JP2539844B2 - Papermaking White water solids recovery method - Google Patents
Papermaking White water solids recovery methodInfo
- Publication number
- JP2539844B2 JP2539844B2 JP62213645A JP21364587A JP2539844B2 JP 2539844 B2 JP2539844 B2 JP 2539844B2 JP 62213645 A JP62213645 A JP 62213645A JP 21364587 A JP21364587 A JP 21364587A JP 2539844 B2 JP2539844 B2 JP 2539844B2
- Authority
- JP
- Japan
- Prior art keywords
- white water
- solid content
- recovery method
- ash
- recovery
- 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 - Fee Related
Links
Landscapes
- Paper (AREA)
Description
【発明の詳細な説明】 (A) 産業上の利用分野 本発明は、抄紙機から発生する白水中の固形分の回収
方法に関する。DETAILED DESCRIPTION OF THE INVENTION (A) Field of Industrial Application The present invention relates to a method for recovering a solid content in white water generated from a paper machine.
(B) 従来の技術 抄紙白水には大量の抄紙原料が含まれており、原材料
コストの低減、又、公害対策の目的で、従来から白水中
の固形分は回収されていた。(B) Conventional Technology Papermaking white water contains a large amount of papermaking raw materials, and solid components in whitewater have been conventionally collected for the purpose of reducing raw material costs and pollution control.
白水中の固形分回収方法としては、古くからフィルタ
ー濾過方法や、白水中の固形分を高分子凝集剤によって
フロック化させたうえで沈降させたり、あるいは浮上さ
せて回収する方法が用いられている。抄紙機から発生す
る白水は、その発生部位によってパルプ濃度、灰分濃
度、比重、空気含有率または濾水度等に差があるにもか
かわらず、一括して上記のいずれかの方法で処理されて
いるのが現状であり、効率の良い固形分回収がなされて
いるとは言えない。As a solid content recovery method in white water, a filter filtration method or a method in which the solid content in white water is flocculated with a polymer coagulant and then settled or floated is used for recovery. . White water generated from a paper machine is treated by any one of the above methods collectively, although there is a difference in pulp concentration, ash concentration, specific gravity, air content or freeness depending on the generation site. However, it cannot be said that the solid content is efficiently collected.
同時に近年、抄紙機の高速化、又、トップワイヤーを
有するツインワイヤーフォーマー化に伴って、ワイヤー
パートから発生する白水中の灰分濃度は、他パートから
発生する白水よりも高くなりつつある。At the same time, in recent years, the ash concentration in the white water generated from the wire part is becoming higher than that of the white water generated from other parts due to the speeding up of paper machines and the shift to the twin wire former having a top wire.
(C) 発明が解決しようとする問題点 フィルター濾過式の回収方法では、フィルターメッシ
ュ表面にプリマット層を形成させる必要があり、白水中
に大量のパルプをスイートナーとして添加しなければな
らない。(C) Problems to be Solved by the Invention In a filter filtration type recovery method, it is necessary to form a premat layer on the surface of the filter mesh, and a large amount of pulp must be added to white water as a sweetener.
従って、銘柄変更のために系内の残留原料を回収する
際、白水中の原料ばかりではなく、スイートナーとして
添加した大量のパルプ原料も回収しなければならず、各
パートの白水を一括して処理する場合、銘柄変更のため
の原料替えに多くの時間と、大きな原料回収槽を必要と
する。Therefore, when recovering the residual raw material in the system for brand change, not only the raw material in white water but also a large amount of pulp raw material added as a sweetener must be collected, and the white water of each part is collectively collected. When processing, it takes a lot of time and a large raw material recovery tank to change raw materials for brand change.
沈降式、また浮上式による回収方法では、スイートナ
ーの添加を必要としないものの、白水中の灰分濃度が低
くなると沈降させにくく、高くなると逆に浮上させにく
いという問題があるため、負荷変動に弱く、あらゆる銘
柄に対応させにくいという欠点があった。Although the sedimentation method and the flotation type recovery method do not require the addition of sweetener, there is a problem that it is difficult to settle when the ash concentration in white water is low, and it is difficult to float when the ash concentration is high, so it is vulnerable to load fluctuations. However, there was a drawback that it was difficult to support all brands.
そこで、本発明は、上記問題点を鑑み、最も効率の良
い白水中の原料回収方法を提供することを目的とするも
のである。In view of the above problems, it is an object of the present invention to provide a most efficient raw material recovery method in white water.
(D) 問題点を解決するための手段 即ち、本発明は、抄紙白水の固形分回収方法に於て、
白水の灰分濃度を0.1%以上のものと、そうでないもの
に集積し、それぞれ独立して固形分を回収をすることを
特徴とする白水の固形分回収方法である。(D) Means for Solving the Problems That is, the present invention provides a method for recovering solid content of papermaking white water, comprising:
This is a method for collecting solid content of white water, which is characterized by accumulating ash concentration of white water of 0.1% or more and that of not, and independently collecting solid content.
通常、灰分濃度レベルとしては、銘柄にかかわらず、
ワイヤー回収シャワー、プレスセーブオール回収白水、
またウエットパート真空セパレーター回収白水は、低い
レベルで安定しており、概略0.1%以下であり、これに
対し、最も発生量の多いワイヤーバックウォーター余剰
白水は、配合、坪量、抄造によって灰分濃度は、大きく
変化するが、一般的に他パートからの白水よりも高いレ
ベル即ち、0.1%以上を示している。これらの灰分濃度
レベルの異なる白水に対し、それぞれ独立して、即ち灰
分濃度負荷に応じた最適な回収方法により所期の目的を
達成する。Normally, the ash concentration level is
Wire recovery shower, press save all recovery white water,
Also, the white water recovered from the wet part vacuum separator is stable at a low level and is approximately 0.1% or less.On the other hand, the wire white water surplus white water that generates the most amount of water has , But it generally shows a higher level than white water from other parts, that is, 0.1% or more. The intended purpose is achieved independently for these white waters having different ash concentration levels, that is, by an optimum recovery method according to the ash concentration load.
本発明では、前述の低灰分レベル白水に対しては、フ
ィルター濾過方式や浮上方式を、後述の灰分高レベル白
水に対しては、沈降方式やフィルター濾過方式を適用す
ることができる。ただし、両者共にフィルター濾過方式
を用いることは、問題点の項で述べたように、原料替え
における欠点があるため避けたい。In the present invention, a filter filtration method or a flotation method can be applied to the low ash content white water described above, and a sedimentation method or a filter filtration method can be applied to the ash content high white water described below. However, it is desirable to avoid using the filter filtration method for both of them because there are drawbacks in changing the raw material as described in the section of the problem.
また、一方にフィルター濾過方式、他方に沈降方式又
は浮上方式を用いた場合、負荷変動に弱い、沈降方式又
は浮上方式の系に異常が発生した場合、水量負荷変動に
強いフィルター濾過方式のラインに、低灰分レベル白水
の一部を逃がすことによって、系を安定させることが可
能である。In addition, if one uses a filter filtration method and the other uses a sedimentation method or a floatation method, it is weak against load fluctuations, and if an abnormality occurs in the system of the sedimentation method or the floatation method, a line of a filter filtration method that is strong against water load fluctuation It is possible to stabilize the system by allowing some of the low ash level white water to escape.
次に第1図のフローを基に、本発明の実施例を説明す
るが、本発明はこれに限定されるものではない。Next, an embodiment of the present invention will be described based on the flow of FIG. 1, but the present invention is not limited to this.
(E) 実施例 白水を、灰分濃度0.1%の線で層別したところ、低灰
分レベル白水には、プレスセーブオール回収白水、ワイ
ヤー回収シャワー、及び真空セパレーター回収白水が相
当し、高灰分レベル白水には、ワイヤーバックウォータ
ー余剰白水が相当した。(E) Example White water was stratified by a line having an ash concentration of 0.1%. The low ash level white water corresponds to press save all recovered white water, wire recovery shower, and vacuum separator recovered white water, and high ash level white water. Corresponds to the wire backwater surplus white water.
この低灰分レベル白水と、高灰分レベル白水の水量は
概略同量となり、低灰分レベル白水の処理にはフィルタ
ー濾過方式を用い、高灰分レベル白水には沈降方式を用
いた。The amounts of the low ash level white water and the high ash level white water were approximately the same, and the low ash level white water was treated by the filter filtration method and the high ash level white water was settled by the sedimentation method.
フローを第1図に示す。1はフィルター、2は沈降
槽、3はタンク、4はポンプを表す。The flow is shown in FIG. 1 is a filter, 2 is a settling tank, 3 is a tank, and 4 is a pump.
特に、低灰分レベル白水処理用のフィルターは、白水
全量を処理する為に必要とするフィルター面積の35%の
面積で処理可能となり、その分、スイートナーの量も減
少し、効率の良い固形分回収ができた。In particular, the filter for low ash level white water treatment can be treated with 35% of the filter area required to treat the total amount of white water, and the amount of sweetener is reduced by that amount, resulting in efficient solid content. I was able to collect it.
(F) 発明の効果 この発明の効果を列挙すれば、以下の通りである。(F) Effects of the Invention The effects of the present invention are listed below.
1) 白水を常に最適回収方法で処理できるため、効率
の良い固形分回収が可能となる。1) Since white water can always be treated by the optimum recovery method, efficient solid content recovery becomes possible.
2) 従って、固形分は、高濃度で回収することが可能
であり、後工程における原料濃度を安定させ易い。2) Therefore, the solid content can be collected at a high concentration, and the raw material concentration in the post-process can be easily stabilized.
3) 白水の固形分回収設備の小型化が可能であり、ラ
ンニングコストを低減することが可能となる。3) The solid content recovery facility for white water can be downsized, and the running cost can be reduced.
第1図は本発明具体例を示すものであり、図中 1……フィルター 2……沈降槽 3……タンク 4……ポンプ をそれぞれ示す。 FIG. 1 shows a specific example of the present invention, in which 1 ... Filter 2 ... Sedimentation tank 3 ... Tank 4 ... Pump are shown.
Claims (1)
白水の固形分回収方法に於いて、白水の灰分濃度を0.1
%以上のものと、そうでないものに集積し、それぞれ独
立して固形分の回収をすることを特徴とする白水の固形
分回収方法。1. A method for recovering solid content of white water generated from each part of a wet part of a paper machine, wherein the ash concentration of white water is 0.1.
% Or more, and those not, and collect solid content independently of each other.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62213645A JP2539844B2 (en) | 1987-08-26 | 1987-08-26 | Papermaking White water solids recovery method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62213645A JP2539844B2 (en) | 1987-08-26 | 1987-08-26 | Papermaking White water solids recovery method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6461590A JPS6461590A (en) | 1989-03-08 |
JP2539844B2 true JP2539844B2 (en) | 1996-10-02 |
Family
ID=16642584
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62213645A Expired - Fee Related JP2539844B2 (en) | 1987-08-26 | 1987-08-26 | Papermaking White water solids recovery method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2539844B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06142946A (en) * | 1992-11-04 | 1994-05-24 | Sanyu Kinzoku:Kk | Cooling tower and cooling method for spot welding machine |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5593722A (en) * | 1978-12-29 | 1980-07-16 | Seiki Kogyo Kk | Line-up and assembly method and device for square body |
-
1987
- 1987-08-26 JP JP62213645A patent/JP2539844B2/en not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
---|
翻訳・監修大江礼三郎外一名「紙およびパルプ製紙の化学と技術第2巻(昭59−2−29)中外産業調査会P.384−406 |
Also Published As
Publication number | Publication date |
---|---|
JPS6461590A (en) | 1989-03-08 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |