JPS60161761A - Cyclone - Google Patents

Cyclone

Info

Publication number
JPS60161761A
JPS60161761A JP1600184A JP1600184A JPS60161761A JP S60161761 A JPS60161761 A JP S60161761A JP 1600184 A JP1600184 A JP 1600184A JP 1600184 A JP1600184 A JP 1600184A JP S60161761 A JPS60161761 A JP S60161761A
Authority
JP
Japan
Prior art keywords
cyclone
dust collection
collection efficiency
introduction part
pressure loss
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
Application number
JP1600184A
Other languages
Japanese (ja)
Inventor
Norimoto Ino
井野 紀元
Kentaro Ogawa
健太郎 小川
Masanori Fukuda
福田 政伯
Yoshimasa Hayashi
林 良正
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.)
Nihon Cement Co Ltd
Original Assignee
Nihon Cement Co 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 Nihon Cement Co Ltd filed Critical Nihon Cement Co Ltd
Priority to JP1600184A priority Critical patent/JPS60161761A/en
Publication of JPS60161761A publication Critical patent/JPS60161761A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To attain to reduce pressure loss and to enhance dust collection efficiency, by forming the introduction part of a cyclone inlet duct into a cyclone into a curved shape. CONSTITUTION:The introduction part of a cyclone inlet duct into a cyclone is formed into a curved shape. In this introduction part, raw particles are flocculated by the action of centrifugal force and the stay time of particles in a centrifugal field becomes long and high dust collection efficiency is obtained. Therefore, the speed of inlet gas is suppressed low and pressure loss is reduced.

Description

【発明の詳細な説明】 本発明はサイクロン特にセメント焼成用サスはンション
プレヒータ付キルンにおいて使用されるサイクロンの改
良に係わるものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to improvements in cyclones, particularly cyclones used in cement firing kilns with suspension preheaters.

従来サスペンションプレヒータで使用されるサイクロン
は第1図〜纂4図に示すようなサイクロンが使用されて
いた。しかしこれら従来のサイクロンはサイクロンへの
導入部分が直線状であったため次のような欠点があった
Conventionally, cyclones such as those shown in Figs. 1 to 4 have been used in suspension preheaters. However, these conventional cyclones had the following drawbacks because the introduction portion into the cyclone was linear.

(1) サイクロンの圧力損失が100〜i 50 m
Aqと大である。
(1) Cyclone pressure loss is 100 to 50 m
Aq is large.

(2) サイクロンの集塵効率が60〜70%と低い。(2) The dust collection efficiency of the cyclone is low at 60-70%.

上記(1)の欠点を解消する方策として横型サイクロン
、縦型軸流サイクロンが提案採用されつつあるが、それ
ら新型サイクロン使用時のデータを見ると圧力損失は低
減しているものの集塵効率が従来型のサイクロンよシ低
く熱量原単位t−慾化せしめておシ、必ずしも満足でき
るものではない。例えば4段サイクロン付プレヒータを
横型サイクロン2基を付属する5段プレヒータに改造し
たセメント焼成プロセスの熱量原単位が普通の4段サイ
クロンプレヒータ付ロータリーキルンの熱量原単位より
高いというデータも多々ある。これは横型サイクロンの
集塵効率が悪いために起る現象であり、サイクロン集塵
効率に対する配慮が不足していたことを示している。
Horizontal cyclones and vertical axial flow cyclones are being proposed and adopted as a measure to eliminate the drawback of (1) above, but looking at the data when using these new cyclones, the dust collection efficiency is lower than that of the conventional cyclones although the pressure loss is reduced. Although it has a lower heat consumption unit than that of a conventional cyclone, it is not necessarily satisfactory. For example, there is a lot of data showing that the heat unit of a cement firing process in which a four-stage cyclone preheater is modified to a five-stage preheater with two horizontal cyclones attached is higher than that of a normal rotary kiln with a four-stage cyclone preheater. This phenomenon is caused by the poor dust collection efficiency of the horizontal cyclone, and shows that consideration was not given to the cyclone dust collection efficiency.

本発明は圧力損失が低くかつ集塵効率の高いサイクロン
ヲ提供しようとするものである。即ち本発明の要旨は、
サイクロン入口ダクトのサインロンへの導入部分を曲線
状に形成したことを特徴とするサイクロンにある。
The present invention aims to provide a cyclone with low pressure loss and high dust collection efficiency. That is, the gist of the present invention is
The cyclone is characterized in that the introduction portion of the cyclone inlet duct into the Signron is formed in a curved shape.

以下図面に基き本発明を説明する。The present invention will be explained below based on the drawings.

第1図は従来型サイクロンの1例で、接線流入型サイク
ロンの平面概念図を示す。第2図は第1図に示すサイク
ロンの縦断面図を示す。図中1はサイクロン円筒部、2
はサイクロン円筒、6はサイクロン導入部分、4はコー
ン部、5は下段サイクロンからの立上シダクトを示す。
FIG. 1 is an example of a conventional cyclone, and shows a conceptual plan view of a tangential flow type cyclone. FIG. 2 shows a longitudinal sectional view of the cyclone shown in FIG. 1. In the figure, 1 is the cyclone cylinder part, 2
6 shows the cyclone cylinder, 6 shows the cyclone introduction part, 4 shows the cone part, and 5 shows the rising side duct from the lower cyclone.

第6図は従来型サイクロンの他の1例で、サイクロン導
入部分を第1図のものに比べやや外側に出した通常リン
デン型サイクロンと呼ばれ。
Figure 6 shows another example of a conventional cyclone, which is usually called a Linden-type cyclone, with the cyclone introduction part placed slightly outside compared to the one in Figure 1.

るものである。第4図は第3図のA−A矢視図である。It is something that FIG. 4 is a view taken along the line A--A in FIG. 3.

なお図中番号は第1図と同じである。Note that the numbers in the figure are the same as in FIG. 1.

第1図、第6図に示すサイクロンでは導入部分6が直線
状であるため、ガスはほぼ直進流でサイクロンに流入、
壁に沿って旋回し、原料粒子はその旋回による遠心力で
ガスから分離されるが、粒子の遠心場における滞留時間
が短いため集塵効率は60〜70%と低く、そのため集
塵効率を高めるためにはサイクロン入口ガス速度“k 
20〜25 rn/’sec (通常)から30 m/
secへと高くせざるを得なかった、そのため必然的此
サイクロンの圧力損失は増大していた。
In the cyclones shown in Figs. 1 and 6, the introduction section 6 is linear, so the gas flows into the cyclone in an almost straight flow.
It rotates along the wall, and the raw material particles are separated from the gas by the centrifugal force caused by the rotation. However, because the residence time of the particles in the centrifugal field is short, the dust collection efficiency is low at 60 to 70%, so the dust collection efficiency is improved. For this, the cyclone inlet gas velocity “k
20-25 rn/'sec (normal) to 30 m/
sec, which inevitably increased the pressure loss of this cyclone.

第5図、第6図は本発明の実施例を示すもので、サイク
ロンへの導入部分3が曲線状となっているので、この部
分においても遠心力の作用により原料粒子が凝集し、か
つ遠心場における粒子の滞留時間が大となシ、高い集塵
効率が得られる。さらに集塵効率が高いため、サイクロ
ンの入口ガス速度を従来の20〜30m/secから1
5m/sec程度にでき圧力損失が小さい。
Figures 5 and 6 show examples of the present invention, in which the introduction section 3 into the cyclone is curved, so that the raw material particles are agglomerated due to the action of centrifugal force in this section as well. Since the residence time of particles in the field is long, high dust collection efficiency can be obtained. Furthermore, because the dust collection efficiency is high, the inlet gas velocity of the cyclone has been reduced from the conventional 20 to 30 m/sec to 1.
The pressure loss can be reduced to about 5 m/sec.

このようにサイクロン入口ガス速度が低くとも従来型サ
イクロンに比べはるかに高い集塵効率を達成できる。
In this way, even with a low cyclone inlet gas velocity, much higher dust collection efficiency can be achieved than with conventional cyclones.

なお、この発明でサイクロン導入部分とはサイクロンの
開口部よシ手前のダクト部分をいう。
In this invention, the cyclone introduction section refers to the duct section in front of the cyclone opening.

さらに該導入部分は多角形を連接して曲線状としてもよ
い。
Further, the introduction portion may be curved by connecting polygons.

実施例 150 t/h SPキルンに第6図に示す本発明のサ
イクロンを適用した例及び第3図に示す従来型サイクロ
ン及び第6図に示す従来型サイクロン°の入口部を拡大
したサイクロンを使用して実験を行った例を表1に示す
Example 150 An example in which the cyclone of the present invention shown in Fig. 6 was applied to a t/h SP kiln, and a conventional cyclone shown in Fig. 3 and a cyclone with an enlarged inlet of the conventional cyclone shown in Fig. 6 were used. Table 1 shows an example of an experiment conducted using the following methods.

表 1 表1に示す結果から従来型サイクロンでは高集塵効率と
低圧力損失の両方を同時に満足することはできなかった
が、本発明のサイクロンではこれら両方を同時に満足で
きたことがわかる。
Table 1 From the results shown in Table 1, it can be seen that the conventional cyclone was unable to simultaneously satisfy both high dust collection efficiency and low pressure loss, but the cyclone of the present invention was able to satisfy both of these at the same time.

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

第1図、第6図は従来型のサイクロン、第2図は第1図
のM断面図、第4図は第3図のA−A矢視図、第5図、
第6図は本発明のサイクロンの実施例である。 1・・・サイクロン円筒部 2・・・サイクロン内筒5
・・・サイクロン導入部分 4・・・サイクロンコーン部 5・・・下段サイクロンからの立上りダクト特許出願人
 日本セメント株式会社 代理人 弁理士伊 東 彰 手続補正書 昭和59年λ月上3日 特許庁長官若杉和夫 殿 1、事件の狭示 昭和59年特許訴願16oot号 2、発明の名称 サイクロン 3、補正をする者 事件の表示 特許出願人 住所 東京都千代田区大手町1丁目6番1号名称 日本
セメント株式会社 代表者 北 岡 徹 4、代理人 〒101 住 所 東京都千代田区神田神保町2丁目42番地5、
補正の対象 願書及び明細書(タイプ浄書) 6、補正の内容 別紙のとお9
Figures 1 and 6 are conventional cyclones, Figure 2 is a cross-sectional view of M in Figure 1, Figure 4 is a view along arrow A-A in Figure 3, Figure 5,
FIG. 6 shows an embodiment of the cyclone of the present invention. 1...Cyclone cylinder part 2...Cyclone inner cylinder 5
... Cyclone introduction section 4 ... Cyclone cone section 5 ... Rise duct from lower cyclone Patent applicant: Nippon Cement Co., Ltd. Agent Patent attorney Akira Ito Procedural amendment dated 3rd January, 1980, Patent Office Chief Justice Kazuo Wakasugi 1, Narrow indication of the case 1982 patent application 16oot No. 2, name of the invention Cyclone 3, person making the amendment Indication of the case Patent applicant address 1-6-1 Otemachi, Chiyoda-ku, Tokyo Name Japan Cement Co., Ltd. Representative Toru Kitaoka 4, Agent 101 Address 2-42-5 Kanda Jimbocho, Chiyoda-ku, Tokyo
Application and specification to be amended (typed copy) 6. Contents of amendment Attachment 9

Claims (1)

【特許請求の範囲】[Claims] サイクロン入口ダクトのサイクロンへの導入部分を曲線
状に形成したことを特徴とするサイクロン
A cyclone characterized in that the introduction part of the cyclone inlet duct into the cyclone is formed in a curved shape.
JP1600184A 1984-02-02 1984-02-02 Cyclone Pending JPS60161761A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1600184A JPS60161761A (en) 1984-02-02 1984-02-02 Cyclone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1600184A JPS60161761A (en) 1984-02-02 1984-02-02 Cyclone

Publications (1)

Publication Number Publication Date
JPS60161761A true JPS60161761A (en) 1985-08-23

Family

ID=11904385

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1600184A Pending JPS60161761A (en) 1984-02-02 1984-02-02 Cyclone

Country Status (1)

Country Link
JP (1) JPS60161761A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS547987A (en) * 1977-06-20 1979-01-20 Hitachi Ltd Method and system for inspecting reactor
JPS5821549U (en) * 1981-08-04 1983-02-09 岸本産業株式会社 Sealing medical drug containers
JPS5823659B2 (en) * 1975-04-23 1983-05-17 ソニー株式会社 Kaiten Hetsudonosokudo Seigiyo Cairo

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5823659B2 (en) * 1975-04-23 1983-05-17 ソニー株式会社 Kaiten Hetsudonosokudo Seigiyo Cairo
JPS547987A (en) * 1977-06-20 1979-01-20 Hitachi Ltd Method and system for inspecting reactor
JPS5821549U (en) * 1981-08-04 1983-02-09 岸本産業株式会社 Sealing medical drug containers

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