JPH01254233A - Prevention of segregation-separation of powdery material - Google Patents

Prevention of segregation-separation of powdery material

Info

Publication number
JPH01254233A
JPH01254233A JP63080255A JP8025588A JPH01254233A JP H01254233 A JPH01254233 A JP H01254233A JP 63080255 A JP63080255 A JP 63080255A JP 8025588 A JP8025588 A JP 8025588A JP H01254233 A JPH01254233 A JP H01254233A
Authority
JP
Japan
Prior art keywords
powder
segregation
mixture
fibers
separation
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
JP63080255A
Other languages
Japanese (ja)
Inventor
Teruo Urano
輝男 浦野
Hiroshi Miyaji
宮路 寛
Tetsuya Shimoda
哲也 下田
Katsuaki Ishikawa
石川 勝章
Masatsune Ogura
正恒 小倉
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.)
Murakashi Lime Industry Co Ltd
Nikko Corp Ltd
Chemours Mitsui Fluoroproducts Co Ltd
Original Assignee
Nippon Hodo Co Ltd
Du Pont Mitsui Fluorochemicals Co Ltd
Murakashi Lime Industry 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 Nippon Hodo Co Ltd, Du Pont Mitsui Fluorochemicals Co Ltd, Murakashi Lime Industry Co Ltd filed Critical Nippon Hodo Co Ltd
Priority to JP63080255A priority Critical patent/JPH01254233A/en
Publication of JPH01254233A publication Critical patent/JPH01254233A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/60Mixing solids with solids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

PURPOSE:To prevent segregation-separation phenomena such as density difference, grain size difference, etc., and to obtain a homogeneous powder by dispersing fine diameter fibers in the powder. CONSTITUTION:Fine diameter fibers such as polytetrafluoroethylene fibrin of 100mum or smaller in diameter are dispersed in powder, especially when a mixture of not less than two kinds of powder is to be obtained, whose grain size distributions, densities, etc., are different from one another. This polytetrafluoroethylene fibrin is chemically inactive, water repellent and has properties low in friction factor and high in non-stickiness. It is possible, therefore, to prevent segregation-separations of particles and to obtain a homogeneous powder.

Description

【発明の詳細な説明】 −の1 本発明は、粉粒体における比重差、粒度差等による偏析
分離現象を防止する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION -1 The present invention relates to a method for preventing segregation and separation phenomena due to differences in specific gravity, differences in particle size, etc. in granular materials.

従Jlu、虹術 粉粒体の流動を伴なう操作において、粒度か比較的粗い
部分と細かい部分とに分かれる現象を粒度偏析と呼ぶ。
In operations involving the flow of powder particles, the phenomenon in which the particle size is divided into relatively coarse portions and fine portions is called particle size segregation.

粒度偏析は閉じた容器内又は厚い粉体層内で粒子が流動
又は振動させられた時にも発生するか、最も著しいのは
粉体か開放面を有して流動する場合である。
Particle size segregation can also occur when particles are flowed or vibrated in a closed container or thick powder bed, or most significantly when the powder is flowed with open surfaces.

さらに、2種類以上の異質な粉粒体の混合物を得ようと
するとき、粉粒体の性質か似かよフている場合には比較
的均質な混合物を得ることかてきるか、粒度分布、密度
、カサ比重、粒子形状、充填特性、流動性、付着性等の
諸性質か異なる粉粒体の混合物を得るには、ミキサーて
の混合時は勿論、貯蔵、輸送1袋詰などの操作で均質状
態からの偏析分離がしばしば重大な問題となっている。
Furthermore, when trying to obtain a mixture of two or more different types of powder and granules, if the properties of the powders and granules are similar, is it possible to obtain a relatively homogeneous mixture? To obtain a mixture of powders and granules with different properties such as density, bulk specific gravity, particle shape, filling characteristics, fluidity, and adhesion, it is possible to obtain a mixture of powders and granules with different properties such as density, bulk specific gravity, particle shape, filling characteristics, fluidity, and adhesion. Segregation from homogeneous conditions is often a serious problem.

特に、比重差の大きい粉粒体や粒度分布か比較的広い粉
粒体同志の場合、均一な混合か難しいばかりでなく、混
合物の貯槽内ての偏析分離が生じやすい。
In particular, in the case of powders with a large difference in specific gravity or particles with a relatively wide particle size distribution, it is not only difficult to mix them uniformly, but also segregation is likely to occur in the mixture storage tank.

異質の粉粒体混合物は、粒度偏析による分離の他、比重
差による分離は一層助長される。これらの分離現象を完
全に防止するのは困難である。
In addition to separation due to particle size segregation, separation due to differences in specific gravity is further promoted in heterogeneous powder mixtures. It is difficult to completely prevent these separation phenomena.

例えば貯蔵においては、サイロへの投入に当り混合物を
ただ単にサイロ上部から落下させるのでなく、シュート
を用いたり、分配器、円錐を用いてリング状に堆積させ
たり、サイロ内に細かく隔室を設けたり、サイロの直径
を小さくし細長い円筒形にしている。また、サイロから
の引き出しに当っても底部に円錐を入れたり、スクリュ
ーフィーダー、ロータリーバルブ等の混合作用を付与さ
せた輸送機を利用するなどの考慮を払っている。
For example, in storage, rather than simply letting the mixture fall from the top of the silo, the mixture may be deposited in a ring shape using a chute, distributor, or cone, or fine compartments may be created within the silo. Or, the diameter of the silo is reduced to make it elongated and cylindrical. In addition, when extracting from the silo, consideration is given to placing a cone in the bottom and using a transport device with a mixing function such as a screw feeder or rotary valve.

しかし、ダンプトラック等による輸送や、袋詰された後
などではその対策が困難で、特に袋詰製品の一部を取出
して使用する場合などでは、分離現象の大きい混合物で
はその影響が大きい。
However, countermeasures against this problem are difficult when the product is transported by dump truck or the like, or after it has been packed in bags, and especially when a part of the packaged product is taken out and used, the effect of this problem is large for mixtures that have a large separation phenomenon.

が  しよ゛と  。 占 本発明は、上記のような問題点を解決し、偏析分離を防
止して均質な粉粒体を得る方法を提供することを目的と
する。
I said, ``I'll do it.'' SUMMARY OF THE INVENTION It is an object of the present invention to solve the above-mentioned problems and provide a method for obtaining homogeneous granular material by preventing segregation.

U古t    た の゛ 本発明による粉粒体の偏析分離防止方法は、粉粒体に微
細径繊維を分散することを特徴とする。
The method for preventing segregation and separation of powder and granular material according to the present invention is characterized by dispersing fine diameter fibers in the powder and granular material.

微細径繊維としては、その直径が1100μm以下のも
のを使用することが好ましい。
It is preferable to use fine diameter fibers having a diameter of 1100 μm or less.

直径が微細であればあるほど、少量の使用で高い偏析分
離効果を得ることができる。
The finer the diameter, the higher the segregation separation effect can be obtained with a smaller amount.

例えば、ポリプロピレン繊維、ポリエチレン繊維、ビニ
ロン繊維などの各種の化学繊維を使用することができる
が、特に、非常に径の小さいポリテトラフルオロエチレ
ンフィブリルを使用することが好ましい。
For example, various chemical fibers such as polypropylene fibers, polyethylene fibers, and vinylon fibers can be used, but it is particularly preferable to use polytetrafluoroethylene fibrils having a very small diameter.

ポリテトラフルオロエチレン(以下PTFEと言う)は
化学的に不活性て、撥水性であり、摩擦係数が低く、非
粘着性が高いなど特異な性質を有している。またPTF
Eは適当な温度条件(50℃以上320℃以下)ではフ
ィブリル(繊維)化し易く、その直径は数十λ程度と非
常に微細なものである。
Polytetrafluoroethylene (hereinafter referred to as PTFE) has unique properties such as being chemically inert, water repellent, having a low coefficient of friction, and being highly non-adhesive. Also PTF
E easily forms into fibrils (fibers) under appropriate temperature conditions (50° C. or higher and 320° C. or lower), and the diameter thereof is very fine, on the order of several tens of λ.

粉粒体にPTFEフィブリルを分散する具体的手段とし
ては、乳化重合により得られるPTFE粒子を対象とす
る粉粒体混合物に混合し、この混合物に通常50〜20
0℃の温度で圧縮−剪断作用を施こすと、PTFE粒子
はフィブリル化して粉粒体中に分散する。
As a specific means for dispersing PTFE fibrils in powder, PTFE particles obtained by emulsion polymerization are mixed into a target powder mixture, and this mixture is usually mixed with 50 to 20
When subjected to compression-shear action at a temperature of 0°C, the PTFE particles fibrillate and are dispersed in the powder.

既に繊維状になっている微細径繊維を分散する場合には
、単なる混合操作でよい。
When dispersing fine-diameter fibers that are already in the form of fibers, a simple mixing operation is sufficient.

本発明は、広い粒度分布を有する1種類の物質の粉粒体
に対しても有効であるが、さらに、比較的大きな比重差
を有する2種類以上の物質の粉粒体の混合物の偏析防止
に特に顕著な効果を発揮する。
The present invention is effective not only for powders of one type of substance having a wide particle size distribution, but also for preventing segregation of mixtures of powders and granules of two or more substances having a relatively large difference in specific gravity. Especially effective.

微細径繊維の必要添加量は、粉粒体の密度(混合物の場
合は密度差)、カサ比重(混合物の場合はカサ比重差)
、粒子形状1粒径分布等によっても異なるが、特に分散
する繊維の径によって大きく異なる0例えば直径がlO
〜looILm程度の繊維の場合は対象とする粉粒体に
対して0.2〜゛ 1重量%程度添加することが好まし
いが、直径が数十λ程度のPTFEフィブリルの場合は
一桁少ない量、即ち0.O1〜0.2重量%程度で同等
以上の効果な発揮する。
The required amount of fine-diameter fibers to be added is determined by the density of the powder (density difference in the case of a mixture), bulk specific gravity (bulk specific gravity difference in the case of a mixture)
, particle shape 1 Although it varies depending on the particle size distribution etc., it varies greatly depending on the diameter of the fibers to be dispersed. For example, the diameter is lO
In the case of fibers with a diameter of ~looILm, it is preferable to add about 0.2 to 1% by weight to the target powder, but in the case of PTFE fibrils with a diameter of several tens of lambda, the amount is one order of magnitude smaller. That is, 0. At about 1 to 0.2% by weight of O, the same or better effect is exhibited.

具体的には、粉粒体を最終的に使用するまでに与えられ
る振動や衝撃を考慮して実験的に定めればよい。
Specifically, it may be determined experimentally by taking into consideration the vibrations and shocks given to the powder or granular material until it is finally used.

1月 粉粒体の個々の粒子は、分散された微細径繊維により拘
束され流動性が低下しているので、輸送時に振動や衝撃
を与えらえれても偏析分離現象を起こしにくくなるもの
と思われる。
Since the individual particles of January powder are restrained by the dispersed fine-diameter fibers and have reduced fluidity, it is thought that they will be less likely to cause segregation even if subjected to vibration or impact during transportation. It will be done.

以下実施例により本発明を具体的に説明する。The present invention will be specifically explained below using Examples.

実施例1 普通ポルトランドセメント(見掛比重1.260)8.
5kgに対して黒耀石系パーライト(見掛比重0.07
4)1.5kgを添加し、さらに上記粉末合計1110
kgに対してPTFE水性懸濁液(PTFE樹脂固形分
30重量%)16.7g、即ちPTFE固形分5g相当
を添加し1分間ミキサーで混合した。この混合物を加温
しlOOoCとしたのち再度ミキサーで1分間混合した
Example 1 Ordinary Portland cement (apparent specific gravity 1.260)8.
perlite based on 5 kg (apparent specific gravity 0.07
4) Added 1.5 kg and further added the above powder to a total of 1110 kg.
16.7 g of PTFE aqueous suspension (PTFE resin solid content: 30% by weight), equivalent to 5 g of PTFE solid content, was added per kg, and mixed for 1 minute with a mixer. This mixture was heated to lOOoC and mixed again for 1 minute using a mixer.

この混合物について、セメントとパーライトか均質な分
散状態を保持しているどうかを確認するため、混合物1
kgを取り、内径100 m m、長さ300mmの円
筒容器に入れ、コンクリート床面より50mm持ち上げ
、そのまま手を離し、20回落下衝撃を加え、円筒容器
の上層部と下層部とに分け、それぞれの見掛比重を測定
した。
In order to confirm whether or not the cement and pearlite were homogeneously dispersed in this mixture,
kg, put it in a cylindrical container with an inner diameter of 100 mm and a length of 300 mm, lift it 50 mm above the concrete floor, let go of it, apply a drop impact 20 times, divide it into the upper and lower parts of the cylindrical container, and separate them into the upper and lower parts. The apparent specific gravity was measured.

またPTFEを添加せずに、実施例1と同様にして上記
セメントとパーライトを混合したサンプルについても同
様な試験を行った。
A similar test was also conducted on a sample in which the cement and pearlite were mixed in the same manner as in Example 1 without adding PTFE.

試験結果を第1表に示す。The test results are shown in Table 1.

PTFEフィブリルを分散させない通常の混合では、パ
ーライト粒子が軽いために混合後衝撃を与えると比重の
異なる粒子が容易に分離してしまい、粉粒体混合物の組
成を均一に保つことは難しい。
In normal mixing without dispersing PTFE fibrils, since the pearlite particles are light, if an impact is applied after mixing, particles with different specific gravity easily separate, making it difficult to maintain a uniform composition of the powder mixture.

一方本発明によりPTFEフィブリルを分散させた混合
物では、上層部でも下層部でも見掛比重が殆ど変化して
おらず、偏析分離現象が抑制されていることが認められ
た。
On the other hand, in the mixture in which PTFE fibrils were dispersed according to the present invention, the apparent specific gravity hardly changed in both the upper layer and the lower layer, and it was observed that the segregation phenomenon was suppressed.

実施例2 実施例1と同様に、普通ポルトランドセメント5.0k
gに対し消石灰(見掛比重0.562)5.0kgの混
合物にPTFE水性懸濁液(PTFE樹脂固形分30重
量%)18.7g、即ちPTFE固形分5g相当を添加
し、130″Cに加熱してPTFEをフィブリル化し粉
体中に分散し、実施例1と同一の要領で粉体の偏析試験
を行なった。
Example 2 Same as Example 1, ordinary Portland cement 5.0k
18.7 g of PTFE aqueous suspension (PTFE resin solid content 30% by weight), equivalent to 5 g of PTFE solid content, was added to a mixture of 5.0 kg of slaked lime (apparent specific gravity 0.562), and heated to 130''C. The PTFE was heated to fibrillate and dispersed in the powder, and the powder was subjected to a segregation test in the same manner as in Example 1.

なお、混合度合は混合物を化学分析し5if2の量て比
較した。結果を第2表に示す。
The degree of mixing was determined by chemically analyzing the mixture and comparing the amount of 5if2. The results are shown in Table 2.

(以下余白) 第  2  表 なお、セメント中の5iOz 22.2%で、消石灰中
のSiO2は0.3%であった。従って平均値は11.
25%である。
(Margin below) Table 2 Note that 5iOz in the cement was 22.2%, and SiO2 in the slaked lime was 0.3%. Therefore, the average value is 11.
It is 25%.

PTFEフィブリルを粉体混合物中に分散した場合、粉
粒体の比重差による分離防止に有効であることか明らか
である。
It is clear that when PTFE fibrils are dispersed in a powder mixture, it is effective in preventing separation of powder and granules due to differences in specific gravity.

実施例3 黒耀石系パーライト100gにPTFE水性懸濁液(P
TFE固形分30瓜量%)を、PTFE固形分が0.0
5重量%になるように添加し1分間ミキサーで混合した
。この混合物を加温し100°Cとしたのち再度ミキサ
ーでlり間混合した。
Example 3 PTFE aqueous suspension (P
TFE solid content 30%), PTFE solid content 0.0
It was added to a concentration of 5% by weight and mixed for 1 minute using a mixer. This mixture was heated to 100°C and then mixed again with a mixer for 1 minute.

この混合物を内径100mm、長さ300 m mの円
筒容器に入れ、コンクリート床面より50mm持ち上げ
、そのまま手を離し、20回落下衝撃を加えた後、円筒
容器の内容物を下の方から■、■、■、■、■の5ブロ
ツクに等分し、それぞれを篩分けして粒度分布を測定し
た。
This mixture was placed in a cylindrical container with an inner diameter of 100 mm and a length of 300 mm, lifted 50 mm above the concrete floor, released and subjected to 20 drops, and then the contents of the cylindrical container were poured from the bottom. It was equally divided into 5 blocks (2), (2), (2), and (3), and each block was sieved to measure the particle size distribution.

またPTFEを添加しないものについても同様な試験を
行った。試験結果を第3表に示す。
A similar test was also conducted on a material to which PTFE was not added. The test results are shown in Table 3.

第3表 PTFEを添加してPTFEフィブリルを分散させた場
合は、無添加の場合に比較して偏析分離が抑制されてい
る。
Table 3 When PTFE is added to disperse PTFE fibrils, segregation is suppressed compared to when no addition is made.

実施例4 黒曜石系パーライト100gに直径50.Bm、長さ3
.0mmのポリプロピレン繊維を0.5重量%添加し、
1分間ミキサーで混合した。
Example 4 100g of obsidian pearlite with a diameter of 50mm. Bm, length 3
.. Adding 0.5% by weight of 0mm polypropylene fibers,
Mixed with a mixer for 1 minute.

この混合物を内径100mm、長さ300mmの円筒容
器に入れ、コンクリート床面より50mm持ち上げ、そ
のまま手を離し、20回落下衝撃を加えた後1円筒容器
の内容物を下の方から■、■、■、■の4ブロツクに等
分し、それぞれを篩分けして粒度分布を測定した。試験
結果を第4表に示す。
Put this mixture into a cylindrical container with an inner diameter of 100 mm and a length of 300 mm, lift it 50 mm above the concrete floor, let go of it, apply a drop impact 20 times, and then pour out the contents of the cylindrical container from the bottom ■, ■, It was equally divided into four blocks (1) and (2), and each block was sieved to measure the particle size distribution. The test results are shown in Table 4.

(以下余白) 第4表 使用量は多く必要とするか、ポリプロピレン繊維を分散
することによっても粉粒体の偏析が抑制されている。
(The following is a blank space) Table 4 Segregation of powder particles is suppressed by requiring a large amount of use or by dispersing polypropylene fibers.

実施例5 ポリプロピレン繊維の代りに直8!lO〜100gm、
長さ2.2mmのポリエチレン繊維(三井石油化学婚製
)を0.5重量%使用した以外は実施例4と同様な試験
を行った。試験結果を第5表に示す。
Example 5 Direct 8 instead of polypropylene fiber! lO~100gm,
The same test as in Example 4 was conducted except that 0.5% by weight of polyethylene fibers having a length of 2.2 mm (manufactured by Mitsui Petroleum Chemical Industry Co., Ltd.) were used. The test results are shown in Table 5.

(以下余白) 第  5  表 使用量は多く必要とするか、ポリエチレン繊維を分散す
ることによっても粉粒体の偏析が抑制されている。
(The following is a blank space) Table 5 Segregation of powder particles is suppressed by requiring a large amount of use or by dispersing polyethylene fibers.

実施例6 ポリプロピレン繊維の代りに直径18pm、長さ3.0
mmのビニロン繊!I(ユニチカ化成■製AA2・4D
)を0.5重量%使用した以外は実施例4と同様な試験
を行った。試験結果を第6表に示す。
Example 6 Instead of polypropylene fibers, diameter 18 pm and length 3.0
mm vinylon fiber! I (Unitika Kasei ■AA2/4D
) was used in an amount of 0.5% by weight, but the same test as in Example 4 was conducted. The test results are shown in Table 6.

(以下余白) 第  6  表 ビニロン繊維を分散することによっても粉粒体の偏析か
抑制されている。
(The following is a blank space) Table 6 Segregation of powder particles is also suppressed by dispersing vinylon fibers.

i更曵亘1 粉粒体又はそれらの混合物における比重差、粒度差等に
よる偏析分離現象を効果的に防止することかでき、均質
な粉粒体を得ることができる。
1. It is possible to effectively prevent segregation and separation phenomena due to differences in specific gravity, particle size, etc. in granular materials or mixtures thereof, and it is possible to obtain homogeneous granular materials.

Claims (1)

【特許請求の範囲】 1 粉粒体に微細径繊維を分散することを特徴とする粉
粒体の偏析分離防止方法。 2 粉粒体が異なる物質の粉粒体の混合物である特許請
求の範囲第1項記載の粉粒体の偏析分離防止方法。 3 微細径繊維の直径が100μm以下である特許請求
の範囲第1項又は第2項記載の粉粒体の偏析分離防止方
法。 4 微細径繊維がポリテトラフルオロエチレンフィブリ
ルである特許請求の範囲第3項記載の粉粒体の偏析分離
防止方法。
[Scope of Claims] 1. A method for preventing segregation and separation of powder and granular material, which comprises dispersing fine diameter fibers in powder and granular material. 2. The method for preventing segregation and separation of powder and granular material according to claim 1, wherein the powder and granular material is a mixture of powder and granular materials of different substances. 3. The method for preventing segregation of powder or granular material according to claim 1 or 2, wherein the fine diameter fibers have a diameter of 100 μm or less. 4. The method for preventing segregation of powder or granular material according to claim 3, wherein the fine diameter fibers are polytetrafluoroethylene fibrils.
JP63080255A 1988-04-02 1988-04-02 Prevention of segregation-separation of powdery material Pending JPH01254233A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63080255A JPH01254233A (en) 1988-04-02 1988-04-02 Prevention of segregation-separation of powdery material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63080255A JPH01254233A (en) 1988-04-02 1988-04-02 Prevention of segregation-separation of powdery material

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JPH01254233A true JPH01254233A (en) 1989-10-11

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JP63080255A Pending JPH01254233A (en) 1988-04-02 1988-04-02 Prevention of segregation-separation of powdery material

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