JPH02298316A - Operation of filter dust collection type exhaust gas treating device - Google Patents
Operation of filter dust collection type exhaust gas treating deviceInfo
- Publication number
- JPH02298316A JPH02298316A JP1116868A JP11686889A JPH02298316A JP H02298316 A JPH02298316 A JP H02298316A JP 1116868 A JP1116868 A JP 1116868A JP 11686889 A JP11686889 A JP 11686889A JP H02298316 A JPH02298316 A JP H02298316A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- gas
- dust
- dust collection
- collection type
- 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
Links
Landscapes
- Treating Waste Gases (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は、濾過集塵式排ガス処理装置を用いて、重金
属やダイオキシンのような有害物質、さらには塩化水素
ガスや硫黄酸化物のような酸性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、これら含有物質
の除去効果を調整するとともに、濾布の目詰まりを防止
する新規運転方法に関する。[Detailed Description of the Invention] [Industrial Application Field] This invention uses a filtration and dust collection type exhaust gas treatment device to remove harmful substances such as heavy metals and dioxins, as well as hydrogen chloride gas and sulfur oxides. The present invention relates to a method for treating combustion exhaust gas containing acidic gases, and more particularly to a new operating method for adjusting the removal effect of these contained substances and preventing clogging of a filter cloth.
[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
て上記のような燃焼排ガスを処理する場合、排ガス中の
重金属やダイオキシンの除去は結果的に達成されるもの
であり、また排ガスの温度調節は専、ら同装置の安全運
転および排ガス中の酸性ガスの除去を目的として行われ
ていた。[Prior art and its problems] When the above-mentioned combustion exhaust gas is treated using a filtration and dust collection type exhaust gas treatment device, such as a bag filter, removal of heavy metals and dioxins from the exhaust gas is achieved as a result. In addition, temperature control of the exhaust gas was carried out exclusively for the purpose of safe operation of the equipment and removal of acid gas from the exhaust gas.
しかし、重金属やダイオキシンと、塩化水素ガスや硫黄
酸化物のような酸性ガスとでは、各々の除去形態が全く
異なり、前者の除去効果は、第4図に示すように排ガス
の温度に大きく依存する一方、後者の除去効果は、第3
図トポすように酸吸着剤の添加量にも直接大きく影響を
受ける。However, the removal methods for heavy metals and dioxins and acidic gases such as hydrogen chloride gas and sulfur oxides are completely different, and the removal effect of the former greatly depends on the temperature of the exhaust gas, as shown in Figure 4. On the other hand, the latter removal effect is
As shown in the figure, it is directly influenced by the amount of acid adsorbent added.
ところで、上記のようにHC/ガスを含む排ガスを濾過
集塵式排ガス処理装置を用いて処理するには、通常、同
装置の前流側で排ガスに脱酸剤として消石灰Ca(OH
)zを添加している。しかし、HC/とCa (OH)
2の反応によって生じたCaCl2は、特に低温におい
て著しい潮解性を示すために、運転停止時や運転準備中
などの低温時にCaCl2が濾布に付普して濾布が目詰
まりを起こすという問題があった。By the way, in order to treat exhaust gas containing HC/gas using a filtration and dust collection type exhaust gas treatment device as described above, slaked lime Ca (OH
)z is added. However, HC/ and Ca (OH)
CaCl2 produced by the reaction in step 2 exhibits remarkable deliquescent properties, especially at low temperatures, so there is a problem that CaCl2 adheres to the filter cloth and causes clogging of the filter cloth at low temperatures such as when the operation is stopped or during preparation for operation. there were.
この発明は、上記の如き実情に鑑み、排ガス中の重金属
やダイオキシンのような有害物質、さらには塩化水素ガ
スや硫黄酸化物のような酸性ガスの除去効果を効率的に
調整するとともに、集塵ダスト中のCaCl2の含有量
を低く抑制することによって、潮解性Ca C/ 2が
濾布に付むして目詰まりを起こすのを回避し、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-mentioned circumstances, this invention efficiently adjusts the removal effect of harmful substances such as heavy metals and dioxins in exhaust gas, as well as acid gases such as hydrogen chloride gas and sulfur oxides, as well as dust collection. To provide a method that prevents deliquescent CaC/2 from adhering to a filter cloth and causing clogging by suppressing the content of CaCl2 in dust, thereby allowing an exhaust gas treatment device to operate without any trouble. The purpose is to
[問題点の解決手段]
この発明による濾過集塵式υFガス処理装置の運転方法
の第1のものは、濾過集塾式排ガス処理装置を用いて燃
焼排ガスを処理するに当たり、処理すべき排ガスの温度
を調節することによって、重金属およびダイオキシンの
除去効果を調整するとともに、排ガスへの脱酸剤の添加
量を調節することによって、酸性ガスの除去効果を調整
することを特徴とする。[Means for Solving Problems] The first method of operating the filtration and dust collection type υF gas treatment device according to the present invention is that when treating combustion exhaust gas using the filtration and collection type exhaust gas treatment device, the exhaust gas to be treated is The method is characterized in that the effect of removing heavy metals and dioxins is adjusted by adjusting the temperature, and the effect of removing acid gases is adjusted by adjusting the amount of deoxidizing agent added to the exhaust gas.
また、この発明による濾過集塵式排ガス処理装置の運転
方法の第2のものは、処理すべき排ガスにCa (OH
) 2を添加して排ガス中のHC/ガスをCaCl2と
して濾過集塵式排ガス処理装置で除去するに当たり、集
塵ダスト中のCa C/ 2の含有量を検知し、CaC
l2の含有量にしたがってCa(OH)2の添加量を調
節することによって、または埋火時にCa(OH)2の
添加量を増加させかつ付着粉塵の払い落とし間隔を密に
することによって、集塵ダスト中のCaCl2の含有量
を低く抑制することを特徴とする。In addition, in the second method of operating the filtering and dust collection type exhaust gas treatment device according to the present invention, the exhaust gas to be treated contains Ca (OH
) 2 is added to remove HC/gas in the exhaust gas as CaCl2 using a filtration/dust collection type exhaust gas treatment device, the content of CaC/2 in the collected dust is detected and CaC/2 is removed.
By adjusting the amount of Ca(OH)2 added according to the content of L2, or by increasing the amount of Ca(OH)2 added at the time of burial and increasing the interval at which the adhering dust is brushed off. It is characterized by suppressing the content of CaCl2 in the dust to a low level.
第1の発明において、脱酸剤としては消石灰Ca (O
H)2が一般的であるが、必ずしもこれに限定されない
。In the first invention, the deoxidizing agent is slaked lime Ca (O
H)2 is common, but is not necessarily limited to this.
処理すべき排ガスの温度調節は、通常は、減温塔におい
て排ガスを水で洗浄することによって行われる。Temperature regulation of the exhaust gas to be treated is usually carried out by washing the exhaust gas with water in a cooling tower.
減温塔への水の供給量の調節および排ガスへの脱酸剤の
添加量の調節は、通常は、処理ガスの温度およびHCl
濃度をそれぞれ検知し、得られた検知信号によって水供
給バルブおよびの脱酸剤供給バルブの開閉を制御するこ
とによって行われる。Adjustment of the amount of water supplied to the cooling tower and the amount of deoxidizing agent added to the exhaust gas are usually performed based on the temperature of the treated gas and the amount of HCl.
This is done by detecting the respective concentrations and controlling the opening and closing of the water supply valve and the deoxidizer supply valve based on the obtained detection signals.
第2の発明において、集塵ダスト中のCaCl2の含有
量は、集塵ダストを一部サンプリングして水に溶解させ
、溶液中のCaa度を測定することによって検知される
。そして、排ガスへのCa (OH)2の添加量および
付着粉塵の払い落とし間隔の調節は、この検知信号によ
ってCa (OH)2の供給バルブの開閉および払い蔭
とし用タイマーを制御することによって行われる。In the second invention, the content of CaCl2 in the collected dust is detected by sampling a part of the collected dust, dissolving it in water, and measuring the degree of Ca in the solution. The amount of Ca(OH)2 added to the exhaust gas and the interval for brushing off the attached dust are adjusted by controlling the opening/closing of the Ca(OH)2 supply valve and the timer for brushing off the dust based on this detection signal. be exposed.
また、埋火時には排ガス中のHC/a度が高くなるので
、埋火操作と同時にCa(OH)2の添加量を増加させ
かつ付着粉塵の払い落とし間隔を密にする。その結果、
集塵ダスト中の潮解性CaCl2の含有量が低く抑制せ
られ、CaCl、が濾布に付着して目詰まりをおこすこ
とが防止される。Furthermore, since the HC/a degree in the exhaust gas increases when the fire is buried, the amount of Ca(OH)2 added is increased at the same time as the fire is buried, and the intervals at which the adhering dust is brushed off are increased. the result,
The content of deliquescent CaCl2 in the collected dust is suppressed to a low level, and CaCl is prevented from adhering to the filter cloth and causing clogging.
[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。[Example] Next, the present invention will be specifically explained with reference to the illustrated example.
実施例1
添付の第1図において、重金属やダイオキシン、さらに
は塩化水素ガスや硫黄酸化物のような酸性ガスを含む燃
焼排ガスは、まず減温塔(1)に通される。開基(1)
の頂部にはバルブ(2)を有する給水管(3)が配され
、間管(3)から水が噴射されている。バルブ(2)の
開閉は、後述する処理ガスの温度を温度検知器(4)に
よって検知して得られた検知信号によって調節される。Example 1 In the attached FIG. 1, combustion exhaust gas containing heavy metals, dioxins, and acid gases such as hydrogen chloride gas and sulfur oxides is first passed through a cooling tower (1). Opening group (1)
A water supply pipe (3) having a valve (2) is arranged at the top of the pipe, and water is injected from the pipe (3). The opening and closing of the valve (2) is regulated by a detection signal obtained by detecting the temperature of the processing gas with a temperature sensor (4), which will be described later.
こうして、水の供給量を制御することによって、排ガス
は減温塔(1)を通過する間に所要の温度に調節される
。In this way, by controlling the amount of water supplied, the exhaust gas is adjusted to the required temperature while passing through the cooling tower (1).
減温塔(1)の後流側には、バルブ(5)を有する脱酸
剤供給管(6)が配され、間管(6)によって排ガスに
脱酸剤としてCa (OH)2が添加されている。Ca
(OH)、の添加量の調節も、後述する処理ガスのH
C/濃度をHC/検知器(7)によって検知し、jすら
れた検知信号によってバルブ(5〉の開閉を制御するこ
とによって行われる。こうして、排ガスに所要量のCa
(OH)2を添加することによって、排ガス中のHC/
ガスはCaCl、になされ、その他の酸性ガスもCa塩
になされる。A deoxidizing agent supply pipe (6) having a valve (5) is arranged on the downstream side of the cooling tower (1), and Ca (OH)2 is added to the exhaust gas as a deoxidizing agent through the intermediate pipe (6). has been done. Ca
The amount of (OH) added can also be adjusted by adjusting the amount of H
This is done by detecting the carbon concentration with the HC detector (7) and controlling the opening and closing of the valve (5) based on the detected signal.In this way, the required amount of Ca is injected into the exhaust gas.
By adding (OH)2, HC/
The gas is made into CaCl, and other acid gases are made into Ca salt.
温度が調節されかつCa(OH)zが添加された排ガス
は、ついでバグフィルタ(8)に通されて集塵処理され
る。この処理ガスの温度およびHC/濃度は、上述のご
とく各検知器(4) (7)によってそれぞれ検知され
、得られた検知信号によってバルブ(2)およびバルブ
(5)の開閉が制御される。The temperature-adjusted exhaust gas to which Ca(OH)z has been added is then passed through a bag filter (8) for dust collection. The temperature and HC/concentration of this process gas are detected by the respective detectors (4) and (7) as described above, and the opening and closing of the valve (2) and the valve (5) are controlled based on the obtained detection signals.
こうして、処理すべき排ガスの温度を減温塔(1)にお
ける水洗によって調節することによって、バグフィルタ
(8)による重金属およびダイオキシンの除去効果が調
整せられるとともに、排ガスへのCa (OH) 2の
添加量を調節することによって、排ガス中の塩化水素ガ
スや硫黄酸化物のような酸性ガスの除去効果が調整せら
れる。In this way, by adjusting the temperature of the exhaust gas to be treated by washing with water in the cooling tower (1), the removal effect of heavy metals and dioxins by the bag filter (8) is adjusted, and at the same time, the removal of Ca (OH) 2 from the exhaust gas is adjusted. By adjusting the amount added, the effect of removing acidic gases such as hydrogen chloride gas and sulfur oxides in exhaust gas can be adjusted.
実施例2
添付の第2図において、バグフィルタ(18)の前流側
に、バルブ(15)を有する脱酸剤供給管(1a)が配
され、間管(16)によって排ガスに脱酸剤としてCa
(OH)2が添加されている。こうして排ガスに所要
量のCa (OH)2を添加することによって、排ガス
中のHC/ガスはCaCl2になされる。Example 2 In the attached FIG. 2, a deoxidizer supply pipe (1a) having a valve (15) is arranged on the upstream side of the bag filter (18), and a deoxidizer is supplied to the exhaust gas through an intermediate pipe (16). As Ca
(OH)2 is added. By thus adding the required amount of Ca(OH)2 to the exhaust gas, the HC/gas in the exhaust gas is converted to CaCl2.
Ca(OH)zが添加された排ガスは、ついでバグフィ
ルタ(18)に通されて集塵処理される。The exhaust gas to which Ca(OH)z has been added is then passed through a bag filter (18) for dust collection.
バグフィルタ(18)には付着粉塵の払い落とし装置が
設けられている。同装置は逆気流、揺動、音波などの手
段によって濾布から粉塵を離脱させるものである。この
払い落とし装置にはタイマー(10)が備え付けられ、
同装置はタイマー(lO)によって間欠的に作動させら
れる。The bag filter (18) is provided with a device for removing attached dust. The device uses means such as reverse airflow, shaking, and sound waves to remove dust from the filter cloth. This dusting device is equipped with a timer (10),
The device is activated intermittently by a timer (IO).
バグフィルタ(18)によって集塵されたダストは、一
部サンプリングされて水に溶解され、検知器(9)によ
って溶液中のCaa度を測定することによって、集塵ダ
スト中のCaCl2の含有量が検知される。この検知信
号によってCa(OH)2の供給バルブ(15)の開閉
が制御される。こうして、集塵ダスト中のCaCl2の
含有量にしたがってCa (01()2の添加量が調節
される。その結果、集塵ダスト中の潮解性CaCl2の
含有量が低く抑制せられ、CaCl2が濾布に付着して
目詰まりをおこすことが防止される。Part of the dust collected by the bag filter (18) is sampled and dissolved in water, and the content of CaCl2 in the collected dust is determined by measuring the degree of Caa in the solution with the detector (9). Detected. This detection signal controls the opening and closing of the Ca(OH)2 supply valve (15). In this way, the amount of Ca(01()2) added is adjusted according to the content of CaCl2 in the collected dust.As a result, the content of deliquescent CaCl2 in the collected dust is suppressed to a low level, and CaCl2 is filtered out. This prevents it from adhering to the cloth and causing clogging.
また、この検知信号によって払い落とし装置のタイマー
(lO)も制御される。Further, the timer (lO) of the brushing device is also controlled by this detection signal.
実施例3
第2図の構成において、埋火時にはυ1.ガス中のHC
/6度が高くなるので、埋火操作と同時にCa(OH)
2の添加量が増加させられ、かつ付着粉塵の払い落とし
間隔が密になされる。Example 3 In the configuration shown in FIG. 2, when the fire is buried, υ1. HC in gas
/6 degrees, so Ca(OH) is removed at the same time as the buried fire operation.
The amount of addition of No. 2 is increased, and the intervals at which the adhering dust is brushed off are made closer.
Ca(OH)zの添加量および付着粉塵の払い落とし間
隔は、バルブ(15)およびタイマー(10)の各設定
値を変更することによって調節される。The amount of Ca(OH)z added and the interval at which adhering dust is brushed off are adjusted by changing the respective set values of the valve (15) and timer (10).
その結果、集塵ダスト中の潮解性Ca C/ 2の含有
量が低く抑制せられ、CaCl2が濾布に付着して目詰
まりをおこすことが防止される。As a result, the content of deliquescent Ca C/2 in the collected dust is suppressed to a low level, and CaCl2 is prevented from adhering to the filter cloth and causing clogging.
その他の構成は、実施例2のものと同じである。The other configurations are the same as those of the second embodiment.
[発明の効果〕
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
、以上の通り構成されているので、排ガス中の重金属や
ダイオキシン、さらには塩化水素ガスや硫黄酸化物のよ
うな酸性ガスの除去効果を効率的に調整することができ
るとともに、集塵ダスト中のCaCl2の含有量を低く
抑制することによって、潮解性Caf、j2が濾布に付
着して目詰まりを起こすのを効果的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。[Effects of the Invention] Since the operating method of the filtration and dust collection type exhaust gas treatment device according to the present invention is configured as described above, heavy metals and dioxins in the exhaust gas, as well as acid gases such as hydrogen chloride gas and sulfur oxide, can be removed. By controlling the content of CaCl2 in the collected dust to a low level, it is possible to effectively prevent deliquescent Caf,j2 from adhering to the filter cloth and causing clogging. Therefore, the exhaust gas treatment device can be operated without any trouble.
第1図および第2図はそれぞれこの発明の実施例を示す
フローシートであり、第3図は消石灰供給量と酸濃度の
関係を示すグラフであり、第4図は温度とダイオキシン
濃度の関係を示すグラフである。
以 上
特許出願人 日立造船 株式会社L;、:!−・
1.・
3h石人相冷i
第3図
第4図Figures 1 and 2 are flow sheets showing examples of the present invention, Figure 3 is a graph showing the relationship between slaked lime supply amount and acid concentration, and Figure 4 is a graph showing the relationship between temperature and dioxin concentration. This is a graph showing. Patent applicant: Hitachi Zosen Corporation L;,:! −・
1.・3h Sekijin Sorei Figure 3 Figure 4
Claims (2)
処理するに当たり、処理すべき排ガスの温度を調節する
ことによって、重金属およびダイオキシンの除去効果を
調整するとともに、排ガスへの脱酸剤の添加量を調節す
ることによって、酸性ガスの除去効果を調整することを
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 combustion exhaust gas using a filtration and dust collection type exhaust gas treatment device, by adjusting the temperature of the exhaust gas to be treated, the removal effect of heavy metals and dioxins can be adjusted, and the deoxidizing agent applied to the exhaust gas can be adjusted. A method for operating a filtration and dust collection type exhaust gas treatment device, characterized in that the acid gas removal effect is adjusted by adjusting the amount added.
排ガス中のHClガスをCaCl_2として濾過集塵式
排ガス処理装置で除去するに当たり、集塵ダスト中のC
aCl_2の含有量を検知し、CaCl_2の含有量に
したがってCa(OH)_2の添加量を調節することに
よって、または埋火時にCa(OH)_2の添加量を増
加させかつ付着粉塵の払い落とし間隔を密にすることに
よって、集塵ダスト中のCaCl_2の含有量を低く抑
制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。(2) When adding Ca(OH)_2 to the exhaust gas to be treated and removing HCl gas in the exhaust gas as CaCl_2 using a filtration and dust collection type exhaust gas treatment device, C in the collected dust is removed.
By detecting the content of aCl_2 and adjusting the amount of Ca(OH)_2 added according to the content of CaCl_2, or by increasing the amount of Ca(OH)_2 added at the time of burial and adjusting the interval for brushing off attached dust. A method for operating a filtration and dust collection type exhaust gas treatment device, characterized in that the content of CaCl_2 in collected dust is suppressed to a low level by making the dust dense.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1116868A JPH0732862B2 (en) | 1989-05-09 | 1989-05-09 | Operating method of filtration dust collection type exhaust gas treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1116868A JPH0732862B2 (en) | 1989-05-09 | 1989-05-09 | Operating method of filtration dust collection type exhaust gas treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02298316A true JPH02298316A (en) | 1990-12-10 |
JPH0732862B2 JPH0732862B2 (en) | 1995-04-12 |
Family
ID=14697620
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1116868A Expired - Lifetime JPH0732862B2 (en) | 1989-05-09 | 1989-05-09 | Operating method of filtration dust collection type exhaust gas treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0732862B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07236804A (en) * | 1994-02-28 | 1995-09-12 | Furukawa Electric Co Ltd:The | Waste gas treatment equipment for optical fiber glass synthesis equipment |
US5500195A (en) * | 1992-11-13 | 1996-03-19 | Foster Wheeler Energy Corporation | Method for reducing gaseous emission of halogen compounds in a fluidized bed reactor |
WO1998048924A1 (en) * | 1997-04-25 | 1998-11-05 | Nkk Corporation | Method of treating exhaust gas |
WO2004023040A1 (en) * | 2002-09-09 | 2004-03-18 | Babcock-Hitachi Kabushiki Kaisha | Exhaust smoke-processing system |
JP2013017956A (en) * | 2011-07-12 | 2013-01-31 | Takuma Co Ltd | Method for controlling additive rate of chelating agent to fly ash |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5210418A (en) * | 1975-07-10 | 1977-01-26 | Katayama Chem Works Co Ltd | Controlling agent against adhesive organisms living in the sea |
-
1989
- 1989-05-09 JP JP1116868A patent/JPH0732862B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5210418A (en) * | 1975-07-10 | 1977-01-26 | Katayama Chem Works Co Ltd | Controlling agent against adhesive organisms living in the sea |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5500195A (en) * | 1992-11-13 | 1996-03-19 | Foster Wheeler Energy Corporation | Method for reducing gaseous emission of halogen compounds in a fluidized bed reactor |
JPH07236804A (en) * | 1994-02-28 | 1995-09-12 | Furukawa Electric Co Ltd:The | Waste gas treatment equipment for optical fiber glass synthesis equipment |
WO1998048924A1 (en) * | 1997-04-25 | 1998-11-05 | Nkk Corporation | Method of treating exhaust gas |
WO2004023040A1 (en) * | 2002-09-09 | 2004-03-18 | Babcock-Hitachi Kabushiki Kaisha | Exhaust smoke-processing system |
US7651389B2 (en) | 2002-09-09 | 2010-01-26 | Babcock-Hitachi Kabushiki Kaisha | Exhaust smoke-processing system |
JP2013017956A (en) * | 2011-07-12 | 2013-01-31 | Takuma Co Ltd | Method for controlling additive rate of chelating agent to fly ash |
Also Published As
Publication number | Publication date |
---|---|
JPH0732862B2 (en) | 1995-04-12 |
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