JPH06316886A - Pressure-type flotation machine - Google Patents
Pressure-type flotation machineInfo
- Publication number
- JPH06316886A JPH06316886A JP10665693A JP10665693A JPH06316886A JP H06316886 A JPH06316886 A JP H06316886A JP 10665693 A JP10665693 A JP 10665693A JP 10665693 A JP10665693 A JP 10665693A JP H06316886 A JPH06316886 A JP H06316886A
- Authority
- JP
- Japan
- Prior art keywords
- flow path
- bubbles
- outlet
- inlet
- flow channel
- 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.)
- Withdrawn
Links
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
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Paper (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は古紙脱インキに適用して
好適な浮選機に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a flotation machine suitable for deinking waste paper.
【0002】[0002]
【従来の技術】加圧型浮選機として図4のものが提案さ
れている。この浮選機は円筒形の浮上セル11の一端に
導入口12、もう一端に良質原料排出口13、フロス排
出口14が設けられ、導入口12から入った処理液1は
気泡2を浮上させながら浮上セル中を進行し、排出口か
ら排出されるようになっている。この浮選機は微小気泡
を積極的に利用できるようにしたという点で画期的なも
のであるが、100μm 以下の微細気泡の浮上という点
ではやや不足であった。2. Description of the Related Art As a pressure type flotation machine, one shown in FIG. 4 has been proposed. In this flotation machine, an inlet 12 is provided at one end of a cylindrical levitation cell 11, and a high-quality raw material outlet 13 and a floss outlet 14 are provided at the other end, and the treatment liquid 1 entering from the inlet 12 floats bubbles 2. While traveling through the floating cell, it is discharged from the discharge port. This flotation machine is epoch-making in that it makes it possible to positively utilize fine bubbles, but it is somewhat insufficient in terms of floating fine bubbles of 100 μm or less.
【0003】セル内の流動を見ると、全体としては導入
口12から排出口13,14への流れであるが、気泡の
上昇による加速効果により流路上部は下部より流速が大
きくなり、更には図4に図示するような循環流が生じて
いた。この循環流における逆行流から浮上した気泡は図
示してあるように順行流に再度取り込まれて循環するこ
ととなりセルでの浮上能力を減殺していた。Looking at the flow in the cell, the flow is from the inlet 12 to the outlets 13 and 14 as a whole, but the flow velocity in the upper part of the flow path becomes higher than that in the lower part due to the acceleration effect due to the rise of bubbles, and A circulating flow as shown in FIG. 4 was generated. The bubbles floating from the retrograde flow in this circulation flow were reintroduced into the anterograde flow and circulated as shown in the figure, and the floating ability in the cell was diminished.
【0004】[0004]
【発明が解決しようとする課題】本発明は、微細気泡の
浮上捕捉率を向上させて脱インキ性能を高めた加圧型浮
選機を提供することを課題としている。SUMMARY OF THE INVENTION It is an object of the present invention to provide a pressure type flotation machine which improves the decapsulation performance by improving the floating capture rate of fine bubbles.
【0005】[0005]
1.本発明者らが模擬液を使っての気泡分布測定の結
果、セル内での逆行流終点となる導入口の下部で気泡が
少ないことが判明した。本発明では、セル内最少気泡点
から良質原料を排出するために導入口下方に排出口を設
け、セル内を上部流路からUターンして下部流路に流れ
るようにする。1. As a result of the bubble distribution measurement using the simulated liquid by the present inventors, it was found that the number of bubbles was small at the lower part of the inlet, which was the end point of the retrograde flow in the cell. In the present invention, a discharge port is provided below the introduction port in order to discharge the good quality raw material from the smallest bubble point in the cell, and the inside of the cell is U-turned from the upper flow path to flow to the lower flow path.
【0006】2.セル内に生ずる循環流において逆行流
から浮上した気泡が順行流中に混入しないようセル内に
仕切壁を設け、仕切壁下面に溜まる気泡を取り出すフロ
ス排出口を設ける。2. A partition wall is provided in the cell so that bubbles floating from the retrograde flow in the circulation flow generated in the cell are not mixed into the forward flow, and a floss discharge port for taking out the bubbles accumulated on the lower surface of the partition wall is provided.
【0007】以上の考えに基づき本発明による加圧型浮
選機では、浮上セル内部を上部流路と下部流路に仕切壁
で分割し、その浮上セル内の上部流路は一方端で原料液
導入口に連通され、上部流路と下部流路は浮上セル内に
おいて他方端で連通され、かつ、下部流路には一方端側
の底部に処理済原料液排出口、そして一方端側の上部に
フロス抜出口を設けた構成を採用する。Based on the above idea, in the pressure type flotation machine according to the present invention, the inside of the levitation cell is divided into an upper flow path and a lower flow path by a partition wall, and the upper flow path in the levitation cell has a raw material liquid at one end. The upper flow path and the lower flow path communicate with each other at the other end in the flotation cell, and the lower flow path has a processed raw material liquid discharge port at the bottom on one end side and an upper part on the one end side. Adopt a structure with a floss outlet.
【0008】[0008]
【作用】気泡のうち大部分は上部流路中で従来と同じよ
うに浮上し、フロス排出口から排出される。一部残った
微細気泡は下部流路中で浮上して仕切壁下面に集合した
後、パルプ液一部と共に取り出され再度浮選処理にかけ
られる。気泡を開放した良質原料は良質原料排出口より
排出され次工程へ送られる。Most of the bubbles float in the upper channel in the same manner as in the conventional case and are discharged from the floss discharge port. Some of the remaining fine bubbles float in the lower channel and gather on the lower surface of the partition wall, and then are taken out together with a part of the pulp liquid and subjected to the flotation treatment again. The high-quality raw material with air bubbles released is discharged from the high-quality raw material outlet and sent to the next process.
【0009】これらの機能により、排出される良質原料
中に含まれる気泡量をほぼ半減することができる。また
脱インキに与える効果を図3に示しているが、本発明の
浮選機によれば脱インキ率はかなり向上しており、本発
明の効果の大きさが判る。なお、仕切壁下部から取り出
されたパルプ液中の気泡はその過程で集合・合体して次
の処理工程での上部流路中で浮上するに充分な大きさの
気泡となっており、微細気泡の蓄積といった問題は生じ
ないことが実験により確認された。With these functions, the amount of bubbles contained in the discharged good quality raw material can be almost halved. Further, the effect on deinking is shown in FIG. 3, and according to the flotation machine of the present invention, the deinking rate is considerably improved, and the effect of the present invention can be seen. It should be noted that the bubbles in the pulp liquid taken out from the lower part of the partition wall are bubbles that are large enough to aggregate and coalesce in the process and float in the upper flow path in the next processing step. It was confirmed by experiments that no problem such as the accumulation of
【0010】[0010]
【実施例】次に、図1,図2に示す本発明による浮選機
の実施例について説明する。先ず図1に示す実施例につ
いて説明する。良質原料排出口13を導入口12の下方
に設けると共に上下方向の中間部に水平な仕切壁15を
設けて導入口12から流入した原料液が他端側で上部流
路20から下方へUターンして導入口12側へ戻る下部
流路21を形成し、この下部流路21にて浮上して仕切
壁15の下面に集合した気泡はアクセプトバイパス口1
6からパルプ液の一部と共に取り出したのち供給原料中
へ混入し(図示せず)再度浮選処理される。導入口12
と反対側の浮上セル11内には上部を開口させた仕切板
19によって区画され、フロス排出口14を具えたフロ
ス排出手段が設けられている。このように構成された浮
上セル11は所定の数(ステージ数)だけ直列に接続さ
れて脱インキ処理を行う。EXAMPLE An example of the flotation machine according to the present invention shown in FIGS. 1 and 2 will be described below. First, the embodiment shown in FIG. 1 will be described. A high-quality raw material discharge port 13 is provided below the introduction port 12, and a horizontal partition wall 15 is provided at an intermediate portion in the vertical direction so that the raw material liquid flowing from the introduction port 12 makes a U-turn downward from the upper flow path 20 at the other end side. Then, the lower flow path 21 that returns to the introduction port 12 side is formed, and the bubbles that have floated up in the lower flow path 21 and collected on the lower surface of the partition wall 15 are the accept bypass port 1
After being taken out together with a part of the pulp liquid from No. 6, it is mixed into the feed material (not shown) and again subjected to the flotation treatment. Inlet 12
Inside the levitation cell 11 on the opposite side, a floss discharging means having a floss discharging port 14 is provided which is partitioned by a partition plate 19 having an open top. The floating cells 11 configured as described above are connected in series by a predetermined number (the number of stages) to perform the deinking process.
【0011】次に図2に示した別の実施例について説明
する。仕切壁15の下面に集合する気泡は量的には僅か
であってそれ自身のみではパルプ液に浮上力を与え浮上
管18から流出させるには不充分であるため浮上管18
の入口に外部から浮上促進空気17を供給して、微少気
泡を多く含んだパルプ液を浮上管18を経由して上部流
路20のフロス層近辺に押し上げて気泡浮上を容易化し
たものである。その他の構成、作用は図1に示したもの
と同様である。Next, another embodiment shown in FIG. 2 will be described. The amount of air bubbles gathering on the lower surface of the partition wall 15 is small in quantity, and the air bubbles themselves are not sufficient to give a levitation force to the pulp liquid and to flow out from the levitation pipe 18.
The levitation promoting air 17 is supplied from the outside to the inlet of the air bubble, and the pulp liquid containing a lot of minute bubbles is pushed up to the vicinity of the froth layer of the upper flow path 20 via the levitation tube 18 to facilitate the levitation of the bubbles. . Other configurations and operations are similar to those shown in FIG.
【0012】[0012]
【発明の効果】以上具体的に説明したように、本発明に
よる加圧型浮選機においては、浮上セル内部を上部流路
と下部流路に仕切壁で分割し、その上部流路は一方端で
原料液導入口に連通され、上部流路と下部流路は浮上セ
ル内において他方端で連通さ、かつ、下部流路には一方
端側の底部に処理済原料液排出口、一方端側の上部にフ
ロス排出口を設けており、これによれば、原料液が上下
流路を流れる間に浮上セル内での微細気泡の浮上捕捉率
が向上して、脱インキ性能が向上し、残留インキの少な
い良質な回収古紙パルプの製造を可能として効果的であ
る。As described above in detail, in the pressure type flotation machine according to the present invention, the inside of the levitation cell is divided into an upper flow passage and a lower flow passage by a partition wall, and the upper flow passage has one end. The upper flow path and the lower flow path communicate with each other at the other end in the levitation cell, and the lower flow path has a processed raw material liquid discharge port at the bottom on one end side and one end side. A froth discharge port is provided on the upper part of this, which improves the floatation capture rate of fine bubbles in the floating cell while the raw material liquid flows through the upper and lower flow paths, improving the deinking performance, It is effective as it enables the production of high quality recovered waste paper pulp with less ink.
【図1】本発明の第1実施例に係る浮選機の断面図。FIG. 1 is a sectional view of a flotation machine according to a first embodiment of the present invention.
【図2】本発明の第2実施例に係る浮選機の断面図。FIG. 2 is a sectional view of a flotation machine according to a second embodiment of the present invention.
【図3】本発明による装置のインキ除去率の効果を示す
実験結果のグラフ。FIG. 3 is a graph of experimental results showing the effect of ink removal rate of the device according to the present invention.
【図4】従来の浮選機を示す断面図。FIG. 4 is a cross-sectional view showing a conventional flotation machine.
1 処理液 2 気泡 11 浮上セル 12 導入口 13 良質原料排出口 14 フロス排出口 15 仕切壁 16 アクセプトバイパス口 17 浮上促進空気 18 浮上管 1 Treatment Liquid 2 Bubbles 11 Floating Cell 12 Inlet 13 High Quality Material Outlet 14 Floss Outlet 15 Partition Wall 16 Accept Bypass Port 17 Flotation Promoting Air 18 Flotation Pipe
フロントページの続き (72)発明者 勝部 良次郎 広島県三原町寿町一丁目1番地 三原菱重 エンジニアリング株式会社内Front page continuation (72) Inventor Ryojiro Katsube 1-1, Shoucho, Mihara-cho, Hiroshima Prefecture Ryoshige Mihara Engineering Co., Ltd.
Claims (1)
入口、他方端に上部を開口させた仕切板で区画されたフ
ロス排出手段を備え、内部を上部流路と下部流路に仕切
壁で分割された浮上セルを有し、同浮上セル内の前記上
部流路は前記一方端で前記原料液導入口に連通され、前
記上部流路と下部流路は前記浮上セル内において前記他
方端で連通され、かつ、前記下部流路には前記一方端側
の底部に処理済原料液排出口、前記一方端側の上部にフ
ロス抜出口が設けられていることを特徴とする加圧型浮
選機。1. A raw material liquid introduction port containing ink particles and bubbles is provided at one end, and a floss discharge means partitioned by a partition plate having an upper opening at the other end, and the inside is divided into an upper flow path and a lower flow path. There is a levitation cell divided by a wall, the upper flow path in the levitation cell communicates with the raw material liquid inlet at the one end, and the upper flow path and the lower flow path are the other in the levitation cell. A pressurizing type floater characterized by being connected to each other at the end and having a treated raw material liquid discharge port at the bottom of the one end side and a froth discharge port at the upper end of the one end side in the lower flow path. Selection machine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10665693A JPH06316886A (en) | 1993-05-07 | 1993-05-07 | Pressure-type flotation machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10665693A JPH06316886A (en) | 1993-05-07 | 1993-05-07 | Pressure-type flotation machine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06316886A true JPH06316886A (en) | 1994-11-15 |
Family
ID=14439150
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10665693A Withdrawn JPH06316886A (en) | 1993-05-07 | 1993-05-07 | Pressure-type flotation machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06316886A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998046979A1 (en) * | 1997-04-14 | 1998-10-22 | Micromeritics Instrument Corporation | System and method for evenly suspending and circulating particles in a liquid |
US6073774A (en) * | 1997-04-14 | 2000-06-13 | Beloit Technologies, Inc. | Pressurized deinking module with vent line |
JP2002285484A (en) * | 2001-03-28 | 2002-10-03 | Ishikawajima Sangyo Kikai Kk | Apparatus for treating froth |
JP2002294575A (en) * | 2001-03-28 | 2002-10-09 | Ishikawajima Sangyo Kikai Kk | Processing equipment for froth |
-
1993
- 1993-05-07 JP JP10665693A patent/JPH06316886A/en not_active Withdrawn
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998046979A1 (en) * | 1997-04-14 | 1998-10-22 | Micromeritics Instrument Corporation | System and method for evenly suspending and circulating particles in a liquid |
US6073774A (en) * | 1997-04-14 | 2000-06-13 | Beloit Technologies, Inc. | Pressurized deinking module with vent line |
JP2002285484A (en) * | 2001-03-28 | 2002-10-03 | Ishikawajima Sangyo Kikai Kk | Apparatus for treating froth |
JP2002294575A (en) * | 2001-03-28 | 2002-10-09 | Ishikawajima Sangyo Kikai Kk | Processing equipment for froth |
JP4530574B2 (en) * | 2001-03-28 | 2010-08-25 | 株式会社Ihi機械システム | Floss processing equipment |
JP4530573B2 (en) * | 2001-03-28 | 2010-08-25 | 株式会社Ihi機械システム | Floss processing equipment |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20000801 |