JPS58156357A - Electric dust collecting apparatus - Google Patents
Electric dust collecting apparatusInfo
- Publication number
- JPS58156357A JPS58156357A JP57015889A JP1588982A JPS58156357A JP S58156357 A JPS58156357 A JP S58156357A JP 57015889 A JP57015889 A JP 57015889A JP 1588982 A JP1588982 A JP 1588982A JP S58156357 A JPS58156357 A JP S58156357A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- dust
- cost
- boiler
- dust collecting
- 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
- Electrostatic Separation (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は例えばボイラ排ガスの如き高温含塵ガスの廃熱
利用に好適な電気集塵装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electrostatic precipitator suitable for utilizing waste heat of high-temperature dust-containing gas such as boiler exhaust gas.
高温電気集塵装置を用いる近時のボイラ排ガスの廃熱利
用として、第1図に示すようにボイラ1からの排ガスを
エコノiイザ2で調温し、高温電気集塵装置3で除塵し
、次いで集塵後のガスの大部分はエヤヒータ4で降温後
脱硫装置5により脱硫処理して大気中に拡散する一方、
この脱硫tSSするガス量を100としてガス量15〜
50はボイラに再循様し一工241・用され℃いる。As shown in Fig. 1, the temperature of the exhaust gas from a boiler 1 is controlled by an economizer 2, and dust is removed by a high-temperature electrostatic precipitator 3, as shown in Fig. 1. Next, most of the gas after dust collection is cooled down by an air heater 4, and then desulfurized by a desulfurization device 5 and diffused into the atmosphere.
The gas amount for this desulfurization tSS is 100, and the gas amount is 15~
50°C is recirculated to the boiler and used at 241°C.
このほか、高温金層ガスの廃熱利用としては、石炭、ア
ッシュ等の看粒体の乾燥用熱ガスとして応用されるもの
である。In addition, the waste heat of high-temperature gold layer gas can be used as hot gas for drying granules such as coal and ash.
ところで、ボイラに再循撫するガスの含塵量はメインガ
JF)O−1f/M11I′に対し0.5f/1rII
IP程度でよいのくもかかわらず、前記の従来システム
ではメインガスと再循環ガスを合わ甘た全量を電気集塵
装置3で処理し、再循撫ガスの含塵量を必要以上に低く
し、かつ電気集塵装置3を必要以上に大きくしており、
排ガス処理のコストアップの要因となっている。By the way, the dust content of the gas recirculated to the boiler is 0.5f/1rII for the main gas JF)O-1f/M11I'.
Despite the fact that IP level is sufficient, in the conventional system described above, the entire amount of the main gas and recirculated gas is treated with the electrostatic precipitator 3, and the dust content of the recirculated gas is lowered than necessary. And the electrostatic precipitator 3 is made larger than necessary,
This is a factor that increases the cost of exhaust gas treatment.
本発明は被処理ガスを夫々の用途に応じた異る含塵量の
ガスとして取出すことを特徴とする電気集塵装置である
。The present invention is an electrostatic precipitator characterized in that the gas to be treated is taken out as gases having different dust contents depending on the respective uses.
以下、本発明を第2図および第3図に示す実施例により
説明すると、集塵i16は排ガス人ロアと、皺集塵室6
の上部で開口するメインガス出口8と、皺集烏*6の途
中で開口するガス出口9とを備え℃おり、集塵室6内に
は集塵極板および放電極線よりなる集塵部10が複数ガ
ス流方向に相隣合わして設置されている。Hereinafter, the present invention will be explained with reference to the embodiment shown in FIGS.
The dust collection chamber 6 has a main gas outlet 8 that opens at the top and a gas outlet 9 that opens in the middle of the wrinkle collecting crow*6. 10 are installed adjacent to each other in the gas flow direction.
使用に際しては、エコノマイず2で調温したボイラ排ガ
スが排ガス人ロアを経て集塵1116内に入り会集塵部
10を順次抜け、まずその一部がガス出口9から排出さ
れボイラへ再循環されるが、これに影餐されずに大部分
のボイラ排ガスはさらに各集塵部10を抜け℃メインガ
ス出口8から排出されるから、集tm*6にはメインガ
ス流ムとサブガス流Bが構成される。しかして、メイン
ガス11は、サブガス12より多くの集塵部10を抜け
て15す、装置運転時該集塵部10により所定の含塵量
以下まで除塵される。In use, the boiler exhaust gas whose temperature has been adjusted by the economizer 2 passes through the exhaust gas lower part, enters the dust collector 1116, passes through the dust collector 10 one after another, and a part of it is first discharged from the gas outlet 9 and recirculated to the boiler. However, without being affected by this, most of the boiler exhaust gas further passes through each dust collecting section 10 and is discharged from the main gas outlet 8 at °C, so the main gas flow B and the sub gas flow B are included in the collection tm*6. configured. Thus, the main gas 11 passes through more dust collectors 10 than the sub gas 12, and is removed by the dust collectors 10 to a predetermined dust content or less during operation of the apparatus.
これ忙対してサブガス12は集塵室6の途中で排出され
るから、メインガス11より集電荷電時間が短く、従っ
て七〇含塵量はメインガス11よりも多くなる。On the other hand, since the sub-gas 12 is discharged midway through the dust collection chamber 6, the charging time is shorter than that of the main gas 11, and therefore the dust content is greater than that of the main gas 11.
なお、メインガス流ムとサブガス流9間は仕切壁で仕切
っても良い。Note that the main gas flow 9 and the sub gas flow 9 may be separated by a partition wall.
以上の通り不発明はサブガスな集塵室の途中で、メイン
ガスの集塵托影響を与えることな(排出する構成である
から、従来サブガスの必要以上の除應に使用していた集
塵機部分(集電極板、放電極線、槌打装置、支持碍子、
電源等)が不要となり、設備費、2ン二ングコストおよ
びメンテナンスコストを確実に低減できる。As mentioned above, the inventive feature is that the main gas is discharged midway through the subgas dust collection chamber without affecting the main gas dust collection chamber, so the dust collector part, which was conventionally used to remove more subgas than necessary, collector electrode plate, discharge electrode wire, hammering device, support insulator,
This eliminates the need for power supplies, etc., and can reliably reduce equipment costs, running costs, and maintenance costs.
上記は、再循環ガスについての実施例を説明したが、サ
ブガスが、七〇會塵量がメインガスより多くて良い他の
用途例えば粉粒体(石炭やアッシュ)等の乾燥用ガスと
しても同様に利用できる。The above example describes the recirculating gas, but the subgas can also be used in other applications where the amount of dust is larger than the main gas, for example, as a drying gas for powder and granules (coal and ash). Available for
Wl、1図は従来のボイラ排ガス処理システムの概要図
、第2図は本発明装置を使用したボイラ排ガス処理シス
テムの概要図、IIE[lは本発明装置の平面図である
。
6・・集塵室、7・・排ガス入口、8・・メインガス出
口、9・・サブガス出口、1o・・集塵部、11・・メ
インガス、12・・含塵量の多いサブガス。Figure 1 is a schematic diagram of a conventional boiler exhaust gas treatment system, Figure 2 is a schematic diagram of a boiler exhaust gas treatment system using the device of the present invention, and IIE [l is a plan view of the device of the present invention. 6. Dust collection chamber, 7. Exhaust gas inlet, 8. Main gas outlet, 9. Sub gas outlet, 1o. Dust collection section, 11. Main gas, 12. Sub gas with high dust content.
Claims (1)
れらを各別KIIE出すことを特徴とする電気集塵装置
。An electrostatic precipitator characterized in that two or more gases having different dust contents are treated as gases to be treated, and each of these gases is discharged as a separate KIIE.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57015889A JPS58156357A (en) | 1982-02-03 | 1982-02-03 | Electric dust collecting apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57015889A JPS58156357A (en) | 1982-02-03 | 1982-02-03 | Electric dust collecting apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58156357A true JPS58156357A (en) | 1983-09-17 |
JPS6126427B2 JPS6126427B2 (en) | 1986-06-20 |
Family
ID=11901353
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57015889A Granted JPS58156357A (en) | 1982-02-03 | 1982-02-03 | Electric dust collecting apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58156357A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0339130Y2 (en) * | 1986-03-31 | 1991-08-19 | ||
JPH01127532U (en) * | 1988-02-26 | 1989-08-31 |
-
1982
- 1982-02-03 JP JP57015889A patent/JPS58156357A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6126427B2 (en) | 1986-06-20 |
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