JPS5938021B2 - Two-stage electrostatic precipitation method - Google Patents

Two-stage electrostatic precipitation method

Info

Publication number
JPS5938021B2
JPS5938021B2 JP49099720A JP9972074A JPS5938021B2 JP S5938021 B2 JPS5938021 B2 JP S5938021B2 JP 49099720 A JP49099720 A JP 49099720A JP 9972074 A JP9972074 A JP 9972074A JP S5938021 B2 JPS5938021 B2 JP S5938021B2
Authority
JP
Japan
Prior art keywords
exhaust gas
boric acid
dust
precipitator
collected
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
Application number
JP49099720A
Other languages
Japanese (ja)
Other versions
JPS5127163A (en
Inventor
進 都倉
功 斎藤
三郎 辻
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 Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies Ltd
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 Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP49099720A priority Critical patent/JPS5938021B2/en
Publication of JPS5127163A publication Critical patent/JPS5127163A/en
Publication of JPS5938021B2 publication Critical patent/JPS5938021B2/en
Expired legal-status Critical Current

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  • Electrostatic Separation (AREA)

Description

【発明の詳細な説明】 この発明は、硼珪酸ガラス溶融炉からの排出ガスの乾式
集塵法に係わり、特に該排出ガスから分離除去した硼酸
を回収利用するに好適な乾式集塵法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a dry dust collection method for exhaust gas from a borosilicate glass melting furnace, and particularly to a dry dust collection method suitable for recovering and utilizing boric acid separated and removed from the exhaust gas.

上記排出ガスに含まれるはい塵には原料である珪砂、石
灰、曹達、加里、硼砂等の粉塵およびガス状のアルカリ
塩類、硼酸等が存在しているが、集塵器に導入される段
階では該排出ガスの温度は260℃位に低下している。
The dust contained in the above exhaust gas contains raw materials such as silica sand, lime, soda, potash, borax, etc., as well as gaseous alkali salts, boric acid, etc., but at the stage of introduction into the dust collector, The temperature of the exhaust gas has decreased to about 260°C.

この温度ではアルカリ塩類は殆んど粉体化しているので
例えば電気集塵器で捕集が十分に可能である。
At this temperature, most of the alkali salts are pulverized, so they can be sufficiently collected using, for example, an electrostatic precipitator.

しかしながら、硼酸は上記温度でも蒸気圧が高いので、
気化状態であって乾式集塵法では除去が困難であった。
However, boric acid has a high vapor pressure even at the above temperature, so
It was in a vaporized state and difficult to remove using dry dust collection.

このため集塵器を通過した後に排出口で該排出ガスが大
気に拡散する際に急冷して上記硼酸は凝縮粉体化し、白
煙発生の原因をなしていた。
For this reason, when the exhaust gas diffuses into the atmosphere at the exhaust port after passing through the dust collector, it is rapidly cooled and the boric acid is condensed into powder, causing white smoke generation.

かかる事態を防止するために、従来技術においては、先
ず高温状態で該排出ガスを乾式集塵したのち、気化状態
にある硼酸を湿式法により除去する方法が一部に行われ
ている。
In order to prevent such a situation, in some prior art methods, the exhaust gas is first subjected to dry dust collection in a high temperature state, and then the boric acid in a vaporized state is removed by a wet method.

しかし、かかる方法では洗滌液中に上記硼酸等が溶解し
、これらの分離除去処理装置が必要になる。
However, in this method, the boric acid and the like are dissolved in the cleaning solution, and a device for separating and removing them is required.

また、上記従来技術では高価な硼酸を棄却せざるを得な
い結果となり、資源再利用の面からも有効適切な該排出
ガスの集塵法が所望されていた。
Further, in the above-mentioned conventional technology, expensive boric acid had to be discarded, and a method for collecting dust from the exhaust gas that is effective and appropriate from the viewpoint of resource reuse has been desired.

また、乾式集塵法において、例えば該排出ガスを冷却し
、気化状態の硼酸を凝縮粉体化したのちに、電気集塵し
た場合は、白煙の発生は防止できるが、捕集粉塵には中
途半端な純度で硼酸が含有し、回収して再利用する価値
はなく、捷だそのまま棄却する場合には硼酸が公害発生
の一因となるため捕集粉塵中の硼酸は極力少くすること
が望ましい。
In addition, in the dry dust collection method, for example, if the exhaust gas is cooled and the vaporized boric acid is condensed into powder, and then electrostatically collected, the generation of white smoke can be prevented, but the collected dust It contains boric acid of intermediate purity, so it is not worth collecting and reusing, and if it is shredded and thrown away, boric acid will contribute to pollution, so it is important to minimize the amount of boric acid in the collected dust. desirable.

本発明の目的は上記従来技術の課題を解決し、湿式法を
用いずに該排出ガスから硼酸を確実に選択的に分離、除
去し、公害防止および資源再利用の観点から、有効適切
な乾式集塵法を提供するにある。
The purpose of the present invention is to solve the above-mentioned problems of the prior art, to reliably and selectively separate and remove boric acid from the exhaust gas without using a wet method, and to provide an effective and appropriate dry method from the viewpoint of pollution prevention and resource reuse. Provides a dust collection method.

本発明は、上記目的を達成する手段として、硼珪酸ガラ
ス溶融炉からの排出ガスを、まず高温状態(約260°
C)のまま第1の集塵器゛に導入し、該排出ガス中に含
有する粉塵の大部分を除去したのち、該排出ガスを10
0℃以下に強制冷却したのち、第2の集塵器である電気
集塵器に導入することを特徴とする。
As a means to achieve the above object, the present invention first converts exhaust gas from a borosilicate glass melting furnace into a high temperature state (approximately 260°
C) is introduced into the first dust collector, and after removing most of the dust contained in the exhaust gas, the exhaust gas is
It is characterized in that after being forcedly cooled to 0° C. or lower, it is introduced into an electric precipitator, which is a second precipitator.

上記の方法において、第1の集塵器としては、当然に乾
式のものが使用され、処理条件により重力沈降式集塵器
、慣性式集塵器、電気集塵器などが使い分けられる。
In the above method, a dry type precipitator is naturally used as the first precipitator, and a gravity sedimentation type precipitator, an inertial type precipitator, an electric precipitator, etc. are used depending on the processing conditions.

第1の集塵器にて粉塵の大部分が分離除去された該排出
ガスを100℃以下に強制冷却する理由は、次の3点で
ある。
There are three reasons why the exhaust gas from which most of the dust has been separated and removed in the first dust collector is forcedly cooled to 100° C. or lower.

まず第1には硼酸を選択的に回収できる点である。First, boric acid can be selectively recovered.

すなわち、上記第1の集塵器の入口側で該排出ガスを強
制冷却する場合には、硼酸が他の粉塵とともに捕集され
、これを回収利用しよへとしても硼酸としては純度が低
下し利用価値が低い。
That is, when the exhaust gas is forcibly cooled on the inlet side of the first dust collector, boric acid is collected together with other dust, and even if this is collected and used, the purity of the boric acid will decrease. Its utility value is low.

第2には、諸文献から明らかなように硼酸は100℃付
近を境にして蒸気圧が急激に変化し、100℃以上では
十分な捕集効果が得られないことである。
Second, as is clear from various literatures, the vapor pressure of boric acid changes rapidly around 100°C, and a sufficient trapping effect cannot be obtained above 100°C.

第3には硼酸自体は電気抵抗値が高く、これを電気集塵
器で捕集しようとしても逆電離現象により十分な捕集効
果をあげることができないことと関連する。
The third problem is that boric acid itself has a high electrical resistance value, and even if an attempt is made to collect it with an electrostatic precipitator, a sufficient collection effect cannot be achieved due to the reverse ionization phenomenon.

すなわち、該排出ガスを100℃以下とすることによっ
て、該排出ガス中の蒸気、硫酸分が凝縮し、湿分を与え
るので、該排出ガスの電気抵抗値が相対的に小さくなり
、電気集塵の性能が発揮され易い条件を創成する。
That is, by keeping the exhaust gas at 100°C or lower, steam and sulfuric acid in the exhaust gas condense and provide moisture, so the electrical resistance value of the exhaust gas becomes relatively small and electrostatic precipitator Create conditions that make it easy to demonstrate performance.

また、本発明において、第2の集塵器として、電気集塵
器を用いた理由は、もともとガス状であった硼酸が急冷
により粉体化した際の粒子はきわめて微細であり、この
微細な硼酸粒子を効率よく回収する乾式集塵器としては
電気集塵器が適切であるということにほかならない以下
、本発明の一実施例を図面に従って説明する。
In addition, in the present invention, the reason why an electric precipitator is used as the second precipitator is that when boric acid, which was originally in a gaseous state, is pulverized by rapid cooling, the particles are extremely fine. An electric precipitator is suitable as a dry precipitator for efficiently collecting boric acid particles.An embodiment of the present invention will be described below with reference to the drawings.

図において、煙道1は硼珪酸ガラス溶融炉からの排出ガ
スの尋人煙道であり、該排出ガスは、煙道1を経て第1
の集塵器である電気集塵器2に導入される。
In the figure, the flue 1 is a flue for exhaust gas from a borosilicate glass melting furnace, and the exhaust gas passes through the flue 1 to the first
is introduced into an electric precipitator 2, which is a precipitator.

この電気集塵器2にて排出ガス中のアルカリ塩類を主体
とする粉塵が分離除去される。
This electric precipitator 2 separates and removes dust mainly composed of alkali salts in the exhaust gas.

第1電気集塵器2の出口煙道3には大気導入配管4が接
続されており、この配管4より大気が煙道3内に導入さ
れ、排出ガスの温度は85℃まで冷却される。
An air introduction pipe 4 is connected to the outlet flue 3 of the first electrostatic precipitator 2, and the air is introduced into the flue 3 through the pipe 4, and the temperature of the exhaust gas is cooled to 85°C.

硼酸の温度による蒸気圧は下記に示すように100℃以
下になると急激に小さくなる。
As shown below, the vapor pressure of boric acid depending on the temperature decreases rapidly when the temperature drops below 100°C.

温度(’C) 20 43.5 66 79 1
00 128蒸気圧(im/Hg) 2 5
16 30 60 242このため排出ガス中の硼酸
の殆んどは凝固粉体化し、また排出ガスの温度が85℃
以下であるため、排出ガス中の蒸気の一部が凝縮し、硼
酸粒子の見掛けの電気抵抗値を下げる効果を有する。
Temperature ('C) 20 43.5 66 79 1
00 128 Vapor pressure (im/Hg) 2 5
16 30 60 242 Therefore, most of the boric acid in the exhaust gas is solidified into powder, and the temperature of the exhaust gas is 85℃.
Since it is below, a part of the vapor in the exhaust gas is condensed, which has the effect of lowering the apparent electrical resistance value of the boric acid particles.

第2電気集塵器5では硼酸を主体とする粉塵が分詠離除
去され、清浄化された排出ガスはブロワ−6を経て煙道
7から大気に放出される。
In the second electrostatic precipitator 5, dust mainly composed of boric acid is separated and removed, and the purified exhaust gas is discharged into the atmosphere from a flue 7 via a blower 6.

試みに第1電気集塵器2および第2電気集塵器で捕集さ
れた粉塵の組成を比較すると下記の通りである。
A comparison of the compositions of the dust collected by the first electrostatic precipitator 2 and the second electrostatic precipitator is as follows.

K2O5i02SO2AS203A1203PbONa
20B203外第1集塵器 13.2 tr
37.6 1.Otr 1.7 12.1
13.2 −第2集塵器 4.2 tr
10.8 tr tr tr
3.8 62.5 −上記からも明らかなように、
第2電気集塵器で捕集された粉塵は硼酸の純度が高く、
再利用に十分に供することができる。
K2O5i02SO2AS203A1203PbONa
20B203 External 1st dust collector 13.2 tr
37.6 1. Otr 1.7 12.1
13.2 - Second dust collector 4.2 tr
10.8 tr tr tr
3.8 62.5 - As is clear from the above,
The dust collected by the second electrostatic precipitator has high purity boric acid,
It can be fully used for reuse.

捷だ、第1電気集塵器で捕集された粉塵は硼酸の純度が
比較的低いので、これをそのまま棄却するか、捷たは公
害防止のための処理をしたのちに棄却する場合でも問題
が少ない。
However, the purity of the boric acid in the dust collected by the first electrostatic precipitator is relatively low, so there is a problem even if it is discarded as is, or it is discarded after being filtered or treated to prevent pollution. Less is.

なお、上記実施例では、排出ガスの冷却法として、大気
導入による直接冷却を用いたが、これは熱交換器等によ
る間接冷却でもよい。
In the above embodiment, direct cooling by introducing atmospheric air was used as a method of cooling the exhaust gas, but indirect cooling using a heat exchanger or the like may also be used.

間接冷却によれば、排出ガスの廃熱回収が可能となり、
寸た排出ガスの量が増大しないので、後段の第2の集塵
器の容量を小さくすることができる。
Indirect cooling makes it possible to recover waste heat from exhaust gas,
Since the amount of exhaust gas does not increase, the capacity of the second dust collector at the subsequent stage can be reduced.

以上述べたように、本発明は硼珪酸ガラス溶融炉からの
排出ガスを白煙を発生させることなく乾式集塵でき、第
2の集塵器での捕集粉塵はその捷ま回収利用できるので
、公害防止および資源再利用の観点から多大な効果を奏
する。
As described above, the present invention enables dry dust collection of the exhaust gas from the borosilicate glass melting furnace without producing white smoke, and the dust collected in the second dust collector can be collected and used by folding it. , has great effects from the viewpoint of pollution prevention and resource reuse.

また、湿式集塵法を用いないので水処理装置を付設する
必要もない。
Furthermore, since a wet dust collection method is not used, there is no need to install a water treatment device.

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

付図は本発明の一実施例を示す概略系統図である。 1,3・・・煙道、2・・・第1電気集塵器、4・・・
大気導入配管、5・・・第2電気集塵器。
The attached figure is a schematic system diagram showing one embodiment of the present invention. 1, 3... Flue, 2... First electrostatic precipitator, 4...
Air introduction piping, 5...second electrostatic precipitator.

Claims (1)

【特許請求の範囲】[Claims] 1 硼珪酸ガラス溶融炉からの排出ガスをまず第1の集
塵器に導入し、該排出ガス中に含有する粉塵の大部分を
除去したのち、該排出ガスを100℃以下に強制冷却し
てのち、第2の集塵器である電気集塵器に導入すること
を特徴とする硼珪酸ガラス溶融炉からの排出ガスの乾式
集塵法。
1. The exhaust gas from the borosilicate glass melting furnace is first introduced into the first dust collector to remove most of the dust contained in the exhaust gas, and then the exhaust gas is forcibly cooled to below 100°C. A dry dust collection method for exhaust gas from a borosilicate glass melting furnace, which is then introduced into an electrostatic precipitator, which is a second dust collector.
JP49099720A 1974-08-30 1974-08-30 Two-stage electrostatic precipitation method Expired JPS5938021B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP49099720A JPS5938021B2 (en) 1974-08-30 1974-08-30 Two-stage electrostatic precipitation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP49099720A JPS5938021B2 (en) 1974-08-30 1974-08-30 Two-stage electrostatic precipitation method

Publications (2)

Publication Number Publication Date
JPS5127163A JPS5127163A (en) 1976-03-06
JPS5938021B2 true JPS5938021B2 (en) 1984-09-13

Family

ID=14254897

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49099720A Expired JPS5938021B2 (en) 1974-08-30 1974-08-30 Two-stage electrostatic precipitation method

Country Status (1)

Country Link
JP (1) JPS5938021B2 (en)

Also Published As

Publication number Publication date
JPS5127163A (en) 1976-03-06

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