CN110055803A - A kind of paper machine system and method producing ox card B paper - Google Patents
A kind of paper machine system and method producing ox card B paper Download PDFInfo
- Publication number
- CN110055803A CN110055803A CN201910347626.2A CN201910347626A CN110055803A CN 110055803 A CN110055803 A CN 110055803A CN 201910347626 A CN201910347626 A CN 201910347626A CN 110055803 A CN110055803 A CN 110055803A
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- paper
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- card
- paper machine
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Classifications
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
-
- 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
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/14—Secondary fibres
Abstract
A kind of paper machine system and method producing ox card B paper provided by the invention, including HC Cleaner of the front end for smashing the hydrabrusher of paper pulp and being handled it is arranged in, HC Cleaner bottom is connected with scalping component to separate long and short fiber, scalping component rear portion is equipped with slurry tower to store it respectively, slurry tower rear portion is connected with bottom feeding station and sizing applicator to generate the ox card B paper of different grammes per square metres, in view of the defects existing in the prior art, after the production method for quoting a kind of monolayer net paper machine production B paper, streaming portion colouring method can be detached from, and level dyeing is carried out in sizing applicator, the corrugated paper machine to monolayer net is completed to produce ox card regeneration B paper, improve the quality and efficiency of papermaking.
Description
Technical field
The present invention relates to papermaking manufacture field more particularly to a kind of paper machine system and methods for producing ox card B paper.
Background technique
Existing market produces all kinds of paper kinds, can only the craft paper machine of Multilayer Network be just able to achieve paper coloring, and all using face
The laminar flow portion of sending addition dyestuff is dyed, and this method can take away dyestuff when wet end is dehydrated, and retention is lower to lead to dosage great achievement
This height, and increase the difficulty of sewage treatment in the plain boiled water of wet end containing dyestuff.Simultaneously with the variation in market, according to customer demand,
From cost consideration, the carton that need to produce a kind of lower end meets market, but is all that the craft paper paper machine of Multilayer Network could give birth at present
Produce carton required facial tissue or in paper, it is at high cost.
Summary of the invention
The object of the present invention is to provide a kind of paper machine system and methods for producing ox card B paper, for of the existing technology
Defect after the production method for quoting a kind of monolayer net paper machine production B paper, can be detached from streaming portion colouring method, and in sizing applicator
Level dyeing is carried out, the corrugated paper machine to monolayer net is completed to produce ox card regeneration B paper, improves the quality and efficiency of papermaking.Tool
Body scheme is as follows:
It is a kind of produce ox card B paper paper machine system, including be arranged in front end for smash paper pulp hydrabrusher and
The HC Cleaner handled it, the HC Cleaner bottom are connected with scalping component to be divided long and short fiber
From scalping component rear portion is equipped with slurry tower to store it respectively, and the slurry tower rear portion is connected with bottom feeding station
And sizing applicator blocks B paper to generate the ox of different grammes per square metres.
Preferably, the scalping component includes classifying screen interconnected and low dense scummer, the classifying screen setting
It is used to play the role of slurry wire-dividing broom purification in front, the low dense scummer is used to improve the cleanliness of long and short fine slurry.
Preferably: the classifying screen pressure difference control guarantees the precision that discharges lower than 35Kpa.
Preferably, implement low dense scummer pressure difference control between 100KPa to 120KPa to guarantee fiber cleanliness.
Preferably, concentration discrete part is equipped between the scalping component and the slurry tower, to improve fibre stuff
The uniformity.
Preferably, the concentration dispersion portion includes polydisc thickener, and the polydisc thickener inlet concentration control is 1.0%
Left and right, thus guarantee slurry by the polydisc thickener concentration after concentration 10% or so.
Preferably, the concentration dispersion portion further includes feeding serew and heat dispersion machine interconnected to gluing in slurry
Object is dispersed, and the heat dispersion machine gap control is in 0.30mm to play beating results.
Preferably, be additionally provided between the slurry tower and the bottom feeding station paper machine stock tank and paper machine stock trough agitator from
And dispersion mixing slurry.
Preferably, web part of paper machine and drying cylinder are additionally provided between bottom feeding station described in the stock trough agitator thus into one
Step realizes the molding and dehydration of wet web.
A method of ox card B paper is produced, uses the paper machine system, comprising the following steps: 100% state gives up in waterpower
It is smashed in pulper, controls size degradation concentration 5%, be more preferably separated into uniform pulp fiber suspension;Pass through HC Cleaner
The above-mentioned slurry smashed is carried out except Slag treatment, pressure difference control preferably removes the weight such as iron wire, stone grain in slurry in 160Kpa
Slag;By scalping component, slurry is screened, removes the light impurities such as foam, plastics in slurry, the control of scalping pressure difference is being lower than
35Kpa;Make the fiber separation in slurry at long and short two kinds of fibre stufves by classifying screen, while wire-dividing broom purification is played to slurry
Effect, classifying screen pressure difference control be lower than 35Kpa;The cleanliness that long and short fine slurry is further increased using low dense scummer, is removed
Slag device pressure difference is controlled in 120KPa or so;Fibre stuff is concentrated by polydisc thickener, the control of polydisc inlet concentration exists
1.0% or so, slurry slurry concentration after polydisc is concentrated is left 10%;Slurry after concentration enters heat partition by feeding serew
Machine disperses sicker in slurry, and wherein at 95 degrees Celsius, the control of heat dispersion machine gap exists heating and temperature control
0.30mm, while playing the role of mashing;Slurry is stored in the production in slurry tower and completing slurrying, the intensity according to different paper kinds
It is required that entering paper machine stock tank after with slurry to long and short fiber progress, pass through the good slurry of paper machine stock trough agitator dispersion mixing;Stream is sent
To web part of paper machine, the molding and most of dehydration of wet web are realized in wet end, in press section by the squeezing of woollen blanket, at paper mass dryness fraction
50% or so;Further removing page moisture is acted on by cylinder dried in preceding drying section, is controlled at paper moisture 6%;Dye
Material is transported to sizing material bottom feeding station, and weld and sizing material mixed proportion are about 1:782, orchil and sizing material mixed proportion
About 1:136 is converted into doing immersion type sizing, sizing material and dyestuff by dyeing slagging-off dress by adjusting bottom film transfer sizing applicator
It sets, realizes that sizing material and dyestuff mixing circulation utilize, reach into paper even dyeing (no dyestuff spot), Lai Shixian paper coloring, sizing
Process, improve page intensity, flatness and water resistant ability and complete staining procedure.It specifically includes: being carried out by sizing applicator
Sizing, front resin added are 2kg/t paper, and reverse side resin added is 3kg/t paper;Paper pulp after sizing is dried to form Niu Kazai
Raw B paper.
A kind of paper machine system and method producing ox card B paper provided by the invention, including setting are used to smash paper in front end
The hydrabrusher of slurry and the HC Cleaner handled it, HC Cleaner bottom are connected with scalping component thus will
Long and short fiber is separated, and scalping component rear portion is equipped with slurry tower to store it respectively, and slurry tower rear portion is connected with bottom
Feeding station and sizing applicator are so that the ox card B paper for generating different grammes per square metres quotes a kind of single layer in view of the defects existing in the prior art
After net paper machine produces the production method of B paper, it can be detached from streaming portion colouring method, and carry out level dyeing in sizing applicator, completed
Ox card regeneration B paper is produced to the corrugated paper machine of monolayer net, improves the quality and efficiency of papermaking.
Detailed description of the invention
The attached drawing for constituting a part of the invention is used to provide further understanding of the present invention, schematic reality of the invention
It applies example and its explanation is used to explain the present invention, do not constitute improper limitations of the present invention.In the accompanying drawings:
Fig. 1 is a kind of overall structure diagram for the paper machine system for producing ox card B paper of the present invention;
Fig. 2 is a kind of schematic diagram for the paper machine method for producing ox card B paper of the present invention;
Fig. 3 is a kind of another schematic diagram for the paper machine method for producing ox card B paper of the present invention.
In the above figure: 1, hydrabrusher;2, HC Cleaner;3, scalping component;31, classifying screen;32, low dense slagging-off
Device;4, tower is starched;5, bottom feeding station;6, discrete part is concentrated;61, polydisc thickener;62, feeding serew;63, heat dispersion machine;
7, paper machine stock tank;8, paper machine stock trough agitator;9, web part of paper machine;10, drying cylinder.
Specific embodiment
In order to make the object, technical scheme and advantages of the embodiment of the invention clearer, below in conjunction with the embodiment of the present invention
In attached drawing, technical scheme in the embodiment of the invention is clearly and completely described, it is clear that described embodiment is
A part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, those of ordinary skill in the art
Every other embodiment obtained without making creative work, shall fall within the protection scope of the present invention.It needs
Illustrate, in the absence of conflict, the features in the embodiments and the embodiments of the present application can mutual any combination.
It is a kind of produce ox card B paper paper machine system, including be arranged in front end for smash paper pulp hydrabrusher 1 and
The HC Cleaner 2 that it is handled, 2 bottom of HC Cleaner be connected with scalping component 3 to by long and short fiber into
Row separation, 3 rear portion of scalping component are equipped with slurry tower 4 to store it respectively, and 4 rear portion of slurry tower is connected with bottom
Feeding station 5 and sizing applicator are described to generate the ox card B paper of different grammes per square metres below by specific embodiment.
Referring to FIG. 1, a kind of overall structure diagram for the paper machine system for producing ox card B paper of the present invention, including setting exist
Front end is used for the HC Cleaner 2 smashing the hydrabrusher 1 of paper pulp and being handled it, 2 bottom of HC Cleaner
Portion is connected with scalping component 3 to separate long and short fiber, and 3 rear portion of scalping component is equipped with slurry tower 4 thus by its point
It not being stored, slurry 4 rear portion of tower is connected with bottom feeding station 5 and sizing applicator to generate the ox of different grammes per square metres card B paper,
To improve quality of finished paper and efficiency.
Further, the scalping component 3 includes classifying screen 31 interconnected and low dense scummer 32, the classification
Front is arranged in for playing the role of wire-dividing broom purification to slurry in sieve 31, and the low dense scummer 32 is for improving long and short fine slurry
The cleanliness of material.
Further, 31 pressure difference of the classifying screen control guarantees the precision that discharges lower than 35Kpa.
Meanwhile implementing low dense 32 pressure difference of scummer control between 100KPa to 120KPa to guarantee fiber cleanliness.
With continued reference to FIG. 1, concentration discrete part 6 is equipped between the scalping component 3 and the slurry tower 4, to improve
The uniformity of fibre stuff.
Further, the concentration discrete part 6 includes polydisc thickener 61, the 61 inlet concentration control of polydisc thickener
System 1.0% or so, thus guarantee slurry by the polydisc thickener 61 concentration after concentration 10% or so.
Further, the concentration dispersion portion further includes 63 pairs of feeding serew 62 and heat dispersion machine slurries interconnected
Sicker is dispersed in material, and 63 gap of the heat dispersion machine control is in 0.30mm to play beating results.
Further, paper machine stock tank 7 and paper machine stock tank are additionally provided between the slurry tower 4 and the bottom feeding station 5
Blender 8 is to dispersion mixing slurry.
Meanwhile web part of paper machine 9 and drying cylinder are additionally provided between the paper machine stock trough agitator 8 and the bottom feeding station 5
10 so that further realize the molding and dehydration of wet web.
Referring to FIG. 2, a kind of schematic diagram for the paper machine method for producing ox card B paper of the present invention, uses the paper machine system, packet
It includes following steps: 100% state being given up and is smashed in hydrabrusher 1, control size degradation concentration 5%, be more preferably separated into uniform
Pulp fiber suspension;The above-mentioned slurry smashed is carried out except Slag treatment by HC Cleaner 2, pressure difference is controlled in 160Kpa,
Preferably remove the weight such as iron wire, stone grain slag in slurry;By scalping component 3, slurry is screened, remove slurry in foam,
The light impurities such as plastics, the control of scalping pressure difference are being lower than 35Kpa;Make the fiber separation in slurry at long and short two by classifying screen 31
Kind fibre stuff, while playing the role of wire-dividing broom purification to slurry, the control of 31 pressure difference of classifying screen is lower than 35Kpa;It dense is removed using low
Slag device 32 further increases the cleanliness of long and short fine slurry, and scummer pressure difference is controlled in 120KPa or so.
Please referring to Fig. 3 is a kind of another schematic diagram for the paper machine method for producing ox card B paper of the present invention, passes through polydisc thickener
61 pairs of fibre stufves are concentrated, and polydisc inlet concentration is controlled 1.0% or so, and slurry slurry concentration after polydisc is concentrated exists
10% or so;Slurry after concentration enters heat dispersion machine 63 by feeding serew 62, disperses to sicker in slurry, wherein
At 95 degrees Celsius, 63 gap of heat dispersion machine is controlled in 0.30mm heating and temperature control, while playing the role of mashing;Slurry storage
The production of slurrying is completed in slurry tower 4, the intensity requirement according to different paper kinds carries out long and short fiber with slurry rear into paper machine
Stock tank 7 passes through the good slurry of 8 dispersion mixing of paper machine stock trough agitator;Stream is sent to web part of paper machine 9, realizes wet web in wet end
Molding and most of dehydration, in press section by the squeezing of woollen blanket, at paper mass dryness fraction 50% or so;Pass through drying cylinder in preceding drying section
10 desiccations further remove page moisture, control at paper moisture 6%;Dyestuff is transported to sizing material bottom feeding station 5, yellow
Dyestuff and sizing material mixed proportion are about 1:782, orchil and sizing material mixed proportion about 1:136, by adjusting bottom film transfer
Sizing applicator is converted into doing immersion type sizing, sizing material and dyestuff by dyeing deslagging device, realizes sizing material and dyestuff mixing circulation benefit
With, reach into paper even dyeing (no dyestuff spot), Lai Shixian paper coloring, sizing process, improve intensity, the flatness of page
With water resistant ability and completion staining procedure.It specifically includes: being glued by sizing applicator, front resin added is 2kg/t paper, reverse side
Resin added is 3kg/t paper;Paper pulp after sizing is dried to form ox card regeneration B paper.
A kind of paper machine system and method producing ox card B paper provided by the invention, including setting are used to smash paper in front end
The hydrabrusher 1 of slurry and the HC Cleaner 2 handled it, 2 bottom of HC Cleaner are connected with scalping portion
To separate long and short fiber, 3 rear portion of scalping component stores it equipped with slurry tower 4 part 3 respectively, described
Slurry 4 rear portion of tower is connected with bottom feeding station 5 and sizing applicator to generate the ox card B paper of different grammes per square metres, deposits for the prior art
Defect, after the production method for quoting a kind of monolayer net paper machine production B paper, streaming portion colouring method can be detached from, and applying
Glue machine carries out level dyeing, completes the corrugated paper machine to monolayer net to produce ox card regeneration B paper, improves the quality and effect of papermaking
Rate.
Descriptions above can combine implementation individually or in various ways, and these variants all exist
Within protection scope of the present invention.
Those of ordinary skill in the art will appreciate that all or part of the steps in the above method can be instructed by program
Related hardware is completed, and described program can store in computer readable storage medium, such as read-only memory, disk or CD
Deng.Optionally, one or more integrated circuits also can be used to realize, accordingly in all or part of the steps of above-described embodiment
Ground, each device/unit in above-described embodiment can take the form of hardware realization, can also use the shape of software function device
Formula is realized.The present invention is not limited to the combinations of the hardware and software of any particular form.
It should be noted that, in this document, the terms "include", "comprise" or its any other variant are intended to non-row
His property includes, so that including the article of a series of elements or equipment not only includes those elements, but also including not having
There is the other element being expressly recited, or further includes for this article or the intrinsic element of equipment.Do not limiting more
In the case where system, the element that is limited by sentence " including ... ", it is not excluded that in the article or equipment for including the element
There is also other identical elements.
The above examples are only used to illustrate the technical scheme of the present invention and are not limiting, reference only to preferred embodiment to this hair
It is bright to be described in detail.Those skilled in the art should understand that can modify to technical solution of the present invention
Or equivalent replacement should all cover in claim model of the invention without departing from the spirit and scope of the technical solution of the present invention
In enclosing.
Claims (10)
1. a kind of paper machine system for producing ox card B paper, it is characterised in that: broken including waterpower of the front end for smashing paper pulp is arranged in
Pulp grinder and the HC Cleaner handled it, the HC Cleaner bottom are connected with scalping component to which length is fine
Dimension is separated, and scalping component rear portion is equipped with slurry tower to store it respectively, and the slurry tower rear portion is connected with bottom
Layer feeding station and sizing applicator are to generate the ox card B paper of different grammes per square metres.
2. the paper machine system of production ox card B paper as described in claim 1, it is characterised in that: the scalping component includes mutually interconnecting
Front is arranged in for playing the role of wire-dividing broom purification, institute to slurry in the classifying screen and low dense scummer connect, the classifying screen
Low dense scummer is stated for improving the cleanliness of long and short fine slurry.
3. the paper machine system of production ox card B paper as claimed in claim 2, it is characterised in that: the classifying screen pressure difference control is lower than
35Kpa is to guarantee the precision that discharges.
4. the paper machine system of production ox card B paper as claimed in claim 2, it is characterised in that: the low dense scummer pressure difference control
To guarantee fiber cleanliness between 100KPa to 120KPa.
5. the paper machine system of production ox card B paper as described in claim 1, it is characterised in that: the scalping component and the slurry tower
Between be equipped with concentration discrete part, to improve the uniformity of fibre stuff.
6. the paper machine system of production ox card B paper as claimed in claim 5, it is characterised in that: the concentration discrete part includes more
Disk thickener, the polydisc thickener inlet concentration control is 1.0% or so, to guarantee slurry by the polydisc thickener
Concentration is 10% or so after concentration.
7. the paper machine system of production ox card B paper as claimed in claim 6, it is characterised in that: the concentration discrete part further includes
Feeding serew and heat dispersion machine interconnected disperse sicker in slurry, and the heat dispersion machine gap control exists
0.30mm is to play beating results.
8. the paper machine system of production ox card B paper as described in claim 1, it is characterised in that: the slurry tower and the bottom feeding
Paper machine stock tank and paper machine stock trough agitator are additionally provided between standing to dispersion mixing slurry.
9. the paper machine system of production ox card B paper as claimed in claim 8, it is characterised in that: the paper machine stock trough agitator and institute
State the molding and dehydration that web part of paper machine and drying cylinder are additionally provided between bottom feeding station to further realize wet web.
10. a kind of method for producing ox card B paper, uses paper machine system described in claim 1-9 any one, it is characterised in that:
The following steps are included:
S1. 100% state is given up and is smashed in hydrabrusher, controlled size degradation concentration 5%, it is fine to be more preferably separated into uniform slurry
Tie up suspension;
S2. the above-mentioned slurry smashed is carried out except Slag treatment by HC Cleaner, pressure difference control is preferably removed in 160Kpa
The weight such as iron wire, stone grain slag in slurry;
S3. by scalping component, slurry is screened, removes the light impurities such as foam, plastics in slurry, the control of scalping pressure difference exists
Lower than 35Kpa;
S4. make the fiber separation in slurry at long and short two kinds of fibre stufves by classifying screen, while wire-dividing broom purification is played to slurry
Effect, classifying screen pressure difference control be lower than 35Kpa;
S5. the cleanliness of long and short fine slurry is further increased using low dense scummer, the control of scummer pressure difference is on the left side 120KPa
It is right;
S6. fibre stuff is concentrated by polydisc thickener, the control of polydisc inlet concentration is 1.0% or so, and slurry is through more
Slurry concentration is 10% or so after disk concentration;
S7. the slurry after being concentrated enters heat dispersion machine by feeding serew, disperses to sicker in slurry, wherein heating temperature
At 95 degrees Celsius, heat dispersion machine gap is controlled in 0.30mm, while playing the role of mashing for degree control;
S8. slurry is stored in the production in slurry tower and completing slurrying, and the intensity requirement according to different paper kinds carries out long and short fiber
Enter paper machine stock tank after with slurry, passes through the good slurry of paper machine stock trough agitator dispersion mixing;
S9. pulp flow realizes the molding and most of dehydration of wet web in wet end, passes through woollen blanket in press section to web part of paper machine
Squeezing, at paper mass dryness fraction 50% or so;
S10. further removing page moisture is acted on by cylinder dried in preceding drying section, controlled at paper moisture 6%;
S11. dyestuff is transported to sizing material bottom feeding station, and weld and sizing material mixed proportion are about 1:782, orchil and glue
Expect mixed proportion about 1:136, is converted into doing immersion type sizing by adjusting bottom film transfer sizing applicator, sizing material and dyestuff pass through dye
Color deslagging device is realized that sizing material and dyestuff mixing circulation utilize, is reached into paper even dyeing (no dyestuff spot), Lai Shixian paper contaminates
Color, sizing process, improve page intensity, flatness and water resistant ability and complete staining procedure.It specifically includes: passing through sizing
Machine is glued, and front resin added is 2kg/t paper, and reverse side resin added is 3kg/t paper;
S12. the paper pulp after sizing is dried to form ox card regeneration B paper.
Priority Applications (1)
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CN201910347626.2A CN110055803A (en) | 2019-04-28 | 2019-04-28 | A kind of paper machine system and method producing ox card B paper |
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CN201910347626.2A CN110055803A (en) | 2019-04-28 | 2019-04-28 | A kind of paper machine system and method producing ox card B paper |
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CN108252137A (en) * | 2017-12-08 | 2018-07-06 | 东莞建晖纸业有限公司 | The preparation process of high resistance to broken environmentally friendly kraft paperboard |
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JP2010077552A (en) * | 2008-09-25 | 2010-04-08 | Oji Paper Co Ltd | Coated liner and corrugated sheet using the same |
CN102041750A (en) * | 2010-12-31 | 2011-05-04 | 东莞理文造纸厂有限公司 | Manufacture process of all waste paper dried noodle cardboard paper |
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Application publication date: 20190726 |