JPH0548116Y2 - - Google Patents
Info
- Publication number
- JPH0548116Y2 JPH0548116Y2 JP1986044465U JP4446586U JPH0548116Y2 JP H0548116 Y2 JPH0548116 Y2 JP H0548116Y2 JP 1986044465 U JP1986044465 U JP 1986044465U JP 4446586 U JP4446586 U JP 4446586U JP H0548116 Y2 JPH0548116 Y2 JP H0548116Y2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- tank
- cylindrical body
- powder sample
- conduit
- 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
Links
- 239000000843 powder Substances 0.000 claims description 33
- 238000005070 sampling Methods 0.000 claims description 6
- 239000000155 melt Substances 0.000 claims description 4
- 239000011261 inert gas Substances 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims 1
- 229920005989 resin Polymers 0.000 claims 1
- 239000004033 plastic Substances 0.000 description 8
- 229920003023 plastic Polymers 0.000 description 8
- 239000000523 sample Substances 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- 229920001169 thermoplastic Polymers 0.000 description 3
- 239000004416 thermosoftening plastic Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000012815 thermoplastic material Substances 0.000 description 1
Landscapes
- Sampling And Sample Adjustment (AREA)
Description
【考案の詳細な説明】
技術分野
本考案は、メルトインデクサMI計に移送する
被試験粉体サンプルの連続採取装置に関する。[Detailed Description of the Invention] Technical Field The present invention relates to a device for continuously collecting powder samples to be tested to be transferred to a melt indexer MI meter.
従来技術
熱可塑性材の品質管理、または客のニーズに対
応する流動性プラスチツクを供給するため、被試
験対象である熱可塑性プラスチツクもその素性に
より定められた温度と圧力の条件のもとで溶融し
た熱可塑性プラスチツクを規定の長さと直径のダ
イを通して押し出し、押し出し時間10分間で押し
出されるプラスチツクの質量をメルトインデクス
MI値として算出することがJIS等で規定されてい
る。このような非連続的な試験方法に対して連続
工程中で試験するMI計がある。これは、細管内
に試料を圧送し、所定長さの圧力差を一定とする
ように回転数が制御された定量ポンプの回転数と
密度の積からMI値を換算するものであるが、従
来は、第2図に示すように熱可塑性プラスチツク
粉体の形でタンク1内に図示しない移送手段によ
る移送され転送される。この結果、プラスチツク
粉体2は図示のごとくタンク1内の閉止空間内に
山積されている。この山積されたプラスチツク粉
体内には濾斗状に開口してプラスチツク粉体を受
けて落下させる移送管3が配設され、電動機によ
り駆動されるスクリユーを有するミニ押出機4に
よりMI計5に移送される。Prior Art In order to control the quality of thermoplastic materials or to supply fluid plastics that meet customer needs, the thermoplastics to be tested are melted under conditions of temperature and pressure determined by their properties. A thermoplastic is extruded through a die of specified length and diameter, and the mass of plastic extruded in 10 minutes of extrusion time is calculated as the melt index.
It is stipulated by JIS etc. to be calculated as MI value. In contrast to such discontinuous testing methods, there is an MI meter that tests in a continuous process. This method involves converting the MI value from the product of the density and the rotation speed of a metering pump whose rotation speed is controlled to maintain a constant pressure difference over a predetermined length of the sample into a thin tube. As shown in FIG. 2, the powder is transferred into the tank 1 in the form of thermoplastic powder by a transfer means (not shown). As a result, the plastic powder 2 is piled up in the closed space inside the tank 1 as shown in the figure. Inside this pile of plastic powder is a transfer pipe 3 that has a funnel-shaped opening to receive and drop the plastic powder, and is transferred to an MI total 5 by a mini extruder 4 having a screw driven by an electric motor. be done.
従来技術の問題点
上述した従来技術においては、プラスチツク粉
体は自然落下によつて移送するが、濾斗状開口部
の粉体圧が少なく、その上粉体摩擦が大きく、ま
た、移送管3が比較的長く且つ傾斜しているた
め、流動抵抗が大きく、落下しない場合があり、
MI計による連続計測ができないという問題が生
じた。また、粒子も小さいので酸化し易く、正し
いMI値を示さないことがあつた。Problems with the prior art In the above-mentioned prior art, plastic powder is transferred by gravity, but the powder pressure at the funnel-shaped opening is small, powder friction is large, and the transfer pipe 3 Because it is relatively long and sloped, the flow resistance is large and it may not fall.
A problem arose in that continuous measurements using the MI meter were not possible. In addition, since the particles were small, they were easily oxidized and did not show correct MI values.
問題点を解決するための手段
本考案は、粉体圧を大きくとり、常に粉体採取
の抵抗を小さくするためスクリユーにより連続し
て移送可能とし、更に不活性な窒素ガスにより酸
化の防止を計つた。Means to Solve the Problems The present invention has a high powder pressure, allows for continuous transfer using a screw to constantly reduce the resistance to powder collection, and also prevents oxidation using inert nitrogen gas. Ivy.
具体例
第1図は、本考案の一実施例を説明するための
図で、図中、第2図に示した従来例と同一の機能
をするものは第2図の場合と同一の番号を付して
ある。而して、本考案においてはタンク壁面にフ
ランジ35の取付手段によりタンク壁面に直交し
て、タンク内に延びるプローブ31を有する筒状
体30を配設し、この筒状体30のタンク1外部
には電動機36を配し、プローブ31と同軸なス
クリユー33を回転する。粉体は粉体採取口32
により採取され、スクリユー33により移送され
るが、粉体採取口32はプローブ31の周上に複
数個開口されており、略均一した粉体圧を利用し
て大きい開口面積を形成している。なお、このよ
うに開口している粉体採取口32はプローブ周上
複数列、または必要に応じて任意に穿孔してもよ
い。スクリユー33により移送された粉体は筒状
体30のタンク外部に達し、筒状体30と直交し
て連通する導管34内を落下する。この際、導管
34の上部より、粉体の酸化を防ぐ目的で、図示
しない窒素ガス源からバルブ6、調圧弁7を介し
て窒素ガスが噴出される。このようにして落下し
たプラスチツク粉体は従来例に説明したようにし
てミニ押出機4によりMI計5に圧送される。Specific Example Figure 1 is a diagram for explaining one embodiment of the present invention. In the diagram, parts having the same functions as the conventional example shown in Figure 2 are designated by the same numbers as in Figure 2. It is attached. Therefore, in the present invention, a cylindrical body 30 having a probe 31 extending into the tank is disposed perpendicularly to the tank wall surface by means of attachment means of a flange 35 on the tank wall surface, and the cylindrical body 30 is connected to the outside of the tank 1. An electric motor 36 is arranged to rotate a screw 33 coaxial with the probe 31. Powder is collected through powder sampling port 32.
The powder is collected by a screw 33, and a plurality of powder sampling ports 32 are opened around the circumference of the probe 31, and a large opening area is formed by utilizing substantially uniform powder pressure. Note that the powder sampling ports 32 opened in this manner may be formed in multiple rows around the circumference of the probe, or may be formed in any number of rows as required. The powder transferred by the screw 33 reaches the outside of the tank of the cylindrical body 30 and falls through a conduit 34 that communicates orthogonally with the cylindrical body 30 . At this time, nitrogen gas is ejected from the upper part of the conduit 34 from a nitrogen gas source (not shown) via the valve 6 and the pressure regulating valve 7 in order to prevent oxidation of the powder. The plastic powder thus dropped is fed under pressure to the MI meter 5 by the mini extruder 4 as explained in the conventional example.
効 果
本考案においては、プローブ31の粉体採取口
32近傍において粉体圧が均等に印加されてお
り、しかも開口面積も広くなるので流動抵抗も小
さく、更にスクリユーにより圧送されるので粉体
の流動が停止することもなく、連続して移送され
る。なお、連続移送された粉体は窒素ガス等の不
活性ガス雰囲気中にあるので化学的に安定な形を
保持しMI形5により連続MI値の計測ができる。Effects In the present invention, the powder pressure is applied evenly near the powder sampling port 32 of the probe 31, and the opening area is also widened, so the flow resistance is small.Furthermore, since the powder is fed under pressure by the screw, the powder is The flow is continuously transferred without stopping. Note that since the continuously transferred powder is in an inert gas atmosphere such as nitrogen gas, it maintains a chemically stable form and can continuously measure MI values using MI type 5.
第1図は、本案の粉体サンプル採取装置の構成
を示す図、第2図は、従来の構成を示す図であ
る。
1……タンク、2……プラスチツク粉体、30
……筒状体、31……プローブ、32……粉体採
取口、33……スクリユー、5……MI計。
FIG. 1 is a diagram showing the configuration of the powder sample collecting device of the present invention, and FIG. 2 is a diagram showing the conventional configuration. 1...Tank, 2...Plastic powder, 30
... Cylindrical body, 31 ... Probe, 32 ... Powder sampling port, 33 ... Screw, 5 ... MI meter.
Claims (1)
ク壁面を貫通してタンク内に水平に装設され軸方
向及び周方向に複数の粉体採取口を穿孔した筒状
体と、該筒状体の軸方向に配設され前記筒状体内
の粉体サンプルをタンク外方向に回転搬送するス
クリユーと、タンク外に配設され前記筒状体に連
通する垂直な導管と、該導管に連通し前記筒状体
及び導管を介して搬送された粉体サンプルをメル
トインデクサに移送する水平なミニ押出機と、前
記筒状体と導管及びミニ押出機に不活性ガスを圧
送する不活性ガス供給手段とにより構成したこと
を特徴とするメルトインデクサにおける粉体サン
プル採取装置。 A tank for storing a resin powder sample, a cylindrical body that is installed horizontally in the tank through a wall surface of the tank and has a plurality of powder sampling ports perforated in the axial and circumferential directions; a screw disposed in the axial direction for rotating and conveying the powder sample inside the cylindrical body toward the outside of the tank; a vertical conduit disposed outside the tank and communicating with the cylindrical body; a horizontal mini-extruder that transfers the powder sample conveyed through the tube and the conduit to the melt indexer, and an inert gas supply means that pumps an inert gas to the tube and the conduit and the mini-extruder. A powder sample collection device in a melt indexer, characterized by comprising:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1986044465U JPH0548116Y2 (en) | 1986-03-26 | 1986-03-26 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1986044465U JPH0548116Y2 (en) | 1986-03-26 | 1986-03-26 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62156850U JPS62156850U (en) | 1987-10-05 |
JPH0548116Y2 true JPH0548116Y2 (en) | 1993-12-20 |
Family
ID=30862302
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1986044465U Expired - Lifetime JPH0548116Y2 (en) | 1986-03-26 | 1986-03-26 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0548116Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2805752B2 (en) * | 1988-04-05 | 1998-09-30 | 三菱マテリアル株式会社 | Granule sorting device |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4948787A (en) * | 1972-05-12 | 1974-05-11 | ||
JPS6078281A (en) * | 1984-01-24 | 1985-05-02 | 株式会社 サタケ | Extracting device for sample in drier |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55100147U (en) * | 1978-12-29 | 1980-07-12 |
-
1986
- 1986-03-26 JP JP1986044465U patent/JPH0548116Y2/ja not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4948787A (en) * | 1972-05-12 | 1974-05-11 | ||
JPS6078281A (en) * | 1984-01-24 | 1985-05-02 | 株式会社 サタケ | Extracting device for sample in drier |
Also Published As
Publication number | Publication date |
---|---|
JPS62156850U (en) | 1987-10-05 |
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