JP2620771B2 - Pulverizer with oxygen concentration controller - Google Patents

Pulverizer with oxygen concentration controller

Info

Publication number
JP2620771B2
JP2620771B2 JP6092993A JP6092993A JP2620771B2 JP 2620771 B2 JP2620771 B2 JP 2620771B2 JP 6092993 A JP6092993 A JP 6092993A JP 6092993 A JP6092993 A JP 6092993A JP 2620771 B2 JP2620771 B2 JP 2620771B2
Authority
JP
Japan
Prior art keywords
pressure
oxygen concentration
pulverizing
inert gas
oxygen
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
JP6092993A
Other languages
Japanese (ja)
Other versions
JPH06246182A (en
Inventor
政昭 三鴨
正 片畑
弘憲 尾崎
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.)
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo KK
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 Kawasaki Jukogyo KK filed Critical Kawasaki Jukogyo KK
Priority to JP6092993A priority Critical patent/JP2620771B2/en
Publication of JPH06246182A publication Critical patent/JPH06246182A/en
Application granted granted Critical
Publication of JP2620771B2 publication Critical patent/JP2620771B2/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】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、反応性の高い金属系材
料等を低酸素雰囲気にて微粉砕するための酸素濃度制御
装置を備えた微粉砕装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pulverizer having an oxygen concentration controller for pulverizing highly reactive metal materials in a low oxygen atmosphere.

【0002】[0002]

【従来の技術】反応性を有する材料、例えば石炭を安全
に微粉砕するために、一酸化炭素または酸素濃度の制御
装置もしくは警報器を備えた微粉砕装置が用いられてい
る。例えば、空気雰囲気での石炭の微粉砕にあたり、雰
囲気の酸素濃度が設定値、例えば15%以上となり、ま
た一酸化炭素濃度が設定値、例えば200ppm 以上とな
ると蒸気,CO2 等の不活性ガスの流量制御を行って、
雰囲気の活性を低減させることにより、微粉砕装置が火
災や爆発を発生させることを防止している(特公平1−
28613号)。
2. Description of the Prior Art In order to safely pulverize a reactive material, for example, coal, a pulverizer equipped with a control device or an alarm for the concentration of carbon monoxide or oxygen is used. For example, when finely pulverizing coal in an air atmosphere, when the oxygen concentration of the atmosphere becomes a set value, for example, 15% or more, and the carbon monoxide concentration becomes a set value, for example, 200 ppm or more, the inert gas such as steam and CO 2 becomes Perform flow control,
By reducing the activity of the atmosphere, the pulverizer is prevented from generating fire or explosion.
No. 28613).

【0003】また、金属系材料の微粉砕にあたり、好ま
しくない過大な表面酸化を回避するために、低酸素雰囲
気にて微粉砕するようにされている。
[0003] In the case of finely pulverizing a metal-based material, in order to avoid undesirably excessive surface oxidation, the pulverization is performed in a low oxygen atmosphere.

【0004】[0004]

【発明が解決しようとする課題】ところが、空気雰囲気
での材料の微粉砕にあたり、雰囲気の活性を低減させて
微粉砕する方式では、石炭等の反応性を有する材料を微
粉砕するには有効であるものの、不活性ガスとしても酸
素原子からなるガスを用いていることもあって反応性の
高い金属系材料を微粉砕するためには、充分な低酸素雰
囲気が形成できないので、砕製品の過大な表面酸化を発
生させ、所望の性状を発揮できなくなる虞れがある。
However, in the method of pulverizing a material in an air atmosphere, the method of pulverizing the material while reducing the activity of the atmosphere is not effective for pulverizing a reactive material such as coal. However, the use of a gas consisting of oxygen atoms as an inert gas also makes it impossible to form a sufficiently low oxygen atmosphere in order to pulverize highly reactive metal-based materials. There is a possibility that the desired properties may not be exhibited due to excessive surface oxidation.

【0005】本発明は、上述した従来技術の問題点を解
決するためになされたものであり、反応性の高い金属系
材料等を低酸素雰囲気にて微粉砕するために、不活性ガ
スとして希ガス、例えばアルゴン等を用いた不活性ガス
雰囲気にて微粉砕し、しかも微粉砕系統内酸素濃度を材
料の表面酸化を抑制するように制御した酸素濃度制御装
置を備えた微粉砕装置を提供することを目的とする。
The present invention has been made in order to solve the above-mentioned problems of the prior art. In order to finely pulverize highly reactive metal materials in a low oxygen atmosphere, rare gases are used as inert gases. Provided is a fine pulverizing apparatus provided with an oxygen concentration control device that pulverizes in an inert gas atmosphere using a gas, for example, argon, and controls the oxygen concentration in the pulverizing system so as to suppress surface oxidation of the material. The purpose is to:

【0006】[0006]

【課題を解決するための手段】かかる目的を達成するた
めに、本発明では、微粉砕系統を通して不活性ガス雰囲
気にて材料を微粉砕させるための微粉砕装置と、微粉砕
装置入口側に接続された不活性ガス導入路に設けられた
不活性ガス流量制御弁と、微粉砕装置に後置され系統内
ガスを流動させるための送風機と、送風機入口側に設け
られた圧力制御弁と、を備えてなる微粉砕装置におい
て、前記微粉砕装置上流の系統内ガスの酸素濃度を検出
する酸素濃度検出器と、酸素濃度検出器の検出酸素濃度
を設定濃度と比較しその偏差により前記酸素濃度が規定
濃度となるように前記不活性ガス流量制御弁を制御する
酸素制御器と、前記送風機入口の系統内ガスの圧力を検
出する圧力検出器と、圧力検出器の検出圧力を設定圧力
と比較しその偏差により前記圧力が規定圧力となるよう
に前記圧力制御弁を制御する圧力制御器と、を具備して
なることを特徴とするものである。
In order to achieve the above object, according to the present invention, a pulverizing apparatus for pulverizing a material in an inert gas atmosphere through a pulverizing system is connected to an inlet side of the pulverizing apparatus. An inert gas flow control valve provided in the inert gas introduction path, a blower that is provided after the pulverizing device to flow gas in the system, and a pressure control valve provided on the blower inlet side, In the provided fine pulverizing device, an oxygen concentration detector that detects the oxygen concentration of the gas in the system upstream of the fine pulverizing device, and the detected oxygen concentration of the oxygen concentration detector is compared with a set concentration, and the difference between the oxygen concentration and the oxygen concentration is determined by the deviation. An oxygen controller that controls the inert gas flow control valve so as to have a specified concentration, a pressure detector that detects the pressure of the gas in the system at the inlet of the blower, and a pressure detected by the pressure detector is compared with a set pressure. To that deviation A pressure controller for controlling the pressure control valve so that the pressure becomes the specified pressure Ri and is characterized by comprising comprises a.

【0007】[0007]

【作用】このようにすれば、外気が系統内に浸入される
ことが抑制されるとともに系統内酸素濃度を希ガスを用
いた不活性ガスの導入により材料の表面酸化を抑制する
ように自動的に制御し、反応性の高い金属系材料等の性
状を低下させることなく効率よく微粉砕させることがで
きる。
In this way, outside air is prevented from entering the system, and the oxygen concentration in the system is automatically controlled so as to suppress surface oxidation of the material by introducing an inert gas using a rare gas. , And can be pulverized efficiently without deteriorating the properties of highly reactive metal-based materials and the like.

【0008】[0008]

【実施例】以下、図面を参照にして本発明の実施例につ
いて説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0009】図1は、本発明の一実施例を示す酸素濃度
制御装置を備えた微粉砕装置の全体構成図である。
FIG. 1 is an overall configuration diagram of a pulverizing apparatus having an oxygen concentration control apparatus according to an embodiment of the present invention.

【0010】図1において、閉回路運転を行う微粉砕装
置の例を示し、10は酸素制御装置であり、圧力制御装
置を含めて示している。12は微粉砕装置であり、材料
供給機14から供給される材料は微粉砕系統30内に分
散導入され、微粉砕装置12内にて微粉砕される。微粉
砕装置12出口側には分級機16、分離器18ならびに
圧力制御弁32、送風機20が直列して配設されてい
る。分級機16は微粉砕品を粗粒と細粉とに分級して、
粗粒は微粉砕装置12に戻されて繰返し粉砕されるとと
もに、細粉は分離器18において固・気分離がなされ砕
製品19の分離回収が行われる。そして、分離器18か
らの系統30内ガスは圧力制御弁32を介し送風機20
により流動されている。この微粉砕系統30内ガスは循
環流動されて、送風機20より再び微粉砕装置12内に
導入されるとともに、一部は外気に放出される。
FIG. 1 shows an example of a fine pulverizer for performing a closed circuit operation, and reference numeral 10 denotes an oxygen controller, including a pressure controller. Reference numeral 12 denotes a fine pulverizing device. The material supplied from the material supply device 14 is dispersed and introduced into a fine pulverizing system 30 and finely pulverized in the fine pulverizing device 12. A classifier 16, a separator 18, a pressure control valve 32, and a blower 20 are arranged in series at the outlet side of the pulverizer 12. The classifier 16 classifies the finely pulverized product into coarse particles and fine powder,
The coarse particles are returned to the fine pulverizer 12 and repeatedly pulverized, and the fine powder is subjected to solid / gas separation in the separator 18 to separate and collect the crushed product 19. The gas in the system 30 from the separator 18 is supplied to the blower 20 through the pressure control valve 32.
Fluidized by The gas in the fine pulverizing system 30 is circulated and flowed, and is again introduced into the fine pulverizing device 12 from the blower 20, and a part of the gas is discharged to the outside air.

【0011】微粉砕系統30における微粉砕装置12入
口側には不活性ガス導入路28が接続され、26は不活
性ガス流量制御弁である。この不活性ガスとしては、希
ガス、例えば一原子気体であるアルゴン等が用いられ、
従来例の不活性ガスである水素化合物からなる水蒸気,
酸素化合物からなる二酸化炭素等の三原子分子と異な
り、反応性が極めて低い化学的不活性を呈するものであ
る。
An inert gas introduction passage 28 is connected to the fine pulverizing system 30 on the inlet side of the fine pulverizing device 12, and 26 is an inert gas flow control valve. As the inert gas, a rare gas, for example, argon which is a monoatomic gas is used,
Water vapor of a hydrogen compound, which is an inert gas of a conventional example,
Unlike triatomic molecules such as carbon dioxide composed of oxygen compounds, they exhibit chemical reactivity with extremely low reactivity.

【0012】22は前記系統30内ガスの酸素濃度を検
出する酸素濃度検出器を示し、例えばジルコニア固体電
解質型の酸素センサが好適であり、微粉砕装置12の上
流側に、詳細に述べれば、材料供給機14の上流側位置
に設置され、酸素濃度検出時に粉じん等が作用すること
を防止している。酸素濃度検出器22からの電気量に変
換された出力信号23は、A/D変換器を介したディジ
タル処理とすることができるが、実施例ではアナログ処
理による場合を示す。出力信号23は酸素制御器24に
入力され、また、25は酸素制御器24の酸素濃度設定
器である。
Reference numeral 22 denotes an oxygen concentration detector for detecting the oxygen concentration of the gas in the system 30. For example, a zirconia solid electrolyte type oxygen sensor is suitable. It is installed at a position on the upstream side of the material feeder 14 to prevent dust and the like from acting when detecting the oxygen concentration. The output signal 23 converted into an electric quantity from the oxygen concentration detector 22 can be digitally processed through an A / D converter, but the embodiment shows a case of analog processing. The output signal 23 is input to an oxygen controller 24, and 25 is an oxygen concentration setting unit of the oxygen controller 24.

【0013】酸素制御器24は所要の制御回路を備えて
おり、酸素濃度検出器22の検出酸素濃度条件に応じ
て、酸素濃度設定器25の設定濃度と比較してその偏差
信号により制御動作がなされ、酸素濃度が規定濃度とな
るように不活性ガス流量制御弁26を制御する操作信号
27が出力される。この設定器25の設定濃度は可変と
することができる。そして、操作信号27は図示しない
電/空変換器に入力し、空気信号として不活性ガス流量
を制御する不活性ガス流量制御弁26に与えられ、系統
30内ガスの酸素濃度が規定濃度となるように制御され
ている。
The oxygen controller 24 has a required control circuit. The oxygen controller 24 performs a control operation in accordance with a detected oxygen concentration condition of the oxygen concentration detector 22 in comparison with a set concentration of an oxygen concentration setter 25 and a deviation signal thereof. Then, an operation signal 27 for controlling the inert gas flow control valve 26 is output so that the oxygen concentration becomes the specified concentration. The set density of the setter 25 can be made variable. Then, the operation signal 27 is input to an electro / pneumatic converter (not shown), and is given as an air signal to an inert gas flow control valve 26 for controlling the inert gas flow, so that the oxygen concentration of the gas in the system 30 becomes a specified concentration. Is controlled as follows.

【0014】なお、酸素制御器24の制御動作として多
位置制御、例えば3位置制御動作とすることができて、
不活性ガス流量制御弁26の動作を3位置にて行わせ
て、制御系の構成を簡易にさせることができる。
The control operation of the oxygen controller 24 can be multi-position control, for example, a three-position control operation.
The operation of the inert gas flow control valve 26 is performed at three positions, so that the configuration of the control system can be simplified.

【0015】反応性の高い金属系材料、例えばアルミニ
ウムを微粉砕装置12において微粉砕する場合には微粉
砕系統30内ガスの酸素濃度を規定濃度、例えば0.1
7〜1.2%にしてアルミニウムの表面酸化が抑制でき
るようにされる。
When a highly reactive metal material, for example, aluminum is pulverized in the pulverizer 12, the oxygen concentration of the gas in the pulverization system 30 is adjusted to a specified concentration, for example, 0.1.
7 to 1.2% is set so that the surface oxidation of aluminum can be suppressed.

【0016】33は前記系統30内ガスの圧力を検出す
る圧力検出器であり、送風機20入口に設置され、圧力
検出器33からの電気量に変換された出力信号35は圧
力制御器34に入力され、また36は圧力制御器34の
圧力設定器36である。
Reference numeral 33 denotes a pressure detector for detecting the pressure of the gas in the system 30. The pressure detector 33 is installed at the inlet of the blower 20, and an output signal 35 converted into an electric quantity from the pressure detector 33 is input to a pressure controller 34. Reference numeral 36 denotes a pressure setting unit 36 of the pressure controller 34.

【0017】圧力制御器34は所要の制御回路を備えて
おり、圧力検出器33の検出圧力条件に応じて、圧力設
定器36の設定圧力と比較してその偏差信号により制御
動作がなされ、圧力が規定圧力となるように圧力制御弁
32を制御する操作信号37が出力される。この設定器
36の設定圧力は可変とすることができる。そして、操
作信号37は図示しない電/空変換器に入力し、空気信
号としてガス圧力を制御する圧力制御弁32に与えら
れ、系統30内ガスの圧力が規定圧力となるように制御
されている。微粉砕系統30内のガス圧力は規定圧力、
例えば0〜100MPa となるように制御されるので、外
気が系統30内に侵入されることが抑制され系統30内
ガスの酸素濃度が増加することを回避している。
The pressure controller 34 has a required control circuit. The pressure controller 34 compares the pressure with a pressure set by a pressure setter 36 in accordance with a detected pressure condition of the pressure detector 33, and performs a control operation based on a deviation signal thereof. An operation signal 37 for controlling the pressure control valve 32 so that the pressure becomes a specified pressure is output. The set pressure of the setter 36 can be made variable. Then, the operation signal 37 is input to an electro-pneumatic converter (not shown), and is supplied as an air signal to the pressure control valve 32 for controlling the gas pressure, so that the pressure of the gas in the system 30 is controlled to a specified pressure. . The gas pressure in the pulverizing system 30 is a specified pressure,
For example, since the pressure is controlled to be 0 to 100 MPa, intrusion of outside air into the system 30 is suppressed, and an increase in the oxygen concentration of the gas in the system 30 is avoided.

【0018】かかる構成によって、反応性の高い金属系
材料を微粉砕装置12において微粉砕するにあたり、希
ガスを用いた不活性ガスの導入により、材料に随伴され
て微粉砕系統30内に導入される酸素による雰囲気濃度
も規定濃度となるようにされ、しかも外気が系統30内
に侵入されることが抑制され、系統30内酸素濃度を材
料の表面酸化を抑制するように自動的に制御できて、前
記材料等の性状を低下させることなく効率よく微粉砕す
ることができる。
With this configuration, when a highly reactive metal-based material is pulverized in the pulverizer 12, the inert gas using a rare gas is introduced into the pulverization system 30 accompanying the material. The atmospheric concentration due to oxygen is also set to a specified concentration, and the intrusion of outside air into the system 30 is suppressed, and the oxygen concentration in the system 30 can be automatically controlled so as to suppress surface oxidation of the material. The fine pulverization can be efficiently performed without deteriorating the properties of the material and the like.

【0019】[0019]

【発明の効果】以上説明したように本発明によれば、反
応性の高い金属材料を微粉砕するにあたり、外気が微粉
砕系統内に浸入されることが抑制されるとともに、系統
内酸素濃度を希ガスを用いた不活性ガスの導入により低
酸素雰囲気のもとで材料の表面酸化を抑制するように自
動的に制御し、反応性の高い金属系材料等の性状を低下
させることなく微粉砕することができる等、多大な効果
が奏せられる。
As described above, according to the present invention, when finely pulverizing a highly reactive metal material, the infiltration of outside air into the fine pulverization system is suppressed and the oxygen concentration in the system is reduced. Introducing an inert gas using a rare gas to automatically control the surface oxidation of the material under a low oxygen atmosphere so that it can be pulverized without deteriorating the properties of highly reactive metal materials. A great effect can be achieved.

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

【図1】本発明の一実施例を示す酸素濃度制御装置を備
えた微粉砕装置の全体構成図。
FIG. 1 is an overall configuration diagram of a pulverizing apparatus provided with an oxygen concentration control device according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 酸素濃度制御装置 12 微粉砕装置 20 送風機 22 酸素濃度検出器 24 酸素制御器 26 不活性ガス流量制御弁 28 不活性ガス導入路 30 微粉砕系統 32 圧力制御弁 34 圧力制御器 DESCRIPTION OF SYMBOLS 10 Oxygen concentration control apparatus 12 Fine crushing apparatus 20 Blower 22 Oxygen concentration detector 24 Oxygen controller 26 Inert gas flow control valve 28 Inert gas introduction path 30 Fine crushing system 32 Pressure control valve 34 Pressure controller

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 微粉砕系統を通して不活性ガス雰囲気に
て材料を微粉砕させるための微粉砕装置と、微粉砕装置
入口側に接続された不活性ガス導入路に設けられた不活
性ガス流量制御弁と、微粉砕装置に後置され系統内ガス
を流動させるための送風機と、送風機入口側に設けられ
た圧力制御弁と、を備えてなる微粉砕装置において、前
記微粉砕装置上流の系統内ガスの酸素濃度を検出する酸
素濃度検出器と、酸素濃度検出器の検出酸素濃度を設定
濃度と比較しその偏差により前記酸素濃度が規定濃度と
なるように前記不活性ガス流量制御弁を制御する酸素制
御器と、前記送風機入口の系統内ガスの圧力を検出する
圧力検出器と、圧力検出器の検出圧力を設定圧力と比較
しその偏差により前記圧力が規定圧力となるように前記
圧力制御弁を制御する圧力制御器と、を具備してなるこ
とを特徴とする酸素濃度制御装置を備えた微粉砕装置。
1. A pulverizing device for pulverizing a material in an inert gas atmosphere through a pulverizing system, and an inert gas flow control provided in an inert gas introduction passage connected to an inlet side of the pulverizing device. A valve, a blower disposed downstream of the pulverizing device for flowing the gas in the system, and a pressure control valve provided on the inlet side of the blower; in a system upstream of the pulverizing device, An oxygen concentration detector for detecting the oxygen concentration of the gas, and comparing the detected oxygen concentration of the oxygen concentration detector with a set concentration, and controlling the inert gas flow control valve such that the oxygen concentration becomes a specified concentration by a deviation thereof. An oxygen controller, a pressure detector that detects the pressure of gas in the system at the inlet of the blower, and a pressure control valve that compares a detected pressure of the pressure detector with a set pressure, and that the pressure becomes a specified pressure by a deviation thereof. Control And a pressure controller, comprising: an oxygen concentration control device.
JP6092993A 1993-02-25 1993-02-25 Pulverizer with oxygen concentration controller Expired - Lifetime JP2620771B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6092993A JP2620771B2 (en) 1993-02-25 1993-02-25 Pulverizer with oxygen concentration controller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6092993A JP2620771B2 (en) 1993-02-25 1993-02-25 Pulverizer with oxygen concentration controller

Publications (2)

Publication Number Publication Date
JPH06246182A JPH06246182A (en) 1994-09-06
JP2620771B2 true JP2620771B2 (en) 1997-06-18

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Cited By (1)

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CN102836773A (en) * 2011-10-28 2012-12-26 南通天华和睿科技创业有限公司 Water injector for mineral crusher

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JP3016064B2 (en) * 1995-09-27 2000-03-06 古河電池株式会社 Method for producing hydrogen storage alloy powder for battery
JP6011933B2 (en) * 2012-11-26 2016-10-25 株式会社日向製錬所 Coal dust ignition prevention system and coal dust ignition prevention method for pulverized coal mill system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102836773A (en) * 2011-10-28 2012-12-26 南通天华和睿科技创业有限公司 Water injector for mineral crusher

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