CN204589695U - The continuous beating system of two kinds of slurries - Google Patents
The continuous beating system of two kinds of slurries Download PDFInfo
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- CN204589695U CN204589695U CN201520123795.5U CN201520123795U CN204589695U CN 204589695 U CN204589695 U CN 204589695U CN 201520123795 U CN201520123795 U CN 201520123795U CN 204589695 U CN204589695 U CN 204589695U
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Abstract
The utility model belongs to paper making equipment technical field, is specifically related to a kind of continuous beating system of two kinds of slurries.This system comprises pulper, side pressure thickener, second kowtows forebay, the second stock pump and intermediate pool, and described side pressure thickener is connected with first in turn and kowtows forebay, the first stock pump, disc mill, cylinder fiberizer and kowtow after-bay; Described second kowtows one end, forebay is connected with pulper, and the other end is connected with the second described stock pump and cylinder fiberizer successively; Described disc mill is by triple valve and described intermediate pool and kowtow after-bay and be connected.This system mixes after pulling an oar respectively, can meet the demand that client is different.And according to different materials, can formulate rational beating process, pull an oar respectively, refining pulp quality is good.Pulled an oar by the series and parallel of multiple disc mill and cylinder fiberizer, improve the quality of slurry and the recovery rate of raw material.In addition this system process controls flexibly, and product variety increases, and reduces production cost.
Description
Technical field
The utility model belongs to paper making equipment technical field, is specifically related to the continuous beating system of two kinds of slurries.
Background technology
Making beating, also known as beating, is the paper pulp fiber utilizing mechanism process to suspend in water, makes it have adaptation and produce required characteristic on a papermaking machine, and make produced paper can reach the operating process of prospective quality.Utilize physical method, carry out machinery or fluid treatment to paper pulp fiber in water, make fiber be subject to shearing force, change the form of fiber, make paper pulp obtain some characteristic, to ensure that the paper be copied into reaches the quality requirement of expection, this process is just referred to as making beating.In pulping process fiber except by parts shearing, rub with except the effect such as combing, simultaneously the cell membrane of fiber be also subjected to displacement, the phenomenon such as deformation and failure and the swollen that absorbs water, produce fibrillating, paper pulp is made to have flexibility, plasticity, also make the hydroxyl in cellulose molecular chain increase and hydrogen chain combination chance, improve interfibrous adhesion.In existing paper, the paper pulp raw material of papermaking is a lot, general according to customer requirement prepare the slurry of copy paper, or layering is starched, and such as a collection of is sole plales, another batch is recycled pulp, be generally adopt mixing making beating, although equipment investment is little, shortcoming is that kind is single, refining pulp quality is not easy to control, easily occur few fibers cross beat, few fibers pulls an oar inadequate situation.Because client is more to paper grades demand, therefore existing beating equipment cannot meet the multiple demand of client.
Utility model content
The utility model, for the deficiencies in the prior art, provides a kind of continuous beating system of two kinds of slurries.This system equipment technology controlling and process is flexible, and product variety is many, refining pulp quality is good, can meet the multiple demand of client.
The technical solution of the utility model is achieved in that a kind of continuous beating system of two kinds of slurries comprises pulper, side pressure thickener, second kowtows forebay, the second stock pump and intermediate pool, and described side pressure thickener is connected with first in turn and kowtows forebay, the first stock pump, disc mill, cylinder fiberizer and kowtow after-bay; Described second kowtows one end, forebay is connected with pulper, and the other end is connected with the second described stock pump and cylinder fiberizer successively; Described disc mill is by triple valve and described intermediate pool and kowtow after-bay and be connected.
Preferably, described disc mill has two at least, is connected between this disc mill by serial or parallel connection mode.
Preferably, described cylinder fiberizer has two at least, is connected between this cylinder fiberizer by serial or parallel connection mode.
Preferably, described pulper is hydrabrusher.
Preferably, described disc mill is double plate disc mill or three dish disc mills.
The utility model solves the defect existed in background technology, has following beneficial effect:
The continuous beating system of two kinds of slurries that the utility model provides, mixes after making beating respectively, can meet the demand that client is different.And according to different materials, can formulate rational beating process, pull an oar respectively, refining pulp quality is good.Pulled an oar by the series and parallel of multiple disc mill and cylinder fiberizer, improve the quality of slurry and the recovery rate of raw material.In addition this system process controls flexibly, and product variety increases, and reduces production cost.
Accompanying drawing explanation
Fig. 1 is the structural representation of the continuous beating system of two kinds of slurries;
In figure: 1-pulper, 2-side pressure thickener, 3-first kowtows forebay, 4-first stock pump, and 5-second kowtows forebay, 6-second stock pump, 7-disc mill, 8-cylinder fiberizer, and 9-kowtows after-bay, 10-intermediate pool.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
The continuous beating system of a kind of two kinds of slurries as shown in Figure 1, the continuous beating system of these two kinds of slurries comprises pulper 1, side pressure thickener 2, second kowtows forebay 5, second stock pump 6 and intermediate pool 10, and described side pressure thickener 2 is connected with first in turn and kowtows forebay 3, first stock pump 4, disc mill 7, cylinder fiberizer 8 and kowtow after-bay 9; Described second kowtows one end, forebay 5 is connected with pulper 1, and the other end is connected with the second described stock pump 6 and cylinder fiberizer 8 successively; Disc mill 7 is by triple valve and described intermediate pool 10 and kowtow after-bay 9 and be connected.Disc mill 7 has 3, is connected between this disc mill 7 by parallel way.Cylinder fiberizer 8 has 3, is connected between this cylinder fiberizer 8 by parallel way.Pulper 1 is hydrabrusher.Disc mill is double plate disc mill or three dish disc mills.
The course of work of the present utility model is: first wood-pulp board pulls an oar through pulper 1, and form thick slurry and enter second and kowtow forebay 5, second kowtows forebay 5 is delivered to cylinder fiberizer 8 through the second stock pump 6 and pulls an oar, and refining is got back to and kowtowed after-bay 9, finally delivers to dexter feeder stock tank by kowtowing after-bay 9; Chemical raw pulps enters first through side pressure thickener 2 and kowtows forebay 3, deliver to disc mill 7 by the first stock pump 4 again to pull an oar, refining flows into and kowtows after-bay 9, delivers to dexter feeder stock tank by kowtowing after-bay 9, the making beating respectively of two kinds of slurries, refining finally imports kowtows after-bay 9 and mixes.Refining part after disc mill 7 making beating simultaneously flows into intermediate pool 10, and intermediate pool 10 is delivered to pond with slurry by stock pump and provides and delivers.Therefore this system process controls flexibly, and according to different materials, can formulate rational beating process, pull an oar respectively, refining pulp quality is good.Product variety is many, reduces cost, can also meet the multiple demand of client.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. the continuous beating system of two kinds of slurries, it is characterized in that, comprise pulper (1), forebay (5) kowtowed by side pressure thickener (2), second, the second stock pump (6) and intermediate pool (10), described side pressure thickener (2) is connected with first in turn and kowtows forebay (3), the first stock pump (4), disc mill (7), cylinder fiberizer (8) and kowtow after-bay (9); Described second kowtows forebay (5) one end is connected with pulper (1), and the other end is connected with described the second stock pump (6) and cylinder fiberizer (8) successively; Described disc mill (7) is by triple valve and described intermediate pool (10) and kowtow after-bay (9) and be connected.
2. the continuous beating system of two kinds of slurries according to claim 1, it is characterized in that: described disc mill (7) has two at least, this disc mill is connected by serial or parallel connection mode between (7).
3. the continuous beating system of two kinds of slurries according to claim 1, is characterized in that: described cylinder fiberizer (8) has two at least, is connected between this cylinder fiberizer (8) by serial or parallel connection mode.
4. the continuous beating system of two kinds of slurries according to claim 1, is characterized in that: described pulper (1) is hydrabrusher.
5. the continuous beating system of two kinds of slurries according to claim 1 and 2, is characterized in that: described disc mill is double plate disc mill or three dish disc mills.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520123795.5U CN204589695U (en) | 2015-03-03 | 2015-03-03 | The continuous beating system of two kinds of slurries |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520123795.5U CN204589695U (en) | 2015-03-03 | 2015-03-03 | The continuous beating system of two kinds of slurries |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204589695U true CN204589695U (en) | 2015-08-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520123795.5U Expired - Fee Related CN204589695U (en) | 2015-03-03 | 2015-03-03 | The continuous beating system of two kinds of slurries |
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| CN (1) | CN204589695U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108316033A (en) * | 2018-03-23 | 2018-07-24 | 玖龙纸业（太仓）有限公司 | A kind of pulping system for high humidity waste and old boxboard by force |
| CN110699998A (en) * | 2019-03-08 | 2020-01-17 | 合肥银山棉麻股份有限公司 | Slurry mixing system in papermaking process |
-
2015
- 2015-03-03 CN CN201520123795.5U patent/CN204589695U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108316033A (en) * | 2018-03-23 | 2018-07-24 | 玖龙纸业（太仓）有限公司 | A kind of pulping system for high humidity waste and old boxboard by force |
| CN108316033B (en) * | 2018-03-23 | 2024-08-13 | 玖龙纸业（太仓）有限公司 | Pulping system for high-wet-strength waste paperboard |
| CN110699998A (en) * | 2019-03-08 | 2020-01-17 | 合肥银山棉麻股份有限公司 | Slurry mixing system in papermaking process |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150826 Termination date: 20170303 |
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| CF01 | Termination of patent right due to non-payment of annual fee |