JPS60216824A - Dust collecting method of combustion exhaust gas - Google Patents
Dust collecting method of combustion exhaust gasInfo
- Publication number
- JPS60216824A JPS60216824A JP59071397A JP7139784A JPS60216824A JP S60216824 A JPS60216824 A JP S60216824A JP 59071397 A JP59071397 A JP 59071397A JP 7139784 A JP7139784 A JP 7139784A JP S60216824 A JPS60216824 A JP S60216824A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- gas
- dust
- cyclone
- soot
- 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.)
- Pending
Links
Abstract
Description
【発明の詳細な説明】
この発明は燃焼排ガス中に含まれる煤塵、特に微小粒子
の煤塵を効率よく集塵できる新規な方法に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel method for efficiently collecting soot and dust contained in combustion exhaust gas, particularly soot and dust of fine particles.
燃焼排ガスの集塵装置としては、水洗方式の外、サイク
ロンのような機械的分離方法或いは排ガス中の煤塵に帯
電させ、粒子相互を吸着凝集させる電気的方法が採用さ
れているが、水洗方式は洗浄後の膨大な量の水処理が問
題であり、機械的方法では比較的粒子の大きい煤塵には
効果があるが、微細粒子には効果が少く、ガスと共に放
出される。As dust collectors for combustion exhaust gas, in addition to the water washing method, mechanical separation methods such as cyclones or electrical methods that charge the soot and dust in the exhaust gas and attract and coagulate the particles are used. Disposal of a huge amount of water after cleaning is a problem, and while mechanical methods are effective against relatively large soot particles, they are less effective against fine particles, which are released along with the gas.
また電気的方法では設備に莫大な費用を要するばかりで
なく、稼動時の帯電装置で消費される電気料が高額とな
る欠点がある。Furthermore, the electrical method not only requires a huge amount of equipment but also has the drawback that the electricity consumed by the charging device during operation is expensive.
この発明は上記あような機械的または電気的集塵の特徴
を活かし、欠点を除去する新規な方法を提供するもので
、以下その実施例を添(=J図面について説明する。The present invention provides a new method that takes advantage of the characteristics of mechanical or electrical dust collection described above and eliminates the drawbacks, and examples thereof will be described below with reference to the accompanying drawings.
第1図はこの発明の基本的な方法を図示したもので、図
中1は煤塵を機械的に分離捕集するザイクロン、2は帯
電装置、3は送気用ブロア、aは燃焼排ガスをサイクロ
ン1へ導入する排ガス導入管、bはサイクロン1のガス
放出管、C,は煤塵が混合ターる燃焼排ガスの一部をサ
イクロン1の下部から抽出して帯電装置2へ供給する抽
出管、dは帯電装置2を通ったガスを排ガス導入管a内
に送り込む混合管で、燃焼排ガスは導入管aからサイク
ロン1内に導入し、同サイクロン内で排ガス中の煤塵を
分離し、下方へ沈降させて捕集排出し、煤塵を分離した
排ガスは、上部のガス放出管すから放出させる。Figure 1 illustrates the basic method of this invention, in which 1 is a Zyclone for mechanically separating and collecting soot and dust, 2 is a charging device, 3 is a blower for blowing air, and a is a cyclone for cleaning combustion exhaust gas. b is a gas discharge pipe of cyclone 1; C is an extraction pipe that extracts a part of the combustion exhaust gas mixed with soot and dust from the lower part of cyclone 1 and supplies it to charging device 2; This is a mixing tube that sends the gas that has passed through the charging device 2 into the exhaust gas introduction pipe a, and the combustion exhaust gas is introduced into the cyclone 1 from the introduction pipe a, where the soot and dust in the exhaust gas is separated and settled downward. The collected exhaust gas and separated soot and dust are released from the upper gas release pipe.
上記サイクロン1の下方適所からガスの一部、例えば燃
焼排ガスの5%〜15%程麿を抽出管C1から抽出して
これを帯電装置2内へ導入する。この抽出ガス中には燃
焼排ガス中に含まれる煤塵が混合しており、この煤塵に
帯電装置2で帯電させた後、混合管dにより排ガス導入
管a内に送り込み、燃焼排ガスと混合させてサイクロン
1へ送り込む。A part of the gas, for example, about 5% to 15% of the combustion exhaust gas, is extracted from an appropriate position below the cyclone 1 through the extraction pipe C1 and introduced into the charging device 2. This extracted gas is mixed with the soot dust contained in the combustion exhaust gas, and after this soot dust is charged with a charging device 2, it is fed into the exhaust gas introduction pipe a through the mixing pipe d, mixed with the combustion exhaust gas, and then passed through the cyclone. Send it to 1.
以上のようにして燃焼排ガスに帯電煤塵を混合すること
により、燃焼排ガス中の微小煤塵は帯電煤塵に吸着凝集
され−て粗大化し、分離捕集され、ガス放出管すから放
出されるガス中にはサイクロンでは捕集できない微小粒
子のないガスだけが放出される。しかも帯電装置2に供
給されるガスおよび煤塵は、燃焼排ガスの一部を抽出し
たもので、排ガス全量に対し少量であるから、帯電装置
2は小容量小形のもので足り、帯電に要する消費電力も
低額ですみ、設備も簡単で優れた集塵効果をあげること
ができる。尚サイクロン1から抽出して帯電装置2へ送
るガス量は混合管dに設けたブロア3または図示してい
ないダンパーにより調節Jる。By mixing the charged soot dust with the combustion exhaust gas as described above, the fine soot dust in the combustion exhaust gas is adsorbed and aggregated by the charged soot dust, becomes coarse, is separated and collected, and is added to the gas released from the gas discharge pipe. Only gas without microscopic particles that cannot be collected by a cyclone is released. Moreover, the gas and dust supplied to the charging device 2 are extracted from a part of the combustion exhaust gas, and are small compared to the total amount of exhaust gas, so the charging device 2 can be small and have a small capacity, and the power consumption required for charging. It is also inexpensive, requires simple equipment, and can provide excellent dust collection effects. The amount of gas extracted from the cyclone 1 and sent to the charging device 2 is adjusted by a blower 3 provided in the mixing tube d or a damper (not shown).
第2図は他の実施例を示すもので、第1図の実施例にお
いて、サイクロン1の下方から、少量のガスと共に煤塵
の一部を抽出し1=のに対し、燃焼排ガス導入管aから
抽出管C2により排ガスの一部を抽出し、これを帯電装
置へ送り込むようにしたもので、この場合抽出ガス中の
煤塵含有率は第1図の場合より低下するが、抽出ガスm
を調整することにより第1図の場合と同様の結果を得る
ことができる。Fig. 2 shows another embodiment. In the embodiment shown in Fig. 1, a part of the soot and dust is extracted from below the cyclone 1 along with a small amount of gas. A part of the exhaust gas is extracted by the extraction pipe C2 and sent to the charging device.In this case, the soot and dust content in the extracted gas is lower than in the case shown in Fig. 1, but the extracted gas m
By adjusting , the same result as in the case of FIG. 1 can be obtained.
第3図はサイクロ刈のガス放出管b′から放出する排気
の一部を抽出管0.により抽出するようにした例で、抽
出ガスに含まれる煤塵はサイクロン1で捕集できなかっ
た煤塵だけとなり、第1図、第2図のものより煤塵含有
率は少なくなるが微細粒子の集塵機能は向上する。Figure 3 shows a part of the exhaust gas released from the gas discharge pipe b' of the cyclo mower into the extraction pipe 0. In this example, the dust contained in the extracted gas is only the dust that could not be collected by cyclone 1, and the dust content is lower than that in Figures 1 and 2, but the dust collection function for fine particles is still effective. will improve.
第4図はこの発明の最も好ましい実施例の一つで、燃焼
排ガスは排ガス導入管aから第1サイクロン4に送り込
み、同サイクロンで分離捕集された煤塵の一部または全
量を第2サイクロン5へ少量の排気ガスと共に供給し、
この第2サイクロンで分離捕集された煤塵は下方から排
出し、ガスは上方から抽出管C4によって帯N装置2へ
送り込み、更に混合管dを経て、排ガス導入管aの排ガ
スに混合さUる。FIG. 4 shows one of the most preferred embodiments of the present invention, in which the combustion exhaust gas is fed into the first cyclone 4 from the exhaust gas introduction pipe a, and part or all of the soot and dust separated and collected in the same cyclone is transferred to the second cyclone 5. together with a small amount of exhaust gas,
The soot dust separated and collected by this second cyclone is discharged from below, and the gas is sent from above to the zone N device 2 through the extraction pipe C4, and further passes through the mixing pipe d, where it is mixed with the exhaust gas in the exhaust gas introduction pipe a. .
上記の第1、第2サイクロン4,5は例えば2μ以上の
煤塵分離能力を有するものを使用し、第1サイクロン4
の煤塵と共に抽出するガスは燃焼排ガス敞の5%〜15
%とすると、第2サイクロンで処理するガスは燃焼ガス
量に比べ少量となり小容量のサイクロンで足り、煤塵は
2個の→ノイクロンで分離捕集されるため良好な集塵結
果が得られ、微小粒子の放出も防止できる。For example, the first and second cyclones 4 and 5 have a soot and dust separation ability of 2μ or more, and the first cyclone 4
The gas extracted together with the soot and dust accounts for 5% to 15% of the combustion exhaust gas.
%, the gas to be treated in the second cyclone is small compared to the amount of combustion gas, so a small-capacity cyclone is sufficient, and the soot and dust is separated and collected by the two → Neuclones, so good dust collection results can be obtained, and fine dust collection can be achieved. The release of particles can also be prevented.
また上記実施例では第1ザイクロン4と第2サイクロン
5の粒度捕集性能の具なるもの、例えば第1サイクロン
4は2μ以上の粒度捕集性能のものを、第2サイクロン
5は10μ以上の粒度捕集性能のものとすれば、第2サ
イクロン5から帯電装置2へ送られる粒子は10μ以下
となり、粒度が揃ったものとなるので帯電装置2による
帯電状態並びに燃焼排ガスとの混合状態がよくなり、第
1サイクロン4による微小煤塵の捕集効果をよくするこ
とができる。Further, in the above embodiment, the first cyclone 4 and the second cyclone 5 have particle size collection performance, for example, the first cyclone 4 has a particle size collection performance of 2μ or more, and the second cyclone 5 has a particle size collection performance of 10μ or more. If the particles have a collection performance, the particles sent from the second cyclone 5 to the charging device 2 will be less than 10μ and have a uniform particle size, so that the charging state by the charging device 2 and the mixing state with the combustion exhaust gas will be improved. , the effect of collecting fine dust by the first cyclone 4 can be improved.
【図面の簡単な説明】
第1図はこの発明の基本的な方法を図示した説明図、第
2図、@3図は他の実施例の説明図、第4図はこの発明
の好ましい実施病の説明図である。
1・・・サイクロン 2・・・帯電装置4・・・第1サ
イクロン 5・・・第2サイクロンa・・・燃焼排ガス
導入管 b・・・ガス放出管C,,Cユ、 C3,C4
・・・抽出管 d・・・混合管特許出願人 西 岡 組
入
代 理 人 弁理士 和 1) 昭[Brief Description of the Drawings] Fig. 1 is an explanatory diagram illustrating the basic method of this invention, Figs. 2 and 3 are explanatory diagrams of other embodiments, and Fig. 4 is an explanatory diagram of a preferred embodiment of this invention. FIG. 1...Cyclone 2...Charging device 4...First cyclone 5...Second cyclone a...Combustion exhaust gas introduction pipe b...Gas discharge pipe C, C3, C4
...Extraction tube d...Mixing tube Patent applicant: Gumi Nishioka Representative: Patent attorney: Kazu 1) Akira
Claims (3)
抽出し、帯電装置により抽出した排ガス中の煤塵に帯電
させ、これをサイクロンに導入する燃焼排ガス中に混入
させることを特徴とする燃焼排ガスの集塵方法。(1) Combustion characterized by extracting part of the soot dust in the combustion exhaust gas together with a small amount of the exhaust gas, charging the soot dust in the extracted exhaust gas with a charging device, and mixing it into the combustion exhaust gas introduced into the cyclone. How to collect dust from exhaust gas.
ンで分離した煤塵を、第2サイクロンに少量のガスと共
に導入し、同サイクロンの排ガスを帯電装置に導入し、
排ガス中に残存する煤塵に帯電させ、これを第1ザイク
ロンに導入する燃焼排ガス中に混入させることを特徴と
する特許請求の範囲第1項記載の燃焼排ガスの集塵方法
。(2) Separate and collect the soot dust in the combustion exhaust gas. The soot dust separated by the first cyclone is introduced into the second cyclone together with a small amount of gas, and the exhaust gas from the cyclone is introduced into the charging device,
A method for collecting dust from combustion exhaust gas according to claim 1, characterized in that the soot dust remaining in the exhaust gas is charged and mixed into the combustion exhaust gas introduced into the first Zykron.
度捕集性能が異なる特許請求の範囲第1項また°は第2
項記載の燃焼排ガスの集塵方法。(3) The first cyclone and the second cyclone have different dust particle size collection performance.
Dust collection method for combustion exhaust gas as described in section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59071397A JPS60216824A (en) | 1984-04-09 | 1984-04-09 | Dust collecting method of combustion exhaust gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59071397A JPS60216824A (en) | 1984-04-09 | 1984-04-09 | Dust collecting method of combustion exhaust gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60216824A true JPS60216824A (en) | 1985-10-30 |
Family
ID=13459337
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59071397A Pending JPS60216824A (en) | 1984-04-09 | 1984-04-09 | Dust collecting method of combustion exhaust gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60216824A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017064863A (en) * | 2015-09-30 | 2017-04-06 | パナソニックIpマネジメント株式会社 | Dust collector |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5252278A (en) * | 1975-10-24 | 1977-04-26 | Lotte Co Ltd | Improvement of dust arrester |
-
1984
- 1984-04-09 JP JP59071397A patent/JPS60216824A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5252278A (en) * | 1975-10-24 | 1977-04-26 | Lotte Co Ltd | Improvement of dust arrester |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017064863A (en) * | 2015-09-30 | 2017-04-06 | パナソニックIpマネジメント株式会社 | Dust collector |
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