JP3068909B2 - Floatator - Google Patents
FloatatorInfo
- Publication number
- JP3068909B2 JP3068909B2 JP24404791A JP24404791A JP3068909B2 JP 3068909 B2 JP3068909 B2 JP 3068909B2 JP 24404791 A JP24404791 A JP 24404791A JP 24404791 A JP24404791 A JP 24404791A JP 3068909 B2 JP3068909 B2 JP 3068909B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- tank body
- ink
- draft tube
- air
- 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
- 239000002994 raw material Substances 0.000 claims description 40
- 241000628997 Flos Species 0.000 claims description 18
- 238000011084 recovery Methods 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 description 13
- 230000000694 effects Effects 0.000 description 8
- 208000034699 Vitreous floaters Diseases 0.000 description 6
- 239000000835 fiber Substances 0.000 description 5
- 238000007667 floating Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 239000002761 deinking Substances 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- 238000007639 printing Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Landscapes
- Crushing And Pulverization Processes (AREA)
- Paper (AREA)
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、新聞、雑誌、その他の
各種印刷物などの古紙の脱墨処理において、原料と分散
されたインキ粒子等の微粒子を浮上選別するためのフロ
ーテータに関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a flotator for flotation and separation of fine particles such as ink particles dispersed in a raw material in a deinking process of used paper such as newspapers, magazines and other various printed materials. .
【0002】[0002]
【従来の技術】従来、古紙の脱墨処理において、分散さ
れたインキ粒子を除去するには、一般にフローテータが
用いられている。このフローテータは、吹き込まれた空
気の気泡に分散されたインキ粒子を付着させて浮上選別
し、フロスとして排出するものであるが、浮上選別効果
を高めるためには、吹込み空気量を多くし、しかも気泡
を微細化することが好ましい。しかるに、吹込み空気量
を多くすれば大きな気泡が発生しやすいから、多量の空
気をできるだけ微細な気泡とするために、空気吹込機構
に種々の改良が行われている。また、フローテータによ
るインキ粒子の浮上選別の前処理として、原料の離解と
印刷インキの剥離、分散が必要であり、この前処理の良
否もフローテータのインキ除去効果に及ぼす影響が大き
い。2. Description of the Related Art Conventionally, a flotator is generally used to remove dispersed ink particles in the deinking treatment of waste paper. This flotator attaches dispersed ink particles to the air bubbles that are blown in, floats and sorts it, and discharges it as floss.In order to enhance the floating sorting effect, increase the amount of blown air. Moreover, it is preferable to make the air bubbles fine. However, if the amount of air to be blown in is increased, large air bubbles are likely to be generated. Therefore, various improvements have been made to the air blowing mechanism in order to make a large amount of air as fine as possible. In addition, as a pretreatment for the floating separation of the ink particles by the floatator, it is necessary to disintegrate the raw materials and to separate and disperse the printing ink, and the quality of the pretreatment greatly affects the ink removing effect of the floatator.
【0003】[0003]
【発明が解決しようとする課題】本発明は、フローテー
タに吹き込まれた空気の気泡を微細化すると同時に原料
からのインキを剥離、分散させる機能を付与し、高イン
キ除去率、原料の高明度、高白色度効果を達成できるフ
ローテータを提供することを目的とするものである。DISCLOSURE OF THE INVENTION The present invention provides a function of removing and dispersing ink from a raw material at the same time as making air bubbles blown into a flotator finer, and providing a high ink removal rate and a high lightness of the raw material. It is an object of the present invention to provide a flotator capable of achieving a high whiteness effect.
【0004】[0004]
【課題を解決するための手段】本発明は、槽体の底部中
央に原料と空気の供給口を設け、該供給口の周囲に昇降
自在に磨砕刃を配備するとともに、供給口の上部に前記
磨砕刃に対向する磨砕刃を固定したロータを設け、さら
に槽体の上部にフロス排出部を、その下部液面下に原料
回収部をそれぞれ設けたことを特徴とするフローテータ
であり、また前記原料回収部に回収される原料の一部を
前記供給口に循環する循環路を開口したこと、あるいは
前記槽体内中心部にドラフトチューブと該ドラフトチュ
ーブの外周間に流路を形成する外筒とを相対的に昇降自
在に配備したことを特徴とするものである。According to the present invention, a supply port for raw material and air is provided at the center of the bottom of the tank body, and a grinding blade is provided around the supply port so as to be able to move up and down. A flotator characterized in that a rotor having a grinding blade opposed to the grinding blade is provided, a floss discharge part is further provided in an upper part of a tank body, and a raw material recovery part is provided below a lower liquid level thereof. In addition, a circulation path that circulates a part of the raw material recovered by the raw material recovery unit to the supply port is opened, or a flow path is formed between a draft tube and an outer periphery of the draft tube in the center of the tank. It is characterized in that the outer cylinder is relatively vertically movable.
【0005】[0005]
【作用】前処理によって離解と印刷インキの剥離、分散
が行われた原料は、空気とともに供給口から槽体内底部
中央に供給されるが、供給口周囲の磨砕刃を昇降させて
ロータに固定された磨砕刃との間隙を調整することによ
り、気泡を微細化すると同時に繊維表面に強力な剪断力
を与え、繊維表面に附着している汚れや、インキ粒子を
剥離、分散させ、微細化された気泡、原料及びインキ粒
子を十分に混合する。次いで微細気泡は、インキ粒子に
付着して浮上し、液面にフロスを形成し、このフロスを
フロス排出部からバキューム等により排出し、インキが
分離された原料はその下部液面下の原料回収部から回収
される。[Function] The raw material, which has been disaggregated and the printing ink is separated and dispersed by pretreatment, is supplied from the supply port to the center of the bottom of the tank together with air. By adjusting the gap with the crushed blade, the bubbles are made finer, and at the same time a strong shearing force is applied to the fiber surface, and the dirt and ink particles attached to the fiber surface are peeled and dispersed to make them finer. The air bubbles, raw materials and ink particles thus obtained are thoroughly mixed. Next, the fine bubbles adhere to the ink particles and float up to form floss on the liquid surface. The floss is discharged from the floss discharge portion by vacuum or the like, and the raw material from which the ink has been separated is recovered under the lower liquid surface. Collected from department.
【0006】また、原料回収部から回収される原料の一
部を、循環路を経て供給口へ循環させることによってフ
ローテータにおける滞留時間を長くすることも好まし
く、高インキ除去率、原料の高明度、高白色度効果が一
層向上する。[0006] It is also preferable to extend the residence time in the flotator by circulating a part of the raw material recovered from the raw material recovery section through a circulation path to a supply port, thereby achieving a high ink removal rate and a high lightness of the raw material. The effect of high whiteness is further improved.
【0007】さらに、槽体内中心部にドラフトチューブ
と、このドラフトチューブの外周間に流路を形成する外
筒とを相対的に昇降自在に配備することにより、ドラフ
トチューブを介して循環流を生起させて気泡によるイン
キ粒子の捕捉作用を促進し、また供給される原料中に含
まれる界面活性剤等の薬品の種類や量、あるいは空気量
等によって、ドラフトチューブ及び外筒の上下位置を調
整し、フロスの分離を確実にする。[0007] Further, by arranging a draft tube and an outer cylinder forming a flow path between the outer circumferences of the draft tube at the center of the tank body so as to be able to move up and down relatively, a circulating flow is generated via the draft tube. This promotes the effect of trapping ink particles by air bubbles, and also adjusts the vertical position of the draft tube and outer cylinder according to the type and amount of chemicals such as surfactants contained in the supplied raw material, or the amount of air. , Ensure floss separation.
【0008】なお、前記の各フローテータを直列多段に
連結して使用することも極めて効果があり、その場合に
は各フローテータに空気を供給する。[0008] It is also extremely effective to use the above-mentioned respective floaters connected in series and in multiple stages, in which case air is supplied to the respective floaters.
【0009】[0009]
【実施例】以下に本発明の実施例を図面を参照しながら
説明する。図1において、槽体1の底部中央には、原料
入口2と空気入口3とを備えた供給管4が開口し、供給
管4の開口部の周囲には磨砕刃5が配備され、磨砕刃5
はハンドル6によって昇降自在となっている。供給管4
内には、ベルトによって駆動されるプーリー7によって
回転する回転軸8が貫通され、槽体1内の端部にロータ
9が固定され、ロータ9の下面に磨砕刃5に対向する磨
砕刃10が固定されている。前記磨砕刃5,10として
は、各種形状のものが使用できるが、例えば図2に示す
ように、多数のランダム方向の凹凸をもったディスク状
のものが好ましい。また、前記槽体1の上部には、液面
に浮上したフロスをバキュームで捕集、排出するための
フロス排出部11が設けられ、槽体1の液面下には原料
回収口12が開口されている。このようなフローテータ
では、原料及び空気が供給管4から槽体1内の底部中央
に供給され、ハンドル6による磨砕刃5の昇降によって
調整された磨砕刃5とロータ9側の磨砕刃10との間隙
を通過する時に、ロータ9の回転によって気泡が微細化
されると同時に、供給された原料中に含まれる繊維に附
着したインキが剥離され、更に繊維表面の汚れも取り除
かれ、磨砕盤間の強力な乱流によって微細気泡と原料及
びインキ粒子とが十分に混合される。次いで、微細気泡
は分散されたインキ粒子に付着して浮上し、液面にフロ
スを形成する。このフロスは、バキュームによりフロス
排出部11に捕集、排出され、インキが除去された原料
は原料回収口12から回収される。Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, a supply pipe 4 having a raw material inlet 2 and an air inlet 3 is opened in the center of the bottom of the tank body 1, and a grinding blade 5 is provided around the opening of the supply pipe 4, Crushing blade 5
Is movable up and down by a handle 6. Supply pipe 4
A rotating shaft 8 that is rotated by a pulley 7 driven by a belt penetrates the inside, a rotor 9 is fixed to an end in the tank body 1, and a grinding blade opposed to the grinding blade 5 is provided on a lower surface of the rotor 9. 10 is fixed. As the grinding blades 5 and 10, various shapes can be used. For example, as shown in FIG. 2, a disk shape having a large number of irregularities in random directions is preferable. Further, a floss discharge unit 11 for collecting and discharging the floss floating on the liquid surface by vacuum is provided at an upper part of the tank body 1, and a raw material recovery port 12 is opened below the liquid level of the tank body 1. Have been. In such a flotator, the raw material and air are supplied from the supply pipe 4 to the center of the bottom inside the tank body 1 and the grinding blade 5 adjusted by raising and lowering the grinding blade 5 by the handle 6 and the grinding on the rotor 9 side. When the air passes through the gap with the blade 10, the air bubbles are made finer by the rotation of the rotor 9, and at the same time, the ink attached to the fibers contained in the supplied raw material is peeled off, and the dirt on the fiber surface is further removed. Due to the strong turbulence between the attritors, the fine bubbles and the raw materials and ink particles are sufficiently mixed. Next, the fine bubbles adhere to the dispersed ink particles and float, forming floss on the liquid surface. This floss is collected and discharged to the floss discharge section 11 by vacuum, and the raw material from which the ink has been removed is recovered from the raw material recovery port 12.
【0010】また、図1に示すように、原料回収口12
と供給管4の間を弁13を有する循環配管14で連通
し、原料回収口12から回収される原料の一部、例えば
1/3程度を再び供給管4中に循環させるようにすれ
ば、原料中に残るインキ粒子は再びフローテーション作
用を受けることができ、インキ除去率が向上し、前記の
ような直列多段使用の際の段数を減らすことができる。Also, as shown in FIG.
And the supply pipe 4 are communicated by a circulation pipe 14 having a valve 13, and a part of the raw material recovered from the raw material recovery port 12, for example, about 3, is circulated through the supply pipe 4 again. The ink particles remaining in the raw material can be subjected to the flotation effect again, so that the ink removal rate can be improved, and the number of stages in the case of using multiple stages in series as described above can be reduced.
【0011】これらのフローテータにより、インキ除去
率を高めるには、複数のフローテータを用い、前段フロ
ーテータの原料回収口12を後段フローテータの原料入
口2に連結し、直列多段にインキの浮上選別を行うのが
好ましく、空気の供給は各段のフローテータに行う必要
がある。In order to increase the ink removal rate by using these floaters, a plurality of floaters are used, and the raw material recovery port 12 of the former-stage floatator is connected to the raw material inlet 2 of the latter-stage floatator, and the ink floats in multiple stages in series. Preferably, sorting is performed, and air supply must be performed to each stage of the flotator.
【0012】さらに本発明の他の実施例は、図3に示す
ように、槽体1の形状を逆円錐状にし、槽体1内中央部
にドラフトチューブ15と、このドラフトチューブ15
の外周間に流路16を形成するような外筒17とを配備
し、ハンドル18でドラフトチューブ15を昇降自在と
し、場合によっては、外筒17もハンドル19により昇
降自在とする。このフローテータでは、槽体1内に供給
され、回転するロータ9と磨砕刃10及び磨砕刃5によ
って微細気泡、原料、インキ粒子が混合されて旋回流と
なって上昇し、気泡が比較的多く集まった中心部付近が
ドラフトチューブ15内を上昇し、インキ粒子に付着し
た気泡は、フロスとして外筒17の上部から溢流し、フ
ロス排出部11から排出される。一方、ドラフトチュー
ブ15に捕集され得なかった気泡は、そのまま旋回しな
がら上昇を続けて再び中心部に集まり、ドラフトチュー
ブ15の外側に配置された外筒15に捕集され、そのま
ま上昇し、フロスとして外筒17の上部から溢流し、フ
ロス排出部11から排出される。排出されるフロスの量
はハンドル18,19によりドラフトチューブ15,外
筒17の位置を調節することにより変更される。一方、
ドラフトチューブ15,外筒17に捕集されなかった原
料は、原料回収口12から回収される。このフローテー
タも、図4に示すように、直列多段に使用して浮上選別
効果を向上させることが好ましい。また、原料回収口1
2から回収される原料の一部(約1/3)を循環させ、
原料循環口20から再びフローテーター内に吹き込むこ
とにより、原料は再び強力にミキシングされ、残留する
インキの除去が行われ、インキ除去率が向上し、前記の
ような直列多段使用の際の段数を減らすことが出来る。Further, in another embodiment of the present invention, as shown in FIG. 3, the shape of the tank 1 is inverted conical, and a draft tube 15
An outer tube 17 is formed between the outer circumferences of the outer tube and the outer tube 17 so that the draft tube 15 can be moved up and down by a handle 18. In some cases, the outer tube 17 can be moved up and down by a handle 19. In this flotator, fine bubbles, raw materials, and ink particles are supplied into the tank body 1 and rotated by the rotating rotor 9, the grinding blades 10, and the grinding blades 5 to rise as a swirling flow. The vicinity of the central portion where the target has gathered rises in the draft tube 15, and the air bubbles adhering to the ink particles overflow from the upper part of the outer cylinder 17 as floss and are discharged from the floss discharge part 11. On the other hand, the air bubbles that could not be collected in the draft tube 15 continue to rise while revolving and collect in the center again, are collected in the outer cylinder 15 disposed outside the draft tube 15, and rise as it is. It overflows from the upper part of the outer cylinder 17 as a floss, and is discharged from the floss discharge part 11. The amount of the floss to be discharged is changed by adjusting the positions of the draft tube 15 and the outer cylinder 17 with the handles 18 and 19. on the other hand,
The raw material not collected in the draft tube 15 and the outer cylinder 17 is recovered from the raw material recovery port 12. As shown in FIG. 4, it is preferable that the floater is also used in multiple stages in series to improve the floating sorting effect. In addition, raw material collection port 1
Circulate a part (about 1/3) of the raw material recovered from 2,
By blowing again into the flotator from the raw material circulation port 20, the raw material is mixed again strongly, the remaining ink is removed, the ink removal rate is improved, and the number of stages in the case of using the series multiple stages as described above is reduced. Can be reduced.
【0013】[0013]
【発明の効果】本発明によれば、フローテータ内に供給
された気泡が微細化されると同時に、繊維に付着してい
る汚れやインキも剥離、分散され、インキ除去率及び原
料の高明度、高白色度効果が向上し、またフローテータ
内に回収される原料の一部を循環させることによって、
さらにインキ除去率を向上することができる。According to the present invention, the bubbles supplied into the flotator are miniaturized, and at the same time, the dirt and ink adhering to the fibers are separated and dispersed, and the ink removal rate and the high brightness of the raw material are obtained. By improving the high whiteness effect and circulating a part of the raw material recovered in the flotator,
Further, the ink removal rate can be improved.
【図1】本発明の実施例を示す縦断側面図である。FIG. 1 is a vertical sectional side view showing an embodiment of the present invention.
【図2】本発明で使用する磨砕刃の一例を示す平面図で
ある。FIG. 2 is a plan view showing an example of a grinding blade used in the present invention.
【図3】本発明の実施例を示す縦断側面図である。FIG. 3 is a longitudinal sectional side view showing an embodiment of the present invention.
【図4】本発明のフローテータの使用の一例を示す説明
図である。FIG. 4 is an explanatory view showing an example of use of the floater of the present invention.
1 槽体 2 原料入口 3 空気入口 4 供給管 5 磨砕刃 6 ハンドル 7 プーリー 8 回転軸 9 ロータ 10 磨砕刃 11 フロス排出部 12 原料回収口 13 弁 14 循環配管 15 ドラフトチューブ 16 流路 17 外筒 18 ハンドル 19 ハンドル Reference Signs List 1 tank body 2 raw material inlet 3 air inlet 4 supply pipe 5 grinding blade 6 handle 7 pulley 8 rotating shaft 9 rotor 10 grinding blade 11 floss discharge section 12 raw material recovery port 13 valve 14 circulation pipe 15 draft tube 16 flow path 17 outside Tube 18 Handle 19 Handle
Claims (3)
設け、該供給口の周囲に昇降自在に磨砕刃を配備すると
ともに、供給口の上部に前記磨砕刃に対向する磨砕刃を
固定したロータを設け、さらに槽体の上部にフロス排出
部を、その下部液面下に原料回収部をそれぞれ設けたこ
とを特徴とするフローテータ。1. A supply port for raw material and air is provided at the center of the bottom of a tank body, and a grinding blade is provided around the supply port so as to be able to move up and down. A flotator comprising: a rotor having a fixed crushing blade; a floss discharge section provided above a tank body; and a raw material recovery section provided below a liquid level below the tank body.
部を前記供給口に循環する循環路を開口した請求項1記
載のフローテータ。2. The floater according to claim 1, wherein a circulation path for circulating a part of the collected material to the supply port is opened in the material collecting section.
該ドラフトチューブの外周間に流路を形成する外筒とを
相対的に昇降自在に配備した請求項1記載のフローテー
タ。3. The floatator according to claim 1, wherein a draft tube and an outer cylinder forming a flow path between the outer periphery of the draft tube are relatively vertically movable at a central portion of the inside of the tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24404791A JP3068909B2 (en) | 1991-08-30 | 1991-08-30 | Floatator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24404791A JP3068909B2 (en) | 1991-08-30 | 1991-08-30 | Floatator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0559679A JPH0559679A (en) | 1993-03-09 |
| JP3068909B2 true JP3068909B2 (en) | 2000-07-24 |
Family
ID=17112938
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24404791A Expired - Lifetime JP3068909B2 (en) | 1991-08-30 | 1991-08-30 | Floatator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3068909B2 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19902148C2 (en) * | 1999-01-20 | 2001-03-29 | Meri Entsorgungstech Papierind | Tangential solids separation device |
| JP4530575B2 (en) * | 2001-03-28 | 2010-08-25 | 株式会社Ihi機械システム | Flotation device |
| JP5339201B2 (en) * | 2009-07-09 | 2013-11-13 | デュプロ精工株式会社 | Deinking device, waste paper recycling processing apparatus, and waste paper recycling processing method |
| JP5692975B2 (en) * | 2009-08-20 | 2015-04-01 | デュプロ精工株式会社 | Waste paper recycling processor |
| JP5724076B2 (en) * | 2009-12-29 | 2015-05-27 | デュプロ精工株式会社 | Deinking processing device and used paper recycling processing device |
| CN111167845B (en) * | 2020-02-27 | 2020-11-10 | 泉州奔众电器有限公司 | Pollute soil with self-interacting flotation separation prosthetic devices |
| CN114011318B (en) * | 2021-11-10 | 2023-10-24 | 黄永松 | A grinding and dispersing processing system and processing technology for ferromagnetic raw materials of magnetic anti-counterfeiting ink |
-
1991
- 1991-08-30 JP JP24404791A patent/JP3068909B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0559679A (en) | 1993-03-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5580446A (en) | Screen, vortex apparatus for cleaning recycled pulp and related process | |
| US4214982A (en) | Process and device for removing printer's ink from a fiber suspension | |
| JP4003923B2 (en) | Waste plastic separation treatment apparatus and separation treatment method thereof | |
| EP0428257B1 (en) | Flotation machine for de-inking | |
| EP1944085B1 (en) | Method of and apparatus for processing corn grains for production of ethanol | |
| US4749473A (en) | Process for removing ink from wastepaper | |
| US4036440A (en) | Method and apparatus for the treatment of waste wood, such as stumps and snag, to make it suitable for the production of paper pulp | |
| US6379505B1 (en) | Pulper | |
| CA1330207C (en) | Reject screen | |
| JP3068909B2 (en) | Floatator | |
| US6120648A (en) | Apparatus for pulping and deinking | |
| GB2198662A (en) | A process and a device for the treatment of mixed waste such as refuse or its fractions for the recovery of plastics sheet material scrap | |
| RU2095153C1 (en) | Flotation machine | |
| US4272315A (en) | Secondary fiber system | |
| JPH05230784A (en) | Improvement of pulper for cellulose pulp cracking and grinding | |
| US3392114A (en) | Apparatus and method for decontaminating pulp and paper machine effluent | |
| DE3605259C1 (en) | Process and installation for removing color particles from a fiber suspension obtained from waste paper | |
| EP0124493B1 (en) | Apparatus for the purification of siliceous sand by means of attrition | |
| CA1098353A (en) | Method and apparatus for recovering paper fiber from waste paper containing materials | |
| US5871160A (en) | Apparatus and associated method for derfibering paper or dry pulp | |
| GB2576022A (en) | Dry separation waste processing and apparatus for achieving such | |
| JPH11200270A (en) | Wastepaper deinking treatment method and floatator | |
| CN215441188U (en) | High recovery rate waste paper pulping system | |
| WO1996036763A1 (en) | Pulping apparatus and related method for recycling paper | |
| JP2001073285A (en) | Pulper |