CN206233030U - The bamboo pulp refining system that a kind of height concentrated phase is combined - Google Patents
The bamboo pulp refining system that a kind of height concentrated phase is combined Download PDFInfo
- Publication number
- CN206233030U CN206233030U CN201621300298.9U CN201621300298U CN206233030U CN 206233030 U CN206233030 U CN 206233030U CN 201621300298 U CN201621300298 U CN 201621300298U CN 206233030 U CN206233030 U CN 206233030U
- Authority
- CN
- China
- Prior art keywords
- stock tank
- combined
- refining system
- bamboo pulp
- concentrated phase
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Abstract
The utility model is related to pulp technology for making paper, more particularly to the bamboo pulp refining system that a kind of height concentrated phase is combined.The purpose of this utility model is to provide a kind of refining system for being combined using height concentrated phase and carrying out mashing raising beating degree guarantee pulp strength, ensure bulk cargo with varying pitch conveyor screw.Its technical scheme：The bamboo pulp refining system that a kind of height concentrated phase is combined, including be sequentially connected by pipeline preposition stock tank, belt filter press, middle high-density paste mill, dilute stock tank, copy preceding stock tank；The dilution stock tank and copy low dense fiberizer is also connected with by pipeline between preceding stock tank；Bulk material spiral is also connected with by pipeline between the belt filter press and middle high-density paste mill, the pitch of the Bulk material spiral is tapered into from feeding mouth to discharging opening.The utility model is applied to the bamboo pulp refining system that a kind of height concentrated phase is combined.
Description
Technical field
The utility model is related to pulp technology for making paper, more particularly to the bamboo pulp refining system that a kind of height concentrated phase is combined.
Background technology
Bamboo pulp fiber is due to fiber very hard, wall thickness, easy transversely cutting.And hemicellulose level is high, during mashing treatment
Easy aquation, beating degree is easy to rise.The characteristics of these bamboo pulp fibers, is (preferably strong to high-quality paper for daily use of being manufactured paper with pulp with it
Degree, pliability and feel very high, stronger water imbibition and preferable bulk) for it is extremely difficult.
Number of patent application is disclosed for the patent of invention of CN87106132, a kind of process for manufacturing offset paper,
Including mashing, applying glue, copy paper operation, in pulping process, with bleached sulfite reed pulp as raw material, concentrated as 18~
Send into high-density paste mill after 30% concentration to be beaten, its abrasive disk space is 0.1~0.4mm, and beating degree raises 16 after mashing
~24 ° of SR.In paper-making process, in flow box or before add 0.05~0.3% consumption relative to absolute dried paper pulp, with
Anion-polyacrylamide and cationic-type polyacrylamide by 2: 1 proportions into concentration be 0.05~0.25%
Molecular weight is 50~700,000 reinforcing agent.
But, the technique grinds only with high-density paste mill to paper pulp, because fibre cutting is few, slurry pulping degree
It is low, thus copy page feel is poor, paper formation is also poor.If using low consistency pulping merely, because the cut-out to fiber is strong,
Slurry intensity in itself declines that loss is too many, and separately because beating degree is higher, drainage is difficult, it is difficult to suitable high-speed paper machine manufacture paper with pulp will
Ask, and power consumption is also big.In pulping process, enter screw conveyor through the paper pulp after press filtration, and common spiral
Conveying equipment does not have bulk cargo function, and paper pulp fiber cannot disperse agglomerating fiber.Also, in screw conveyor to high-density paste mill
During feeding, pressure is usually unstable, it is difficult to ensure high-density paste mill equably defibrination.
Utility model content
The utility model overcomes the deficiencies in the prior art, there is provided one kind is combined be beaten improving using height concentrated phase and beaten
The degree of beating ensures pulp strength, ensures the refining system of bulk cargo with varying pitch conveyor screw.
To solve above-mentioned technical problem, the utility model uses following technical scheme：
The bamboo pulp refining system that a kind of height concentrated phase is combined, including preposition stock tank, the belt pressure being sequentially connected by pipeline
Filter, middle high-density paste mill, dilute stock tank, copy preceding stock tank；The dilution stock tank and being copied also connected by pipeline between preceding stock tank
There is low dense fiberizer；Bulk material spiral, institute are also connected with by pipeline between the belt filter press and middle high-density paste mill
The pitch for stating Bulk material spiral is tapered into from feeding mouth to discharging opening.
Used as preferred scheme of the present utility model, the filter press cloth of the belt filter press is double nets.
As preferred scheme of the present utility model, slurry is connected with by pipeline between the preposition stock tank and belt filter press
Pump.
As preferred scheme of the present utility model, the preposition stock tank, stock tank is diluted, to be copied and be mounted on concentration on preceding stock tank
Adjuster.
Compared with prior art, the beneficial effects of the utility model are：
1st, the utility model also also passes through pipe except being provided with middle and high concentration fiberizer between stock tank before diluting stock tank and copying
Road is connected with low dense fiberizer, rises in high consistency beating section fully wire-dividing broom purification, profit, rubs, crimp kink, and at low dense section to starching
Material carries out appropriate cut-out, and keeps certain beating degree.This height consistency pulping is combined mode, to ensure paper strength,
Bulk, absorbability and feel and drainability and cost control can obtain the optimum efficiency of Comprehensive Control.Bulk material spiral shell
The pitch of rotation is tapered into from feeding mouth to discharging opening, and bamboo pulp fiber can be made preferably to disperse agglomerating fiber, makes defibrination electric current
It is more stable, certain pressure can be formed during feeding uniformly and stably slurry propulsion high consistency refining area.
2nd, the filter press cloth of belt filter press is double nets, and bamboo pulp concentration can be made to reach 18%-23%.
3rd, stock pump, stock pump increase bamboo pulp delivery pressure are connected with by pipeline between the preposition stock tank and belt filter press
Power, it is ensured that belt filter press equably carries out press filtration to bamboo pulp.
4th, the preposition stock tank, dilute stock tank, to copy and be mounted on consistencyregulator on preceding stock tank, each stock tank can be carried out dense
Degree regulation, it is ensured that the bamboo pulp concentration of each stock tank reaches requirement.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure, the preposition stock tanks of 1-, 2- belt filter presses, high-density paste mill in 3-, 4- dilution stock tanks, stock tank before 5-, 6- is low
Dense fiberizer, 7- Bulk material spirals, 8- stock pumps.
Specific embodiment
Below in conjunction with the accompanying drawings, the utility model is described in detail.
In order that the purpose of this utility model, technical scheme and advantage become more apparent, below in conjunction with accompanying drawing and implementation
Example, is further elaborated to the utility model.It should be appreciated that specific embodiment described herein is only used to explain this
Utility model, is not used to limit the utility model.
Embodiment one
The bamboo pulp refining system that a kind of height concentrated phase is combined, including preposition stock tank 1, the belt pressure being sequentially connected by pipeline
Filter 2, middle high-density paste mill 3, dilution stock tank 4, copy preceding stock tank 5；Characterized in that, it is described dilution stock tank 4 with copy preceding stock tank 5 it
Between low dense fiberizer 6 is also connected with by pipeline；Also connected by pipeline between the belt filter press 2 and middle high-density paste mill 3
Bulk material spiral 7 is connected to, the pitch of the Bulk material spiral 7 is from the feeding mouth of Bulk material spiral 7 to Bulk material spiral shell
The discharging opening of rotation 7 is tapered into.
The utility model also also passes through except being provided with middle and high concentration fiberizer 3 between stock tank 5 before diluting stock tank 4 and copying
Pipeline is connected with low dense fiberizer 6, rises, rubs, crimps kink in high consistency beating section fully wire-dividing broom purification, profit, and low dense section
Appropriate cut-out is carried out to slurry, and keeps certain beating degree.This height consistency pulping is combined mode, strong to ensureing page
Degree, bulk, absorbability and feel and drainability and cost control can obtain the optimum efficiency of Comprehensive Control.Bulk material
The pitch of spiral 7 is tapered into from feeding mouth to discharging opening, and bamboo pulp fiber can be made preferably to disperse agglomerating fiber, makes defibrination electricity
Stream is more stable, and certain pressure can be formed during feeding uniformly and stably slurry propulsion high consistency refining area.
Embodiment two
The bamboo pulp refining system that a kind of height concentrated phase is combined, including preposition stock tank 1, the belt pressure being sequentially connected by pipeline
Filter 2, middle high-density paste mill 3, dilution stock tank 4, copy preceding stock tank 5；Characterized in that, it is described dilution stock tank 4 with copy preceding stock tank 5 it
Between low dense fiberizer 6 is also connected with by pipeline；Also connected by pipeline between the belt filter press 2 and middle high-density paste mill 3
Bulk material spiral 7 is connected to, the pitch of the Bulk material spiral 7 is from the feeding mouth of Bulk material spiral 7 to Bulk material spiral shell
The discharging opening of rotation 7 is tapered into.
The utility model also also passes through except being provided with middle and high concentration fiberizer 3 between stock tank 5 before diluting stock tank 4 and copying
Pipeline is connected with low dense fiberizer 6, rises, rubs, crimps kink in high consistency beating section fully wire-dividing broom purification, profit, and low dense section
Appropriate cut-out is carried out to slurry, and keeps certain beating degree.This height consistency pulping is combined mode, strong to ensureing page
Degree, bulk, absorbability and feel and drainability and cost control can obtain the optimum efficiency of Comprehensive Control.Bulk material
The pitch of spiral 7 is tapered into from feeding mouth to discharging opening, and bamboo pulp fiber can be made preferably to disperse agglomerating fiber, makes defibrination electricity
Stream is more stable, and certain pressure can be formed during feeding uniformly and stably slurry propulsion high consistency refining area.
The filter press cloth of the belt filter press 2 is double nets, and bamboo pulp concentration can be made to reach 18%-23%.The preposition stock tank 1
Stock pump 8 is connected with by pipeline between belt filter press 2, it is ensured that belt filter press 2 equably carries out press filtration to bamboo pulp.It is described
Preposition stock tank 1, dilution stock tank 4, to copy and be mounted on consistencyregulator on preceding stock tank 5, concentration regulation can be carried out to each stock tank, it is ensured that
The bamboo pulp concentration of each stock tank reaches requirement.
Specific implementation process of the present utility model：
After the utility model is using double net press filtration magma, concentration reaches 18~23%, using special Bulk material spiral,
It is isometrical displacement near dial portion, can makes screw conveyor that there is bulk cargo function, can helps preferably disperse agglomerating fibre
Dimension.Make defibrination electric current more stable, can be formed during feeding certain pressure uniformly and stably slurry is advanced it is highly concentrated
Defibrination area.High consistency refining system chassis are inner liner stainless steel, and forward and back knife system uses hydraulic control, by regulating pressure of hydro-cylinder
Main shaft is promoted to make axially to reciprocate, so as to reach gap and the pressure between two mills of regulation.Middle high-density paste mill is configured with
One main motor of 630KW-6P, and a high pressure soft starting cabinet of 10KV.Slurry is mutually rubbed in mill area by between fiber
Rub with the hands, compress and rub against effect so that fiber obtains sufficient wire-dividing broom purification, and the length of fiber is without obvious cut-out.Through highly concentrated place
Based on pulp fiber inside sub-wire layering after reason, fiber softens, and knee free hydroxyl group increases, and fiber entanglement curling is obvious.
The sub-wire layering of fibrous inside can be obviously improved the pliability of page, and the anti-tensile that the wire-dividing broom purification of inside and outside can lift page is strong
Degree, fiber is tightly combined.The curling kink of fiber can improve the absorbability of paper, toughness and bulk.Dense beaten using high and low
The bamboo pulp beating process that is combined of slurry, rises in high consistency beating section fully wire-dividing broom purification, profit, rubs, crimps kink, and low dense section
Appropriate cut-out is carried out to slurry, and keeps certain beating degree.This height consistency pulping is combined method, strong to ensureing page
Degree, bulk, absorbability and feel and drainability and cost control can obtain the optimum efficiency of Comprehensive Control.Specific work
Skill：High consistency beating：20~240SR of the degree of beating, 10~12g of weight in wet base；Low consistency pulping：30~360SR, weight in wet base：7.5~9.5g.
Claims (4)
1. the bamboo pulp refining system that a kind of height concentrated phase is combined, including preposition stock tank (1), the belt pressure being sequentially connected by pipeline
Filter (2), middle high-density paste mill (3), dilution stock tank (4), copy preceding stock tank (5)；Characterized in that, it is described dilution stock tank (4) with
Copy and low dense fiberizer (6) is also connected with by pipeline between preceding stock tank (5)；The belt filter press (2) and middle high-density paste mill
(3) Bulk material spiral (7) is also connected with by pipeline between, the pitch of the Bulk material spiral (7) is from Bulk material spiral shell
The feeding mouth for revolving (7) is tapered into the discharging opening of Bulk material spiral (7).
2. the bamboo pulp refining system that a kind of height concentrated phase according to claim 1 is combined, it is characterised in that the belt pressure
The filter press cloth of filter (2) is double nets.
3. the bamboo pulp refining system that a kind of height concentrated phase according to claim 1 is combined, it is characterised in that the preposition slurry
Stock pump (8) is connected with by pipeline between pond (1) and belt filter press (2).
4. the bamboo pulp refining system that a kind of height concentrated phase according to claim 1 is combined, it is characterised in that the preposition slurry
Pond (1), dilution stock tank (4), to copy and be mounted on consistencyregulator on preceding stock tank (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621300298.9U CN206233030U (en) | 2016-11-30 | 2016-11-30 | The bamboo pulp refining system that a kind of height concentrated phase is combined |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621300298.9U CN206233030U (en) | 2016-11-30 | 2016-11-30 | The bamboo pulp refining system that a kind of height concentrated phase is combined |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206233030U true CN206233030U (en) | 2017-06-09 |
Family
ID=58979902
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621300298.9U Active CN206233030U (en) | 2016-11-30 | 2016-11-30 | The bamboo pulp refining system that a kind of height concentrated phase is combined |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206233030U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107485487A (en) * | 2017-08-28 | 2017-12-19 | 芜湖悠派护理用品科技股份有限公司 | A kind of bamboo pulp anti-bacterial nursing pad processing unit (plant) |
| CN109554952A (en) * | 2018-11-23 | 2019-04-02 | 福建省青山纸业股份有限公司 | A kind of wood sand base paper production method |
| CN109706773A (en) * | 2018-12-29 | 2019-05-03 | 重庆理文卫生用纸制造有限公司 | A kind of pulping process of high-cleanness, high primary colors bamboo pulp |
| CN110700010A (en) * | 2019-10-15 | 2020-01-17 | 玛纳斯源源纸业有限公司 | Manufacturing process for grinding medium surface paper of vulcanized fiber paper |
-
2016
- 2016-11-30 CN CN201621300298.9U patent/CN206233030U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107485487A (en) * | 2017-08-28 | 2017-12-19 | 芜湖悠派护理用品科技股份有限公司 | A kind of bamboo pulp anti-bacterial nursing pad processing unit (plant) |
| CN107485487B (en) * | 2017-08-28 | 2021-01-29 | 芜湖悠派护理用品科技股份有限公司 | Processing device for bamboo pulp antibacterial nursing pad |
| CN109554952A (en) * | 2018-11-23 | 2019-04-02 | 福建省青山纸业股份有限公司 | A kind of wood sand base paper production method |
| CN109706773A (en) * | 2018-12-29 | 2019-05-03 | 重庆理文卫生用纸制造有限公司 | A kind of pulping process of high-cleanness, high primary colors bamboo pulp |
| CN110700010A (en) * | 2019-10-15 | 2020-01-17 | 玛纳斯源源纸业有限公司 | Manufacturing process for grinding medium surface paper of vulcanized fiber paper |
| CN110700010B (en) * | 2019-10-15 | 2021-09-17 | 新疆源一科创有限公司 | Manufacturing process for grinding medium surface paper of vulcanized fiber paper |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206233030U (en) | The bamboo pulp refining system that a kind of height concentrated phase is combined | |
| CN105696393B (en) | A kind of wet strong waste paper recycles chemical mechanical pulp-making method | |
| CN106283824B (en) | A kind of high weight high-strength fluting medium process for cleanly preparing | |
| CN103005658B (en) | New technology for improving tobacco stalk pulping quality | |
| CN102002892A (en) | Production process of low-quantitative straw wrapping paper | |
| CN101260630B (en) | Straw and/ or ryegrass raw material semi-chemical pulp preparation method | |
| CN109235125B (en) | Household paper and preparation method thereof | |
| CN204982521U (en) | Living paper's high enriched mill thick liquid system | |
| JP2019531417A (en) | Method for producing cellulose filament using less beating energy | |
| CN102242511A (en) | Independent pulp proportioning technique for toilet-roll base paper | |
| CN103410045B (en) | Paper and preparation method thereof | |
| CN110258155B (en) | TF series paper tube base paper and preparation process thereof | |
| CN103362012B (en) | Fiber and filler mixed enzymatic defibrination method | |
| CN109750554A (en) | A kind of corrugated paper preparation process and equipment | |
| CN110924228A (en) | Light green non-heat-sealing type tea filter paper and preparation method thereof | |
| CN109056420A (en) | A kind of preparation method of Deinking Pulp fruit paper bag | |
| CN115110333A (en) | Method for producing full waste paper kraft paperboard by using biological enzyme to enhance energy conservation | |
| CN204982520U (en) | Living paper's high enriched mill thick liquid and system of soaking | |
| CN114481659A (en) | High-strength craft paper and production process thereof | |
| CN105648817B (en) | A kind of wet strong waste paper recycling pulping system | |
| CN103653231B (en) | A kind of offal pulping process | |
| CN112442913A (en) | Process for making paper substituted fiber ebony slag pulp | |
| CN114541175A (en) | Preparation method of high wet strength paper and high wet strength paper | |
| CN204763381U (en) | Papermaking method reconstituted tobacco's of high calcium carbonate content preparation system | |
| CN104957756B (en) | A kind of improve the method for calcium carbonate retention rate in papermaking-method reconstituted tobaccos |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: No.2, group 9, Yongping village, Xiaogu Town, Qianwei County, Leshan City, Sichuan Province Patentee after: Sichuan Fengsheng Paper Technology Co., Ltd Address before: 614405, Yongping County, Leshan, Qianwei, Sichuan Province nine Patentee before: SICHUAN QIANWEI FENGSHENG PAPER LLC |
|
| CP03 | Change of name, title or address |