CN204702996U - Interval and continuous beating system - Google Patents
Interval and continuous beating system Download PDFInfo
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- CN204702996U CN204702996U CN201520123619.1U CN201520123619U CN204702996U CN 204702996 U CN204702996 U CN 204702996U CN 201520123619 U CN201520123619 U CN 201520123619U CN 204702996 U CN204702996 U CN 204702996U
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- jordan
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- pulper
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Abstract
The utility model belongs to paper making equipment technical field, is specifically related to a kind of interval and continuous beating system.This system comprises the pulper, circulation stock tank, jordan and the machine chest that connect successively, the first stock pump is provided with between described pulper and circulation stock tank, the second stock pump and gate valve is provided with between circulation stock tank and jordan, described jordan comprises first, second, and third cylinder jordan, described first, second, and third its stock inlet of cylinder jordan is connected with described second stock pump, and its grout outlet is connected with machine chest with described circulation stock tank respectively.This refining system not only can adopt batch (-type) but also continous mode can be adopted to pull an oar, wide adaptability.Pulled an oar by the carrying out of multi-level oil pulp grinder, improve quality and the productivity ratio of slurry; Pulled an oar by the recovery repeatedly of circulation stock tank, improve the recovery rate of raw material, save production cost, decrease environmental pollution simultaneously, energy-conserving and environment-protective.
Description
Technical field
The utility model belongs to paper making equipment technical field, is specifically related to a kind of interval and continuous beating system.
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.Existing wood-pulp board refining system by the mode of production, can be divided into interval making beating and continuous beating, but all have that raw material recovery rate is low, raw material can not circulation beating and multistage making beating, causes defects such as yielding poorly, wastage of material is large, production efficiency is low, environmental pollution is large.Refining pulp quality also awaits improving simultaneously.
Utility model content
The utility model, for the deficiencies in the prior art, provides a kind of refining system that not only can adopt batch (-type) but also can adopt continous mode.
The technical solution of the utility model is achieved in that a kind of interval and continuous beating system comprise pulper, circulation stock tank, jordan and the machine chest connected successively, the first stock pump is provided with between described pulper and circulation stock tank, the second stock pump and gate valve is provided with between circulation stock tank and jordan, described jordan comprises first, second, and third cylinder jordan, described first, second, and third its stock inlet of cylinder jordan is connected with described second stock pump, and its grout outlet is connected with machine chest with described circulation stock tank respectively.
Preferably, connected by serial or parallel connection mode between described first, second, and third cylinder jordan.
Preferably, described pulper is hydrabrusher.
Preferably, described jordan also comprises double plate disc mill or three dish disc mills.
The utility model solves the defect existed in background technology, has following beneficial effect:
The interval that the utility model provides and continuous beating system, not only can adopt batch (-type) but also continous mode can be adopted to pull an oar, wide adaptability.Pulled an oar by the carrying out of multi-level oil pulp grinder, improve quality and the productivity ratio of slurry; Pulled an oar by the recovery repeatedly of circulation stock tank, improve the recovery rate of raw material, save production cost, decrease environmental pollution simultaneously, energy-conserving and environment-protective.
Accompanying drawing explanation
Fig. 1 is the structural representation of interval and continuous beating system;
In figure: 1-pulper, 2-first stock pump, 3-circulation stock tank, 4-second stock pump, 5-first cylinder jordan, 6-second cylinder jordan, 7-three cylindrical jordan, 8-machine chest.
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.
A kind of interval as shown in Figure 1 and continuous beating system, this interval and continuous beating system comprise the pulper 1, circulation stock tank 3, jordan and the machine chest 8 that connect successively, the first stock pump 2 is provided with between pulper 1 and circulation stock tank 3, the second stock pump 4 and gate valve is provided with between circulation stock tank 3 and jordan, jordan comprises first, second, and third cylinder jordan 5,6,7, first, second, and third cylinder jordan 5,6,7 its stock inlets are connected with described second stock pump 4, and its grout outlet is connected with machine chest 8 with described circulation stock tank 3 respectively.First, second, and third cylinder jordan 5,6, is connected by serial or parallel connection mode between 7.Pulper 1 is hydrabrusher.Jordan also comprises double plate disc mill or three dish disc mills.
The course of work of the present utility model is: first wood-pulp board or slush pulp carry out size degradation by hydrabrusher 1 and form thick slurry, and thick slurry is evacuated to circulation stock tank 3 by the first stock pump 2, pulls an oar being evacuated to jordan by circulation 3 by the second stock pump 4 simultaneously.According to refining pulp quality requirement, first, second, and third cylinder jordan is connected in series or parallel.In the slurries of jordan making beating some comparatively crude fibre again enter circulation stock tank 3 by gate valve and carry out circulating and pull an oar again.It is stand-by or send into dexter feeder stock tank for machine room starching that the finished pulp that last jordan is made is transported to machine chest 8.
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 (4)
1. an interval and continuous beating system, it is characterized in that, comprise the pulper (1) connected successively, circulation stock tank (3), jordan and machine chest (8), the first stock pump (2) is provided with between described pulper (1) and circulation stock tank (3), the second stock pump (4) and gate valve is provided with between circulation stock tank (3) and jordan, described jordan comprises first, second and three cylindrical jordan (5, 6, 7), described first, second and three cylindrical jordan (5, 6, 7), its stock inlet is connected with described second stock pump (4), its grout outlet is connected with machine chest (8) with described circulation stock tank (3) respectively.
2. an interval according to claim 1 and continuous beating system, is characterized in that: connected by serial or parallel connection mode between described first, second, and third cylinder jordan (5,6,7).
3. an interval according to claim 1 and continuous beating system, is characterized in that: described pulper (1) is hydrabrusher.
4. an interval according to claim 1 and continuous beating system, is characterized in that: described jordan also comprises double plate disc mill or three dish disc mills.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520123619.1U CN204702996U (en) | 2015-03-03 | 2015-03-03 | Interval and continuous beating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520123619.1U CN204702996U (en) | 2015-03-03 | 2015-03-03 | Interval and continuous beating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204702996U true CN204702996U (en) | 2015-10-14 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520123619.1U Expired - Fee Related CN204702996U (en) | 2015-03-03 | 2015-03-03 | Interval and continuous beating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204702996U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN110699997A (en) * | 2019-03-08 | 2020-01-17 | 合肥银山棉麻股份有限公司 | Recycling defective pulp system for pulping by adopting hydrapulper |
-
2015
- 2015-03-03 CN CN201520123619.1U patent/CN204702996U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN110699997A (en) * | 2019-03-08 | 2020-01-17 | 合肥银山棉麻股份有限公司 | Recycling defective pulp system for pulping by adopting hydrapulper |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151014 Termination date: 20170303 |