JPH0776738B2 - Granule sampling device and granule sampling method - Google Patents

Granule sampling device and granule sampling method

Info

Publication number
JPH0776738B2
JPH0776738B2 JP4283060A JP28306092A JPH0776738B2 JP H0776738 B2 JPH0776738 B2 JP H0776738B2 JP 4283060 A JP4283060 A JP 4283060A JP 28306092 A JP28306092 A JP 28306092A JP H0776738 B2 JPH0776738 B2 JP H0776738B2
Authority
JP
Japan
Prior art keywords
powder
pipe
sample
plant
granular material
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 - Fee Related
Application number
JP4283060A
Other languages
Japanese (ja)
Other versions
JPH06129959A (en
Inventor
貴史 千野
敬介 加藤
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.)
Nikkiso Co Ltd
Original Assignee
Nikkiso 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 Nikkiso Co Ltd filed Critical Nikkiso Co Ltd
Priority to JP4283060A priority Critical patent/JPH0776738B2/en
Publication of JPH06129959A publication Critical patent/JPH06129959A/en
Publication of JPH0776738B2 publication Critical patent/JPH0776738B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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、粉粒体のサンプリング
装置及び粉粒体のサンプリング方法に関し、さらに詳述
すると、高分子化合物、小麦粉、セメント粉、石炭粉等
の各種粉粒体のサンプリングを、粉粒体の帯電を防止し
つつ、かつコンタミネーションなく行うことのできるサ
ンプリング装置及びサンプリング方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sampling device for powder and granules and a method for sampling powder and granules. More specifically, sampling of various powders and granules such as polymer compounds, wheat flour, cement powder and coal powder. The present invention relates to a sampling device and a sampling method that can perform the above while preventing the electrostatic charge of the powder and granules and without contamination.

【0002】[0002]

【従来の技術】従来、上述したような各種粉粒体のサン
プリングを行う手段として、例えば、プラント配管中に
手動扉付きのサンプラーを配置し、品質検査員が必要に
応じて前記サンプラーの位置まで行って手動扉を開いて
必要量の粉粒体を採取していた。
2. Description of the Related Art Conventionally, as a means for sampling various powders and granules as described above, for example, a sampler with a manual door is arranged in a plant pipe, and a quality inspector can reach the position of the sampler as needed. I went to open the manual door and collected the required amount of powder.

【0003】さらに、粉粒体が帯電し易いものであれ
ば、検査室で自然放置による除電後、この粉粒体の粒度
分布測定、カサ比重測定等を行っていた。
Further, if the powder or granules are easily charged, the particle size distribution of the powder or granules and the bulk specific gravity of the powder or granules are measured after the static electricity is removed by leaving it in the inspection room.

【0004】[0004]

【発明が解決しようとする課題】粉粒体の製造プロセス
の自動化は非常に進んでいるが、粉粒体のサンプリング
は上述したように人手作業に依存しているのが実情であ
る。
Although the automation of the manufacturing process of powder and granules is very advanced, the actual situation is that sampling of powder and granules depends on manual work as described above.

【0005】そして、安価で簡易な構成のサンプリング
装置をプラント配管中に配置し、省力化、省人化を図り
たいという要請が強まっているが、他品種少量生産のプ
ラントの場合、サンプラー中での粉粒体が帯電してしま
って集合状態で粉粒体を採取することができないという
問題やサンプリングしようとしてもそれ以前の品種によ
ってサンプラー中が汚染されていて高い純度でサンプル
試料を採取することができないという問題があり、実用
化が遅れているのが現状である。
There is a growing demand for labor-saving and labor-saving by arranging an inexpensive and simple sampling device in the plant piping. The problem that the powder and granules in the sample are charged and it is not possible to collect the powder and granules in an aggregated state, or even if you try to sample, the sampler is contaminated in the sampler before that and collect the sample sample with high purity However, there is a problem that it is not possible to do so, and it is the current situation that practical application is delayed.

【0006】そこで、本発明は、安価で簡易な構成であ
り、かつ、帯電による問題もなく、サンプリング以前の
品種による汚染の問題もなく、簡単な操作で粉粒体のサ
ンプリングを行うことが可能な粉粒体のサンプリング装
置及びサンプリング方法を提供することを目的とする。
Therefore, the present invention has an inexpensive and simple structure, and there is no problem due to electrification, there is no problem of contamination due to the type of product before sampling, and it is possible to sample powder or granules by a simple operation. An object of the present invention is to provide a sampling device and a sampling method for fine powder particles.

【0007】[0007]

【課題を解決するための手段】請求項1記載の発明
は、粉粒体が所定の圧力下で流通するプラント配管に接
続されたサンプル抜き出し管と、前記サンプル抜き出し
管の途中に設けられた開閉手段と、サンプル抜き出し管
に接続された粉粒体分離槽と、前記開閉手段を開状態に
して前記サンプル抜き出し管からプラント配管へ洗浄気
体を供給してサンプル抜き出し管中を洗浄する洗浄気体
供給手段と、洗浄気体供給手段からの気体供給を停止し
た状態で前記開閉手段を開状態にすることによりプラン
ト配管からサンプル抜き出し管を介して供給された粉粒
体を有する前記粉粒体分離槽内に調湿気体を供給する除
電用気体供給手段とを有することを特徴とする粉粒体の
サンプリング装置であり、請求項2に記載の発明は、粉
粒体が所定の圧力下で流通するプラント配管に接続され
たサンプル抜き出し管に設けられた開閉手段を開状態に
し、洗浄気体供給手段によりサンプル抜き出し管からプ
ラント配管へと洗浄気体を流通させることによりサンプ
ル抜き出し管中を洗浄してから、洗浄気体供給手段によ
る洗浄気体の供給を停止すると共にプラント配管から粉
粒体分離槽内へと粉粒体を流通させてサンプル抜き出し
管中を共洗いし、前記開閉手段を閉鎖状態にして共洗い
により粉粒体分離槽内で集合した粉粒体を廃棄し、その
後に前記開閉手段を解放状態にして、プラント配管から
粉粒体分離槽内へと粉粒体を流通させると同時に粉粒体
分離槽内に除電用気体供給手段から調湿気体を供給し
て、集合した粉粒体を分離することを特徴とする粉粒体
のサンプリング方法である。
SUMMARY OF THE INVENTION The first aspect of the present invention, a sample discharge pipe which is tangent <br/> connection to plant piping granular material to flow under a predetermined pressure, the sample withdrawn
Opening and closing means provided in the middle of the tube, powder and granular material separation tank connected to the sample extraction tube, and the opening and closing means
Clean air from the sample extraction pipe to the plant pipe.
Cleaning gas that supplies the body and cleans the inside of the sample extraction tube
Stop the gas supply from the supply means and the cleaning gas supply means.
Plan by opening the opening and closing means in the open state
Particles supplied from the sample pipe through the sample extraction pipe
A sampling device for granular material characterized by having a charge removing gas supply means for supplying the powder or granular material separation tank in regulating moisture having a body, the invention of claim 2, granular Open the open / close means provided in the sample withdrawal pipe connected to the plant pipe body is flowing under a predetermined pressure, by flowing the cleaning gas from the sample withdrawal pipe to the plant pipe by the cleaning gas supply means sample After the inside of the extraction pipe is washed, the supply of the cleaning gas by the cleaning gas supply means is stopped and the powder and granules are circulated from the plant piping into the powder and granular material separation tank to be washed together in the sample extraction pipe, With the opening / closing means closed, the granular material collected in the granular material separation tank by co-washing is discarded, and then the opening / closing means is opened, and the plant piping enters the granular material separating tank. Granules is supplied from tone moisture body neutralizing gas supply means to the circulation is allowed at the same time granular material separation tank and is a method of sampling particulate material and separating the granular material was set .

【0008】[0008]

【作用】上述した構成の粉粒体のサンプリング装置によ
るサンプリング方法について以下に説明する。
The sampling method by the sampling device of the above-structured powder or granular material will be described below.

【0009】開閉手段を解放状態にし、洗浄気体供給手
段から洗浄気体をサンプル抜き出し管を通じてプラント
配管内に供給する。これによってサンプル抜き出し管内
の洗浄が行われる。次いで、洗浄気体供給手段からの洗
浄気体の供給を停止する。その後、プラント配管内には
所定圧力で粉粒体が流通しているので、開閉手段を解放
状態にしたまま洗浄気体供給手段からの洗浄気体の流通
を停止することにより、プラント配管から粉粒体がサン
プル抜き出し管に流れ込み、粉粒体分離槽内に流れ込
む。プラント配管から粉粒体分離槽への粉粒体の流通を
一定時間継続することによりサンプル抜き出し管内を共
洗いする。この共洗いによって、サンプル抜き出し管内
に存在するであろうところの、以前の他の品種の、ある
いは同品種ではあるがロットの異なる粉粒体を除去す
る。一定時間かけて粉粒体を粉粒体分離槽内に供給する
と、この粉粒体分離槽で粉粒体が集合状態になって、貯
留する。その後、前記開閉手段を閉鎖状態にしてから、
粉粒体分離槽内で集合状態になっている粉粒体を粉粒体
分離槽内から除去する。そして、開閉手段を解放状態に
することにより、プラント配管から粉粒体を粉粒体分離
槽に流通させると共に除電用気体供給手段から粉粒体分
離槽内に調湿気体を供給する。これにより粉粒体分離槽
内では粉粒体が除電される。したがって、粉粒体分離槽
内で粉粒体が帯電することによる粉粒体の集合阻害が防
止され、粉粒体分離槽内で粉粒体が帯電することなく集
合する。集合した粉粒体を粉粒体分離槽内から分離す
る。
The opening / closing means is opened, and the cleaning gas is supplied from the cleaning gas supply means into the plant piping through the sample extracting pipe. As a result, the inside of the sample extraction tube is cleaned. Then, the supply of the cleaning gas from the cleaning gas supply means is stopped. After that, since the granular material is flowing in the plant pipe at a predetermined pressure, by stopping the flow of the cleaning gas from the cleaning gas supply means while keeping the opening / closing means in the open state, the granular material is discharged from the plant piping. Flows into the sample withdrawal pipe and into the powder / particle separation tank. The inside of the sample extracting pipe is washed together by continuing the flow of the powder and granules from the plant pipe to the powder and granule separation tank for a certain period of time. This co-washing removes the previous granules of other varieties, or of the same varieties but in different lots, that would be present in the sample withdrawal tube. When the powder or granular material is supplied into the powder or granular material separating tank over a certain period of time, the powder or granular material is gathered and stored in the powder or granular material separating tank. Then, after closing the opening and closing means,
The powder particles that are in an aggregated state in the powder particle separation tank are removed from the powder particle separation tank. Then, by opening and closing the opening / closing means, the granular material is circulated from the plant pipe to the granular material separating tank, and the humidity control body is supplied from the static elimination gas supply means into the granular material separating tank. As a result, the powder and granules are discharged in the powder and granule separation tank. Therefore, it is possible to prevent the aggregation of the particles due to the charging of the particles in the particle separation tank, and the particles are aggregated without being charged in the particle separation tank. The aggregated granular material is separated from the granular material separation tank.

【0010】以上により、簡易な操作の下に帯電のな
い、しかもそれ以前の粉粒体による汚染もない高純度の
粉粒体のサンプリングを行うことが可能となる。
As described above, it is possible to perform sampling of a high-purity powder or granular material which is free from electrification and is free from contamination by the powder or granular material before that under a simple operation.

【0011】[0011]

【実施例】以下に、本発明の実施例を詳細に説明する。EXAMPLES Examples of the present invention will be described in detail below.

【0012】図1に示す粉粒体のサンプリング装置1
は、高分子化合物、ポリ塩化ビニール、小麦粉、セメン
ト、石炭粉等の粉粒体が所定の圧力下で流通するプラン
ト配管2と、このプラント配管2に接続した切替弁4、
サンプリング弁5を有するサンプル抜き出し管系3と、
このサンプル抜き出し管系3に接続した粉粒体に旋回運
動による遠心力を作用させる粉粒体分離槽としてのサイ
クロン6と、このサイクロン6の上端部に接続した空気
の吸引を行うバキュームクリーナからなる吸引手段7
と、前記サンプル抜き出し管系3に除電用の調湿気体を
送る除電用気体供給手段8と、前記サイクロン6の下部
取り出し口側に接続した粉粒体の収集又は廃棄を行う吐
出配管系9と、前記切替弁4を介してプラント配管2に
洗浄気体を送るとともに、サンプル抜き出し管系3、
イクロン6及び吐出配管系9に洗浄気体を送る洗浄気体
供給手段10とを有している。
A sampling device 1 for powder particles shown in FIG.
Is a plant pipe 2 through which a granular material such as a high molecular compound, polyvinyl chloride, wheat flour, cement, and coal powder flows under a predetermined pressure, and a switching valve 4 connected to this plant pipe 2.
A sample withdrawal tubing system 3 having a sampling valve 5;
It consists of a cyclone 6 as a granular material separating tank for applying a centrifugal force to the granular material connected to the sample extracting pipe system 3 by a swirling motion, and a vacuum cleaner connected to the upper end of the cyclone 6 for sucking air. Suction means 7
And a static elimination gas supply means 8 for sending a humidity adjusting body for static elimination to the sample extracting pipe system 3, and a discharge piping system 9 for collecting or discarding powder particles connected to the lower outlet side of the cyclone 6. The cleaning gas supply means 10 supplies the cleaning gas to the plant pipe 2 through the switching valve 4 and supplies the cleaning gas to the sample withdrawing pipe system 3, the cyclone 6 and the discharge pipe system 9.

【0013】ここで、前記調湿気体としては、一定の湿
度たとえば飽和状態に調整された空気を挙げることがで
きる。また、洗浄気体としては乾燥し、かつフィルター
等により清浄にされた空気を挙げることができる。
Here, as the humidity control body, there can be mentioned air adjusted to a constant humidity, for example, a saturated state. The cleaning gas may be air that has been dried and cleaned with a filter or the like.

【0014】前記サンプル抜き出し管系3の切替弁4
は、空気作動式ボール弁により構成され、洗浄気体供給
手段10とプラント配管2とを連通する動作と、プラン
ト配管2とサンプリング弁5側とを連通する動作とに切
り替わるようになっている。
Switching valve 4 of the sample withdrawing pipe system 3
Is constituted by an air-operated ball valve, and is switched between an operation for communicating the cleaning gas supply means 10 and the plant pipe 2 and an operation for communicating the plant pipe 2 and the sampling valve 5 side.

【0015】前記サンプリング弁5は、空気作動式ボー
ル弁により構成され、かつ空気圧によりサンプル抜き出
し管系3の流路を開閉するようになっている。
The sampling valve 5 is composed of an air-actuated ball valve and is adapted to open and close the flow path of the sample withdrawing pipe system 3 by air pressure.

【0016】前記除電用気体供給手段8は、サンプル抜
き出し管系3により採取される粉粒体に対し除電用の調
湿気体を送り、帯電した粉粒体の電荷を除去するもので
あり、除電気体供給源11と、空気作動式ボール弁によ
り構成され、かつ空気圧により動作する調湿気体供給弁
12とを具備している。
The destaticizing gas supply means 8 sends a humidity control body for destaticization to the powder particles collected by the sample extracting pipe system 3 to remove the charge of the charged powder particles. It is provided with an electric body supply source 11 and a humidity control body supply valve 12 which is constituted by an air-actuated ball valve and is operated by air pressure.

【0017】前記吐出配管系9は、前記サイクロン6の
下部取り出し口側に接続した空気作動式ボール弁により
構成した第1の吐出弁13と、この第1の吐出弁13に
直列に接続した第2の吐出弁14と、この第2の吐出弁
14の下方に配置した廃棄受箱15と、第1の吐出弁1
3と、第2の吐出弁14との間に接続した粉粒体収集用
の電磁弁からなる、大気開放弁である開放弁16とを具
備し、開放弁16の出口側を図示しない粒度分析装置、
カサ比重測定装置等の分析装置に接続している。
The discharge piping system 9 is composed of a first discharge valve 13 composed of an air operated ball valve connected to the lower outlet side of the cyclone 6, and a first discharge valve 13 connected in series to the first discharge valve 13. Second discharge valve 14, a waste container 15 arranged below the second discharge valve 14, and the first discharge valve 1
3 and a release valve 16 which is an atmosphere release valve composed of a solenoid valve for collecting powder and granules, which is connected between the second discharge valve 14 and the second discharge valve 14. apparatus,
It is connected to an analyzer such as a bulk specific gravity measuring device.

【0018】前記洗浄気体供給手段10は、洗浄気体を
送り出す洗浄気体供給手段17と、この洗浄気体供給手
段10に接続した気体レギュレータ18と、この気体レ
ギュレータ18と前記切替弁4との間に接続した電磁弁
からなる第1の気体弁19と、気体レギュレータ18と
前記サンプリング弁5との間に接続した電磁弁からなる
第2の気体弁20とを具備している。
The cleaning gas supply means 10 is connected between the cleaning gas supply means 17 for supplying the cleaning gas, the gas regulator 18 connected to the cleaning gas supply means 10, and the gas regulator 18 and the switching valve 4. The first gas valve 19 is a solenoid valve and the second gas valve 20 is a solenoid valve connected between the gas regulator 18 and the sampling valve 5.

【0019】尚、図1中、21、22は、洗浄気体供給
手段10の一部を構成する絞り弁である。
In FIG. 1, reference numerals 21 and 22 are throttle valves forming a part of the cleaning gas supply means 10.

【0020】次に、上述した構成の粉粒体のサンプリン
グ装置1を用いた粉粒体の自動サンプリング方法につい
て説明する。
Next, a method for automatically sampling powder or granules using the sampling device 1 for powder or granules having the above configuration will be described.

【0021】まず、前記切替弁4を、洗浄気体供給手段
10と、プラント配管2とが連通する状態に切り替える
とともに、第1の気体弁19を開き、第2の気体弁22
は閉じる。この状態で、図1に点線で示すように、洗浄
気体供給源17を始動することにより、レギュレータ1
8、第1の気体弁19及び切替弁4を介してプラント配
管2に洗浄気体を送り、サンプル抜き出し管系3のプラ
ント配管2から切り替え弁4までの内部を洗浄する。
First, the switching valve 4 is switched to a state in which the cleaning gas supply means 10 and the plant pipe 2 are in communication with each other, the first gas valve 19 is opened, and the second gas valve 22 is opened.
Closes. In this state, the cleaning gas supply source 17 is started as shown by the dotted line in FIG.
8, the cleaning gas is sent to the plant pipe 2 through the first gas valve 19 and the switching valve 4, and the inside of the sample withdrawing pipe system 3 from the plant pipe 2 to the switching valve 4 is cleaned.

【0022】このようにサンプル抜き出し管系3を洗浄
するのは、このサンプル抜き出し管系3はプラント配管
2と直接に結合されているので、プラント配管2中を流
れる粉粒体が滞留し、しかもプラントにおける品種変え
が頻繁に行われると種々の粉粒体がサンプル抜き出し管
系3に混入しかつ滞留することがあるので、このような
種々の粉粒体による汚染を防止するためである。
The cleaning of the sample withdrawing pipe system 3 in this manner is performed because the sample withdrawing pipe system 3 is directly connected to the plant pipe 2, so that the powder or granular material flowing in the plant pipe 2 stays, and This is because various powders and granules may be mixed and retained in the sample withdrawing pipe system 3 if the product type is frequently changed in the plant, so that contamination by such various powders and granules is prevented.

【0023】次に、切替弁4を、サンプル抜き出し管系
3と、プラント配管2とが連通する状態に切り替えると
ともに、サンプリング弁5を開、第1の吐出弁13を
開、第2の吐出弁14を閉、第1、第2の気体弁19、
20を閉、調湿気体供給弁12を閉、サイクロン6を動
作状態、吸引手段7をオンにして、図2に示すように、
前記プラント配管2、サンプル抜き出し管系3、サイク
ロン6及び吐出配管系9の洗浄を行う共洗いブロー洗浄
を行う。この段階で、サンプル抜き出し管系3、サイク
ロン6及び吐出配管系9の流路中には粉粒体が残存す
る。
Next, the switching valve 4 is switched to a state in which the sample withdrawing pipe system 3 and the plant pipe 2 are in communication with each other, the sampling valve 5 is opened, the first discharge valve 13 is opened, and the second discharge valve is opened. 14, the first and second gas valves 19,
20 is closed, the humidity control body supply valve 12 is closed, the cyclone 6 is in an operating state, the suction means 7 is turned on, and as shown in FIG.
The co-wash blow cleaning for cleaning the plant pipe 2, the sample extraction pipe system 3, the cyclone 6, and the discharge pipe system 9 is performed. At this stage, the granular material remains in the flow paths of the sample extracting pipe system 3, the cyclone 6, and the discharge pipe system 9.

【0024】さらに、図2に示す状態から、第1の吐出
弁13を閉、第2の吐出弁14を開、開放弁16を開に
して、図3に点線で示すように、前記サンプル抜き出し
管系3のサンプリング弁5からサイクロン6に至る流
路、サイクロン6及び吐出配管系9の洗浄を行い、これ
らの流路中に残存する粉粒体を廃棄受箱15に廃棄する
前処理を行う。
Further, from the state shown in FIG. 2, the first discharge valve 13 is closed, the second discharge valve 14 is opened, the open valve 16 is opened, and as shown by the dotted line in FIG. The flow path from the sampling valve 5 of the pipe system 3 to the cyclone 6, the cyclone 6 and the discharge pipe system 9 are washed, and a pretreatment for discarding the powder or granules remaining in these flow paths to the waste receiving box 15 is performed. .

【0025】次に、前記サンプリング弁5を開、第1の
吐出弁13を開、第2の吐出弁14を閉、切替弁4をサ
ンプル抜き出し管系3とプラント配管2とが連通する状
態、第1、第2の気体弁19、20を閉、調湿気体供給
弁12を開、開放弁16を開閉動作の状態とし、図4に
示すように、前記プラント配管2、サンプル抜き出し管
系3、サイクロン6及び吐出配管系9に至る流路を形成
して、除電用気体供給手段8によりサンプル抜き出し管
系3に除電用の調湿気体を送りプラント配管2内の圧力
を利用して粉粒体を前記流路を通じて除電しつつ所定量
サンプリングする。サンプリングされた所定量の粉粒体
は、開放弁16から図示しない粒度分析装置、カサ比重
測定装置等の分析装置に送られ、粒度分布の分析、カサ
比重の測定等が行われる。
Next, the sampling valve 5 is opened, the first discharge valve 13 is opened, the second discharge valve 14 is closed, and the switching valve 4 is in a state in which the sample withdrawing pipe system 3 and the plant pipe 2 communicate with each other. The first and second gas valves 19 and 20 are closed, the humidity control body supply valve 12 is opened, and the opening valve 16 is opened and closed. As shown in FIG. 4, the plant pipe 2 and the sample extraction pipe system 3 are connected. , A cyclone 6 and a discharge pipe system 9 are formed, and a static elimination humidity control body is sent to the sample extraction pipe system 3 by the static elimination gas supply means 8 to use the pressure in the plant pipe 2 to form powder particles. A predetermined amount is sampled while the body is discharged through the flow path. A predetermined amount of the sampled powder or granules is sent from the open valve 16 to an analyzer such as a particle size analyzer or a bulk specific gravity measuring device (not shown), where the particle size distribution is analyzed and the bulk specific gravity is measured.

【0026】最後に、前記サンプリング弁を閉、第1の
吐出弁13を開、第2の吐出弁14を開、切替弁4を洗
浄気体供給手段とプラント配管2とが連通する状態、第
1、第2の気体弁19、20を開、調湿気体供給弁12
を閉、開放弁16を開の状態とし、図5に示すように、
洗浄気体供給手段10によりサンプル抜き出し管系3の
切替弁4を介して洗浄気体をプラント配管2に送るとと
もに、洗浄気体供給手段10によりサンプル抜き出し管
系3、サイクロン6及び吐出配管系9に洗浄気体を送り
全体の洗浄を行う。
Finally, the sampling valve is closed, the first discharge valve 13 is opened, the second discharge valve 14 is opened, and the switching valve 4 is in a state in which the cleaning gas supply means and the plant pipe 2 communicate with each other. , The second gas valves 19 and 20 are opened, and the humidity control body supply valve 12
Closed and the open valve 16 opened, as shown in FIG.
The cleaning gas is sent to the plant pipe 2 by the cleaning gas supply means 10 through the switching valve 4 of the sample withdrawal pipe system 3, and the cleaning gas is supplied to the sample withdrawal pipe system 3, the cyclone 6 and the discharge pipe system 9 by the cleaning gas supply means 10. To clean the whole.

【0027】以上の工程により、安価で簡易な構成と簡
略な動作のもとに帯電のない粉粒体のサンプリングを簡
単な弁操作によって全自動で行うことが可能となる。
By the steps described above, it becomes possible to fully automatically perform the sampling of the non-charged powdery particles by a simple valve operation based on the inexpensive and simple structure and the simple operation.

【0028】即ち、本実施例装置1によれば、プラント
配管2からの粉粒体のサンプリング中に、この粉粒体の
帯電を除去でき、プラント配管2に多品種少量の各種の
粉粒体を流通させる場合でも、プラント配管2の汚染を
完全に防止し、かつ、粉粒体の性状(粒径等)を変化さ
せることなく、高精度の分析に寄与し得る。
That is, according to the apparatus 1 of the present embodiment, during the sampling of the powder or granular material from the plant pipe 2, the electrostatic charge of the powder or granular material can be removed, and the plant pipe 2 can be provided with a variety of small amounts of various powder or granular materials. Even in the case of circulating, it is possible to completely prevent the contamination of the plant pipe 2 and contribute to highly accurate analysis without changing the properties (particle size, etc.) of the powder or granular material.

【0029】また、前記各弁の開閉時間の調整を適切に
行うことで、必要量の粉粒体を効率よく採取できる。ま
た、前記各弁の動作の組み合わせにより粉粒体の自動サ
ンプリングを行うことができるので、製造コスト、維持
コストの低減、保守の容易化を図ることができる。
Further, by appropriately adjusting the opening / closing time of each valve, the required amount of powder or granules can be efficiently collected. Further, since the powdery particles can be automatically sampled by the combination of the operations of the respective valves, the manufacturing cost and the maintenance cost can be reduced, and the maintenance can be facilitated.

【0030】本発明は、上述した実施例に限定されるも
のではなく、その要旨の範囲内で種々の変形が可能であ
る。
The present invention is not limited to the above-described embodiments, but various modifications can be made within the scope of the invention.

【0031】[0031]

【発明の効果】以上詳述した本発明によれば、上述した
構成としたので、帯電汚染の問題もなく粉粒体のサンプ
リングを全自動で行うことが可能な粉粒体のサンプリン
グ装置を提供することができる。
According to the present invention described in detail above, since it has the above-mentioned structure, it is possible to provide a powdery-particle sampling apparatus capable of fully automatically sampling powdery-particles without the problem of electrostatic contamination. can do.

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

【図1】図1は本発明の実施例装置の配管構成図であ
る。
FIG. 1 is a piping configuration diagram of an apparatus according to an embodiment of the present invention.

【図2】図2は本発明の実施例装置の動作説明図であ
る。
FIG. 2 is an operation explanatory diagram of an apparatus according to an embodiment of the present invention.

【図3】図3は本発明の実施例装置の動作説明図であ
る。
FIG. 3 is an operation explanatory diagram of the apparatus according to the embodiment of the present invention.

【図4】図4は本発明の実施例装置の動作説明図であ
る。
FIG. 4 is an operation explanatory diagram of an apparatus according to an embodiment of the present invention.

【図5】図5は本発明の実施例装置の動作説明図であ
る。
FIG. 5 is an operation explanatory diagram of an apparatus according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 粉粒体のサンプリング装置 2 プラント配管 3 採取配管系 4 切替弁 5 サンプリング弁 6 サイクロン 7 吸引手段 8 調湿気体供給手段 9 吐出配管系 10 洗浄気体供給手段 1 Sampling Device for Powder and Granules 2 Plant Piping 3 Collection Piping System 4 Switching Valve 5 Sampling Valve 6 Cyclone 7 Suction Means 8 Moisture Conditioning Body Supply Means 9 Discharge Piping System 10 Cleaning Gas Supply Means

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 粉粒体が所定の圧力下で流通するプラン
ト配管に接続されたサンプル抜き出し管と、前記サンプ
ル抜き出し管の途中に設けられた開閉手段と、サンプル
抜き出し管に接続された粉粒体分離槽と、前記開閉手段
を開状態にして前記サンプル抜き出し管からプラント配
管へ洗浄気体を供給してサンプル抜き出し管中を洗浄す
る洗浄気体供給手段と、洗浄気体供給手段からの気体供
給を停止した状態で前記開閉手段を開状態にすることに
よりプラント配管からサンプル抜き出し管を介して供給
された粉粒体を有する前記粉粒体分離槽内に調湿気体
供給する除電用気体供給手段とを有することを特徴とす
る粉粒体のサンプリング装置。
1. A and sample discharge pipe which is connected to the plant piping granular material to flow under a predetermined pressure, the sump
Opening / closing means provided in the middle of the sample withdrawing tube, a powder / granule separation tank connected to the sample extracting tube, and the opening / closing means
Open the plant and connect the plant from the sample extraction pipe.
Supply a cleaning gas to the tube to extract the sample and clean the inside of the tube.
Cleaning gas supply means and the gas supply from the cleaning gas supply means.
To open the opening and closing means with the supply stopped
Supplied via the sample extraction pipe from the plant piping
A powder / granule sampling device, comprising: a static elimination gas supply means for supplying a humidity control body into the powder / granule separation tank having the granulated powder.
【請求項2】 粉粒体が所定の圧力下で流通するプラン
ト配管に接続されたサンプル抜き出し管に設けられた開
閉手段を開状態にし、洗浄気体供給手段によりサンプル
抜き出し管からプラント配管へと洗浄気体を流通させる
ことによりサンプル抜き出し管中を洗浄してから、洗浄
気体供給手段による洗浄気体の供給を停止すると共にプ
ラント配管から粉粒体分離槽内へと粉粒体を流通させて
サンプル抜き出し管中を共洗いし、前記開閉手段を閉鎖
状態にして共洗いにより粉粒体分離槽内で集合した粉粒
体を廃棄し、その後に前記開閉手段を解放状態にして、
プラント配管から粉粒体分離槽内へと粉粒体を流通させ
ると同時に粉粒体分離槽内に除電用気体供給手段から調
湿気体を供給して、集合した粉粒体を分離することを特
徴とする粉粒体のサンプリング方法。
2. An open / close means provided in a sample withdrawal pipe connected to a plant pipe through which the powder and granules flow under a predetermined pressure is opened, and a cleaning gas supply means is used to wash the sample withdrawal pipe into the plant pipe. After cleaning the inside of the sample withdrawing pipe by circulating a gas, stop the supply of the cleaning gas by the cleaning gas supply means and allow the powder and granules to circulate from the plant pipe into the powder and granule separation tank The inside is washed together, the opening / closing means is closed, and the granular material collected in the granular material separation tank is discarded by co-washing, and then the opening / closing means is released,
Tone from neutralization gas supply means to the plant from the pipe to the granular material separation tank when circulating the granular material at the same time granular material separation tank
A method for sampling powder and granules, which comprises supplying a damp material to separate the collected powder and granules.
JP4283060A 1992-10-21 1992-10-21 Granule sampling device and granule sampling method Expired - Fee Related JPH0776738B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4283060A JPH0776738B2 (en) 1992-10-21 1992-10-21 Granule sampling device and granule sampling method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4283060A JPH0776738B2 (en) 1992-10-21 1992-10-21 Granule sampling device and granule sampling method

Publications (2)

Publication Number Publication Date
JPH06129959A JPH06129959A (en) 1994-05-13
JPH0776738B2 true JPH0776738B2 (en) 1995-08-16

Family

ID=17660688

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4283060A Expired - Fee Related JPH0776738B2 (en) 1992-10-21 1992-10-21 Granule sampling device and granule sampling method

Country Status (1)

Country Link
JP (1) JPH0776738B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITVC20040002A1 (en) * 2004-04-09 2004-07-14 Domenico Bruzzi flue gas extraction probe from the oven for O2, CO, NOX analysis ... (turbo-probe O2)
JP5009688B2 (en) * 2007-06-01 2012-08-22 独立行政法人海洋研究開発機構 Powder collection device
KR100973492B1 (en) * 2009-10-05 2010-08-03 전제금 Sampling apparatus of pulverized coals
JP6033740B2 (en) * 2012-07-04 2016-11-30 西川ゴム工業株式会社 Powder input device
JP6061738B2 (en) * 2013-03-12 2017-01-18 株式会社日立製作所 Substance analysis apparatus and analysis method
JP6030083B2 (en) * 2014-03-12 2016-11-24 中国電力株式会社 How to clean the sampling tube
JP6951283B2 (en) * 2018-03-30 2021-10-20 株式会社日立製作所 Fine particle analyzer, fine particle analysis system and cleaning method

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58223737A (en) * 1982-06-23 1983-12-26 Sankyo Dengiyou Kk Sampling pipe
JPH0621011Y2 (en) * 1988-07-19 1994-06-01 日本アルミニウム工業株式会社 Powder sample inspection device
JPH02127417U (en) * 1989-03-31 1990-10-19
JP2505469Y2 (en) * 1990-07-18 1996-07-31 中部電力株式会社 Powder automatic sampling device

Also Published As

Publication number Publication date
JPH06129959A (en) 1994-05-13

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