JPH04503537A - Method and apparatus for washing pulp suspension - Google Patents

Method and apparatus for washing pulp suspension

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Publication number
JPH04503537A
JPH04503537A JP2-503387A JP50338790A JPH04503537A JP H04503537 A JPH04503537 A JP H04503537A JP 50338790 A JP50338790 A JP 50338790A JP H04503537 A JPH04503537 A JP H04503537A
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Japan
Prior art keywords
container
suction tube
cone
particles
diameter
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Pending
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JP2-503387A
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Japanese (ja)
Inventor
ボーマン,オーケ
Original Assignee
コルマン,ミラン
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Application filed by コルマン,ミラン filed Critical コルマン,ミラン
Publication of JPH04503537A publication Critical patent/JPH04503537A/en
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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】 パルプ懸濁液を洗浄する方法及び装置 本発明はパルプ懸濁液を洗浄して軽重に関係なく汚染粒子を除去し、しかも繊維 損失を伴なわない洗浄方法及び装置に係わる。[Detailed description of the invention] Method and apparatus for washing pulp suspension The present invention cleans pulp suspensions to remove contaminant particles regardless of weight and fibers. Relates to lossless cleaning methods and devices.

本発明の目的は軽重に関係なく汚染粒子を除去することのできる効率の高いパル プ懸濁液洗浄方法及び装置を提供することにある。本発明を公知技術と区別する 特徴は後掲の請求の範囲に開示した通りである。The purpose of the present invention is to develop a highly efficient pulp that can remove contaminant particles regardless of their weight or weight. An object of the present invention is to provide a method and apparatus for cleaning a liquid suspension. Distinguishing the invention from known technology The features are as disclosed in the claims below.

添付の図面に沿って本発明を以下に詳述する。添付図面中、 図1は重い汚染粒子を分離する場合について本発明の繊維回収系の好ましい実施 例を一部断面に略図する側面図である。The invention will be described in detail below with reference to the accompanying drawings. In the attached drawings, FIG. 1 shows a preferred implementation of the fiber recovery system of the present invention for the separation of heavy contaminant particles. FIG. 3 is a schematic side view, partially in section, of an example;

図2はポリマーや粘着物のような軽い汚染粒子を分離する場合について本発明の 繊維回収系の実施例を一部断面で略示する側面図である。Figure 2 shows the method of the present invention for separating light contaminant particles such as polymers and sticky substances. FIG. 2 is a side view schematically showing an example of a fiber recovery system, partially in cross section.

図1に示す本発明の繊維回収系は円錐体1、これに続く円錐状筐体2、吸引管3 、容器4,5及び少なくとも2つの容器4.5を設けた場合なら少なくとも1本 の接続管6を含む接続機構から成る。図示しないサイクロンの下方円錐体及びフ ランジを円錐体1のフランジ7と連結する。The fiber recovery system of the present invention shown in FIG. , containers 4, 5 and at least one if at least two containers 4.5 are provided. The connecting mechanism includes a connecting pipe 6. Lower cone and flap of cyclone (not shown) Connect the flange with the flange 7 of the cone 1.

洗浄すべき繊維またはパルプ懸濁液を所定圧下にサイクロンの入口から接線方向 に注入する。サイクロンにおいて懸濁液は合格分(洗浄ずみ懸濁液)と不合格分 (重い汚染粒子はもちろん、軽い汚染粒子であってもとにかく汚染粒子を含有し たままの未洗浄懸濁液)とに分けられる。公知技術ではすべての繊維をリサイク ルさせ、洗浄液に回収することは不可能であり、繊維の一部は海中へ放出される 。これに反して本発明ではすべての繊維がリサイクルされ、例えば洗浄設備の最 終段階で回収される。The fibers or pulp suspension to be cleaned is tangentially removed from the cyclone inlet under a predetermined pressure. Inject into. In the cyclone, the suspension is separated into a passed part (washed suspension) and a rejected part. (Not only heavy contaminant particles, but also light contaminant particles contain contaminant particles. (unwashed suspension) and Known technology recycles all fibers It is impossible to collect the fibers in cleaning solutions, and some of the fibers are released into the sea. . In contrast, in the present invention all fibers are recycled, e.g. It is collected at the final stage.

本発明の方法による洗浄または分離は不合格分を円錐体1に押入し、半径dの出 口13にむかって押圧することによって行われる。不合格分は円錐筐体2内で広 がり、容器4と吸引管3の間の間隙17から容器4へ流入する。Cleaning or separation according to the method of the invention involves forcing the rejects into a cone 1 and exiting with radius d. This is done by pressing towards the mouth 13. The rejected portion is spread out inside the conical casing 2. The liquid flows into the container 4 through the gap 17 between the container 4 and the suction tube 3.

高さHが繊維回収系における滞留時間を決定する容器4゜5において、重い汚染 粒子が分離される(例えば懸濁液中の砂)。パルプ懸濁液は接続管6を通って容 器5に流入するが、この過程が細かい砂を分離するのに都合よく作用する。重い 汚染粒子は両容器の底に沈積するから、両容器の底から手作業でまたは自動的に 沈積物を取出すことができる。Heavy contamination occurs in the vessel 4°5, the height H of which determines the residence time in the fiber recovery system. Particles are separated (e.g. sand in suspension). The pulp suspension passes through the connecting pipe 6. This process favorably separates the fine sand. heavy Contaminant particles settle at the bottom of both containers, so remove them manually or automatically from the bottom of both containers. You can take out the sludge.

懸濁液が間隙17から容器4へ流入する時、円錐体1の直径dの出口と吸引管3 の直径りの開口端16との間に真空ゾーンが発生し、その結果、吸引管3の尾端 18のレベルに達した懸濁液は残らず円錐体1を通ってサイクロンへ逆流する。When the suspension flows into the container 4 through the gap 17, the outlet of diameter d of the cone 1 and the suction tube 3 A vacuum zone is generated between the open end 16 of the diameter of the suction tube 3 and the tail end of the suction tube 3 All of the suspension that has reached the level 18 flows back through the cone 1 to the cyclone.

円錐体1の出口13の直径dと吸引管3の開口端16の直径りは以下に述べるよ うに極めて重要である。容量が小さい、例えば1001/mtnのサイクロンま たはクリーナの場合、円錐体1の出口直径dが小さい(例えば数mm)のが特徴 である。吸引管3には円錐体1の直径dの出口13よりも繊維が詰まり易いから 、吸引管3の開口端16は円錐体1の出口13と同じ大きさに設定してはならな い。The diameter d of the outlet 13 of the cone 1 and the diameter of the open end 16 of the suction tube 3 are as described below. Sea urchins are extremely important. A cyclone with a small capacity, e.g. 1001/mtn In the case of a cone or cleaner, the outlet diameter d of the cone 1 is small (for example, several mm). It is. This is because the suction tube 3 is more likely to be clogged with fibers than the outlet 13 of the cone body 1 having a diameter of d. , the open end 16 of the suction tube 3 must be sized the same as the outlet 13 of the cone 1. stomach.

吸引管3の開口端16の直径りは直径dよりもはるかに大きくなければならない 。円錐体1の直径dが約30〜40m+nに達する場合にのみ、直径りも40m mに設定できる。dを大きく取る場合、直径りは直径dより小さくてもよく、図 1に示す距離Aはゼロにまで縮めることができる。円錐体1及び吸引管3の幾何 的条件、円錐体1の直径dの出口13から吸引管3の直径りの開口端16までの 距離A、(高さHに応じて異なる)容器内での懸濁液の滞留時間及び容器の数の 総てが繊維回収系の洗浄効率の決定に関係する。The diameter of the open end 16 of the suction tube 3 must be much larger than the diameter d. . Only if the diameter d of the cone 1 reaches approximately 30-40 m+n, the diameter also reaches 40 m. It can be set to m. If d is set large, the diameter may be smaller than the diameter d, as shown in Fig. The distance A shown in 1 can be reduced to zero. Geometry of cone 1 and suction tube 3 conditions, from the outlet 13 of the cone 1 with a diameter d to the diametrically open end 16 of the suction tube 3. of the distance A, the residence time of the suspension in the container (depending on the height H) and the number of containers. All are relevant to determining the cleaning efficiency of the fiber recovery system.

繊維回収系が吸引管3を具えた単一の容器4を含むように構成してもよいし、接 続管6を介して互いに接続する複数の容器を含むように構成してもよい。容器4 には希釈を必要とする場合に給水するための弁8を設ける。The fiber recovery system may be configured to include a single container 4 with a suction tube 3 or a It may be configured to include a plurality of containers connected to each other via the continuation pipe 6. container 4 A valve 8 is provided for supplying water when dilution is required.

繊維粘稠度を低下させれば洗浄効率が高まる。Reducing fiber consistency increases cleaning efficiency.

ある種のパルプ懸濁液中に存在することがある例えば接着性物質(粘着物)のよ うな軽い汚染粒子の分離は図2に示す構成によって行うことができる。このよう な粘着物は特に故紙からリサイクルされた繊維中に存在し、封筒(糊)や書籍の 背などから出て来る。不合格分に含まれる繊維を粘着物から分離し、この洗浄ず み繊維を合格分に戻すには一部の変更はあるが重い汚染粒子に関して述べたのと 同様に処理する。接続管9は接続される単数または複数の容器の上部で終るよう に構成する。即ち、粘着物は容器上部の表面に集合(集積)するからである。For example, adhesive substances (stickies) that may be present in some pulp suspensions. Separation of such light contaminant particles can be achieved by the configuration shown in FIG. like this Sticky substances are especially present in fibers recycled from waste paper, and are found in envelopes (glue) and books. It comes out from the back. The fibers contained in the rejected material are separated from the sticky material, and the cleaning process The same method as described for heavy contaminant particles is used, although there are some changes to bring the fibers back to acceptable quality. Process in the same way. The connecting tube 9 terminates at the top of the vessel or vessels to be connected. Configure. That is, the sticky substance collects (accumulates) on the upper surface of the container.

粘着物を含んでいないパルプ懸濁液を吸引するため、容器の底に近い比較的低い レベルに吸引管10を設ける。relatively low near the bottom of the container to aspirate the pulp suspension that does not contain sticky substances. A suction pipe 10 is provided at the level.

接続管9の上部の直ぐ下に弁11を設けることにより、濃縮された粘着物を含む 懸濁液を放出する。軽い汚染粒子は外部から、例えば、軽い汚染粒子を分離する が多量の良質繊維をも保持しているサイクロンから図2に示す容器5の接続管1 2に供給される。By providing a valve 11 just below the top of the connecting pipe 9, it is possible to contain concentrated sticky substances. Release the suspension. Light pollution particles are separated from the outside, e.g. The connecting pipe 1 of the container 5 shown in FIG. 2.

補正書の写しく翻訳文)提出書 (特許法第184条の8) 平成3年8月13日同Copy and translation of written amendment) Submission form (Article 184-8 of the Patent Law) Same as August 13, 1991

Claims (3)

【特許請求の範囲】[Claims] 1.パルプ懸濁液を洗浄して重い汚染粒子だけでなく軽い汚染粒子をも除去する ため繊維回収系が接続手段(1,2)を介してサイクロンまたはクリーナと接続 可能な開口部(15)を有する少なくとも1つの容器(4,5)から成る装置に おいて、前記接続手段(1,2)が容器(4)にむかって収斂し、端部が所定の 直径(d)を有する出口(13)を画定する円錐体(1)から成り、この円錐体 (1)の前記出口(13)が容器(4)の開口部(15)から所定の距離(A) に位置するように前記円錐体(1)を容器(4)の開口部(15)に自由端部( 14)を固定した円錐状筐体(2)内に挿入配置し、且つ容器(4)が吸引管( 3)を含み、この吸引管(3)がその一端に容器(4)の開口部(15)と同心 関係の位置を占める所定の直径(D)の開口端(16)を有して前記開口部(1 5)において吸引管(3)と容器(4)の間に環状間隙(17)を形成し、前記 吸引管(3)が下向きに延設されて容器(4)または隣接の容器内に達し、容器 底から所定の距離に第2の端部(18)を有し、パルプ懸濁液から分離すべき汚 染粒子の軽重に従って前記距離が決定されることを特徴とする装置。1. Washing the pulp suspension to remove not only heavy contamination particles but also light contamination particles Therefore, the fiber recovery system is connected to the cyclone or cleaner via connecting means (1, 2). a device consisting of at least one container (4, 5) with a possible opening (15); , the connecting means (1, 2) converge towards the container (4) and the ends meet in a predetermined position. consisting of a cone (1) defining an outlet (13) with a diameter (d); The outlet (13) of (1) is at a predetermined distance (A) from the opening (15) of the container (4). Insert the cone (1) into the opening (15) of the container (4) so that the free end ( 14) is inserted into the fixed conical casing (2), and the container (4) is connected to the suction tube ( 3), the suction tube (3) having one end thereof concentric with the opening (15) of the container (4). said opening (1) with an open end (16) of a predetermined diameter (D) occupying a position in relation to said 5) forming an annular gap (17) between the suction tube (3) and the container (4); A suction tube (3) extends downward into the container (4) or an adjacent container, having a second end (18) at a predetermined distance from the bottom and containing the dirt to be separated from the pulp suspension; An apparatus characterized in that the distance is determined according to the weight and weight of dye particles. 2.吸引管(3)の開口端(16)の直径(D)が好ましくは円錐体(1)の出 口(13)の直径(d)よりも大きいことを特徴とする請求項1記載の装置。2. The diameter (D) of the open end (16) of the suction tube (3) preferably corresponds to the exit of the cone (1). Device according to claim 1, characterized in that it is larger than the diameter (d) of the mouth (13). 3.請求項1記載の装置を含む繊維回収系によってパルプ懸濁液から重い汚染粒 子だけでなく軽い汚染粒子をも除去する洗浄方法において、サイクロンから供給 される不合格分を円錐体(1)に押入し、その出口(13)から下方へ押出すこ とによって円錐状筐体(2)内で膨拡させ、間隙(17)から容器(4)へ流入 させることで真空を発生させ、この真空により吸引管(3)の末端(18)付近 のパルプ懸濁液を残らず吸引管(3)へ、さらに円錐体(1)を通ってサイクロ ンまたはクリーナへ逆流させることを特徴とする洗浄方法。3. Heavy contaminated particles are removed from the pulp suspension by a fiber recovery system comprising an apparatus according to claim 1. In a cleaning method that removes not only particles but also light contaminant particles, The rejected portion is pushed into the cone (1) and pushed out from the outlet (13) downwards. It expands and expands within the conical casing (2) and flows into the container (4) through the gap (17). This generates a vacuum, which causes the suction tube (3) near the end (18) The entire pulp suspension is passed through the suction tube (3) and through the cone (1) into the cyclone. A cleaning method characterized by backflowing into a tank or cleaner.
JP2-503387A 1989-02-13 1990-02-13 Method and apparatus for washing pulp suspension Pending JPH04503537A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE8900472-5 1989-02-13

Publications (1)

Publication Number Publication Date
JPH04503537A true JPH04503537A (en) 1992-06-25

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