JPS58156360A - Removal of dust from sampled gas and apparatus therefor - Google Patents
Removal of dust from sampled gas and apparatus thereforInfo
- Publication number
- JPS58156360A JPS58156360A JP3866382A JP3866382A JPS58156360A JP S58156360 A JPS58156360 A JP S58156360A JP 3866382 A JP3866382 A JP 3866382A JP 3866382 A JP3866382 A JP 3866382A JP S58156360 A JPS58156360 A JP S58156360A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- dust
- flue
- removal
- dust catcher
- 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、ダストを含んだ煙道ガスの分析型に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a type of analysis of dust-laden flue gases.
一般に、ダストを含んだ煙道ガスを分析するには、同ガ
スのサンプリングガスを予め完全に除塵しておく必要が
ある。そのため従来は、第1図に示すように、煙道(1
)から分析計(2)へ至るサンプリングガス導管(3)
に、1次フィルタ(4)と2次フィルタ(5)をポンプ
(6)を介して設け、これらフィルタ+41 +51で
除塵を行っていた。しかしこの方法では、ダスト濃度が
高いと、1次フィルタ(4)が短時間で目詰りをきたし
、フィルタ交換を頻繁に行なわねばならなかった。Generally, in order to analyze flue gas containing dust, it is necessary to completely remove dust from the sampling gas. Therefore, conventionally, as shown in Figure 1, the flue (1
) to the analyzer (2) sampling gas conduit (3)
A primary filter (4) and a secondary filter (5) were installed via a pump (6), and dust removal was performed by these filters +41 to +51. However, in this method, when the dust concentration is high, the primary filter (4) becomes clogged in a short period of time, requiring frequent filter replacement.
この発明は、上記のような点に鑑みてなされたもので、
サイクロン型集塵装置を改良して、除塵効率を向上させ
るとともに、同装置の長時間連続使用を可能にすること
により完成せられたものである。This invention was made in view of the above points,
This was completed by improving the cyclone type dust collector to improve the dust removal efficiency and making it possible to use the device continuously for a long time.
この発明によるサンプリングガスの除塵方法は、サイク
ロン型集塵装置の下端から流入ガスの70%以上の量の
ガスを抜出すことを特徴とする。抜出したガスは煙道に
戻すか、または大気中に放散する。ガス抜率が70%以
上に限定されるのは、後述する第4図に示すように、7
0%未満では除塵効果が十分でないからである。The sampling gas dust removal method according to the present invention is characterized in that 70% or more of the incoming gas is extracted from the lower end of the cyclone type dust collector. The extracted gas is returned to the flue or dissipated into the atmosphere. The degassing rate is limited to 70% or more, as shown in Figure 4 below.
This is because if it is less than 0%, the dust removal effect will not be sufficient.
この発明による除塵方法の概略を第2図に示す。すなわ
ち煙道(111から分析計(121へ至るサンプリング
ガス導管(131に、サイクロン型集塵装置(141と
これの下流側のフィルタ(151とを、ポンプ(161
を介して配する。そして煙道ガスの一部をサイクロン型
集塵装置041に導いて除塵し、同装置141の下端か
ら流入ガスの70%以上の量のガスを抜この発明による
除塵方法に直接使用する除塵装置の代表例を第3図に示
す。この除塵装置はサイクロン型集塵装置を改良したも
のであって、側部に入口r211を有しかつ頂部に出口
@を有する円筒部のと、これの下端に設けられた逆円錐
部24)と、これの下端に設けられた集塵部□□□と、
これの下端に設けられたガス抜口■とからなる。FIG. 2 shows an outline of the dust removal method according to the present invention. That is, a sampling gas conduit (131) leading from the flue (111 to the analyzer (121), a cyclone type dust collector (141) and a filter (151 downstream of this), and a pump (161)
Allocate via. A part of the flue gas is then guided to a cyclone type dust collector 041 for dust removal, and 70% or more of the inflow gas is removed from the lower end of the same device 141. A typical example is shown in Figure 3. This dust removal device is an improved version of the cyclone type dust collector, and includes a cylindrical portion having an inlet r211 on the side and an outlet at the top, and an inverted conical portion 24) provided at the lower end of the cylindrical portion. , a dust collection section □□□ provided at the lower end of this,
It consists of a gas vent (■) provided at the lower end of this.
入口@は円筒部(2)の径の半分以下の径を有する円筒
状をなし、集塵部(ハ)は円筒部(ハ)の径より!小さ
くかつこれの175より大きい径を有する円筒状をなす
。そして入口囚から流入だサンプリングガスは、円筒部
(ハ)および逆円錐部(財)の内周面に沿ってスパイラ
ル状に回転しながら下降し為逆円錐部■の下端付近で流
れを反転して上昇するとともに、ここで除塵される。気
流と分けられたダストは、ガスの反転に伴って上昇する
ことがなく、ガス抜目□□□から抜かれたガスによって
煙道(21)へ戻される。The inlet @ has a cylindrical shape with a diameter less than half the diameter of the cylindrical part (2), and the dust collection part (c) is larger than the diameter of the cylindrical part (c)! It is small and has a cylindrical shape with a diameter larger than 175 mm. The sampling gas flowing in from the inlet flows downward while rotating in a spiral along the inner peripheral surfaces of the cylindrical part (C) and the inverted conical part (2), and reverses its flow near the lower end of the inverted conical part (2). As the dust rises, the dust is removed here. The dust separated from the airflow does not rise as the gas reverses, and is returned to the flue (21) by the gas extracted from the gas vent □□□.
第4図は、出口■の径が円筒部(ハ)の径の0.3倍で
かつ集塵部(2)の径が円筒部(ハ)の径の半分である
場合におけるガス抜率とダスト(フライアッシュ)の除
塵率の関係を示すグラフである。Figure 4 shows the gas removal rate when the diameter of the outlet (■) is 0.3 times the diameter of the cylindrical part (c) and the diameter of the dust collecting part (2) is half the diameter of the cylindrical part (c). It is a graph showing the relationship between the dust removal rate of dust (fly ash).
同図かられかるように、ガス抜率70%付近で除塵率が
急上昇している。As can be seen from the figure, the dust removal rate increases rapidly when the degassing rate is around 70%.
この発明は以上のとおり構成されているので、集塵装置
の取換えを要せずζこ、サンプリングガスの除塵を長時
間連続的に行なうことができ、しかも除塵率の大幅な向
上を果すことができる。Since the present invention is constructed as described above, it is possible to continuously remove dust from the sampling gas for a long time without the need to replace the dust collector, and the dust removal rate can be greatly improved. Can be done.
第1図は従来法を示す除塵方法のフロー図、第2図はこ
の発明の実施例を示す除塵方法の7係を示すグラフであ
る。
01)・・・煙道、02・・・分析計、0J0・サンプ
リングガス導管、ti41・拳・サイクロン型集塵装置
、u81・・・導管、@拳・・ガス抜目。
以 上
特許出願人 日立造船株式会社
昭和5フイ[5月21口
1 ・It l’1.の )、1− 昭和57年
特、i′liK・11 第38663 号2 を
明の名称 サンプリングガスの除塵方法およびその
装置3、補1丁:を°rる各
ITf’1.、ヒの関係 持、γl出願人(11
“n 大阪市西区江戸堀1丁目6番14、号氏名°名
称 (511)日立造船株式会社、11代 理 人
住 所 大阪市内1×鰻谷西之町57番地の6
rナベビル6階外4名
5 補iT′命令の日付 昭和 年 (1「]
6、 Mn11により増加する発明の数7 補IFの
χI VJ 明細書の発明の詳細な説明の欄。
補 正 の 内 容
(1)明細書4頁13行「ガスは、」を「ガスは、ガス
抜率70%以下の場合、」(こ¥rIEする。
(2) 同4頁16行〜5頁2行「気流〜ことがなく
、」を[この際、一部のダクトが再び上昇する気流に同
伴させるために、分離効率が悪い。一方、ガス抜率70
%以上の場合、流れが反転しなくなり、捕集されたダス
トが気流中に再飛散することがなくて、ダストは」に訂
正する。
以 上FIG. 1 is a flowchart of a conventional dust removal method, and FIG. 2 is a graph showing seven stages of the dust removal method according to an embodiment of the present invention. 01)... Flue, 02... Analyzer, 0J0, Sampling gas conduit, ti41, Fist, Cyclone type dust collector, u81... Conduit, @ Fist... Gas outlet. Patent applicant: Hitachi Zosen Co., Ltd., Showa 5F [May 21, 1933] It l'1. ), 1-Special Issue of 1981, i'liK・11 No. 38663 2 Name of Ming Sampling Gas Dust Removal Method and Apparatus 3, Supplement 1: Each ITf'1. , relationship between γl applicant (11
“n 1-6-14 Edobori, Nishi-ku, Osaka City, Name (511) Hitachi Zosen Co., Ltd., 11th Director Address: 6-57, 1 x Unagidani Nishinocho, Osaka City
4 people outside the 6th floor of Nabe Building 5 Date of supplementary iT' order Showa year (1")
6. Number of inventions increased by Mn11 7 Supplementary IF χI VJ Detailed description of the invention in the specification column. Contents of the amendment (1) Change ``Gas,'' on page 4, line 13 of the specification to ``if the degassing rate is 70% or less.'' (2) Page 4, lines 16 to 5 Page 2, line 2, "airflow ~ never happens" [In this case, some of the ducts are entrained in the rising airflow again, so the separation efficiency is poor.On the other hand, the gas removal rate is 70
% or more, the flow no longer reverses, the collected dust is not re-splattered into the airflow, and the dust is corrected to ``. that's all
Claims (2)
%以上の量のガスを抜出すことを特徴とするサンプリン
グガスの除塵方法。(1) 70 mm of gas flowing in from the bottom of the cyclone type dust collector
A sampling gas dust removal method characterized by extracting gas in an amount of % or more.
記載の方法。 下端に設けられた逆円錐齢す下端に設けられた集塵部と
からなるサイクロン型集塵装置において、下端にガス抜
目を設けたことを特徴とするサンプリングガスの除塵装
置。(2) The method according to claim 1, in which the extracted gas is returned to the flue. A cyclone type dust collector comprising an inverted conical stage provided at the lower end and a dust collection section provided at the lower end, the sampling gas dust removing device comprising a gas vent provided at the lower end.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3866382A JPS58156360A (en) | 1982-03-10 | 1982-03-10 | Removal of dust from sampled gas and apparatus therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3866382A JPS58156360A (en) | 1982-03-10 | 1982-03-10 | Removal of dust from sampled gas and apparatus therefor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58156360A true JPS58156360A (en) | 1983-09-17 |
Family
ID=12531502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3866382A Pending JPS58156360A (en) | 1982-03-10 | 1982-03-10 | Removal of dust from sampled gas and apparatus therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58156360A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030053883A (en) * | 2001-12-24 | 2003-07-02 | 한국남동발전 주식회사 | Methode and Apparatus for Gathering Fly Ash by Using a Cyclone for Unburned Carbon Analysis in a Power Plant |
JP2010502974A (en) * | 2006-09-04 | 2010-01-28 | ベルタン・テクノロジーズ | Device for collecting and separating particles and microorganisms present in ambient air |
-
1982
- 1982-03-10 JP JP3866382A patent/JPS58156360A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030053883A (en) * | 2001-12-24 | 2003-07-02 | 한국남동발전 주식회사 | Methode and Apparatus for Gathering Fly Ash by Using a Cyclone for Unburned Carbon Analysis in a Power Plant |
JP2010502974A (en) * | 2006-09-04 | 2010-01-28 | ベルタン・テクノロジーズ | Device for collecting and separating particles and microorganisms present in ambient air |
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