JPH0729068B2 - Pre-milling mill exhaust gas condensation prevention device - Google Patents

Pre-milling mill exhaust gas condensation prevention device

Info

Publication number
JPH0729068B2
JPH0729068B2 JP63192235A JP19223588A JPH0729068B2 JP H0729068 B2 JPH0729068 B2 JP H0729068B2 JP 63192235 A JP63192235 A JP 63192235A JP 19223588 A JP19223588 A JP 19223588A JP H0729068 B2 JPH0729068 B2 JP H0729068B2
Authority
JP
Japan
Prior art keywords
exhaust gas
mill
preliminary
crushing mill
flow path
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 - Lifetime
Application number
JP63192235A
Other languages
Japanese (ja)
Other versions
JPH0240245A (en
Inventor
哲 富永
新悟 向井
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP63192235A priority Critical patent/JPH0729068B2/en
Publication of JPH0240245A publication Critical patent/JPH0240245A/en
Publication of JPH0729068B2 publication Critical patent/JPH0729068B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明はセメント等の混合原料を予備粉砕ミル及び二次
粉砕ミルにより二段粉砕する設備における予備粉砕ミル
排ガスの結露防止装置に関するものである。
TECHNICAL FIELD The present invention relates to an apparatus for preventing dew condensation of exhaust gas from a preliminary crushing mill in a facility for crushing a mixed raw material such as cement by a preliminary crushing mill and a secondary crushing mill in two stages. .

[従来の技術] 例えば、セメント等の粉砕混合製品を製造する場合、焼
成した絶乾状のクリンカと水分を10〜20%含む石膏及び
石灰石をミルにより混合し、粉砕している。
[Prior Art] For example, in the case of producing a crushed and mixed product such as cement, a baked clinker is mixed with gypsum and limestone containing 10 to 20% of water by a mill and crushed.

又、ミルからの排ガスは公害防止のため、フィルタによ
り除塵している。
In addition, the exhaust gas from the mill is removed by a filter to prevent pollution.

[発明が解決しようとする課題] しかし、排ガス中の粉塵はセメントと略同一の組成であ
り、しかも水蒸気も含まれているため、排ガスの温度が
水蒸気の露点以下まで低下すると結露し、結露した水が
フィルタに捕捉されたセメントと略同一組成の粉塵と接
触し、該粉塵が硬化してフィルタの機能が急速に損なわ
れてしまう。
[Problems to be Solved by the Invention] However, since the dust in the exhaust gas has substantially the same composition as the cement and also contains water vapor, dew condensation occurs when the temperature of the exhaust gas falls below the dew point of the water vapor, causing dew condensation. The water comes into contact with the dust having substantially the same composition as the cement captured in the filter, and the dust is hardened to rapidly impair the function of the filter.

又、セメントと同一組成の粉塵でなくとも、フィルタが
凝縮した水によりベタベタになり集塵機能が低下する。
Further, even if the dust is not the same composition as the cement, the water condensed by the filter becomes sticky and the dust collecting function deteriorates.

これを防止するためには、前記排ガスの温度を水蒸気の
露点以上になるよう昇温しなければならず、外部から多
大な熱エネルギを投入する必要があった。
In order to prevent this, it is necessary to raise the temperature of the exhaust gas to be equal to or higher than the dew point of water vapor, and it is necessary to input a large amount of heat energy from the outside.

本発明は斯かる実情に鑑みてなしたもので、セメント等
の混合原料を予備粉砕ミル及び二次粉砕ミルにより二段
粉砕する設備において、外部から多大な熱エネルギを投
入することなく予備粉砕ミル排ガスを露点温度以上に保
持することを目的としている。
The present invention has been made in view of such a situation, in a facility for pulverizing a mixed raw material such as cement in two stages by a preliminary pulverizing mill and a secondary pulverizing mill, the preliminary pulverizing mill without inputting a large amount of heat energy from the outside. The purpose is to keep the exhaust gas above the dew point temperature.

[課題を解決するための手段] 本発明は、二次粉砕ミル排ガス流路を予備粉砕ミルに接
続し、該二次粉砕ミル排ガス流路から分岐した分岐流路
を開度調整可能なダンパを介して予備粉砕ミル排ガス流
路に接続したことを特徴とする予備粉砕ミル排ガスの結
露防止装置、にかかるものである。
[Means for Solving the Problem] The present invention provides a damper in which a secondary crushing mill exhaust gas flow path is connected to a preliminary crushing mill, and a branch flow path branched from the secondary crushing mill exhaust gas flow path can be adjusted in opening degree. The present invention relates to a device for preventing dew condensation of exhaust gas from a preliminary crushing mill, which is connected to an exhaust gas flow path from the preliminary crushing mill.

[作用] 従って本発明では、二次粉砕ミルで自然発生した熱エネ
ルギにより高温となった二次粉砕ミル排ガスを予備粉砕
ミルに導入することにより、該予備粉砕ミルから予備粉
砕ミル排ガス流路にかけて予備粉砕ミル排ガスを露点温
度以上に昇温して該予備粉砕ミル排ガスの結露を防止す
ることが可能となる。
[Operation] Therefore, in the present invention, by introducing the secondary pulverizing mill exhaust gas, which has been heated to a high temperature by the heat energy naturally generated in the secondary pulverizing mill, into the preliminary pulverizing mill, the preliminary pulverizing mill is connected to the preliminary pulverizing mill exhaust gas passage. Condensation of the exhaust gas of the preliminary crushing mill can be prevented by raising the exhaust gas of the preliminary crushing mill to a temperature above the dew point temperature.

このとき、分岐流路のダンパを開度調整することにより
二次粉砕ミル排ガスの一部を分岐して、予備粉砕ミルに
導く二次粉砕ミル排ガスの流量を必要最小限に抑える
と、予備粉砕ミルを経由させることにより生じる圧力損
失を抑えることが可能となり、依って、排ガス系全体の
圧力損失を必要最小限に抑制することが可能となる。一
方、予備粉砕ミル排ガス流路側では、その中途部で分岐
流路からの比較的温度の高い二次粉砕ミル排ガスを導入
されることにより、除塵を行う直前で再度予備粉砕ミル
排ガスが昇温されることになり、結露による除塵器の機
能低下が一層確実に防止される。
At this time, by adjusting the opening of the damper of the branch flow path, a part of the exhaust gas of the secondary pulverizing mill is branched and the flow rate of the exhaust gas of the secondary pulverizing mill leading to the preliminary pulverizing mill is suppressed to the necessary minimum. It is possible to suppress the pressure loss caused by passing through the mill, and thus it is possible to suppress the pressure loss of the entire exhaust gas system to the necessary minimum. On the other hand, on the side of the preliminary crushing mill exhaust gas flow path, the secondary crushing mill exhaust gas with a relatively high temperature from the branch flow path is introduced in the middle thereof, so that the temperature of the preliminary crushing mill exhaust gas is raised again immediately before dust removal. As a result, the function of the dust remover is prevented from deteriorating due to dew condensation.

[実施例] 以下、本発明の実施例を図面を参照しつつ説明する。Embodiments Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の一実施例であり、予備粉砕ミル1の原
料投入口2の上方に原料供給用のコンベア3を設け、該
予備粉砕ミル1で粉砕した原料を二次粉砕ミル4に送っ
て更に微細に粉砕するようにする。該二次粉砕ミル4の
排ガス流路5を前記原料投入口2を介して予備粉砕ミル
1に接続し、該二次粉砕ミル排ガス流路5を分岐し、該
分岐流路6を前記予備粉砕ミル1の排ガス流路7に接続
し、該分岐流路6にダンパ8を設けて開度調整可能とす
る。図中、9は除塵器、10はファンを示す。
FIG. 1 shows an embodiment of the present invention, in which a raw material supply conveyor 3 is provided above a raw material input port 2 of a preliminary crushing mill 1 and a raw material crushed by the preliminary crushing mill 1 is fed to a secondary crushing mill 4. Send it for further fine crushing. The exhaust gas flow path 5 of the secondary crushing mill 4 is connected to the preliminary crushing mill 1 through the raw material charging port 2, the secondary crushing mill exhaust gas flow path 5 is branched, and the branched flow path 6 is subjected to the preliminary crushing. It is connected to the exhaust gas passage 7 of the mill 1 and a damper 8 is provided in the branch passage 6 so that the opening degree can be adjusted. In the figure, 9 indicates a dust remover and 10 indicates a fan.

以上のように構成したので、例えば水分を約1%含む供
給鉱石を原料投入口2から毎時150トンの流量で予備粉
砕ミル1に供給して該予備粉砕ミル1により粉砕する
と、該予備粉砕ミル1内の蒸発水は、 となる。
With the above-described structure, for example, a supply ore containing about 1% of water is supplied from the raw material inlet 2 to the preliminary crushing mill 1 at a flow rate of 150 tons per hour and crushed by the preliminary crushing mill 1. Evaporated water in 1 is Becomes

予備粉砕ミル1により粉砕された供給鉱石は二次粉砕ミ
ル4に送られて、更に粉砕される。該二次粉砕ミル4に
おいては駆動エネルギ及び機械的摩擦力が熱エネルギに
変換されて昇温するので、二次粉砕ミル4から排出され
る排ガスは約100℃に達し、毎分1000m3排出される。な
お該二次粉砕ミル排ガス中の蒸発水は、予備粉砕ミル1
の搬送空気と略同量の水分を含む。
The supplied ore crushed by the preliminary crushing mill 1 is sent to the secondary crushing mill 4 and further crushed. In the secondary crushing mill 4, the driving energy and the mechanical frictional force are converted into heat energy to raise the temperature, so that the exhaust gas discharged from the secondary crushing mill 4 reaches about 100 ° C. and is discharged at 1000 m 3 / min. It The evaporated water in the exhaust gas of the secondary crushing mill is the same as the preliminary crushing mill 1.
It contains almost the same amount of water as the carrier air.

従って、ダンパ8により、二次粉砕ミル排ガスの70%を
予備粉砕ミル排ガス流路7に流し、30%を予備粉砕ミル
1に導入すると、予備粉砕ミル1に導入される二次粉砕
ミル排ガス中の蒸発水分は、 となる。
Therefore, when the damper 8 causes 70% of the exhaust gas of the secondary crushing mill to flow into the exhaust gas passage 7 of the preliminary crushing mill and 30% of the exhaust gas is introduced into the preliminary crushing mill 1, the exhaust gas of the secondary crushing mill is introduced into the preliminary crushing mill 1. The evaporated water of Becomes

予備粉砕ミル排ガスは約100℃、300m3/minとなり、蒸発
水は前記供給鉱石からの蒸発水と導入される二次粉砕ミ
ル排ガス中の蒸発水の合計量すなわち40m3/minとなり、
露点温度は約60℃となる。
The exhaust gas of the preliminary crushing mill is about 100 ° C. and 300 m 3 / min, the evaporated water is the total amount of evaporated water in the exhaust gas of the secondary crushing mill introduced with the evaporated water from the supply ore, that is, 40 m 3 / min,
The dew point temperature is about 60 ℃.

これにより、予備粉砕ミル1から予備粉砕ミル排ガス流
路7にかけて予備粉砕ミル排ガスが露点温度以上に昇温
されて結露することなく除塵器9へと送られ、更に分岐
流路6から予備粉砕ミル排ガス流路7に導入される約10
0℃、700m3/minの二次粉砕ミル排ガスと共に除塵器9で
除塵される。
As a result, the exhaust gas of the preliminary grinding mill from the preliminary grinding mill 1 to the exhaust gas passage 7 of the preliminary grinding mill is heated to the dew point temperature or higher and is sent to the dust remover 9 without dew condensation. About 10 introduced into the exhaust gas flow path 7
The dust is removed by the dust remover 9 together with the exhaust gas of the secondary grinding mill at 0 ° C. and 700 m 3 / min.

このとき、分岐流路6のダンパ8を開度調整することに
より二次粉砕ミル排ガスの一部を分岐して、予備粉砕ミ
ル1に導く二次粉砕ミル排ガスの流量を必要最小限に抑
えると、予備粉砕ミル1を経由させることにより生じる
圧力損失を抑えることが可能となり、依って、排ガス系
全体の圧力損失を必要最小限に抑制することが可能とな
る。
At this time, by adjusting the opening degree of the damper 8 of the branch flow path 6, a part of the secondary crushing mill exhaust gas is branched and the flow rate of the secondary crushing mill exhaust gas guided to the preliminary crushing mill 1 can be minimized. The pressure loss caused by passing through the preliminary crushing mill 1 can be suppressed, and thus the pressure loss of the entire exhaust gas system can be suppressed to the necessary minimum.

一方、予備粉砕ミル排ガス流路7側では、その中途部で
分岐流路6からの比較的温度の高い二次粉砕ミル排ガス
を導入されることにより、除塵を行う直前で再度予備粉
砕ミル排ガスが昇温されることになり、結露による除塵
器の機能低下が一層確実に防止される。
On the other hand, on the side of the preliminary crushing mill exhaust gas flow path 7, the secondary crushing mill exhaust gas having a relatively high temperature is introduced from the branch flow path 6 at a midway portion thereof, so that the preliminary crushing mill exhaust gas is again discharged immediately before dust removal. Since the temperature is raised, the functional deterioration of the dust remover due to dew condensation can be prevented more reliably.

尚、本発明の予備粉砕ミル排ガスの結露防止装置は、上
述の実施例にのみ限定されるものではなく、本発明の要
旨を逸脱しない範囲内において種々変更を加え得ること
は勿論である。
The dew condensation prevention device for the exhaust gas of the preliminary crushing mill of the present invention is not limited to the above-mentioned embodiment, and it goes without saying that various modifications can be made without departing from the scope of the present invention.

[発明の効果] 以上説明したように、本発明の予備粉砕ミル排ガスの結
露防止装置によれば、下記の如き種々の優れた効果を奏
し得る。
[Effects of the Invention] As described above, according to the dew condensation prevention device for the exhaust gas of the preliminary crushing mill of the present invention, various excellent effects as described below can be obtained.

(I)二次粉砕ミル排ガス流路を予備粉砕ミルに接続し
たことにより、二次粉砕ミルで自然発生した熱エネルギ
により高温となった二次粉砕ミル排ガスを予備粉砕ミル
に導入することができ、これによって、予備粉砕ミルか
ら予備粉砕ミル排ガス流路にかけて予備粉砕ミル排ガス
を結露温度以上に昇温して該予備粉砕ミル排ガスの結露
を防止することができ、結露防止用として外部から新た
に熱エネルギを投入する必要をなくすか或いは著しく僅
かとすることができてトータル的な省エネルギ化を図る
ことができる。
(I) By connecting the exhaust gas passage of the secondary pulverizing mill to the preliminary pulverizing mill, the exhaust gas of the secondary pulverizing mill having a high temperature due to the heat energy naturally generated in the secondary pulverizing mill can be introduced into the preliminary pulverizing mill. As a result, it is possible to prevent the dew condensation of the exhaust gas of the preliminary crushing mill by increasing the temperature of the exhaust gas of the preliminary crushing mill from the preliminary crushing mill to the exhaust gas flow path of the preliminary crushing mill and to prevent the condensation of the exhaust gas of the preliminary crushing mill from outside. It is possible to eliminate or remarkably reduce the need to input heat energy, thereby achieving total energy saving.

(II)二次粉砕ミル排ガス流路から分岐した分岐流路を
開度調整可能なダンパを介して予備粉砕ミル排ガス流路
に接続したことにより、前記分岐流路のダンパを開度調
整して予備粉砕ミルに導く二次粉砕ミル排ガスの流量を
必要最小限に抑えることができるので、予備粉砕ミルを
経由させることにより生じる圧力損失を抑えることがで
き、依って、排ガス系全体の圧力損失を必要最小限に抑
制することができる。
(II) The opening of the damper of the branch passage is adjusted by connecting the branch passage branched from the exhaust passage of the secondary grinding mill to the exhaust passage of the preliminary grinding mill through a damper capable of adjusting the opening. Since the flow rate of the exhaust gas of the secondary crushing mill leading to the preliminary crushing mill can be suppressed to the necessary minimum, the pressure loss caused by passing through the preliminary crushing mill can be suppressed, and therefore the pressure loss of the entire exhaust gas system can be reduced. It can be suppressed to the necessary minimum.

(III)予備粉砕ミル排ガス流路の下流側にある除塵器
の直前で分岐流路からの比較的温度の高い二次粉砕ミル
排ガスを導入させるようにすれば、除塵を行う直前で再
度予備粉砕ミル排ガスを昇温することができ、結露によ
る除塵器の機能低下を一層確実に防止することができ、
安定した操業を行うことができる。
(III) Preliminary crushing mill If the exhaust gas of the secondary crushing mill having a relatively high temperature from the branch flow path is introduced just before the dust remover on the downstream side of the exhaust gas flow path, the preliminary crushing will be performed again immediately before dust removal. The temperature of the mill exhaust gas can be raised, and the deterioration of the dust remover function due to dew condensation can be prevented more reliably.
A stable operation can be performed.

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

第1図は本発明の装置の一実施例の説明図である。 1は予備粉砕ミル、4は二次粉砕ミル、5は二次粉砕ミ
ル排ガス流路、6は分岐流路、7は予備粉砕ミル排ガス
流路、8はダンパ、9は除塵器を示す。
FIG. 1 is an illustration of an embodiment of the apparatus of the present invention. Reference numeral 1 is a preliminary pulverizing mill, 4 is a secondary pulverizing mill, 5 is a secondary pulverizing mill exhaust gas passage, 6 is a branch passage, 7 is a preliminary pulverizing mill exhaust gas passage, 8 is a damper, and 9 is a dust remover.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】二次粉砕ミル排ガス流路を予備粉砕ミルに
接続し、該二次粉砕ミル排ガス流路から分岐した分岐流
路を開度調整可能なダンパを介して予備粉砕ミル排ガス
流路に接続したことを特徴とする予備粉砕ミル排ガスの
結露防止装置。
1. A secondary crushing mill exhaust gas flow path is connected to a secondary crushing mill exhaust gas flow path, and a branching flow path branched from the secondary crushing mill exhaust gas flow path is connected to a preliminary crushing mill exhaust gas flow path through a damper whose opening can be adjusted. Condensation prevention device for exhaust gas from the preliminary crushing mill, which is connected to the.
JP63192235A 1988-08-01 1988-08-01 Pre-milling mill exhaust gas condensation prevention device Expired - Lifetime JPH0729068B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63192235A JPH0729068B2 (en) 1988-08-01 1988-08-01 Pre-milling mill exhaust gas condensation prevention device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63192235A JPH0729068B2 (en) 1988-08-01 1988-08-01 Pre-milling mill exhaust gas condensation prevention device

Publications (2)

Publication Number Publication Date
JPH0240245A JPH0240245A (en) 1990-02-09
JPH0729068B2 true JPH0729068B2 (en) 1995-04-05

Family

ID=16287900

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63192235A Expired - Lifetime JPH0729068B2 (en) 1988-08-01 1988-08-01 Pre-milling mill exhaust gas condensation prevention device

Country Status (1)

Country Link
JP (1) JPH0729068B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4035730C2 (en) * 1990-11-09 1993-10-14 Loesche Gmbh Process and device for the treatment of moist gas-dust mixtures
JP2000281419A (en) * 1999-03-29 2000-10-10 Sumitomo Osaka Cement Co Ltd Production of mixed cement
CN104003635B (en) * 2013-02-21 2016-11-16 高县天顺建材有限责任公司 Waste heat grinding process and equipment
CN108855941B (en) * 2018-07-26 2024-05-31 郑州沃特节能科技股份有限公司 Steel slag micro powder selecting system utilizing waste heat flue gas of steel plant

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5156703A (en) * 1974-11-14 1976-05-18 Kawasaki Heavy Ind Ltd KOSEKIRUINOHASAIKANSOHOHO OYOBI SOCHI
JPS59131695A (en) * 1983-01-19 1984-07-28 Mitsubishi Heavy Ind Ltd Production of inert gas for mill
JPS6320047A (en) * 1986-07-10 1988-01-27 石川島播磨重工業株式会社 Method and device for crushing raw material lump

Also Published As

Publication number Publication date
JPH0240245A (en) 1990-02-09

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