JPS5826981B2 - How to operate a dry electrostatic precipitator equipped with a water film electrostatic precipitator - Google Patents
How to operate a dry electrostatic precipitator equipped with a water film electrostatic precipitatorInfo
- Publication number
- JPS5826981B2 JPS5826981B2 JP10311479A JP10311479A JPS5826981B2 JP S5826981 B2 JPS5826981 B2 JP S5826981B2 JP 10311479 A JP10311479 A JP 10311479A JP 10311479 A JP10311479 A JP 10311479A JP S5826981 B2 JPS5826981 B2 JP S5826981B2
- Authority
- JP
- Japan
- Prior art keywords
- electrostatic precipitator
- water film
- dry
- water
- hammering
- 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
Landscapes
- Electrostatic Separation (AREA)
Description
【発明の詳細な説明】
本発明は、水膜式電気集じん部を有する乾式電気集じん
設備の運転方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of operating a dry electrostatic precipitator having a water film electrostatic precipitator.
従来、重油焚きゃ石炭焚きボイラの排ガスの集じん、お
よびセメントキルンや仕上げミルの排ガスの集じん、な
らびにごみ焼却炉の排ガスの集じんなと、広い分野で乾
式電気集じん装置が使用されているが、従来の乾式電気
集じん装置では、槌打時におけるダストの飛散およびば
いじんの濃度ピークの発生などに問題があり、とりわけ
、ガス流に対して最後部室のものについてこれらの問題
があった。Traditionally, dry electrostatic precipitators have been used in a wide range of fields, including the collection of exhaust gas from heavy oil-fired and coal-fired boilers, the collection of exhaust gas from cement kilns and finishing mills, and the collection of exhaust gas from garbage incinerators. However, conventional dry electrostatic precipitators have problems such as dust scattering during hammering and the occurrence of dust concentration peaks, especially those in the rearmost chamber relative to the gas flow. .
そこで、最近の研究により、乾式電気集じん部の後流部
に水膜式電気集じん部を配置することによって、上述の
問題については、一応は解決されたが、その水膜式電気
集じん部の乗じん極に連続的に給水をしていたので、使
用清水量が犬であって、不経済であるばかりでなく、集
じん後の廃水の浄化処理にも多大な費用を投じなければ
ならないし、また乗じん後のガスの温度が蓄しく低下す
るので、そのガスを再加熱したのちに、煙突から排出す
るなどの手段を必要とし、そのための設備費および運転
費が問題となっていた。According to recent research, the above-mentioned problem has been solved to some extent by placing a water film type electrostatic precipitator downstream of the dry type electrostatic precipitator. Since water was being supplied continuously to the dust collector in the building, the amount of fresh water used was not only uneconomical, but also a large amount of money had to be spent on purifying the wastewater after dust collection. Moreover, since the temperature of the gas accumulates and drops after being multiplied, it is necessary to reheat the gas and then discharge it from the chimney, which raises the problem of equipment and operating costs. Ta.
そこで、さらに本発明者等が、水膜式電気集じん部を乾
式電気集じん部に後置した集じん装置について研究をし
、重油焚きボイラの排ガスの集じんについて調査した結
果、乾式電気集じん部の集じん極の無槌打時におけろ水
膜式電気集じん部の集じん極の集じん効率は約40〜5
0%であるのに対し、乾式電気集じん部の集じん極の槌
打時におけろ水膜式電気集じん部の集じん極の集じん効
率は約80〜90%というように、槌打時における集じ
ん効率は高いが、無槌時におけるそれは比較的低いこと
を見い出した。Therefore, the present inventors further researched a dust collector in which a water film type electrostatic precipitator is placed after a dry type electrostatic precipitator, and as a result of investigating dust collection of exhaust gas from heavy oil-fired boilers, the dry type electrostatic precipitator The dust collection efficiency of the dust collection electrode of the water film type electrostatic dust collection part is approximately 40 to 5 when the dust collection electrode of the dust part is not hammered.
0%, while the dust collection efficiency of the dust collecting electrode of the water film type electrostatic precipitator is about 80 to 90% when hammering the dust collecting electrode of the dry type electrostatic precipitator. It was found that the dust collection efficiency is high when using a hammer, but it is relatively low when no hammer is used.
すなわち、乾式電気集じん都の集じん極の無槌時に水膜
式電気集じん部の集じん極に給水する効果は、すくない
ことを究明した。In other words, it has been found that the effect of supplying water to the dust collecting electrode of the water film type electrostatic precipitator when the dust collecting electrode of the dry type electrostatic precipitator is not hammered is small.
したがって、本発明は、水膜式電気集じん部の集じん極
に、連続的に給水することなく、乾式電気集じん部の最
終室の槌打期に同期させて間欠的に給水するようにした
もので、その実施態様について、図面を参照しながら説
明する。Therefore, the present invention provides a method for supplying water intermittently to the dust collection electrode of a water film type electrostatic precipitator in synchronization with the hammering period of the final chamber of the dry type electrostatic precipitator, without continuously supplying water. Embodiments thereof will be described with reference to the drawings.
第1図は水膜式電気集じん部を有する乾式電気集じん設
備を示した概略図である。FIG. 1 is a schematic diagram showing a dry electrostatic precipitator having a water film electrostatic precipitator.
第1図において、1は初段乾式電気集じん部、2は最終
段乾式電気集じん部、3は水膜式電気集じん部である。In FIG. 1, 1 is a first stage dry type electrostatic precipitator, 2 is a final stage dry type electrostatic precipitator, and 3 is a water film type electrostatic precipitator.
そして、水膜式電気集じん部3は最終段乾式電気集じん
部2の後流部に設けられており、平板状集じん極をガス
流に平行に並べ、その各表面Gこ水膜を形成させる型式
、あるいはガス流をさえぎる方向に溝形電極を複数配設
し、その電極表面に水膜を形成させる型式等、つまり、
集じん極に水膜を形成させる型式のものからなっている
。The water film type electrostatic precipitator 3 is provided downstream of the final stage dry type electrostatic precipitator 2, and flat plate-shaped dust collecting electrodes are arranged parallel to the gas flow, each surface of which has a water film. A type in which a water film is formed on the surface of the electrode, or a type in which multiple groove-shaped electrodes are arranged in the direction that blocks the gas flow, and a water film is formed on the electrode surface.
It consists of a type that forms a water film on the dust collection electrode.
4は前記最終段乾式電気集じん部2の槌打装置、5は前
記水膜式電気集じん部3への給水装置、6は前記水膜式
電気集じん部3への荷電装置であり、これら給水装置5
および荷電装置6は前記槌打装置4に同期して作動する
ように電気的に結線されているか、または該槌打装置4
と連動させたタイマーによって作動するようになってい
る。4 is a hammering device of the final stage dry electrostatic precipitator 2; 5 is a water supply device to the water film electrostatic precipitator 3; 6 is a charging device for the water film electrostatic precipitator 3; These water supply devices 5
and the charging device 6 is electrically connected to operate in synchronization with the hammering device 4, or the charging device 6 is
It is activated by a timer linked to the
また矢印7は排ガスの流入を、矢印8は集じんされた排
ガスの流出を示したものである。Further, arrow 7 indicates the inflow of exhaust gas, and arrow 8 indicates the outflow of collected exhaust gas.
第2図は本発明方法の第1実施例を示したもので、横軸
にサイクルタイムtをとって、前記槌打装置4の作動状
態をaで表わし、給水装置5の作動状態をbで表わし、
荷電装置6の作動状態をCで表わしたものである。FIG. 2 shows the first embodiment of the method of the present invention, where the cycle time t is plotted on the horizontal axis, the operating state of the hammering device 4 is represented by a, and the operating state of the water supply device 5 is represented by b. Representation,
The operating state of the charging device 6 is represented by C.
すなわち、水膜式電気集じん部3の集じん極への給水す
および荷電Cを連ミ続的に行なうのではなく、最終段乾
式電気集じん部2の槌打期aとタイミングを合せて、そ
のaの直前から直後までの間だけ行なう。That is, instead of continuously supplying water to the dust collecting electrode of the water film type electrostatic precipitator 3 and charging C, the timing is adjusted to the hammering period a of the final stage dry type electrostatic precipitator 2. , only from immediately before to immediately after a.
第3図は本発明方法の第2実施例を示したもので、第3
図のaとbについては、第2図の場合と同様であるが、
水膜式電気集じん部3の集じん極の荷電については、C
I 、 C2+ C3というように、やや連続的に行な
う。FIG. 3 shows a second embodiment of the method of the present invention.
Regarding a and b in the figure, it is the same as in Figure 2, but
Regarding the charge of the dust collecting electrode of the water film type electrostatic precipitator 3, C
I, C2+C3, and so on, done somewhat sequentially.
第4図は乾式電気集じん部2の槌打特性を示したもので
、横軸Nは槌打回数を、縦軸Fは槌打力である。FIG. 4 shows the hammering characteristics of the dry electrostatic precipitator 2, where the horizontal axis N is the number of hammerings and the vertical axis F is the hammering force.
またkはピーク倍率であり、dは99,9%の剥離点に
ついての曲線である。Also, k is the peak magnification, and d is the curve for the 99.9% peeling point.
すなわち、乾式電気集じん部2の出口におけるダスト濃
度のピーク値は、はぼ槌打回数Nと槌打力Fによって決
まるが、水膜式電気集じん部3によって槌打時の集じん
効率が上るので、槌打回数Nを減じ、槌打力Fを増し、
結果としてピーク倍率が上っても、その分を水膜式電気
集じん部3で補足することができる。In other words, the peak value of the dust concentration at the outlet of the dry electrostatic precipitator 2 is determined by the number of hammer strikes N and the hammering force F, but the water film electrostatic precipitator 3 increases the dust collection efficiency during hammering. Since it goes up, reduce the number of hammer strikes N, increase the hammer strike force F,
Even if the peak magnification increases as a result, the water film type electrostatic precipitator 3 can compensate for the increase.
つぎに、従来方法と本発明方法の比較衣を第1表に示す
。Next, Table 1 shows comparative clothing between the conventional method and the method of the present invention.
第1表において、■は従来の乾式電気集じん器によるも
の、■は乾式電気集じん部の後流部に水膜式電気集じん
部を配置した集じん装置において、水膜式電気集じん部
の乗じん極に連続的(1日当り24時間)に給水および
荷電した場合、■は本発明の第1実施例(第2図の例)
によるもの、■は本発明の第2実施例(第3図の例)に
よるものである。In Table 1, ■ indicates a conventional dry electrostatic precipitator, and ■ indicates a water film electrostatic precipitator in which a water film electrostatic precipitator is placed downstream of the dry electrostatic precipitator. When water is supplied and charged continuously (24 hours per day) to the multiplier electrode of
2 is based on the second embodiment of the present invention (the example shown in FIG. 3).
第1表かられかるように、本発明の実施例■と■では、
ガス温度をほとんど従来の乾式電気集じん器Iと変らず
に、しかも、該Iの出口濃度以下におさえることができ
る。As can be seen from Table 1, in Examples ■ and ■ of the present invention,
The gas temperature can be kept almost the same as in the conventional dry electrostatic precipitator I, and can be kept below the outlet concentration of said I.
また■と■の給水時間1 つまり給水量は■に比較して−と−であり、荷2 8 電時間についても、■は■に比較して−である。Also, water supply time 1 for ■ and ■ In other words, the water supply amount is - and - compared to ■, and the load 2 8 Regarding the electric time, ■ is also negative compared to ■.
4
したがって、本発明の運転方法は、水膜式電気集じん部
の集じん極に連続的に給水することなく、乾式集じん部
の最終室の槌打期に同期させて間欠的に給水を行なうか
ら、水の使用量が著しく低減されて低コストで運転がで
きるのみならず、ガス温度の降下もすくないので、省エ
ネルギー的であり、その奏する効果は、きわめて犬であ
る。4 Therefore, the operating method of the present invention does not continuously supply water to the dust collecting electrode of the water film type electrostatic precipitator, but intermittently supplies water in synchronization with the hammering period of the final chamber of the dry type dust collector. Because of this, not only is the amount of water used significantly reduced, making it possible to operate at low cost, but also the drop in gas temperature is small, resulting in energy savings, and the effects achieved are extremely impressive.
第1図は本発明方法によって運転される集じん設備の概
要を示した断面側面図、第2図は本発明方法の第1実施
例のサイクルの説明図、第3図は本発明方法の第2実施
例の同様な説明図、第4図は槌打回数と槌打力の関係の
説明図である。
1・・・・・・初段乾式電気集じん部、2・・・・・・
最終段乾式電気集じん部、3・・・・・・水膜式電気集
じん部、4・・・・・・槌打装置、5・・・・・・給水
装置、6・・・・・・荷電装置、a・・・・・・槌打期
、b・・・・・・給水量、Cp C1、C2+c3・・
・・・・荷電剤。FIG. 1 is a cross-sectional side view showing an outline of the dust collection equipment operated by the method of the present invention, FIG. 2 is an explanatory diagram of the cycle of the first embodiment of the method of the present invention, and FIG. A similar explanatory diagram of the second embodiment, FIG. 4, is an explanatory diagram of the relationship between the number of hammerings and the hammering force. 1... First stage dry electrostatic precipitator, 2...
Final stage dry type electrostatic precipitator, 3... Water film type electrostatic precipitator, 4... Hammering device, 5... Water supply device, 6...・Charging device, a... Hammering period, b... Water supply amount, Cp C1, C2+c3...
...Charged agent.
Claims (1)
配置して該乾式集じん都の集じん極を間欠的に槌打する
電気集じん設備において、該乾式集じん部の最終室の槌
打期に同期させて前記水膜式電気集じん部の集じん極に
給水を間欠的に行なうことを特徴とする、水膜式電気集
じん部を有°する乾式電気集じん設備の運転方法。1. In electrostatic precipitator equipment in which a water film electrostatic precipitator is disposed downstream of the dry electrostatic precipitator and the dust collection electrode of the dry precipitator is intermittently hammered, A dry electrostatic precipitator having a water film electrostatic precipitator, characterized in that water is intermittently supplied to the dust collecting electrode of the water film electrostatic precipitator in synchronization with the hammering period of the final chamber. How to operate the equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10311479A JPS5826981B2 (en) | 1979-08-15 | 1979-08-15 | How to operate a dry electrostatic precipitator equipped with a water film electrostatic precipitator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10311479A JPS5826981B2 (en) | 1979-08-15 | 1979-08-15 | How to operate a dry electrostatic precipitator equipped with a water film electrostatic precipitator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5628658A JPS5628658A (en) | 1981-03-20 |
JPS5826981B2 true JPS5826981B2 (en) | 1983-06-06 |
Family
ID=14345565
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10311479A Expired JPS5826981B2 (en) | 1979-08-15 | 1979-08-15 | How to operate a dry electrostatic precipitator equipped with a water film electrostatic precipitator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5826981B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6013229U (en) * | 1983-07-05 | 1985-01-29 | 石川島播磨重工業株式会社 | Exhaust gas treatment equipment |
-
1979
- 1979-08-15 JP JP10311479A patent/JPS5826981B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5628658A (en) | 1981-03-20 |
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