて濾布の目詰まりのおそれがなくなる。
[Operation] In the operating method according to the present invention, when the exhaust gas treatment device is stopped or is prepared, the exhaust gas in the device is replaced with air by using the reverse air flow fan, and a heater is installed in the device to control the temperature by the heater. Since the air is circulated, the filter cloth is heated by the circulating hot air, and as a result, the deliquescent of CaCl 2 is prevented and the filter cloth is not clogged.

[実施例] つぎに、図示の実施例によりこの発明を具体的に説明す
る。
[Examples] Next, the present invention will be described in detail with reference to the illustrated examples.

添付の図面において、バグフィルタ本体(1)は4つの部
屋(2)(3)(4)(5)に区分されており、角部屋にはそれぞれ
濾布(12)が張設されている。また、各部屋(2)(3)(4)(5)
の頂部にはそれぞれ処理ガス通路(2a)(3a)(4a)(5a)と逆
気流通路(2b)(3b)(4b)(5b)とが設けられている。処理ガ
ス通路(2a)(3a)(4a)(5a)にはそれぞれ集塵用ダンパ(6)
が取り付けられ、逆気流通路(2b)(3b)(4b)(5b)にはそれ
ぞれ逆気流用ダンパ(7)が取り付けられている。そし
て、処理ガス通路(2a)(3a)(4a)(5a)にはそれぞれ処理ガ
ス導管(8)の入口端分岐部(8a)が接続され、逆気流通路
(2b)(3b)(4b)(5b)にはそれぞれ逆気流導管(9)の入口端
分岐部(9a)が接続されている。処理ガス導管(8)には処
理ガス通路から処理ガスを引く誘引ファン(10)が設けら
れている。また、逆気流導管(9)には濾布(12)に付着し
た粉塵を払い落とすために逆気流通路へ気流を送る逆気
流ファン(11)が設けられている。処理ガス導管(8)はま
た逆気流ファン(11)の入気側にも接続されている。各部
屋(2)(3)(4)(5)において、濾布(12)の後流側であってか
つ逆気流通路(2b)(3b)(4b)(5b)の下側にそれぞれヒータ
(13)が設けられている。
In the attached drawings, the bag filter body (1) is divided into four chambers (2), (3), (4) and (5), and a filter cloth (12) is stretched in each corner chamber. Also, each room (2) (3) (4) (5)
Process gas passages (2a) (3a) (4a) (5a) and reverse air flow passages (2b) (3b) (4b) (5b) are provided at the top of each. The process gas passages (2a) (3a) (4a) (5a) each have a dust collecting damper (6).
And a reverse airflow damper (7) is attached to each of the reverse airflow passages (2b), (3b), (4b), and (5b). Then, the processing gas passages (2a) (3a) (4a) (5a) are connected to the inlet end branch portion (8a) of the processing gas conduit (8), respectively, and
(2b), (3b), (4b), and (5b) are connected to the inlet end branch portion (9a) of the reverse airflow conduit (9), respectively. The processing gas conduit (8) is provided with an induction fan (10) for drawing the processing gas from the processing gas passage. Further, the reverse airflow conduit (9) is provided with a reverse airflow fan (11) that sends an airflow to the reverse airflow passage in order to scavenge the dust adhering to the filter cloth (12). The process gas conduit (8) is also connected to the inlet side of the backflow fan (11). In each room (2) (3) (4) (5), a heater is provided on the downstream side of the filter cloth (12) and below the reverse airflow passages (2b) (3b) (4b) (5b).
(13) is provided.

上記構成のバグフィルタにおいて、通常の集塵運転時に
は、すべての集塵用ダンパ(6)を開きかつすべての逆気
流用ダンパ(7)を閉じて、逆気流ファン(11)を停止させ
かつ誘引ファン(10)を作動させることによって、排ガス
の集塵処理が行われる。
In the bag filter with the above configuration, during normal dust collection operation, all dust collection dampers (6) are opened and all reverse airflow dampers (7) are closed to stop and attract the reverse airflow fan (11). By operating the fan (10), dust collection processing of exhaust gas is performed.

また、バグフィルタの運転停止時ないしは準備時には、
部屋(2)(3)(4)(5)のうちの部屋(2)と部屋(4)における気
体の流れ方向をそのまま集塵処理方向を維持し、かつ部
屋(3)と部屋(5)の流れ方向を集塵処理方向の逆方向に代
える。すなわち、部屋(2)と部屋(4)の各集塵用ダンパ
(6)をそのまま開いておき、かつ部屋(3)と部屋(5)の各
集塵用ダンパ(6)をいずれも閉じるとともに、部屋(2)と
部屋(4)の各逆気流用ダンパ(7)をそのまま閉じておき、
かつ部屋(3)と部屋(5)の各逆気流用ダンパ(7)をいずれ
も開く。そして、誘引ファン(10)を停止させかつ逆気流
ファン(11)を作動させる。その結果、バグフフィルタ本
体(1)内の排ガスは空気置換されるとともに、ヒータ(1
3)によって生成させられた温度100〜150℃の温風
がバグフィルタ本体(1)内を循環させられる。こうし
て、この循環温風によって濾布(12)が加温され、CaC
の潮解が防止されて濾布の目詰まりのおそれがなく
なる。
Also, when the bag filter is stopped or prepared,
The direction of gas flow in the room (2) and the room (4) among the rooms (2), (3), (4) and (5) is maintained as the dust collection processing direction, and the room (3) and the room (5) are maintained. The flow direction of is changed to the opposite direction of the dust collection processing direction. That is, dampers for dust collection in room (2) and room (4)
(6) is opened as it is, and both the dust collecting dampers (6) of the room (3) and the room (5) are closed, and the reverse air flow dampers ((2) and (4)) 7) Keep it closed,
At the same time, open the backflow dampers (7) in the room (3) and room (5). Then, the attraction fan (10) is stopped and the reverse airflow fan (11) is operated. As a result, the exhaust gas in the bag filter main body (1) is replaced with air and the heater (1
The hot air having a temperature of 100 to 150 ° C. generated by 3) is circulated in the bag filter body (1). Thus, the circulating warm air heats the filter cloth (12), and CaC
The deliquescent of l 2 is prevented, and the risk of clogging of the filter cloth is eliminated.

ついで、各集塵用ダンパ(6)および逆気流用ダンパ(7)の
開閉状態を上記状態の逆にして、部屋(2)と部屋(4)にお
ける循環温風の流れ方向を逆流方向に代え、かつ部屋
(3)と部屋(5)の循環温風の流れ方向を集塵処理方向に代
える。このダンパ(6)(7)の開閉は、タイマーによって
または圧力損失などを検知することによって、制御せら
れる。こうして、すべての部屋(2)(3)(4)(5)において濾
布(12)の加温および濾布(12)に付着した粉塵の払い落と
しが均等に行なわれる。
Next, the open / closed state of each dust collecting damper (6) and reverse airflow damper (7) is reversed to the above state, and the flow direction of the circulating hot air in the room (2) and the room (4) is changed to the reverse flow direction. , And the room
The flow direction of circulating hot air in (3) and the room (5) is changed to the dust collection processing direction. The opening / closing of the dampers 6 and 7 is controlled by a timer or by detecting pressure loss or the like. In this way, the heating of the filter cloth (12) and the dust adhering to the filter cloth (12) are uniformly removed in all the rooms (2) (3) (4) (5).

[発明の効果] この発明による運転方法では、排ガス処理装置の運転停
止時ないしは準備時にその逆気流ファンを利用して装置
内の排ガスを空気置換するとともに、装置内にヒータを
設置してヒータによる温風を循環させるので、循環温風
によって濾布を加温させ、その結果CaClの潮解が
生じるのを防止して、潮解性のCaClによって濾布
が目詰まりをきたすのを確実に回避することができ、以
って排ガス処理装置を支障なく運転することができる。
[Advantages of the Invention] In the operating method according to the present invention, the exhaust gas in the device is replaced with air by using the reverse airflow fan when the exhaust gas treatment device is stopped or prepared, and the heater is installed in the device. since circulating hot air, circulating hot air the filter cloth is allowed to warm by to prevent the the result of CaCl 2 deliquescence arises, reliably prevent the filter cloth by deliquescence of CaCl 2 is causing clogging Therefore, the exhaust gas treatment device can be operated without any trouble.

【図面の簡単な説明】[Brief description of drawings]

図面はこの発明の実施例を示すバグフィルタの切欠正面
図である。 (1)……バグフィルタ本体、(2)(3)(4)(5)……部屋、(6)
……集塵用ダンパ、(7)……逆気流用ダンパ、(8)……処
理ガス導管、(9)……逆気流導管、(10)……誘引ファ
ン、(11)……逆気流ファン、(12)……濾布、(13)……ヒ
ータ。
The drawing is a cutaway front view of a bag filter showing an embodiment of the present invention. (1) …… Bug filter body, (2) (3) (4) (5) …… Room, (6)
…… Dust collection damper, (7) …… Backflow air damper, (8) …… Process gas conduit, (9) …… Backflow air conduit, (10) …… Induction fan, (11) …… Backflow air Fan, (12) …… filter cloth, (13) …… heater.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】逆気流ファンを備えた濾過集塵式排ガス処
理装置を用いて塩化水素ガスを含む燃焼排ガスを処理す
るに当たり、同処理装置の運転停止時ないしは準備時に
逆気流ファンを利用して装置内の排ガスを空気置換する
とともに、装置内にヒータを設置してヒータによる温風
を循環させることによって、濾布を加温することを特徴
とする、濾過集塵式排ガス処理装置の運転方法。
1. When treating a combustion exhaust gas containing hydrogen chloride gas by using a filter dust collecting type exhaust gas treatment apparatus equipped with a reverse air flow fan, the reverse air flow fan is utilized at the time of shutdown or preparation of the treatment apparatus. A method for operating a filter dust collecting type exhaust gas treatment apparatus, characterized in that the exhaust gas in the apparatus is replaced with air, and a heater is installed in the apparatus and warm air is circulated by the heater to heat the filter cloth. .
JP1094090A 1989-04-13 1989-04-13 Operating method of filtration dust collection type exhaust gas treatment equipment Expired - Lifetime JPH0657289B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1094090A JPH0657289B2 (en) 1989-04-13 1989-04-13 Operating method of filtration dust collection type exhaust gas treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1094090A JPH0657289B2 (en) 1989-04-13 1989-04-13 Operating method of filtration dust collection type exhaust gas treatment equipment

Publications (2)

Publication Number Publication Date
JPH02273508A JPH02273508A (en) 1990-11-08
JPH0657289B2 true JPH0657289B2 (en) 1994-08-03

Family

ID=14100759

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1094090A Expired - Lifetime JPH0657289B2 (en) 1989-04-13 1989-04-13 Operating method of filtration dust collection type exhaust gas treatment equipment

Country Status (1)

Country Link
JP (1) JPH0657289B2 (en)

Also Published As

Publication number Publication date
JPH02273508A (en) 1990-11-08

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