JP2523789Y2 - Pulper - Google Patents
PulperInfo
- Publication number
- JP2523789Y2 JP2523789Y2 JP11158890U JP11158890U JP2523789Y2 JP 2523789 Y2 JP2523789 Y2 JP 2523789Y2 JP 11158890 U JP11158890 U JP 11158890U JP 11158890 U JP11158890 U JP 11158890U JP 2523789 Y2 JP2523789 Y2 JP 2523789Y2
- Authority
- JP
- Japan
- Prior art keywords
- processing chamber
- chamber
- strainer
- raw material
- 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.)
- Expired - Fee Related
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
- Crushing And Grinding (AREA)
- Paper (AREA)
Description
【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、主として原料中に異物を含む故紙の再離解
等の製紙原料処理に用いられるパルパーに関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention mainly relates to a pulper used for papermaking raw material processing such as re-disintegration of waste paper containing foreign matter in the raw material.
この種のパルパーとしては、第４図に示すように、タ
ブ21内の底部付近に原料に回流を与えるロータ22を回転
可能に備え、このロータ22に近接して５〜20mmφ程度の
孔径をもつストレーナ23を設け、ストレーナ23の下部を
処理原料室24とし、処理原料室24に排出管25を連結した
ものが知られている。As shown in FIG. 4, this type of pulper is provided with a rotatable rotor 22 for circulating the raw material near the bottom of the tub 21 and having a hole diameter of about 5 to 20 mmφ in the vicinity of the rotor 22. It is known that a strainer 23 is provided, a lower portion of the strainer 23 is a processing raw material chamber 24, and a discharge pipe 25 is connected to the processing raw material chamber 24.
上記従来のパルパーによる処理においては、原料中の
異物は次第にタブ21内に溜り、時間の経過と共にタブ21
内の異物濃度が高まり、異物はロータ22の回転によって
破砕され、ストレーナ23を通過し、処理原料室25を経て
処理原料と共に排出管25から排出されて次工程に送られ
てしまい、製品の品質低下、抄紙機用具の汚れ等を生
じ、抄紙機での生産性を低下させることが多かった。In the above-mentioned conventional treatment with a pulper, foreign substances in the raw material gradually accumulate in the tub 21, and as time elapses, the tub 21 is removed.
The concentration of foreign matter in the inside increases, and the foreign matter is crushed by the rotation of the rotor 22, passes through the strainer 23, passes through the processing raw material chamber 25, is discharged from the discharge pipe 25 together with the processing raw material, and is sent to the next process. In many cases, the productivity and the productivity of the paper machine are reduced.
従って、異物は破砕される前に大きな状態で系外に除
去することが重要であり、そのための一方法として、第
５図に示すように、ストレーナ23の一部を大きな孔径
（例えば50mmφ）として、この部分に処理原料室24を貫
通した異物抜出管26を開口し、異物を含んだ原料を抜き
出しポンプ27で図示しない粗選機等に送る方法がある
が、この方法ではストレーナ23の開口面積が小さくな
り、パルパーの処理能力を低下させるという問題があっ
た。Therefore, it is important to remove the foreign matter from the system in a large state before being crushed. As one method for this purpose, as shown in FIG. 5, a part of the strainer 23 is formed with a large hole diameter (for example, 50 mmφ). In this part, there is a method of opening a foreign matter extraction pipe 26 penetrating the processing raw material chamber 24 and extracting the raw material containing the foreign matter with a pump 27 and sending it to a roughing machine (not shown). In this method, the opening of the strainer 23 is used. There is a problem that the area becomes small and the processing capacity of the pulper is reduced.
また、パルパーは、通常の故紙処理では25〜65m3もの
大きな容量のタブを必要とし、タブ内に供給された原料
はロータとの接触で離解されることから、タンク，ロー
タの形状等を種々工夫して、できるだけ原料とロータと
の接触回数を増すようにしているが限界がある。そこ
で、タブ内の滞留時間を８〜15分と長くとる必要があ
り、そのために大きな設備を必要としていた。Further, pulper, in the normal waste paper processing requires a tab of larger capacity 25～65M 3 things, various raw material supplied to the tub from being macerated in contact with the rotor, a tank, the shape of the rotor or the like By devising, the number of times of contact between the raw material and the rotor is increased as much as possible, but there is a limit. Therefore, it is necessary to increase the residence time in the tub to 8 to 15 minutes, which requires a large facility.
本考案は、これら従来の問題点を解消し、パルパー処
理を効果的にし、原料中の有用繊維を効率よく回収し、
処理能力の増大を図り、合理的な運転が可能となり、信
頼性が高まるパルパーを提供することを目的とするもの
である。The present invention solves these conventional problems, makes the pulper treatment effective, efficiently collects useful fibers in the raw material,
It is an object of the present invention to provide a pulper that increases the processing capacity, enables rational operation, and increases reliability.
本考案においては、上述の目的を達成するため、タブ
内を垂直隔壁で１次処理室と２次処理室とに区画すると
ともに、前記１次処理室を２次処理室よりも高く位置さ
せ、各室の底部付近にロータを回転可能に備え、該ロー
タに近接してストレーナを設けてその下部を処理原料室
とし、前記１次処理室の処理原料室と２次処理室のスト
レーナより上部とを移送管で連結し、前記２次処理室の
ストレーナより上部に異物排出部を設けるとともに、前
記２次処理室の処理原料室に処理原料排出部を設け、さ
らに前記２次処理室のストレーナの孔径を１次処理室の
ストレーナの孔径よりも小さくするようにしている。In the present invention, in order to achieve the above object, the inside of the tub is partitioned into a primary processing chamber and a secondary processing chamber by a vertical partition, and the primary processing chamber is positioned higher than the secondary processing chamber, A rotor is rotatably provided near the bottom of each chamber, and a strainer is provided near the rotor to make a lower part thereof a processing raw material chamber, and a processing raw material chamber of the primary processing chamber and an upper part than a strainer of the secondary processing chamber. Are connected by a transfer pipe, a foreign matter discharge section is provided above the strainer of the secondary processing chamber, a processing material discharge section is provided in the processing raw material chamber of the secondary processing chamber, and a strainer of the secondary processing chamber is further provided. The hole diameter is made smaller than the hole diameter of the strainer in the primary processing chamber.
本考案のパルパーでは、原料はまず１次処理室に供給
され、ロータによって回流が与えられ、原料がロータと
接触して離解が行われる。この時、原料中に含まれる粗
大異物を、ラガー又はホーク式異物除去装置（特公昭45
-561号公報参照）、あるいは他の公知の異物除去装置で
取り除く。In the pulper according to the present invention, the raw material is first supplied to the primary treatment chamber, and then circulated by the rotor, and the raw material comes into contact with the rotor to be disintegrated. At this time, large foreign substances contained in the raw material are removed by a lager or hawk type foreign substance removing device
-561) or another known foreign matter removing device.
１次処理室で離解が行われた原料は、細かい異物と共
にストレーナを通過して処理原料室に至るが、原料がス
トレーナを通過する際にさらにロータと原料が効果的に
接触し離解が促進され、この１次処理室原料は処理原料
室から移送管を経て２次処理室に移送される。The raw material that has been disaggregated in the primary processing chamber passes through the strainer together with fine foreign substances to reach the processing raw material chamber. However, when the raw material passes through the strainer, the rotor and the raw material are more effectively contacted to promote disaggregation. The raw material in the primary processing chamber is transferred from the processing raw material chamber to the secondary processing chamber via a transfer pipe.
２次処理室に移送された１次処理原料は、２次処理室
のストレーナの孔径が１次処理室のストレーナの孔径よ
りも小さいため、１次処理原料はそのままストレーナを
通過することなく、ロータによって回流が与えられ、さ
らにロータと接触して離解されると同時にストレーナを
通過しない異物等は異物排出部から排出される。The primary processing raw material transferred to the secondary processing chamber has a hole diameter of the strainer in the secondary processing chamber smaller than that of the strainer in the primary processing chamber. Thus, foreign matter and the like which are disintegrated while being in contact with the rotor and not passing through the strainer are discharged from the foreign matter discharge portion.
このように、１次処理室と２次処理室とで２回にわた
って効果的に離解された原料は、２次処理室のストレー
ナを通過して２次処理原料として処理原料室に至り、原
料排出部から排出されて次工程へ導かれる。As described above, the raw material effectively disintegrated twice in the primary processing chamber and the secondary processing chamber passes through the strainer of the secondary processing chamber, reaches the processing raw material chamber as the secondary processing raw material, and discharges the raw material. It is discharged from the section and led to the next process.
本考案の一実施例を第１図及び第２図を参照しながら
説明すれば、タブ１内は垂直隔壁２によって１次処理室
３−１と２次処理室３−２とに区画され、１次処理室３
−１内の底部付近には１次ロータ４−１が回転可能に備
えられ、１次ロータ４−１に近接して50〜150mmφ程度
の孔径をもった１次ストレーナ５−１が設けられ、１次
ストレーナ５−１の下部を１次処理原料室６−１として
ある。One embodiment of the present invention will be described with reference to FIGS. 1 and 2. The inside of a tub 1 is divided into a primary processing chamber 3-1 and a secondary processing chamber 3-2 by a vertical partition 2, Primary processing room 3
-1, a primary rotor 4-1 is rotatably provided near the bottom, and a primary strainer 5-1 having a hole diameter of about 50 to 150 mmφ is provided near the primary rotor 4-1. The lower part of the primary strainer 5-1 is a primary processing raw material chamber 6-1.
なお、１次処理室３−１には大型異物を除去するため
のラガーその他の異物除去装置（図示せず）が備えられ
ている。The primary processing chamber 3-1 is provided with a lager or other foreign matter removing device (not shown) for removing large foreign matter.
また、２次処理室３−２内の底部付近には２次ロータ
４−２が回転可能に備えられ、２次ロータ４−２に近接
して１次ストレーナ５−１の孔径より小さい５〜25mmφ
程度の孔径をもった２次ストレーナ５−２が設けられ、
２次ストレーナ５−２の下部を２次処理原料室としてあ
る。A secondary rotor 4-2 is rotatably provided near the bottom in the secondary processing chamber 3-2. The secondary rotor 4-2 is close to the secondary rotor 4-2 and smaller than the hole diameter of the primary strainer 5-1. 25mmφ
A secondary strainer 5-2 having a hole diameter of about
The lower part of the secondary strainer 5-2 is a secondary processing material chamber.
さらに、１次処理室３−１の１次処理原料室６−１と
２次処理室３−２の２次ストレーナ５−２より上部と
は、移送管７で連結されて１次処理室３−１の１次処理
原料が２次処理室３−２へ移送されるようになってお
り、１次処理室３−１と２次処理室３−２に図示例のよ
うに段差をつけて自然流下で移送が行われるようにした
が、移送管７中にポンプを介在させる（第３図参照）こ
ともできる。Furthermore, the primary processing chamber 6-1 of the primary processing chamber 3-1 and the upper part of the secondary processing chamber 3-2 above the secondary strainer 5-2 are connected by a transfer pipe 7 so as to be connected to the primary processing chamber 3-1. -1 is transferred to the secondary processing chamber 3-2, and the primary processing chamber 3-1 and the secondary processing chamber 3-2 are provided with a step as shown in the illustrated example. Although the transfer is performed under the natural flow, a pump can be interposed in the transfer pipe 7 (see FIG. 3).
また、２次処理室３−２の２次ストレーナ５−２より
上部に異物排出管９が開口し、２次処理原料室６−２に
はポンプ11（第３図参照）の吸込側に連なる２次処理原
料排出管10が開口している。A foreign matter discharge pipe 9 opens above the secondary strainer 5-2 of the secondary processing chamber 3-2, and the secondary processing raw material chamber 6-2 is connected to the suction side of the pump 11 (see FIG. 3). The secondary processing raw material discharge pipe 10 is open.
第３図は前記本考案のパルパーの一使用例を示す系統
説明図で、２次処理室３−２の異物排出管９をポンプ12
を介してサイクロン式のメタルトラップ13及び粗選器14
へ連結してある。FIG. 3 is a system explanatory view showing an example of use of the pulper according to the present invention.
Through the cyclone-type metal trap 13 and roughing device 14
Connected to
従って、原料は１次処理室３−１に供給され、原料中
のなわ、ひも等の大型異物は、１次処理室３−１に付属
されるラガー等で除去され、１次ロータ４−１によって
離解が行われる。１次処理室３−１の１次ストレーナ５
−１の孔径は50〜150mmφと大きいために、大型異物だ
けをラガー等で除去すれば、その他の異物は原料と共に
１次ストレーナ５−１を通って１次処理原料室６−１に
至り、移送管７を経て２次処理室３−２に送られる。こ
れらの異物は２次処理室３−２の２次ストレーナ５−２
より上部に開口された異物排出管９から原料の一部と共
にポンプ12によって抜き出され、メタルトラップ13及び
粗選機14へ送られる。この異物と原料は、１次処理室３
−１の50〜150mmφの１次ストレーナ５−１を通過した
ものであるため、移送用のポンプ8,12等に詰りを発生さ
せることなく、操業が安定する。また、メタルトラップ
13、粗選機14は、場所を選ばずにいかなる所にも設置で
きるので、設置場所の制限を受けず、これらから廃棄さ
れる粕の処理も容易となる。Therefore, the raw material is supplied to the primary processing chamber 3-1 and large foreign substances such as lines and strings in the raw material are removed by a lager or the like attached to the primary processing chamber 3-1 and the primary rotor 4-1. Disintegration is performed. Primary strainer 5 of primary processing chamber 3-1
Since the hole diameter of -1 is as large as 50 to 150 mmφ, if only large foreign matter is removed with a lager or the like, the other foreign matter passes through the primary strainer 5-1 together with the raw material to reach the primary processing raw material chamber 6-1. It is sent to the secondary processing chamber 3-2 via the transfer pipe 7. These foreign substances are removed from the secondary strainer 5-2 of the secondary processing chamber 3-2.
A part of the raw material is taken out of the foreign matter discharge pipe 9 opened at the upper part by a pump 12 together with a part of the raw material, and sent to a metal trap 13 and a roughing machine 14. The foreign matter and the raw material are supplied to the first processing chamber 3
-1 has passed through the primary strainer 5-1 having a diameter of 50 to 150 mmφ, so that the operation is stabilized without causing clogging of the transfer pumps 8, 12 and the like. Also metal trap
13. Since the roughing machine 14 can be installed in any place regardless of the place, there is no restriction on the installation place, and the treatment of the waste discarded from these can be facilitated.
一方、２次処理室３−２で再び離解された原料は、２
次ストレーナ５−２を通過して２次処理原料室６−２に
至り、２次処理原料排出管10からポンプ11により次工程
へ移送される。また、粗選機14で分離された原料は次工
程あるいは２次処理室３−２にリサイクルされる。On the other hand, the raw material re-disintegrated in the secondary processing chamber 3-2 is
After passing through the next strainer 5-2, it reaches the secondary processing raw material chamber 6-2, and is transferred from the secondary processing raw material discharge pipe 10 to the next process by the pump 11. The raw materials separated by the roughing machine 14 are recycled to the next process or the secondary processing chamber 3-2.
以上のように本考案によれば、タブ内を垂直隔壁で１
次処理室と２次処理室とに区画するとともに、前記１次
処理室を２次処理室よりも高く位置させ、各室の底部付
近にロータを回転可能に備え、該ロータに近接してスト
レーナを設けてその下部を処理原料室とし、前記１次処
理室の処理原料室と２次処理室のストレーナより上部と
を移送管で連結し、前記２次処理室のストレーナより上
部に異物排出部を設けるとともに、前記２次処理室の処
理原料室に処理原料排出部を設け、さらに前記２次処理
室のストレーナの孔径を１次処理室のストレーナの孔径
よりも小さくするようにしているので、タブ内の原料に
対して２回にわたって充分な離解作用を施すことがで
き、効果的な離解を行って有用繊維を極めて効率よく回
収することができるという効果がある。また、原料の滞
留時間を短くし、処理能力を増大させて安定した運転が
可能になり、信頼性が大幅に高まり、しかも、設備の縮
小にもつながる等の多くの有用なる効果を奏する。さら
に、１次処理室を２次処理室よりも高く位置させるの
で、移送管に処理原料の詰まることがなく、これを通じ
て円滑なパルパー作業が大いに期待できる。As described above, according to the present invention, the inside of the tub is separated by a vertical partition.
A first processing chamber is positioned higher than the second processing chamber, a rotor is rotatably provided near a bottom of each chamber, and a strainer is provided near the rotor. And a lower portion thereof is used as a processing material chamber, and a processing material chamber of the primary processing chamber is connected to an upper part of a strainer of the secondary processing chamber by a transfer pipe, and a foreign matter discharge section is provided above the strainer of the secondary processing chamber. And a processing material discharge part is provided in the processing material chamber of the secondary processing chamber, and the hole diameter of the strainer of the secondary processing chamber is made smaller than the hole diameter of the strainer of the primary processing chamber. The material in the tub can be sufficiently disintegrated twice, and there is an effect that effective disintegration can be performed and useful fibers can be collected extremely efficiently. In addition, a stable operation can be performed by shortening the residence time of the raw material and increasing the processing capacity, so that the reliability is greatly increased, and moreover, many useful effects such as reduction in equipment are exhibited. Further, since the primary processing chamber is positioned higher than the secondary processing chamber, the transfer pipe is not clogged with the processing raw material, through which smooth pulper work can be greatly expected.
第１図は本考案の一実施例を示す縦断側面図、第２図は
平面図、第３図は本考案の一使用例を示す系統説明図、
第４図及び第５図は従来例の縦断側面図である。 １……タブ、２……垂直隔壁、３−１……１次処理室、
３−２……２次処理室、４−１……１次ロータ、４−２
……２次ロータ、５−１……１次ストレーナ、５−２…
…２次ストレーナ、６……１次処理原料室、６−２……
２次処理原料室、７……移送管、９……異物排出管、10
……２次処理原料排出管、21……タブ、22……ロータ、
23……ストレーナ、24……処理原料室、25……排出管、
26……異物抜出管。FIG. 1 is a longitudinal side view showing one embodiment of the present invention, FIG. 2 is a plan view, FIG. 3 is a system explanatory diagram showing one use example of the present invention,
4 and 5 are longitudinal sectional side views of a conventional example. 1 ... tab, 2 ... vertical partition, 3-1 ... primary processing chamber,
3-2: Secondary processing chamber, 4-1: Primary rotor, 4-2
…… Secondary rotor, 5-1 …… Primary strainer, 5-2…
... Secondary strainer, 6 ... Primary processing raw material chamber, 6-2 ...
Secondary processing raw material chamber, 7 Transfer pipe, 9 Foreign matter discharge pipe, 10
…… Secondary processing material discharge pipe, 21 …… Tab, 22 …… Rotor
23 …… Strainer, 24 …… Processing material room, 25 …… Discharge pipe,
26 ... Foreign matter extraction tube.
Claims (1)
室とに区画するとともに、前記１次処理室を２次処理室
よりも高く位置させ、各室の底部付近にロータを回転可
能に備え、該ロータに近接してストレーナを設けてその
下部を処理原料室とし、前記１次処理室の処理原料室と
２次処理室のストレーナより上部とを移送管で連結し、
前記２次処理室のストレーナより上部に異物排出部を設
けるとともに、前記２次処理室の処理原料室に処理原料
排出部を設け、さらに前記２次処理室のストレーナの孔
径を１次処理室のストレーナの孔径よりも小さくしたこ
とを特徴とするパルパー。1. The inside of a tub is partitioned into a primary processing chamber and a secondary processing chamber by a vertical partition, and the primary processing chamber is positioned higher than the secondary processing chamber, and a rotor is provided near the bottom of each chamber. Provided rotatably, a strainer is provided in proximity to the rotor, the lower part of which is a processing material chamber, and the processing material chamber of the primary processing chamber and the upper part of the strainer of the secondary processing chamber are connected by a transfer pipe,
A foreign matter discharge section is provided above the strainer of the secondary processing chamber, a processing material discharge section is provided in the processing raw material chamber of the secondary processing chamber, and the hole diameter of the strainer of the secondary processing chamber is reduced. A pulper characterized by having a smaller diameter than the strainer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11158890U JP2523789Y2 (en) | 1990-10-26 | 1990-10-26 | Pulper |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11158890U JP2523789Y2 (en) | 1990-10-26 | 1990-10-26 | Pulper |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0469494U JPH0469494U (en) | 1992-06-19 |
| JP2523789Y2 true JP2523789Y2 (en) | 1997-01-29 |
Family
ID=31859055
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11158890U Expired - Fee Related JP2523789Y2 (en) | 1990-10-26 | 1990-10-26 | Pulper |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2523789Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4686070B2 (en) * | 2001-08-01 | 2011-05-18 | 道栄紙業株式会社 | Pulper |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3925150A (en) * | 1973-04-06 | 1975-12-09 | Black Clawson Co | Selective reclamation of waste paper products |
| JPH0219585A (en) * | 1988-07-06 | 1990-01-23 | Iwashina Seisakusho:Kk | Apparatus for removing foreign material of pulper |
-
1990
- 1990-10-26 JP JP11158890U patent/JP2523789Y2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0469494U (en) | 1992-06-19 |
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| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |