JPS61134569A - Method of dehydrating powdered and granular body - Google Patents
Method of dehydrating powdered and granular bodyInfo
- Publication number
- JPS61134569A JPS61134569A JP25655984A JP25655984A JPS61134569A JP S61134569 A JPS61134569 A JP S61134569A JP 25655984 A JP25655984 A JP 25655984A JP 25655984 A JP25655984 A JP 25655984A JP S61134569 A JPS61134569 A JP S61134569A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- water
- resin
- dehydrating
- dried
- 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
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、石炭類をはじめ各種鉱石類の粉粒体の湿分を
熱を使用せず、また遠心力等の高速機械力を使用せずに
除去する方法に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention is a method for removing moisture from powder and granules of various ores including coal without using heat and without using high-speed mechanical force such as centrifugal force. This article concerns a method for removing it without removing it.
[従来技術]
従来、粉粒体の脱水・乾燥には粉粒体の粒度に応じて機
械的並びに熱的方法が採られてきた。粉粒体の粒度が非
常に小さくなってくると経費だけでなく、ハンドリング
も非常に面倒なものとなってくる。一般には微粉は多量
の水分を含有し、高い粘性及び付着性をもっているので
、どのような方法で脱水するにも特別な工夫を必要とす
るところである。[Prior Art] Conventionally, mechanical and thermal methods have been used for dehydration and drying of powder and granular materials depending on the particle size of the powder and granular material. When the particle size of the powder material becomes extremely small, it becomes not only expensive but also extremely troublesome to handle. Generally, fine powder contains a large amount of water and has high viscosity and adhesiveness, so special measures are required to dehydrate it by any method.
[目 的]
本発明は、従来法に見られる難点を解決し、吸湿性樹脂
を用いることにより、多量のエネルギーを必要とせず、
樹脂の81費に伴う費用が経済的な粉粒体の脱水方法を
提供することを目的とする。[Purpose] The present invention solves the difficulties seen in conventional methods, and by using a hygroscopic resin, does not require a large amount of energy.
The object of the present invention is to provide a method for dehydrating powder and granular material that is economical in costs associated with resin costs.
[構 成]
本発明は、表面の濡れた粉粒体あるいは固体濃度の高い
スラリーに吸湿性樹脂粉末を混合し、ドラムの回転運動
により、前記の高湿分粉粒体中の水分を該樹脂粉末に移
行せしめて乾燥粉粒体と含水樹脂粉末集合体を分離する
ことを特徴とする粉粒体の脱水方法を提供するものであ
る。[Structure] In the present invention, a hygroscopic resin powder is mixed with a powdery material having a wet surface or a slurry with a high solid concentration, and the moisture in the high-humidity powdery material is removed by the rotational movement of a drum. The present invention provides a method for dehydrating powder and granules, which is characterized by converting the powder into powder and separating dry powder and granules from a water-containing resin powder aggregate.
本発明は、含水微粉中に高吸湿性の樹脂粉末を直接混合
し、微粉が含有する水分を樹脂に吸収させたのち含水樹
脂と乾燥微粉を分離し、樹脂は乾燥して再使用するかあ
るいは吸水状態で畑に散布して畑の乾燥防止に使用する
こともできる。また、従来の脱水法あるいは乾燥法では
処理の厄介な極めて細かい微粉中の水分を簡単な装置で
しかも容易に除去できる。さらに被乾物質に熱をかけず
また大きな力の場をかけることがないのでそれらによる
劣化や破壊がなく、処理時間も短く製品も特に固結性が
強くない限り団塊状にならないので製品を粉砕しないで
済む。また樹脂は被乾物に比べて極めて少量で済み、被
乾物に付着して持ち去られても経済的な損失はほとんど
なく、吸湿後は連続体となって粒度が大きくなるため被
乾物との分離は極めて容易であり、しかも大気の乾燥し
た状態で特に加熱することなく除々に放湿して再利用で
きる。In the present invention, highly hygroscopic resin powder is directly mixed into water-containing fine powder, the water contained in the fine powder is absorbed into the resin, and then the water-containing resin and dry fine powder are separated, and the resin can be dried and reused or It can also be used to prevent fields from drying out by spraying them in a water-absorbing state. In addition, moisture in extremely fine powder, which is difficult to process using conventional dehydration or drying methods, can be easily removed using a simple device. Furthermore, since no heat is applied to the material to be dried and no large force field is applied, there is no deterioration or destruction caused by such materials, and the processing time is short, and the product does not form into lumps unless it has a particularly strong caking property, so the product can be pulverized. You don't have to. In addition, the amount of resin is extremely small compared to the material to be dried, and even if it adheres to the material to be dried and is carried away, there is almost no economic loss.After absorbing moisture, it becomes a continuum and the particle size increases, so it is difficult to separate it from the material to be dried. It is extremely easy to use and can be reused in dry conditions by gradually releasing moisture without heating.
本発明で用いる吸湿性樹脂粉末は、従来公知のものであ
り、一般には、ポリアクリル酸ソーダを主体とするもの
が用いられる。本発明で用いる粉粒体及びスラリー中の
固形分粒子の粒径は特に制約されないが、一般には、0
.5m m以下、好ましくは2〜3mm以下である。ま
た、吸湿性樹脂粉末の粒径は、必要に応じて5〜10m
mまでのものが調整可能である。この吸湿性樹脂粉末
は、水を吸収して相互に結合し、増加された粒径、例え
ば20〜50mmの集合体粒子を形成する。The hygroscopic resin powder used in the present invention is a conventionally known one, and is generally composed mainly of sodium polyacrylate. The particle size of the solid particles in the powder and granular material and slurry used in the present invention is not particularly limited, but is generally 0.
.. It is 5 mm or less, preferably 2 to 3 mm or less. In addition, the particle size of the hygroscopic resin powder may be adjusted from 5 to 10 m as necessary.
It is adjustable up to m. This hygroscopic resin powder absorbs water and bonds with each other to form aggregate particles of increased particle size, for example 20-50 mm.
[実施例]
次に、本発明の実施例を第1図を用いて説明する。原料
としての被乾物である含水微粉1に吸湿粉の接触が生じ
、水が樹脂へと移行するが、時間の経過とともにドラム
内ではこまかい粒子とあらい粒子や比重の重い物質と軽
い物質が運動状態を 1異にするために生ずる一種
の偏析現象があられれ、樹脂の膚と被乾物の層が分離し
てくる。したがって、ドラム内に被乾物と吸湿性樹脂を
混合して回転運動を与えることは、水の移動と物質の分
離という二つの作用を同時に進行させることになる。[Example] Next, an example of the present invention will be described using FIG. 1. The moisture-absorbing powder comes into contact with the water-containing fine powder 1, which is the material to be dried as a raw material, and the water transfers to the resin, but as time passes, fine particles and coarse particles, substances with heavy specific gravity and substances with light specific gravity become in a state of motion inside the drum. A type of segregation phenomenon occurs due to the difference in the amount of water, and the resin layer and the dried material layer separate. Therefore, when the material to be dried and the hygroscopic resin are mixed in the drum and given a rotational motion, the two functions of water movement and substance separation proceed simultaneously.
吸水した樹脂粉末は集合したときには、吸水量がある程
度以上になると互いに結合して造粒体となり、被乾物の
粒度よりも大きくなるので、この時撮動1!!4などを
通すことによって容易に乾燥物と含水樹脂とを分離する
ことができる。被乾物の種類によっては、樹脂と粒度及
び比重が似ていて回転ドラム内で偏析現象が起こらない
場合も考えられるが、そのような場合には樹脂の粒度を
変えるかあるいは布製の袋に樹脂を入れて混入するよう
° にする。When the water-absorbed resin powder aggregates, if the amount of water absorption exceeds a certain level, they combine with each other to form granules, which become larger than the particle size of the material to be dried. ! 4 or the like, the dried material and the water-containing resin can be easily separated. Depending on the type of material to be dried, the particle size and specific gravity may be similar to that of the resin, and segregation may not occur within the rotating drum. In such cases, it is necessary to change the particle size of the resin or place the resin in a cloth bag. Add and stir to mix.
このように吸湿性樹脂粉末を添加することにより加熱等
を行わず常温の操作により被乾物中の水分を低下させる
ことができるのでエネルギー消費量を大巾に低減するこ
とができる。また、前述の樹脂類の粉末は吸水能力が極
めて大であり、自重の数百倍〜千倍程度の水を吸収する
ため被乾物へあるとして概略計算すれば、0.08%程
度の樹脂使用量で済む。樹脂粉末は、原末状態では50
μm程度の微粉であり水に不溶性であり、特殊な場合を
除き被乾物との反応は起こさない。また、樹脂の粒径は
必要に応じて適当に調整することもできる。By adding the hygroscopic resin powder in this manner, it is possible to reduce the moisture content in the dried material by operating at room temperature without heating or the like, and therefore energy consumption can be significantly reduced. In addition, the resin powder mentioned above has extremely high water absorption capacity, and can absorb several hundred to 1,000 times its own weight in water, so if you roughly calculate that it will be in the dry material, the amount of resin used will be about 0.08%. It's all about quantity. The resin powder is 50% in bulk state.
It is a fine powder on the order of μm in size and is insoluble in water, so it does not react with the dried material except in special cases. Further, the particle size of the resin can be adjusted appropriately as necessary.
[効 果]
本発明により含水微粉やスラリー等の脱水や濃縮が比較
的簡単な装置で、低コスト、低エネルギーで行なわれ、
従来の脱水・乾燥等に要した費用を大巾に低減すること
ができるので実用化すれば極めC大きな経済的効果を得
ることが期待できる[Effects] According to the present invention, dehydration and concentration of water-containing fine powder, slurry, etc. can be performed with a relatively simple device, at low cost, and with low energy.
The cost required for conventional dehydration and drying can be significantly reduced, so if it is put into practical use, it can be expected to have an extremely large economic effect.
図面は本発明の実施例のフローシートである。 1・・・被乾物含水微粉 2・・・吸湿性樹脂粉末 The drawing is a flow sheet of an embodiment of the present invention. 1... Dry matter hydrated fine powder 2...Hygroscopic resin powder
Claims (1)
リーに吸湿性樹脂粉末を混合し、ドラムの回転運動によ
り、前記の高湿分粉粒体中の水分を該樹脂粉末に移行せ
しめて乾燥粉粒体と含水樹脂粉末集合体を分離すること
を特徴とする粉粒体の脱水方法。(1) A hygroscopic resin powder is mixed with a powdery material with a wet surface or a slurry with a high solid concentration, and the water in the high-humidity powdery material is transferred to the resin powder by the rotational movement of a drum. A method for dehydrating a powder or granule material, the method comprising separating a dry powder or granule material from a water-containing resin powder aggregate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25655984A JPS61134569A (en) | 1984-12-06 | 1984-12-06 | Method of dehydrating powdered and granular body |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25655984A JPS61134569A (en) | 1984-12-06 | 1984-12-06 | Method of dehydrating powdered and granular body |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61134569A true JPS61134569A (en) | 1986-06-21 |
Family
ID=17294318
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25655984A Pending JPS61134569A (en) | 1984-12-06 | 1984-12-06 | Method of dehydrating powdered and granular body |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61134569A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63134008A (en) * | 1986-11-25 | 1988-06-06 | Nippon Steel Corp | Method for removing water in particulate matter |
JP2013544299A (en) * | 2010-11-09 | 2013-12-12 | ロス テクノロジー コーポレーション. | Method and composition for drying coal |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4918305U (en) * | 1972-05-17 | 1974-02-16 |
-
1984
- 1984-12-06 JP JP25655984A patent/JPS61134569A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4918305U (en) * | 1972-05-17 | 1974-02-16 |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63134008A (en) * | 1986-11-25 | 1988-06-06 | Nippon Steel Corp | Method for removing water in particulate matter |
JP2013544299A (en) * | 2010-11-09 | 2013-12-12 | ロス テクノロジー コーポレーション. | Method and composition for drying coal |
AU2010363641B2 (en) * | 2010-11-09 | 2016-10-20 | Ross Technology Corporation | Methods and compositions for drying coal |
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