US20100276100A1 - Dewatering device of used paper recycling apparatus and used paper recycling apparatus - Google Patents

Dewatering device of used paper recycling apparatus and used paper recycling apparatus Download PDF

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Publication number
US20100276100A1
US20100276100A1 US12/759,177 US75917710A US2010276100A1 US 20100276100 A1 US20100276100 A1 US 20100276100A1 US 75917710 A US75917710 A US 75917710A US 2010276100 A1 US2010276100 A1 US 2010276100A1
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United States
Prior art keywords
dewatering
roll
paper
unit
used paper
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Abandoned
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US12/759,177
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English (en)
Inventor
Shigeru Tamai
Yuji Koyama
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Seed Co Ltd
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Seed Co Ltd
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Assigned to SEED COMPANY LIMITED reassignment SEED COMPANY LIMITED ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: KOYAMA, YUJI, TAMAI, SHIGERU
Assigned to SEED COMPANY LIMITED reassignment SEED COMPANY LIMITED CORRECTIVE ASSIGNMENT TO CORRECT THE EXECUTION DATES OF THE ASSIGNORS PREVIOUSLY RECORDED ON REEL 024224 FRAME 0343. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Assignors: KOYAMA, YUJI, TAMAI, SHIGERU
Publication of US20100276100A1 publication Critical patent/US20100276100A1/en
Abandoned legal-status Critical Current

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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00—Fibrous raw materials or their mechanical treatment
    • D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30—Defibrating by other means
    • D21B1/32—Defibrating by other means of waste paper
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F3/00—Press section of machines for making continuous webs of paper
    • D21F3/02—Wet presses
    • D21F3/04—Arrangements thereof
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F9/00—Complete machines for making continuous webs of paper
    • D21F9/003—Complete machines for making continuous webs of paper of the twin-wire type
    • 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

Definitions

  • the present invention relates to a dewatering device of used paper recycling apparatus and a used paper recycling apparatus, and more particularly to a dewatering technology in a used paper recycling apparatus of furniture size, installed at the site of origin of used paper, for recycling and processing into reusable paper at the site without discarding the generated used paper.
  • Used paper of various types occurs not only in government offices or private companies, but also in daily life or general household. Used paper is usually discarded, incinerated, or disposed as refuse.
  • This used paper recycling apparatus is a realization of used paper recycling technology of large scale such as used paper recycling plant in a small size that can be installed in a small shop or a room in general household, and includes, in an apparatus case of furniture size, a pulp making unit for macerating and beating used paper to manufacture used paper pulp, a paper making unit for making recycled paper from the used paper pulp manufactured in this pulp making unit, and a control unit for driving and controlling the pulp making unit and the paper making unit in cooperation, in which the pulp making unit is composed of a macerating unit for agitating, crushing and macerating the used paper, and a beating unit for beating the used paper macerated in this macerating unit.
  • the used paper is agitated, macerated and beaten by the macerating unit of the pulp making unit, and made into pulp, and is further beaten and pulverized by the beating unit, and desired used paper pulp is obtained, and then this used paper pulp is processed in the paper making unit, that is, filtered and dewatered, squeezed and dewatered, and heated and dried, and recycled paper obtained.
  • the used paper in the state of pulp, the used paper is decomposed into fiber level, and the printed characters and diagrams are completely decomposed and lost, and cannot be restored, so that leak or disclosure of confidential information or personal information composed in printed characters and diagrams can be securely prevented.
  • the dewatering device of the used paper recycling apparatus of the present invention is a device for composing the dewatering unit of the paper making unit for manufacturing recycled paper from the used paper pulp manufactured in the pulp making unit of a preceding process, in the used paper recycling apparatus of furniture size to be installed at the site of origin of the used paper, being formed as dewatering roll means disposed at a linkage part between a paper making net conveyor unit for making wet paper by making from the slurry-type pulp suspension mixed of used paper pulp and water sent from the pulp making unit, and a drying belt conveyor unit for obtaining recycled paper by drying the wet paper made and formed in the paper making net conveyor unit, for squeezing and dewatering the wet paper on the mesh belt, by rolling and squeezing a mesh belt of the paper making net conveyor unit and a smooth surface belt of the drying belt conveyor unit, from both upper and lower sides in a compressed state, and this dewatering roll means includes at least a preliminary dewatering roll unit for squeezing and dewatering
  • Preferred embodiments include the following.
  • the preliminary squeezing force of the preliminary dewatering roll unit for preliminarily squeezing and dewatering the wet paper on the mesh belt is set so that the water content of the wet paper on the mesh belt after the preliminary dewatering process may be in a range of 80 to 75%.
  • the preliminary dewatering roll unit includes a preliminary squeezing roll pair consisting of a preliminary dewatering roll for rolling on the mesh belt from the lower side, and a preliminary press roll for rolling and pressurizing on the smooth surface belt from the upper side in cooperation with this preliminary dewatering roll, and by this preliminary squeezing roll pair, the mesh belt and the smooth surface belt are rolled and squeezed from the upper and lower sides in a compressed state at a specified preliminary pressure, so that the water content in the wet paper on the mesh belt is preliminarily removed.
  • the preliminary press roll is a cylindrical roll made of a material of high rigidity.
  • the preliminary press roll has an elastic layer made of hard rubber formed on the outer circumference of the cylindrical roll made of a material of high rigidity.
  • the preliminary dewatering roll is a cylindrical roll made of a material of high rigidity.
  • the preliminary dewatering roll has an elastic layer made of soft rubber formed on the outer circumference of the cylindrical roll made of a material of high rigidity.
  • the preliminary dewatering roll has a water absorbing layer made of a water absorbing material formed on the outer circumference of the cylindrical roll made of a material of high rigidity.
  • the water absorbing layer of the preliminary dewatering roll is made of a porous material having fine continuous pores.
  • the water absorbing layer of the preliminary dewatering roll is made of a fine fiber material having a bundled structure of ultra-fine fibers.
  • the water absorbing layer of the preliminary dewatering roll is made of Clarino.
  • the final squeezing pressure of the final dewatering roll unit for final squeezing and dewatering the wet paper on the mesh belt is set so that the water content of the dry paper on the mesh belt after the final dewatering process may be in a range of 70 to 65%.
  • the final dewatering roll unit includes at least one set of a set of final squeezing roll pair consisting of a final dewatering roll for rolling on the mesh belt from the lower side, and a final press roll for rolling and pressurizing on the smooth surface belt from the upper side in cooperation with this final dewatering roll, and by this final squeezing roll pair, the mesh belt and the smooth surface belt are rolled and squeezed from the upper and lower sides in a compressed state at a specified final pressure, so that the water content in the wet paper on the mesh belt is finally removed, and dry paper of a desired water content may be obtained.
  • the squeezing force of the final squeezing roll pair in the final dewatering roll unit is set at a same magnitude.
  • the squeezing force of the final squeezing roll pair in the final dewatering roll unit is to be greater gradually from the upstream side to the downstream side of the array direction.
  • the final press roll is a cylindrical roll made of a material of high rigidity.
  • the final press roll has an elastic layer made of hard rubber formed on the outer circumference of the cylindrical roll made of a material of high rigidity.
  • the final dewatering roll has a water absorbing layer made of a water absorbing material formed on the outer circumference of the cylindrical roll made of a material of high rigidity.
  • the water absorbing layer of the final dewatering roll is made of a porous material having fine continuous pores.
  • the water absorbing layer of the final dewatering roll is made of a fine fiber material having a bundled structure of ultra-fine fibers.
  • the water absorbing layer of the final dewatering roll is made of Clarino.
  • angle defining means is provided for defining the insertion angle of the mesh belt and the smooth surface belt into this preliminary dewatering roll unit.
  • the inclination angle of the mesh belt and the smooth surface belt is set at 1 to 20 degrees.
  • the angle defining means includes a mesh belt guide roll for defining the insertion angle of the mesh belt into the preliminary dewatering roll unit by rolling on the mesh belt from the lower side, and a smooth surface belt guide roll for defining the insertion angle of the smooth surface belt into the preliminary dewatering roll unit by rolling on the smooth surface belt from the upper side.
  • the mesh belt guide roll has a dewatering layer made of a porous material of fine continuous pores, formed on the outer circumference of the cylindrical roll of a material of high rigidity.
  • the smooth surface belt guide roll is a cylindrical roll made of a material of high rigidity.
  • the used paper recycling apparatus of the present invention includes, in an apparatus case of furniture size, a pulp making unit for manufacturing used paper pulp by macerating and beating used paper, a paper making unit for manufacturing recycled paper by making from the used paper pulp manufactured in this pulp making unit, and a control unit for driving and controlling the pulp making unit and the paper making unit in cooperation, in which the paper making unit includes the dewatering device as a dewatering unit.
  • this dewatering roll means includes at least a preliminary dewatering roll unit for squeezing and dewatering preliminarily the wet paper on the mesh belt, and a final dewatering roll unit for final squeezing and dewatering the wet paper on the mesh belt preliminarily dewatered in the preliminary dewatering roll unit to obtain dry paper of specified water content, and therefore in a very narrow used
  • the wet paper on the mesh belt is preliminarily squeezed and dewatered by the preliminary dewatering roll unit, and the wet paper preliminarily dewatered on the mesh belt is finally squeezed and dewatered by the final dewatering roll unit, and dry paper of specified water content is obtained, and therefore in a very narrow dewatering processing space in the linkage part between the paper making net conveyor unit and the drying belt conveyor unit, the wet paper of high water content can be squeezed and dewatered efficiently and securely and dry paper is obtained, and hence by the subsequent heating and drying process, recycled paper of high quality can be manufactured.
  • the present invention presents a used paper recycling apparatus of furniture size that can be installed not only in a large office, but also in a small shop or a general household, being friendly to the environment, low in running cost, capable of preventing leak or disclosure of confidential information, personal information, and various types of information, and capable of maintaining a high confidentiality.
  • FIG. 1 is a front sectional view of an overall outline configuration of a used paper recycling apparatus in preferred embodiment 1 of the present invention.
  • FIG. 2 is a side sectional view of an overall outline configuration of the same used paper recycling apparatus.
  • FIG. 3 is a circuit diagram of configuration of a used paper pulp circulation route of a beating unit of the used paper recycling apparatus.
  • FIG. 4 is a block diagram of configuration of a pulp concentration adjustment unit of the used paper recycling apparatus.
  • FIG. 5 is a magnified front view of configuration of a dewatering roll unit of the used paper recycling apparatus.
  • FIG. 6 is a perspective view of outline configuration of the used paper recycling apparatus.
  • FIG. 7 is a magnified front view of configuration of a dewatering roll unit of a used paper recycling apparatus in preferred embodiment 2 of the present invention.
  • FIG. 8 is a magnified front view of configuration of a dewatering roll unit of a used paper recycling apparatus in preferred embodiment 3 of the present invention.
  • the used paper recycling apparatus of the present invention is shown in FIG. 1 to FIG. 6 , and this used paper recycling apparatus 1 is specifically installed at the site of origin of used paper, and it is an apparatus for recycling into a re-usable paper at the site without discarding the generated used paper UP, and the used paper UP includes confidential documents of government offices or private companies, personal letters and others in the general household, and other used and unnecessary documents.
  • the used paper recycling apparatus 1 is a furniture size as shown in FIG. 6 , that is, small in size and shape similar to furniture, such as document rack, locker, office desk, copier or personal computer used in an office, and mainly includes, as shown in FIG. 1 , a pulp making unit 2 , a pulp concentration adjustment unit 3 , a paper making unit 4 , and an apparatus control unit (control unit) 5 , and the paper making unit 4 includes a dewatering device 10 which is a characteristic component of the present invention as a dewatering unit, and this dewatering device 10 is composed as a dewatering roll unit (dewatering roll means) for rolling, squeezing and dewatering the wet paper RP 0 on a mesh belt 105 of a paper making net conveyor 95 as described below.
  • a dewatering device 10 which is a characteristic component of the present invention as a dewatering unit
  • this dewatering device 10 is composed as a dewatering roll unit (dewatering roll means) for rolling, squeez
  • the apparatus case 6 is a furniture size as mentioned above, and specific dimensions and shapes may be designed appropriately depending on the purpose or application.
  • the apparatus case 6 in the shown preferred embodiment is a rectangular box having dimensions and shapes similar to a copier installed and used in a general office, and the top plate of the apparatus case 6 has an inlet 7 which is opened and closed for supplying used paper UP, and an outlet 8 is provided at the side for discharging recycled paper RP, RP, . . . .
  • a recycled paper receiving tray 9 is detachably provided for receiving recycled paper RP, RP, . . . discharged from the outlet 8 .
  • the pulp making unit 2 is a process for manufacturing used paper pulp by macerating and beating the used paper UP, and is composed of a macerating unit 20 for agitating, crushing and macerating the used paper UP, and a beating unit 21 for beating the used paper UP macerated in the macerating unit 20 .
  • the macerating unit 20 is a process for agitating, crushing and macerating the used paper UP, and is mainly composed of a macerating tank 25 , an agitating device 26 , and a water feed device 27 .
  • the macerating tank 25 has the inlet 7 formed in its ceiling wall as shown in FIG. 2 for charging and supplying the used paper UP, and a discharge port 28 is provided in its bottom wall for discharging the macerated used paper pulp UPP to the downstream side.
  • the inner volume of the macerating tank 25 is determined depending on the number of sheets of used paper UP to be processed in batch.
  • the macerating tank 25 has a capacity of agitating and treating (in batch) a total of about 500 sheets (about 2000 g) of used paper UP of A4 format PPC (plain paper copier) by adding about 98 liters of water.
  • the concentration of the used paper pulp UPP to be macerated is about 2%. The concentration is adjusted by supplying water from the water feed device 27 , and this water feed device 27 is a part of the pulp concentration adjustment unit 3 described below.
  • the inlet 7 has a structure to be opened and closed to the outside of a case cover 6 a of the apparatus case 6 , the discharge port 28 is opened and closed by an opening and closing valve 29 , and communicates with a used paper pulp circulation route 49 described below.
  • a debris filter 30 is provided for removing obstacles for the next beating process, such as clips, staples, pins and others used for binding the used paper UP, UP, . . . .
  • the opening and closing valve 29 opens and closes specifically by the crank motion of a crank mechanism 36 driven by a drive motor 35 .
  • the drive motor 35 is specifically an electric motor, and this drive motor 35 is electrically connected to the apparatus control unit 5 .
  • the agitating device 26 is provided inside of the macerating tank 25 , and includes an agitation impeller 40 and a drive motor 41 .
  • the agitation impeller 40 has its rotation shaft 40 a supported rotatably in an upright position in the central position of the bottom of the maceration tank 25 , and is rotatable in the horizontal direction, and the lower end of the rotation shaft 40 a is driven and coupled to a rotation shaft 41 a of the drive motor 41 by way of transmission means 42 composed of a transmission pulley 42 a, a transmission belt 42 b, and a transmission pulley 42 c.
  • the water feed device 27 is to supply water into the macerating tank 25 , and forms a beating concentration adjustment unit 3 A of the pulp concentration adjustment unit 3 , as described below.
  • the water feed device 27 in the illustrated preferred embodiment includes, as shown in FIG. 1 , a white water collection tank 45 , a water feed pump 46 for beating concentration adjustment, and a water feed tank 47 for paper making concentration adjustment.
  • the white water collection tank 45 is, as described below, designed to collect white water W (pulp water of very low concentration filtered through a paper making mesh in the paper making process) filtered and dewatered in the paper making unit 4 , and the white water W collected in the white water collection tank 45 is first supplied into the macerating tank 25 from the water feed pump 46 , and then into a concentration adjustment tank 85 described below from the water feed pump 47 .
  • a weight sensor 48 is provided in the bottom of the macerating tank 25 , and the used paper UP, UP, . . . and the water to be processed in batch in the macerating tank 25 are weighed and controlled, and the weight sensor 48 is electrically connected to the apparatus control unit 5 .
  • the weight sensor 48 of the illustrated preferred embodiment is a load cell, and is designed to sense and measure the total weight of weight of used paper UP, UP, . . . and water charged and supplied in the macerating tank 25 .
  • the weight is sensed and measured by the weight sensor 48 , and the water feed device 27 is driven, and the water W corresponding to the measured weight is supplied by the water feed pump 46 into the macerating tank 25 from the white water collection tank 45 .
  • the used paper UP, UP, . . . charged into the macerating tank 25 from the charging opening of the apparatus case 6 , that is, the inlet 7 are agitated and mixed for a specified time (10 to 20 minutes in the illustrated preferred embodiment) in the water supplied from the water feed device 27 by normal and reverse rotation of the agitation impeller 40 by the drive motor 41 , and thereby the used paper UP, UP, . . . are macerated and beaten into used paper pulp UPP.
  • the discharge port 28 of the macerating tank 25 is closed by the opening and closing valve 29 during operation of the macerating unit 20 , and flow of used paper UP or used paper pulp UPP from the macerating tank 25 into the used paper pulp circulation route 49 is blocked, while the inlet 7 is opened by the opening and closing valve 29 during operation of the beating unit 21 described later, and the flowing and circulating loop of the used paper pulp UPP from the macerating tank 25 into the used paper pulp circulation route 49 is allowed.
  • the beating unit 21 is a process for beating the used paper UP macerated in the macerating unit 20 , and is specifically designed to pressurize and beat the used paper UP macerated in the macerating unit 20 , and to grind and pulverize (into micro-fibers) the inks forming characters and patterns on the used paper UP (printing inks forming characters and patterns on the used paper UP by various printing technologies, or inks forming characters and patterns on the used paper UP by pencil, ball-point pen, fountain pen, and other writing tools)
  • This beating unit 21 mainly includes a grinder 50 .
  • This grinder 50 includes, as shown in FIG. 3 , a pair of beating disks 51 , 52 rotated and driven relatively, and the pair of beating disks 51 , 52 have beating action surfaces 51 a, 52 a disposed oppositely and concentrically across a tiny beating gap G.
  • the beating gap G of the beating action surfaces 51 a, 52 a of the grinder 50 is determined so as to be narrowed gradually, as described below, from the grinder 50 in an initial period of beating process to the grinder 50 in a later period.
  • the used paper pulp circulation route 49 having the grinder 50 is formed, and the used paper pulp UP is circulated and beaten for a specified time by way of the grinder 50 in a circulation system.
  • one grinder 50 carries out the whole beating process throughout the entire process of the beating process, and this one grinder 50 has the functions of a plurality of grinders from the grinder in an initial period of beating process to the grinder in a later period. More specifically, the beating gap G of the beating action surfaces 51 a, 52 a of the grinder 50 is controlled and adjusted so as to be narrower gradually from the initial period to the final period of the beating process.
  • the grinder 50 of the illustrated preferred embodiment is disposed, as shown in FIG. 2 , adjacently to the macerating tank 25 of the macerating unit 20 , on an apparatus machine body 54 composing the apparatus case 6 , and as shown in FIG. 3 , it further includes a beating tank 55 communicating with the macerating tank 25 of the macerating unit 20 , the pair of beating disks 51 , 52 provided relatively and rotatably in this beating tank 55 , a rotation drive source 56 for relatively rotating the pair of beating disks 51 , 52 , and gap adjusting means 57 for adjusting the beating gap G of the pair of beating disks 51 , 52 .
  • the beating tank 55 is formed in a closed cylindrical shape for accommodating the pair of beating disks 51 , 52 , and has a supply port 55 a for supplying the used paper pulp UPP from the upstream side, and a discharge port 55 b for discharging the beaten used paper pulp UPP to the downstream side.
  • the supply port 55 a is opened in the center of the bottom of the beating tank 55 toward the vertical direction, and the discharge port 55 b is opened at the cylindrical side of the beating tank 55 toward the horizontal direction.
  • the supply port 55 a and the discharge port 55 b are connected to communicate with the macerating tank 25 of the macerating unit 20 , respectively by way of circulation pipings 49 a, 49 b as shown in FIG. 3 , and the discharge port 55 b is further connected to communicate with a used paper pulp collection tank 60 by way of a discharge piping 59 .
  • Reference numeral 61 shows a direction changeover valve, by the changeover operation of this direction changeover valve 61 , the used paper pulp UPP discharged from the discharge port 55 b is selectively returned to the macerating tank 25 , or collected in the used paper pulp collection tank 60 .
  • the direction changeover valve 61 is specifically an electromagnetic valve, and is electrically connected to the apparatus control unit 5 .
  • the pair of beating disks 51 , 52 one is a fixed side beating disk fixed in the rotating direction, and other is a rotating side beating disk which is rotatable.
  • the upper side beating disk 51 is the rotating side
  • the lower side beating disk 52 is the fixed side
  • the rotating side beating disk 51 of the upper side is disposed oppositely to the fixed side beating disk 52 of the lower side, concentrically and rotatably across a tiny beating gap G.
  • the rotating side beating disk 51 is driven and coupled to a drive motor 56 by way of a rotation main shaft 64 pivoted rotatably to the fixed side of the apparatus machine body 54 and movably in the axial direction.
  • the rotation main shaft 64 is rotatably pivoted on an elevating member of the gap adjusting means 57 , and the rotating side beating disk 51 is concentrically and integrally attached at its leading end, and its base end part is driven and coupled integrally in the rotating direction and relatively movably in the axial direction on the rotation shaft of the drive motor 56 .
  • the drive motor 56 is a rotation drive source, and relatively rotates the pair of beating disks 51 , 52 , and specifically an electric motor is used, and the drive motor 56 as its drive source is electrically connected to the apparatus control unit 5 .
  • the opposite sides 51 a, 52 a of the both beating disks 51 , 52 forming the tiny beating gap G mutually collaborate to form beating action surfaces.
  • These opposite beating action surfaces 51 a, 52 a are formed as wheel sides having a multiplicity of abrasive grains bonded by a bonding agent.
  • the both beating action surfaces 51 a, 52 a are, as shown in FIG. 3 , formed in a taper shape continuously increased in the diameter size in the mutually opposite directions, and are formed as annular flat surfaces parallel to each other at the outermost peripheral edges, and these annular flat surfaces form the beating gap G.
  • an inlet 70 is formed to communicate coaxially with the supply port 55 a of the beating tank, and the two annular flat surfaces formed on the outer peripheral edges of the beating action surfaces 51 a, 52 a of the pair of beating disks 51 , 52 form an outlet 71 communicating with the discharge port 55 b of the beating tank 55 and having the beating gap G.
  • a plurality of blades 72 , 72 , . . . are formed at intervals in the circumferential direction, and these blades 72 , 72 , . . . push out the used paper pulp UPP discharged from the outlet 71 in pumping action toward the discharge port 55 b of the beating tank 5 b by centrifugal force by rotation of the rotating side beating disk 51 .
  • the drive motor 56 as the drive source, when the rotating side beating disk 51 is rotated and driven to the fixed side beating disk 52 , the used paper pulp UPP supplied into a beating gap B by way of the supply port 55 a of the beating tank 55 and the inlet 70 from the macerating tank 25 of the macerating unit 20 flows into the beating space B from the inlet 70 , and passes through this beating space B, and is pressurized and beaten by the relatively rotating beating action surfaces 51 a, 52 a, and the inks forming the characters and patterns on the used paper UP are ground and pulverized, and then it is discharged by way of the discharge port 55 b of the beating tank 55 from the outlet 71 .
  • the used paper pulp UPP is further pressurized and beaten at the location of the outlet 71 having the beating gap G, and is pulverized to a specified micron size (to become micro-fiber) defined by this beating gap G.
  • this one grinder 50 has the functions of a plurality of grinders from the grinder in an initial period of beating process to the grinder in a final period, and more specifically, the beating gap G of the grinder 50 is controlled and adjusted by the gap adjusting means 57 so as to be narrower gradually from the initial period to the final period of the beating process.
  • the gap adjusting means 57 is not particularly illustrated, but is designed to move the pair of beating disks 51 , 52 relatively in the rotation axial direction, to and control and adjust the beating gap G of these beating disks 51 , 52 , and is mainly composed of moving means (not shown) for moving the rotating side beating disk 51 in the rotation axial direction, that is, in the axial direction of a rotation main shaft 64 , and a drive source 66 for driving this moving means.
  • the drive source is specifically an electric motor, and this drive motor 66 is electrically connected to the apparatus control unit 5 .
  • this electric motor 66 By the rotation of this electric motor 66 , the rotating main shaft 64 is moved up and down by way of the moving means, and therefore the rotating side beating disk 51 formed integrally with the rotation main shaft 64 is moved in the vertical direction to the fixed side beating disk 52 , that is, in the rotation axial direction, and the beating gap G between the two beating disks 51 , 52 is controlled and adjusted.
  • a position detection sensor (not shown) is provided for detecting the ascending and descending position of the rotating side beating disk 51 , and depending on the result of detection by this position detection sensor, the drive motor 66 is driven and controlled.
  • the position detection sensor is electrically connected to the apparatus control unit 5 .
  • the beating gap G of the beating disks 51 , 52 is controlled and adjusted by the gap adjusting means 57 in the circulation system beating process by the used paper pulp circulation route 49 shown in FIG. 3 , in mutual interaction with a circulation pump 69 which is circulating means.
  • the used paper pulp UPP macerated by the macerating unit 20 is circulated through the used paper pulp circulation route 49 by the circulation pump 69 , and is beaten by the grinder 50 , and at this time the beating gap G of the beating action surfaces 51 a, 52 a of the grinder 50 is controlled by the gap adjusting means 57 so as to be narrower gradually from the initial period to the terminal period of the beating process.
  • the macerating tank 25 of the macerating unit 20 is included, and in this beating process, the agitating device 26 of the macerating unit 20 is driven and controlled, and the macerating unit 20 is driven simultaneously with the beating unit 21 .
  • the used paper pulp UPP flows out into the used paper pulp circulation route 49 from the macerating tank 25 , while the used paper pulp UPP beaten by the grinder 50 flows into the macerating tank 25 , and therefore in the macerating tank 25 , the used paper pulp UPP of different degrees of beating is mixed, and by the agitating action by the agitating device 26 , the degree of beating of the used paper pulp UPP in the macerating tank 25 is made uniform, and the beating process is promoted.
  • the used paper pulp collection tank 60 is a location for collecting the used paper pulp UPP beaten and pulverized to a desired size by the beating unit 21 , and the used paper pulp UPP collected herein is mixed and adjusted to a paper making concentration corresponding to the finished paper quality of the recycled paper RP to be regenerated as a pulp suspension PS, and is sent to the paper making unit 4 in a next paper making process.
  • the pulp concentration adjusting unit 3 is weight type device for adjusting the concentration of the used paper pulp UPP supplied in the paper making unit 4 , by measuring the weight and adjusting the mixing rate of used paper UP and water W supplied into the apparatus, and more specifically as shown in FIG. 4 , it includes a beating concentration adjusting unit 3 A, a paper making concentration adjusting unit 3 B, and a pulp concentration control unit 3 C.
  • the beating concentration adjusting unit 3 A is to adjust the beating concentration of the used paper pulp UPP in the pulp making unit 2 , corresponding to the beating efficiency by the beating unit 21 , and as mentioned above, it is mainly composed of the water feed pump 46 and the beating concentration control unit 75 for adjusting the beating concentration of the water feed device 27 .
  • the supply amount of white water W by the water feed pump 46 of the beating concentration adjusting unit 3 A is preferred to be set so that the beating concentration of the used paper pulp UPP macerated and beaten by the agitating device 26 may be, for example, the maximum concentration allowable for the beating capacity of the grinder 50 of the beating unit 21 for executing the next step of the beating process, and in the illustrated preferred embodiment, it is set to be a beating concentration of about 2% as mentioned above.
  • the beating concentration control unit 75 drives and controls the water feed pump 46 so as to supply a necessary amount of water into the macerating tank 25 , as mentioned above, depending on the result of measurement from the weight sensor 48 .
  • This beating concentration control unit 75 composes a part of the apparatus control unit 5 as described below.
  • the paper making concentration adjusting unit 3 B is to adjust the paper making concentration of the used paper pulp UPP in the paper making unit 4 , to an appropriate concentration corresponding to the finished paper quality of the recycled paper RP to be regenerated, and is more specifically designed to adjust the concentration of the used paper pulp UPP manufactured in the pulp making unit 2 by a division system, and it mainly includes a division extraction unit 80 , a suspension preparing unit 81 , and a paper making concentration control unit 82 .
  • the division extraction unit 80 is to divide and extract by a specified small portion from the total volume of the used paper pulp UPP manufactured in the pulp making unit 2 in the preceding process, and includes a used paper pulp supply pump 86 for division and extraction for extracting the used paper pulp UPP of the used paper pulp collection tank 60 and sending to a concentration adjusting tank 85 .
  • the suspension preparing unit 81 is to prepare a pulp suspension PS of a specified concentration by adding a prescribed amount of water W for concentration adjustment to the specified small portion of the used paper pulp UPP divided and extracted by the division extraction unit 80 , and mainly includes a water feed pump 47 of the water feed device 27 .
  • a weight sensor 87 composed of a load cell is provided, and is designed to measure and control the amount of the used paper pulp UPP and water W for concentration adjustment supplied into the concentration adjusting tank 85 , and the weight sensor 87 is electrically connected to the apparatus control unit 5 .
  • the paper making concentration control unit 82 controls by interacting the division extraction unit 80 and the suspension preparing unit 81 , and forms apart of the apparatus control unit 5 , and controls the pump 86 , 47 of the division extraction unit 80 and the suspension preparing unit 81 by interaction so as to execute the following step of the paper making concentration adjusting process.
  • the used paper pulp UPP of a specified portion (1 L in the illustrated preferred embodiment) is divided by the used paper pulp supply pump 86 , and is transferred and contained in the concentration adjusting tank 85 .
  • its weight is sensed and measured by the weight sensor 87 , and the result is sent to the apparatus control unit 5 .
  • diluting water W is supplied from the water feed pump 47 into the concentration adjusting tank 85 from the white water collection tank 45 by a specified volume (9 L in the illustrated preferred embodiment, actually as weighed and measured by the weight sensor 87 )
  • the concentration adjusting tank 85 the used paper pulp UPP of beating concentration (2% in the illustrated preferred embodiment) and the water W are mixed and diluted, and a pulp suspension PS of a specified concentration (about 0.2% concentration or target concentration in the illustrated preferred embodiment) is mixed and prepared.
  • the target concentration of the pulp suspension PS to be prepared is determined in consideration of the paper making capacity in the paper making unit 4 described below on the basis of the results of the preliminary experiment, and it is set to about 0.2% in the illustrated preferred embodiment.
  • the pulp suspension PS prepared to the paper making concentration (0.2%) of the target concentration in the concentration adjusting tank 85 is transferred and supplied into a pulp supply tank 89 from the concentration adjusting tank 85 by a first suspension supply pump 88 , and is stored in preparation for the next process of paper making unit 4 . Thereafter, this paper making concentration adjustment process is repeated similarly for the entire volume of the used paper pulp UPP in the used paper pulp collection tank 60 .
  • the pulp supply tank 89 is provided with a second suspension supply pump 90 for sending the pulp suspension PS into a paper making net conveyor 95 of the paper making unit 4 .
  • An agitating device 91 is provided in the pulp supply tank 89 , and by the agitating action of this agitating device 87 , the paper making concentration of the entire stored and held pulp suspension PS is uniformly kept at a specific value.
  • the concentration is adjusted by the paper making concentration adjusting unit 3 is adjusted not in batch, but in divided portions, that is, in small portions, and the water consumption is saved substantially, and the concentration adjusting tank 85 can be reduced in size and shape substantially, and hence the used paper recycling apparatus 1 is entirely built in a compact design.
  • the pulp concentration control unit 3 C is to drive and control the beating concentration adjusting unit 3 A and the paper making concentration adjusting unit 3 B in interlock, and specifically by receiving the pulp concentration control information (the charging amount of the used paper UP, the water supply amount into the macerating tank 25 , the beating concentration of the used paper pulp UPP, etc.) from the beating concentration control unit 75 of the beating concentration adjusting unit 3 A, the paper making concentration information (the target paper making concentration of the used paper pulp UPP, the division extraction amount of the used paper pulp UPP from the used paper pulp collection tank 60 , the water supply amount into the concentration adjusting tank 85 , etc.) for adjusting the concentration of the used paper pulp UPP manufactured in the pulp making unit 2 to the target concentration (the paper making concentration) depending on this control information is sent to the paper making concentration control unit 82 of the paper making concentration adjusting unit 3 B, and thereby the paper making concentration adjusting process is executed.
  • the pulp concentration control information the charging amount of the used paper UP, the water supply amount into the macerating tank 25 , the
  • the paper making unit 4 is a process for manufacturing recycled paper RP from the used paper pulp UPP manufactured in the pulp making unit 2 , and is mainly composed of the paper making net conveyor unit 95 , the dewatering roll unit 10 as the dewatering unit (the dewatering device), and the drying belt conveyor unit 96 .
  • the paper making net conveyor unit 95 is a location for making wet paper by making from slurry-like pulp suspension PS composed of the water W and the used paper pulp UPP sent from the pulp supply tank 89 of the pulp making unit 2 , and mainly includes a paper making conveyor 100 and a pulp supply unit 101 .
  • the paper making conveyor 100 is for conveying the pulp suspension while making paper therefrom, and a mesh belt 105 of paper making mesh structure composed of numerous mesh cells for filtering and dewatering the pulp suspension PS is disposed to run straightly toward its running direction.
  • the paper making conveyor 100 includes the mesh belt 105 of an endless belt form for conveying the pulp suspension PS while making paper therefrom, and a drive motor 106 for driving and moving this mesh belt 105 .
  • the plate member of the paper making mesh structure for composing the mesh belt 105 is a material capable of filtering and dewatering the pulp suspension PS appropriately by way of the numerous mesh cells of the paper making mesh structure, and preferred materials include polypropylene (PP), polyethylene terephthalate (PET), polyamide (PA) (generally known as Nylon, a registered trademark), stainless steel (SUS), and other corrosion resistant materials, and in the illustrated preferred embodiment, a heat-resistant PET-made mesh belt 105 is used.
  • PP polypropylene
  • PET polyethylene terephthalate
  • PA polyamide
  • SUS stainless steel
  • the mesh belt 105 is, as shown in FIG. 1 , rotatably supported by way of a drive roller 107 , a drive roller 108 , a support roller 109 , and a dewatering roll unit 10 , and is driven and coupled to the drive motor 106 by way of the drive roller 107 .
  • the paper making process length in the mesh belt 105 is determined in a range of upper side running direction length of the mesh belt 105 in the apparatus case 6 of furniture size (in the illustrated preferred embodiment, the lateral direction length from the pulp supply unit 101 to the dewatering roll unit 10 in FIG. 1 ).
  • the running speed of the mesh belt 105 is determined in consideration of various conditions in the paper making process, and it is preferably set at 0.1 m/min to 1 m/min, and in the illustrated preferred embodiment, it is set at 0.2 m/min. In the conventional used paper recycling plant or other large plants, the running speed of such paper making belt is set at least over 100 m/min, and set at even faster than 1000 m/min in a high-speed model.
  • the mesh belt 105 is, as shown in FIG. 1 , disposed and composed so as to run upward obliquely and straightly toward its running direction, and the paper making process length can be extended as much as possible within the limited installation space, and the filtering and dewatering rate is raised in relation to the paper making mesh structure of the mesh belt 105 .
  • the drive motor 106 for moving and driving the mesh belt 105 is specifically an electric motor, and is connected electrically to the apparatus control unit 5 .
  • This drive motor 106 is also used as the running and driving source of the dewatering roll unit 10 and the drying belt conveyor unit 96 described below.
  • the pulp supply unit 101 is a location for supplying a pulp suspension PS onto the mesh belt 105 from the pulp manufacturing unit 2 , and although not shown specifically, the pulp suspension PS is supplied from this pulp supply unit 101 and is spread uniformly on the mesh belt 105 .
  • the pulp supply unit 101 is provided at the start end position of the paper making process of the paper making conveyor 100 .
  • the pulp suspension PS supplied into the pulp supply unit 101 from the pulp supply tank 89 is stored and reserved by a specified amount in this pulp supply unit 101 , and by this reserving action, it is diffused uniformly on the top surface of the mesh belt 105 .
  • the pulp suspension PS diffused uniformly on the top surface of the mesh belt 105 is conveyed together with the mesh belt 105 by the driving action of the mesh belt 105 in the arrow direction, and is filtered by weight by the mesh cells of the mesh belt 105 , and is dewatered, and wet paper RP 0 (water content 90 to 80% in the illustrated preferred embodiment) is obtained.
  • the white water W filtered and dewatered by this mesh belt 105 (pulp water of ultra-low concentration filtered by the paper making mesh in the paper making process) is collected in the white water collection tank 45 of the water feed device 27 as mentioned above.
  • the dewatering roll unit 10 forms a location for squeezing and dewatering the wet paper RP 0 on the mesh belt 105 at the linkage position of the paper making net conveyor unit 95 and the drying belt conveyor unit 96 described below.
  • a smooth surface belt 145 mentioned below of the drying belt conveyor unit 96 at the downstream side, and the mesh belt 105 of the paper making net conveyor unit 95 at the upstream side are disposed in upper and lower layers as shown in FIG. 1 , and the upper and lower adjacent portions of the smooth surface belt 145 and the mesh belt 105 are formed at the linkage portion, and at this linkage portion, the dewatering roll unit 10 rolls and compresses the mesh belt 105 and the smooth surface belt 145 from upper and lower sides, thereby dewatering the wet paper.
  • the dewatering roll unit 10 includes at least a preliminary dewatering roll unit 10 A, and a final dewatering roll unit 10 B as principal components.
  • the preliminary dewatering roll unit 10 A is a location for squeezing and dewatering the wet paper on the mesh belt 105 preliminarily
  • the final dewatering roll unit 10 B is a location for squeezing and dewatering further the wet paper on the mesh belt 105 preliminarily dewatered in the preliminary dewatering roll unit 10 A, and obtaining a dry paper of a specified water content, that is, the dewatering process is composed of two sections, the one for squeezing and dewatering the wet paper RP 0 of high water content on the mesh belt 105 preliminarily by the preliminary dewatering roll unit 10 A, and the other for squeezing and dewatering further the wet paper PR 0 preliminarily, and obtaining a dry paper of a specified water content, that is, recycled paper RP by the final dewatering roll unit 10 B, and therefore the used paper recycling technology conventionally operated in a large-scale plant such as used paper recycling plant is realized in an
  • the squeezing and dewatering technology of dewatering the wet paper RP0 of high water content manufactured from the pulp suspension PS to a dry paper RP of specified water content suited to heating and drying is a very important technology for obtaining a recycled paper RP of high quality after the subsequent and final step of heating and drying process, and such important squeezing and dewatering technology must be established efficiently and at high precision, in a process working space of furniture size (narrow and short) of the present invention.
  • the present inventor disclosed a fundamental technology of squeezing and dewatering process in Japanese Patent Application Laid-Open No. 2007-084967, for example, as mentioned above, and accumulated researches and experiments for realizing an excellent squeezing and dewatering effect of high efficiency and high precision without causing any adverse effect on the paper quality, and finally discovered that an excellent squeezing and dewatering effect of high efficiency and high precision can be obtained in an extremely narrow and short process working space of furniture size, by dividing the squeezing and dewatering process in two steps of a preliminary dewatering process by a small squeezing force, and a final dewatering process of a large squeezing force, instead of the conventional single process of a large squeezing force. Further, as a result of trials and errors by the present inventor, the squeezing and dewatering structure of the present invention is completed.
  • This dewatering roll 10 is, as specifically shown in FIG. 5 , mainly composed of a preliminary dewatering roll unit 10 A, a final dewatering roll unit 10 B, and an angle defining roll unit (angle defining means) 100 as auxiliary means.
  • the preliminary dewatering roll unit 10 A is for preliminarily squeezing and dewatering the wet paper RP 0 on the mesh belt 105 , and specifically includes a preliminary squeezing roll pair 122 consisting of a preliminary dewatering roll 120 for rolling on the mesh belt 105 from the lower side, a preliminary press roll 121 for rolling and pressing the smooth surface belt 145 from the upper side in cooperation with the preliminary dewatering roll 120 .
  • a specific structure of the preliminary dewatering roll 120 preferably includes, for example, (i) a form of a cylindrical roll composed of high rigidity material, (ii) a form of forming an elastic layer of soft rubber material on the outer circumference of a cylindrical roll composed of high rigidity material, and (iii) a form of forming a water absorbing layer of water absorbing material on the outer circumference of a cylindrical roll composed of high rigidity material.
  • the preliminary dewatering roll 120 in the illustrated preferred embodiment is composed by winding and forming an elastic layer 120 b of soft rubber material on the outer circumference of a cylindrical roll 120 a of high rigidity material.
  • the cylindrical roll 120 a is specifically made of stainless steel, and the inside is a hollow cylindrical space. Hence, a specified elastic property is given to the outer circumference of the preliminary dewater roll 120 , and an appropriate squeezing force is applied in a preliminary dewatering process as mentioned above.
  • a specific structure of the preliminary press roll 121 preferably includes, for example, (i) a form of a cylindrical roll composed of high rigidity material, and (ii) a form of forming an elastic layer of hard rubber material on the outer circumference of a cylindrical roll composed of high rigidity material.
  • the preliminary press roll 121 in the illustrated preferred embodiment is a cylindrical roll composed of high rigidity material, and is specifically a cylindrical roll made of stainless steel, and the inside is a hollow cylindrical space.
  • the preliminary squeezing roll pair 122 consisting of the preliminary dewatering roll 120 and the preliminary press roll 121 , the mesh belt 105 and the smooth surface belt 145 are rolled and squeezed from both upper and lower sides at a specified preliminary pressure in a compressed state, and the water content in the wet paper RP 0 on the mesh belt 105 (water content 90 to 80% in the illustrated preferred embodiment) is removed preliminarily.
  • the preliminary pressure that is, the preliminary squeezing force of the preliminary dewatering roll 10 A for preliminarily squeezing and dewatering the wet paper RP 0 on the mesh belt 105 is set at a magnitude so as not to destroy the wet paper RP 0 of high water content.
  • this preliminary squeezing force basically, it is set by judging the state before and after preliminary squeezing of the wet paper RP 0 , while directly measuring the preliminary squeezing force by the preliminary dewatering roll 120 and the preliminary press roll 121 , but as a result of various tests and studies, it is found that a desired effect is obtained stably by setting the preliminary squeezing force so that the water content of the wet paper on the mesh belt 105 after the preliminary dewatering process may be a specified value (in a range of water content of 80 to 75% in the illustrated preferred embodiment).
  • the axial distance is measured between a rotation support shaft 123 of the preliminary dewatering roll 120 , and a rotation support shaft 124 of the preliminary press roll 121 .
  • the final dewatering roll unit 10 B is for obtaining a dry paper specified water content (recycled paper) RP by further squeezing and dewatering the wet paper RP 0 on the mesh belt 105 after preliminary dewatering by the preliminary dewatering roll unit 10 A, and specifically includes at least one set of a final squeezing roll pair 127 consisting of a final dewatering roll 125 rolling on the mesh belt 105 from the lower side, and a final press roll 126 rolling and pressing on the smooth surface belt 145 from the upper side in cooperation with the final dewatering roll 125 .
  • a water absorbing layer 125 b of water absorbing material is formed on the outer circumference of the cylindrical roll 125 a of high rigidity material.
  • the water absorbing layer 125 b is preferably a porous material having fine continuous pores, or a fine fiber material having a bundled structure of ultra-fine fibers.
  • the final dewatering roll 125 in the illustrated preferred embodiment is composed by forming a fine fiber material having a bundled structure of ultra-fine fibers as the water absorbing layer 125 b on the outer circumference of the cylindrical roll 125 a made of stainless steel, and specifically Clarino is used (a registered trademark of Kuraray Co.).
  • the inside of the cylindrical roll 125 a is a hollow cylindrical space.
  • the winding structure of the water absorbing layer 125 b on the cylindrical roll 125 a includes one-turn winding of the water absorbing layer 125 b of a certain thickness around the outer circumference of the cylindrical roll 125 a, a single-layer structure of the cylindrical water absorbing layer 125 b externally fitted to the cylindrical roll 125 a, and a multi-layer structure of winding a thin water absorbing layer 125 b by plural turns around the outer circumference of the cylindrical roll 125 a.
  • the final dewatering roll 125 in the illustrated preferred embodiment is a single-layer structure having the water absorbing layer 125 b of Clarino wound a turn around the cylindrical outer circumference of the cylindrical roll 125 a made of stainless steel.
  • a specific structure of the final press roll 126 preferably includes, same as the preliminary press roll 121 mentioned above, for example, (i) a form of a cylindrical roll composed of high rigidity material, and (ii) a form of forming an elastic layer of hard rubber material on the outer circumference of a cylindrical roll composed of high rigidity material.
  • the final press roll 126 in the illustrated preferred embodiment is a cylindrical roll composed of high rigidity material, and is specifically a cylindrical roll made of stainless steel, and the inside is a hollow cylindrical space.
  • the final squeezing roll pair 127 consisting of the final dewatering roll 125 and the final press roll 126 , the mesh belt 105 and the smooth surface belt 145 are rolled and squeezed from both upper and lower sides at a specified final pressure in a compressed state, and the water content in the wet paper RP 0 on the mesh belt 105 is finally removed, and a dry paper of specified water content, that is, recycled paper RP is obtained.
  • the final pressure that is, the final squeezing force of the final dewatering roll 10 B for finally squeezing and dewatering the wet paper RP 0 on the mesh belt 105 is set to such a magnitude for obtaining a specified dewatering effect securely about the preliminarily dewatered wet paper RP 0 .
  • the water content of the dry paper (recycled paper) RP on the mesh belt 105 after final dewatering may be a specified value (in a range of water content of 70 to 65% in the illustrated preferred embodiment), but in actual setting and adjustment of the final squeezing force, it is determined by adjusting the axial distance of the rotation support shaft 128 of the final dewatering roll 125 and the rotation support shaft 129 of the final press roll 121 .
  • these rolls 120 , 121 , 125 , 126 are rotated and controlled so as to roll and contact mutually at a slight rotating speed difference mutually on the outer circumferential surfaces of the upper and lower rolls 120 , 125 and the outer circumferential surfaces of 121 , 126 , on the contact surfaces (the lower side of the mesh belt 105 and the upper side of the smooth surface belt 145 ) of the mesh belt 105 and the smooth surface belt 145 rolled and squeezed in a compressed state between the outer circumferential surfaces.
  • the rotating speed of the upper side preliminary and final press rolls 121 , 126 is set slightly larger than the rotating speed of the lower side preliminary and final dewatering rolls 120 , 125 , and therefore the running speed of the smooth surface belt 145 is set slightly larger than the running speed of the mesh belt 105 .
  • the running speed of the smooth surface belt 145 is set slightly larger than the running speed of the mesh belt 105 .
  • the angle defining roll unit (angle defining means) 100 is for assisting the squeezing and dewatering action of the preliminary dewatering roll unit 10 A and the final dewatering roll unit 10 B to be effective, and it is provided at the upstream side of the preliminary dewatering roll unit 10 A, and defines the inclination angle between the mesh belt 105 and the smooth surface belt 145 inserted in the preliminary dewatering roll unit 10 A.
  • the angle defining roll unit 10 C is specifically for defining the inclination angle ⁇ between the mesh belt 105 and the smooth surface belt 145 inserted in the preliminary dewatering roll unit 10 A, and more specifically it includes a mesh belt guide roll 130 rolling on the mesh belt 105 from the lower side, and defining the insertion angle of the mesh belt 105 in the preliminary dewatering roll unit 10 A, and a smooth surface belt guide roll 131 rolling on the smooth surface belt 145 from the upper side, and defining the insertion angle of the smooth surface belt 145 in the preliminary dewatering roll unit 10 A.
  • a specific structure of the mesh belt guide roll 130 is composed by forming a dewatering layer 130 b of a porous material having fine continuous pores, on the outer circumference of a cylindrical roll 130 a of high rigidity material.
  • the mesh belt guide roll 130 is a single-layer structure having a cylindrical dewatering layer 130 b of ultra-fine continuous foaming material having ultra-fine continuous pores of micron size, externally fitted to the cylindrical outer circumference of the cylindrical roll 130 a of stainless steel.
  • the inside of the cylindrical roll 130 a is a hollow cylindrical space.
  • the wet paper RP 0 diffused uniformly on the upper side of the mesh belt 105 and conveyed together with the mesh belt 105 is filtered and dewatered by the mesh belt 105 , and is absorbed and dewatered also by the mesh belt guide roll 130 , and therefore the mesh belt guide roll 130 assists the preliminary squeezing and dewatering action of the preliminary dewatering roll unit 10 A, and also defines the insertion angle of the mesh belt 105 in the preliminary dewatering roll unit 10 A.
  • a specific structure of the smooth surface belt guide roll 131 is a cylindrical roll of high rigidity material, and in the illustrated preferred embodiment, the smooth surface belt guide roll 131 is a cylindrical roll made of stainless steel.
  • the inside of the smooth surface belt guide roll 131 in the illustrated preferred embodiment is a hollow cylindrical space.
  • the insertion angle of the mesh belt 105 in the preliminary dewatering roll unit 10 A is defined, and by the smooth surface belt guide roll 131 , the insertion angle of the smooth surface belt 145 in the preliminary dewatering roll unit 10 A is defined, and therefore the inclination angle ⁇ between the mesh belt 105 and the smooth surface belt 145 is indirectly determined in a specified range.
  • the insertion angle of the mesh belt 105 and the insertion angle of the smooth surface belt 145 are defined independently, and the inclination angle ⁇ between the mesh belt 105 and the smooth surface belt 145 is set in the specified range, and if the mesh belt 105 and the smooth surface belt 145 are designed individually in configuration depending on the purpose, an ideal inclination angle ⁇ is always obtained.
  • the inclination angle ⁇ is determined so as to prevent effectively the wet paper RP 0 from returning to slurry by re-absorption of a large volume of squeezed water into the wet paper RP 0 after the water contained in the wet paper RP 0 is once squeezed substantially to the upstream side of the preliminary dewatering roll unit 10 A by the preliminary dewatering action by the preliminary dewatering roll unit 10 A.
  • the upper side smooth surface belt 145 is apart from the wet paper RP 0 on the lower side mesh belt 105 , and hence a part of the abundant squeezed water contained in the wet paper RP 0 may be absorbed again in the wet paper RP 0 , and the wet paper RP 0 may become slurry again.
  • the inclination angle ⁇ between the mesh belt 105 and the smooth surface belt 145 is preferably set in a range of 1 to 20 degrees as a result of various tests, preferably 3 to 7 degrees, and it is set at 5 degrees in the illustrated preferred embodiment.
  • the rolls 120 , 121 , 125 , 126 of the preliminary dewatering roll 10 A and the final dewatering roll 10 B in the dewatering roll unit 10 are put in rotation, and first by the preliminary squeezing roll pair 122 in the preliminary dewatering roll 10 A, the mesh belt 105 and the smooth surface belt 145 are rolled and squeezed from both upper and lower sides in a compressed state at a specified preliminary pressure, and the water contained in the wet paper RP 0 on the mesh belt 105 is preliminarily removed (in the illustrated preferred embodiment, the water content in the wet paper RP 0 is reduced from 90 to 85% to 80 to 75%).
  • the mesh belt 105 and the smooth surface belt 145 are rolled and squeezed from both upper and lower sides in a compressed state at a specified final pressure, and the water contained in the wet paper RP 0 on the mesh belt 105 is finally remove, and the dry paper of specified water content, that is, the recycled paper RP is obtained (in the illustrated embodiment, the wet paper RP 0 of water content of 80 to 75% is dewatered to the dry paper RP of water content of 70 to 65%).
  • the white water W squeezed and dewatered from the wet paper RP 0 is collected in the white water collection tank 45 in the water feed device 27 .
  • the dry paper (recycled paper) RP squeezed and dewatered by the dewatering roll unit 10 is transferred and conveyed to the lower side of the upper side smooth surface belt 145 from the upper side of the lower side mesh belt 105 , at a downstream side location of the dewatering roll unit 10 , and is conveyed together with the smooth surface belt 145 , and is dried by the drying belt conveyor unit 96 in the drying process.
  • This transfer action is considered to be caused by a smooth surface structure of the smooth surface belt 145 . That is, the surface of the lower side mesh belt 105 is a fine rough surface having multiple fine continuous pores, whereas the surface of the upper side smooth surface belt 145 is a smooth surface without pores, and hence the dry paper RP slightly containing water seems to be adsorbed by the surface tension against the surface of the smooth surface belt 145 .
  • the drying belt conveyor unit 96 is a location for producing generated paper RP by further heating and drying the dry paper RP once squeezed and dewatered in the dewatering roll unit 10 after the paper making process in the paper making net conveyor unit 95 , and mainly includes a drying conveyor 140 and a heating and drying unit 141 .
  • the drying conveyor 140 is for smoothing and conveying the wet paper RP 0 squeezed and dewatered in the dewatering roll unit 10 , and mainly includes the smooth surface belt 145 , and the drive moor 106 for driving and moving this smooth surface belt 145 .
  • the smooth surface belt 145 is to convey the wet paper RP 0 while heating and drying, and is specifically an endless belt connected and formed in an annular shape of a specified length of a plate material of smooth surface structure having a specified width.
  • the plate material of smooth surface structure is finished inn an appropriate smooth surface at one side of the surface of the wet paper RP 0 , and is made of a material capable of withstanding the heating action of the heating and drying unit 141 described below, and preferably an elastic heat resistant material is used such as fluorine resin or stainless steel, and a fluorine resin belt is used in the illustrated preferred embodiment.
  • This smooth surface belt 145 is, as shown in FIG. 1 , rotatably supported and held by way of a drive roller 146 , driven rollers 147 , 148 , and the dewatering roll unit 10 , and is driven and coupled to the drive motor 106 by way of the drive roller 146 .
  • the drive motor 106 for driving and moving the smooth surface belt 145 is commonly used as the running and driving source of the paper making conveyor 100 and the dewatering roll unit 10 as described above.
  • the heating and drying unit 141 is a location for heating and drying the wet paper RP 0 on the smooth surface belt 145 , and includes a heater plate 150 , as a heating unit, disposed in the mist of the running route of the smooth surface belt 145 .
  • This heater plate 150 is specifically configured to heat and dry the wet paper RP 0 on the smooth surface belt 145 indirectly by way of the smooth surface belt 145 .
  • two smooth surface finishing rolls 149 , 149 are disposed, and are configured so as to roll and pressurize the wet paper RP 0 on the smooth surface belt 145 sequentially, and thereby the surface of one side and the surface of opposite side of the wet paper RP 0 contacting with the surface of the smooth surface belt 145 may be finished to a proper smooth surface.
  • a peeling member 151 is provided, and the dry paper dried and conveyed on the smooth surface belt 145 , that is, the recycled paper RP (water content 10 to 7%) is sequentially peeled from the holding side of the smooth surface belt 145 .
  • a fixed size cutter unit 152 is provided at the terminal end position of the running route of the smooth surface belt 145 at the downstream side of this peeling member 151 , and the recycled paper RP peeled off from the smooth surface belt 145 is cut to a specified size (an A4 format in the illustrated preferred embodiment), and is discharged from the discharge port 8 of the apparatus case 6 .
  • the apparatus control unit 5 is to control the operations of the drive units of the pulp making unit 2 , the pulp concentration adjusting unit 3 , and the paper making unit 4 automatically by interacting with each other, and is specifically composed of a microcomputer having a CPU, a ROM, a RAM, and an I/O port.
  • This apparatus control unit 5 incorporates programs for executing the pulp making process of the pulp making unit 2 , the concentration adjusting process of the concentration adjusting unit 3 , and the paper making process of the paper making unit 4 , by interacting with each other, and also stores various items of information necessary for driving of the components 2 ( 20 , 21 ), 3 ( 3 A, 3 B), and 4 ( 95 , 10 , 96 ), for example, the driving time and rotating speed of the agitating device 26 in the macerating unit 20 , the water feed timing and water feed amount of the water feed device 27 , the driving time and circulation amount of the circulation pump 69 in the beating unit 21 , the driving time and rotating speed of the grinder 50 , the adjusting timing and beating gap G adjusting amount of the gap adjusting means 57 , the running speed of the conveyors 100 , 140 in the paper making unit 4 , the driving time of the heating and drying unit 141 , and the operation timing of the fixed size cutter unit 152 , preliminarily as data, or from the keyboard as appropriate selective input
  • the weight sensors 48 , 87 , the position detection sensor, and the drive units 35 , 56 , 61 , 66 , 106 are connected electrically, and the apparatus control unit 5 controls these drive units 35 , 56 , 61 , 66 , 106 according to the measured values and the control data.
  • the used paper recycling apparatus 1 having such configuration is started when the power source is turned on, and the components 2 ( 20 , 21 ), 3 ( 3 A, 3 B), and 4 ( 95 , 10 , 96 ) are controlled automatically by the apparatus control unit 5 in mutual interaction, and the used paper UP, UP, . . .
  • the dewatering roll unit 10 is provided at the linkage position of the paper making net conveyor 95 for manufacturing wet paper RP 0 from the slurry-like pulp suspension PS mixing water W and used paper pulp UPP sent from the pulp making unit 2 of the preceding process, and the drying belt conveyor unit 96 for manufacturing recycled paper RP by drying the wet paper RP 0 manufactured on the paper making net conveyor 95 , and the mesh belt 105 of the paper making net conveyor unit 95 , and the smooth surface belt 145 of the drying belt conveyor 96 are rolled and squeezed from the upper and lower sides in a compressed state, and this dewatering roll unit 10 includes the preliminary dewatering roll unit 10 A for preliminarily squeezing and dewatering the wet paper RP 0 on the mesh belt 105 , and the final dewatering roll unit 105 for obtaining dry paper RP of specified water content by finally squeezing and dewatering the wet paper RP 0 on the mesh belt 105 preliminarily dewatered in the preliminary
  • the wet paper RP 0 on the mesh belt 105 is preliminarily squeezed and dewatered by the preliminary dewatering roll 10 A, and the preliminarily dewatered wet paper RP 0 on the mesh belt 105 is finally squeezed and dewatered by the final dewatering roll unit 10 B, and dry paper RP of specified water content is obtained, and therefore in a very short dewatering process space at the intersection position of the paper making net conveyor unit 95 and the drying belt conveyor unit 96 , by squeezing and dewatering efficiently and securely from the wet paper RP 0 of high water content, dry paper RP can be obtained, and the recycled paper RP of high quality is manufactured by way of the successive heating and drying process by the heating and drying unit 141 .
  • the apparatus can be installed in a room of a small shop or a general household, and it is friendly to the environment, and is lowered in the running cost, and leak or disclosure of confidential information or personal information, and various information can be securely prevented, and the used paper recycling apparatus 1 of furniture size capable of maintaining a high level of confidentiality can be presented.
  • FIG. 7 This preferred embodiment is shown in FIG. 7 , which is similar to preferred embodiment 1, except that the configuration of the dewatering roll unit 10 and the final dewatering roll unit 10 B is modified.
  • the final dewatering roll 10 B of this preferred embodiment includes two sets of final squeezing roll pair 127 A and 127 B disposed side by side in the running direction of the mesh belt 105 and the smooth surface belt 145 .
  • the final dewatering roll unit 125 and the final press roll 126 for composing them are mutually identical in configuration, and the specific structure is substantially same as in preferred embodiment 1.
  • the squeezing force of the upstream side final squeezing roll pair 127 A and the downstream side final squeezing roller pair 127 B in the direction of arrangement is set in (i) a configuration of same magnitude, or (ii) in a configuration gradually larger from the upstream side to the downstream side in the direction of arrangement, that is, larger in the downstream side final squeezing roller pair 127 B than in the upstream side final squeezing roller pair 127 A, depending on the purpose.
  • the final squeezing force of the final dewatering roll unit 10 B on the whole is same as in preferred embodiment 1, that is, a specified dewatering effect is obtained securely in the preliminarily dewatered wet paper RP 0 , and more specifically the water content of the dry paper (recycled paper) RP on the mesh belt 105 after final squeezing and dewatering by the downstream side final squeezing roll pair 127 B is set in a range of 70 to 65% same as in preferred embodiment 1, and on the basis of the final squeezing force of the downstream side final squeezing roll pair 127 B, the final squeezing force of the final squeezing roll pair 127 A at the upstream side is determined.
  • the final squeezing force of the final squeezing roll pair 127 A at the upstream side is set same as or smaller than the final squeezing force of the final squeezing roll pair 127 B at the downstream side, and larger than the preliminary squeezing force of the preliminary squeezing roll pair 122 .
  • FIG. 8 This preferred embodiment is shown in FIG. 8 , which is similar to preferred embodiment 2, except that the configuration of the final dewatering roll unit 10 B in the dewatering roll unit 10 in preferred embodiment 1 is modified.
  • the final dewatering roll 10 B of this preferred embodiment includes three sets of final squeezing roll pair 127 A, 127 B, and 127 C disposed side by side in the running direction of the mesh belt 105 and the smooth surface belt 145 .
  • the final dewatering roll unit 125 and the final press roll 126 for composing them are mutually identical in configuration, and the specific structure is substantially same as in preferred embodiment 1.
  • the squeezing force of the final squeezing roll pair 127 A, 127 B, and 127 C from the upstream side to the downstream side in the direction of arrangement is set in (i) a configuration of same magnitude, (ii) in a configuration gradually larger from the upstream side to the downstream side in the direction of arrangement, or (iii) in a combination of (i) and (ii), that is, larger in the ultimate downstream side final squeezing roller pair 127 C than in the ultimate upstream side final squeezing roller pair 127 A, and the central final squeezing roll pair 127 B identical with the final squeezing roll pair 127 A or 127 C.
  • the final squeezing force of the final dewatering roll unit 10 B on the whole is same as in preferred embodiment 1, that is, a nearly same specified dewatering effect is obtained securely in the preliminarily dewatered wet paper RP 0 , and more specifically the water content of the dry paper (recycled paper) RP on the mesh belt 105 after final squeezing and dewatering by the ultimate downstream side final squeezing roll pair 127 C is set in a range of 70 to 65% same as in preferred embodiment 1, and on the basis of the final squeezing force of the ultimate downstream side final squeezing roll pair 127 C, the final squeezing force of the final squeezing roll pairs 127 A and 127 B at the upstream side is determined. Moreover, the final squeezing force of the final squeezing roll pair 127 A at the ultimate upstream side is set larger than the preliminary squeezing force of the preliminary squeezing roll pair 122 .
  • the specific configuration of the dewatering roll unit 10 is not limited to the illustrated preferred embodiments 1 to 3, but may be realized by a different structure having similar functions.

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)
US12/759,177 2009-05-02 2010-04-13 Dewatering device of used paper recycling apparatus and used paper recycling apparatus Abandoned US20100276100A1 (en)

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JP2009112369A JP2010261119A (ja) 2009-05-02 2009-05-02 古紙再生装置の脱水装置および古紙再生装置
JP2009-112369 2009-05-02

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JP (1) JP2010261119A (zh)
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WO2019011750A1 (en) 2017-07-10 2019-01-17 Pexa Ab NEW SYSTEM FOR COLLECTING EXPIRED PARTICLES
US10941521B2 (en) 2013-03-11 2021-03-09 International Paper Company Method and apparatus for measuring and removing rotational variability from a nip pressure profile of a covered roll of a nip press
CN113338069A (zh) * 2021-07-06 2021-09-03 丰城市星泽科技有限公司 一种瓦楞纸板印刷加工用纸张控湿预处理装置
CN113584929A (zh) * 2021-07-08 2021-11-02 张新华 一种挤压式纤维素卷材抄纸装置

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CN103451997B (zh) * 2013-08-23 2015-10-28 华南理工大学 基于置换抽滤两步法屏蔽造纸纤维氢键的方法
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CN107604725A (zh) * 2017-09-28 2018-01-19 济南大学 一种先粉后磨式制浆设备
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CN110284353B (zh) * 2019-06-26 2020-11-03 浙江鸣春纺织股份有限公司 自动加料的小型立式分层造纸机
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Publication number Priority date Publication date Assignee Title
US10941521B2 (en) 2013-03-11 2021-03-09 International Paper Company Method and apparatus for measuring and removing rotational variability from a nip pressure profile of a covered roll of a nip press
US11629461B2 (en) 2013-03-11 2023-04-18 International Paper Company Method and apparatus for measuring and removing rotational variability from a nip pressure profile of a covered roll of a nip press
WO2019011750A1 (en) 2017-07-10 2019-01-17 Pexa Ab NEW SYSTEM FOR COLLECTING EXPIRED PARTICLES
US11534082B2 (en) 2017-07-10 2022-12-27 Pexa Ab System for collecting exhaled particles
CN113338069A (zh) * 2021-07-06 2021-09-03 丰城市星泽科技有限公司 一种瓦楞纸板印刷加工用纸张控湿预处理装置
CN113584929A (zh) * 2021-07-08 2021-11-02 张新华 一种挤压式纤维素卷材抄纸装置

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KR20100119842A (ko) 2010-11-11
CN101876152A (zh) 2010-11-03

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