JPH0369688A - Deaeration tank for paper-making raw material - Google Patents

Deaeration tank for paper-making raw material

Info

Publication number
JPH0369688A
JPH0369688A JP20241389A JP20241389A JPH0369688A JP H0369688 A JPH0369688 A JP H0369688A JP 20241389 A JP20241389 A JP 20241389A JP 20241389 A JP20241389 A JP 20241389A JP H0369688 A JPH0369688 A JP H0369688A
Authority
JP
Japan
Prior art keywords
accept
tank
deaeration tank
deaeration
primary
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.)
Granted
Application number
JP20241389A
Other languages
Japanese (ja)
Other versions
JP2758448B2 (en
Inventor
Tomoyuki Shimizu
智之 清水
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.)
Mitsubishi Paper Mills Ltd
Original Assignee
Mitsubishi Paper Mills 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 Mitsubishi Paper Mills Ltd filed Critical Mitsubishi Paper Mills Ltd
Priority to JP20241389A priority Critical patent/JP2758448B2/en
Publication of JPH0369688A publication Critical patent/JPH0369688A/en
Application granted granted Critical
Publication of JP2758448B2 publication Critical patent/JP2758448B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the subject tank for the deaeration of a paper-making raw material, producible at a low cost and effective in reduction the electrical power consumption and improving the quality of the produced sheet by placing plural cleaners, plural feed pipes, etc., in an deaeration tank. CONSTITUTION:The objective tank is produced by providing a primary cleaner accept feed pipe 3 or plural primary accept feed pipes 2, an outlet port 4 of the deaeration tank, a secondary cleaner accept feed pipe 6 or plural secondary accept feed pipes 5, a weir 7 and a deaeration tank overflow port 8 in a deaeration tank 1 in the order.

Description

【発明の詳細な説明】 (A)産業上の利用分野 スクリーン、クリーナー等により除塵された後の抄紙原
料の脱気に関する。
DETAILED DESCRIPTION OF THE INVENTION (A) Industrial Application Field This invention relates to the degassing of papermaking raw materials after dust removal by screens, cleaners, etc.

(B)従来の技術 第3図及び第4図に基き、従来の脱気タンクを説明する
と、第3図は1次クリーナーアクセプトのみ供給するシ
ングルアクセプト方式で、脱気タンク■の内部に複数の
1次アクセプトフィードパイプ2、脱気タンク出口4、
堰7、脱気タンクオーバーフロー8を順次設け、脱気タ
ンク1の下部には複数の1次アクセプトフィードパイプ
2が接続する1次クリーナーアクセプト供給パイプ3が
設けられ、脱気タンク1の上部他端には真空ポンプサク
シコンロ9を設けたアールストローム社製Ensava
cの脱気タンクである。
(B) Conventional technology To explain a conventional deaeration tank based on Figs. 3 and 4, Fig. 3 shows a single-accept system that supplies only the primary cleaner accept. Primary accept feed pipe 2, deaeration tank outlet 4,
A weir 7 and a degassing tank overflow 8 are sequentially provided, and a primary cleaner accept supply pipe 3 to which a plurality of primary accept feed pipes 2 are connected is provided at the bottom of the degassing tank 1, and the other end of the top of the degassing tank 1 is connected to a primary cleaner accept feed pipe 3. Ahlstrom's Ensava equipped with a vacuum pump Sakshi stove 9.
This is the degassing tank of c.

第4図は脱気タンク内部に複数の1次アクセプトフィー
ドパイプ2、複数の2次アクセプトフィードパイプ5、
脱気タンク出口4、i[7、脱気タンクオーバーフロー
8を順次設け、脱気タンク1の下部には複数の1次アク
セプトフィードパイプ2が接続する1次クリーナーアク
セプト供給パイプ3と複数の2次アクセプトフィードパ
イプ5が接続する2次クリーナーアクセプト供給バイブ
ロが設けられ、脱気タンク1の上部他端には真空ポンプ
サクシコンロ9を設けたダブルアクセプト方式の脱気タ
ンクである。
Figure 4 shows a plurality of primary accept feed pipes 2, a plurality of secondary accept feed pipes 5,
A deaeration tank outlet 4, i[7, and a deaeration tank overflow 8 are provided in sequence, and the lower part of the deaeration tank 1 has a primary cleaner accept supply pipe 3 to which a plurality of primary accept feed pipes 2 are connected, and a plurality of secondary This is a double-accept type degassing tank, in which a secondary cleaner accept supply vibro to which an accept feed pipe 5 is connected is provided, and a vacuum pump sushi stove 9 is provided at the other end of the top of the degassing tank 1.

(C)発明が解決しようとする課題 シングルアクセプト方式では■次アクセプトフィードパ
イプ2より供給される良い原料だけが脱気タンク出口4
より送り出されるため、ゴミに関して特に問題はない。
(C) Problems to be solved by the invention In the single-accept system, only good raw materials supplied from the next accept feed pipe 2 are fed to the degassing tank outlet 4.
There are no particular problems with garbage as it is sent out more than once.

しかし、脱気タンクオーバーフロー口8からも良い原料
が流出して再循環するため、スクリーン、クリーナー、
ポンプ等の流通システムが大きくなり、設備のイニシャ
ルコスト大、ポンプの消費電力増のコストアップとなる
ため、近年では2次アクセプトフィードパイプ5からも
供給されるダブルアクセプト方式が採用されている。
However, since good raw materials also flow out from the deaeration tank overflow port 8 and are recirculated, screens, cleaners,
Since the size of the distribution system such as a pump increases, which increases the initial cost of the equipment and increases the power consumption of the pump, in recent years a double-accept system in which the feed is also supplied from the secondary accept feed pipe 5 has been adopted.

ダブルアクセプト方式の場合、従来だと第4図において
脱気タンク出口4より1次クリーナーアクセプトの良い
原料と2次クリーナーアクセプトのやや悪い原料と混入
したものが出て行く。また、脱気タンクオーバーロ8か
らも同様に混入した原料が流出して行く問題がある。
In the case of the double-accept method, in the conventional case, a mixture of raw material with good primary cleaner acceptance and raw material with slightly poor secondary cleaner acceptance exits from the degassing tank outlet 4 in FIG. 4. Additionally, there is a problem in that mixed raw materials also flow out from the degassing tank overflow 8.

(D)課題を解決するための手段 ダブルアクセプト方式において、脱気タンクの内部に、
1次クリーナーアクセプト供給パイプ又は複数の1次ア
クセプトフィードパイプ、脱気タンク出口、2次クリー
ナーアクセプト供給パイプ又は複数の2次アクセプトフ
ィードパイプ、堰、脱気タンクオーバーフロー口を順次
設けたことを特徴とする抄紙原料の脱気タンクに関する
ものである。
(D) Means for solving the problem In the double-accept method, inside the degassing tank,
It is characterized by sequentially providing a primary cleaner accept supply pipe or a plurality of primary accept feed pipes, a degassing tank outlet, a secondary cleaner accept supply pipe or a plurality of secondary accept feed pipes, a weir, and a degassing tank overflow port. This relates to a degassing tank for papermaking raw materials.

(E)作用 図示してはいないが、脱タンク出口の先は、ヘッドボッ
クスに継っており、製品シートとなるため、1次クリー
ナーアクセプトの良い原料は全量使用させねばならず、
逆に2次クリーナーアクセプトのやや悪い原料はポンプ
脈動による坪量変動を防ぐため、脱気タンクのレベルコ
ントロールに使用するので極力脱気タンクオーバーフロ
ー口8より流出させ再循環、再クリーニングさせる為に
、脱気タンク出口4の取付は位置を1次アクセプトと2
次アクセプト供給の間に設けるものである。
(E) Although not shown in the diagram, the end of the tank removal outlet is connected to the head box and becomes a product sheet, so all raw materials with good primary cleaner acceptance must be used.
On the other hand, raw materials with slightly poor secondary cleaner acceptance are used to control the level of the deaeration tank in order to prevent fluctuations in basis weight due to pump pulsation, so they should be flowed out from the deaeration tank overflow port 8 as much as possible to be recirculated and re-cleaned. When installing the deaeration tank outlet 4, the position is the primary accept and 2.
This is provided during the next acceptance supply.

(F)実施例 本発明の実施例を図面に基づき説明する。(F) Example Embodiments of the present invention will be described based on the drawings.

実施例工 第1図はフィードパイプを用いたダブルアクセプト方式
の脱気タンクであり、1次クリーナーアクセプト供給パ
イプ3に接続した複数の1次アクセプトフィードパイプ
2を脱気タンクlの下部より内部に挿入し、その先端が
堰7によって形成される液面よりも上に出るように配置
し、その脇には脱気タンク出口4を脱気タンク1の下部
に設け、2次クリーナーアクセプト供給バイブロに接続
した複数の2次アクセプトフィードパイプ5を脱気タン
ク1の下部より内部に挿入し、1次アクセプトフィード
パイプ2と同様に液面上になるように配置し、次に脱気
タンク1内に液溜まり形成するための堰7を設け、堰7
の脇には脱気タンクオーバーフロー口8を脱気タンク1
の下部に設け、脱気タンク1の上部他端には真空ポンプ
サクシコンロ9を設けたものである。
Example work Figure 1 shows a double-accept deaeration tank using feed pipes, in which a plurality of primary accept feed pipes 2 connected to a primary cleaner accept supply pipe 3 are inserted into the interior from the lower part of the deaeration tank l. Insert it and place it so that its tip comes out above the liquid level formed by the weir 7, and beside it, a deaeration tank outlet 4 is provided at the bottom of the deaeration tank 1, and a secondary cleaner accept supply vibro is installed. Insert the plurality of connected secondary accept feed pipes 5 into the deaeration tank 1 from the bottom, place them above the liquid level in the same way as the primary accept feed pipes 2, and then insert them into the deaeration tank 1. A weir 7 is provided to form a liquid pool, and the weir 7
Next to the deaeration tank overflow port 8 is the deaeration tank 1.
A vacuum pump and a stove 9 are provided at the other end of the upper part of the degassing tank 1.

1次及び2次アクセプト原料は複数の1次及び2次アク
セプトフィードパイプ2.5より脱気タンク1内に供給
され、1次アクセプトフィードパイプ2より流入した良
い原料は、真空ポンプサクシコンロ9に接続している真
空ポンプ(図示せず)によって脱気され全量脱気タンク
出口4より次の工程に送られ製品シートとなる。
The primary and secondary accept raw materials are supplied into the degassing tank 1 through a plurality of primary and secondary accept feed pipes 2.5, and the good raw materials flowing from the primary accept feed pipe 2 are sent to the vacuum pump sacsi stove 9. It is degassed by a connected vacuum pump (not shown) and sent to the next process from the entire degassing tank outlet 4 to become a product sheet.

2次アクセプトフィードパイプ5より流入したやや悪い
原料も■次アクセプトと同様に脱気され一部は脱気タン
ク出口4より次の工程に送られ、残りの2次アクセプト
は堰7で形成される脱気タンク1の液溜まりのレベルコ
ントロールのため少量基7よりオバーし、脱気タンクオ
ーバーフロー口8より流出し2次クリーナーへ戻され再
循環する。
The slightly bad raw material flowing in from the secondary accept feed pipe 5 is also degassed in the same way as the secondary accept, and a portion is sent to the next process from the degassing tank outlet 4, and the remaining secondary accept is formed at the weir 7. In order to control the level of the liquid pool in the deaeration tank 1, a small amount of liquid is allowed to exceed the base 7, flows out from the deaeration tank overflow port 8, is returned to the secondary cleaner, and is recirculated.

脱気の方法は、脱気タンク本体壁への衝突による拡散と
真空ポンプによる脱気が基本であり、脱タンク本体の構
造は多種多様を呈するためタンクの構造は限定しない。
The degassing method is basically based on diffusion by collision with the wall of the degassing tank body and degassing by a vacuum pump, and since the structure of the degassing tank body can vary widely, the structure of the tank is not limited.

実施例2 第2図に示す本発明の他の実施例を説明すると、実施例
1(第1図)の■次アクセプトフィードパイプ2と2次
アクセプトフィードパイプ5に替えて、1次クリーナー
アクセプト供給パイプ10及び2次クリーナーアクセプ
ト供給パイプ11を脱気タンク1本体の横から入って、
堰7によって形成された液面上を1次及び2次クリーナ
ーアクセプト供給パイプ10.11が走っており、その
クリーナーアクセプト供給パイプの上部には、原料供給
の為の多数の小さい穴があいた構造のもので、各部側の
配置順序及び原料の流通経路は第1図の時と同様である
Embodiment 2 To explain another embodiment of the present invention shown in FIG. 2, in place of the secondary accept feed pipe 2 and secondary accept feed pipe 5 of Embodiment 1 (FIG. 1), a primary cleaner accept supply is used. Insert the pipe 10 and the secondary cleaner accept supply pipe 11 from the side of the deaeration tank 1 body,
Primary and secondary cleaner accept supply pipes 10 and 11 run above the liquid level formed by the weir 7, and the upper part of the cleaner accept supply pipe has a structure with many small holes for feeding raw materials. The arrangement order of each part and the distribution route of raw materials are the same as in FIG. 1.

(G)発明の効果 本発明はコストダウンタイプのダブルアクセプト方式を
採用した脱気タンクで、スクリーン、クリーナー、ポン
プ等の設備コストが安く、消費電力の減少が図れ、ゴミ
の少ない原料を用いて製品シートを抄造することにより
、製品シートの品質を向上させることができる。
(G) Effects of the Invention The present invention is a degassing tank that adopts a cost-reducing double-accept system, which has low equipment costs for screens, cleaners, pumps, etc., reduces power consumption, and uses raw materials with less waste. By paper-making the product sheet, the quality of the product sheet can be improved.

【図面の簡単な説明】[Brief explanation of drawings]

第1図及び第2図は本発明の代表的な実施例を示す概略
図である。第3図は従来のシングルアクセルト方式の脱
気タンクの概略図、第4図は従来のダブルアクセプト方
式の脱気タンクを示す概略図である。 1:脱タンク、 ¥1lffi メ2図 1次アクセプトフィードパイプ、 1次クリーナーアクセプト供給パイプ、脱気タンク出口
、 2次アクセプトフィードパイプ、 2次クリーナーアクセプト供給パイプ、堰、 脱気タンクオーバーフローロ、 真空ボンプサクションロ、 1次クリーナーアクセプト供給パイプ 2次クリーナーアクセプト供給パイプ、第31¥1 第41男
1 and 2 are schematic diagrams showing representative embodiments of the present invention. FIG. 3 is a schematic diagram of a conventional single-accept type degassing tank, and FIG. 4 is a schematic diagram showing a conventional double-accept type degassing tank. 1: Detank, ¥1lffi Me 2 Figure 1st accept feed pipe, 1st cleaner accept supply pipe, deaeration tank outlet, 2nd accept feed pipe, 2nd cleaner accept supply pipe, weir, deaeration tank overflow, vacuum Bonpsakushonro, 1st cleaner accept supply pipe 2nd cleaner accept supply pipe, 31 yen 1 41st man

Claims (1)

【特許請求の範囲】[Claims] 脱気タンクの内部に、1次クリーナーアクセプト供給パ
イプ又は複数の1次アクセプトフィードパイプ、脱気タ
ンク出口、2次クリーナーアクセプト供給パイプ又は複
数の2次アクセプトフィードパイプ、堰、脱気タンクオ
ーバーフロー口を順次設けたことを特徴とする抄紙原料
の脱気タンク。
A primary cleaner accept supply pipe or a plurality of primary accept feed pipes, a deaeration tank outlet, a secondary cleaner accept supply pipe or a plurality of secondary accept feed pipes, a weir, and a deaeration tank overflow port are installed inside the deaeration tank. A deaeration tank for papermaking raw materials, which is characterized by being installed sequentially.
JP20241389A 1989-08-03 1989-08-03 Deaeration tank for papermaking raw materials Expired - Fee Related JP2758448B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20241389A JP2758448B2 (en) 1989-08-03 1989-08-03 Deaeration tank for papermaking raw materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20241389A JP2758448B2 (en) 1989-08-03 1989-08-03 Deaeration tank for papermaking raw materials

Publications (2)

Publication Number Publication Date
JPH0369688A true JPH0369688A (en) 1991-03-26
JP2758448B2 JP2758448B2 (en) 1998-05-28

Family

ID=16457095

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20241389A Expired - Fee Related JP2758448B2 (en) 1989-08-03 1989-08-03 Deaeration tank for papermaking raw materials

Country Status (1)

Country Link
JP (1) JP2758448B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0671109A (en) * 1991-10-16 1994-03-15 A Ahlstroem Oy Deaeration tank
JP2014034014A (en) * 2012-08-09 2014-02-24 Mitsubishi Heavy Ind Ltd Co2 recovery system, and co2 recovery method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0671109A (en) * 1991-10-16 1994-03-15 A Ahlstroem Oy Deaeration tank
JP2014034014A (en) * 2012-08-09 2014-02-24 Mitsubishi Heavy Ind Ltd Co2 recovery system, and co2 recovery method
US9901873B2 (en) 2012-08-09 2018-02-27 Mitsubishi Heavy Industries, Ltd. CO2 recovery device and CO2 recovery method

Also Published As

Publication number Publication date
JP2758448B2 (en) 1998-05-28

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