CN205576620U - High concentration deslagging system - Google Patents
High concentration deslagging system Download PDFInfo
- Publication number
- CN205576620U CN205576620U CN201620296776.7U CN201620296776U CN205576620U CN 205576620 U CN205576620 U CN 205576620U CN 201620296776 U CN201620296776 U CN 201620296776U CN 205576620 U CN205576620 U CN 205576620U
- Authority
- CN
- China
- Prior art keywords
- cleaner
- section
- pulper
- high concentration
- stage nitration
- 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
Landscapes
- Paper (AREA)
Abstract
The utility model relates to a high concentration deslagging system, high concentration deslagging system includes: the pulper, the pulper is used for the size degradation thick liquids, one section high enriched dross removal mechanism, one section high enriched dross removal mechanism with the pulper links to each other, is used for receiving accepted stock behind the pulper size degradation, the high enriched scummer of two -stage process, the high enriched scummer of two -stage process with one section high enriched dross removal mechanism links to each other, and the tower of unloading, unload the tower with the high enriched scummer of two -stage process links to each other. The utility model provides a high concentration deslagging system has improved the slurrying productivity under the prerequisite of guaranteeing the thick liquids quality, the also circulation because of having reduced thick liquids has simultaneously reduced the power consumption.
Description
Technical field
This utility model relates to pulp technology for making paper, is specifically related to a kind of high concentration slag removing system.
Background technology
Along with improving constantly of papermaking production capacity, oleo stock ability can not meet capacity requirements.Prior art
Slag removing system, after slurry returns to pulping system, because of size circulations, cause power consumption to increase.Both
Cause the increase of power consumption, reduce again efficiency.
Utility model content
In view of this, the purpose of this utility model is to provide a kind of coating felt, existing to solve
The problem that in technology, phase length tamed by felt.
The high concentration slag removing system that this utility model provides includes:
Pulper, described pulper is used for size degradation slurry；
One section of highly concentrated deslagging device, one section of highly concentrated deslagging device is connected with described pulper, is used for connecing
Receive the accepted stock after described pulper size degradation；
Two-stage nitration HC Cleaner, described two-stage nitration HC Cleaner and described one section of highly concentrated deslagging device phase
Even；And
Discharging tower, described discharging tower is connected with described two-stage nitration HC Cleaner.
Preferably, described one section of highly concentrated deslagging device include one section of HC Cleaner and with described one section
The collection slag ladle that HC Cleaner afterbody is connected；Described one section of HC Cleaner is connected with described discharging tower,
The good slurry that described one section of HC Cleaner is separated enters in described discharging tower, and tailings enters described
Collection slag ladle；Described collection slag ladle is connected with described two-stage nitration HC Cleaner, and described collection slag ladle is used for separating
Fiber in described one section of HC Cleaner tailings and heavy seeds, described two-stage nitration HC Cleaner is from institute
State the extraction of collection slag ladle top and eliminate the slurry of heavy seeds.
Preferably, described collection slag ladle bottom is additionally provided with automatic discharge system, described automatic discharge system
The heavy seeds separated by described collection slag ladle discharges system.
Preferably, described two-stage nitration HC Cleaner is connected with pulper.
The high concentration slag removing system that this utility model provides, on the premise of ensureing stock quality, improves
Slurrying production capacity, simultaneously also because decreasing the circulation of slurry, reduces power consumption.
Accompanying drawing explanation
By description to this utility model embodiment referring to the drawings, of the present utility model above-mentioned
And other objects, features and advantages will be apparent from, in the accompanying drawings:
Fig. 1 illustrates structural representation of the present utility model.
Detailed description of the invention
It is more fully described various embodiment of the present utility model hereinafter with reference to accompanying drawing.Attached at each
In figure, identical element uses same or similar reference to represent.For the sake of clarity,
Various piece in accompanying drawing is not necessarily to scale.
High concentration slag removing system of the present utility model include 1, one section of highly concentrated deslagging device 2 of pulper,
Two-stage nitration HC Cleaner 3 and discharging tower 4.
Specifically, described one section of highly concentrated deslagging device 2 includes one section of HC Cleaner 20 and with described
The collection slag ladle 21 that one section of HC Cleaner 20 afterbody is connected.
Specifically, described collection slag ladle 21 bottom is additionally provided with automatic discharge system 22.
Specifically, described pulper 1 and one section of highly concentrated slagging-off of described one section of highly concentrated deslagging device 2
Device 20 is connected, collection slag ladle 21 and the highly concentrated slagging-off of described two-stage nitration of described one section of highly concentrated deslagging device 2
Device 3 is connected, and described two-stage nitration HC Cleaner 3 is connected with described discharging tower 4.
Preferably, described one section of HC Cleaner 20 is also connected with described discharging tower 4.
Preferably, described two-stage nitration HC Cleaner 3 is connected with pulper 1.
Specifically, described pulper 1 is for size degradation slurry, described one section of highly concentrated deslagging device
One section of HC Cleaner 20 of 2 receives the accepted stock after described pulper 1 size degradation, and removes desizing
Heavy seeds in material, the good slurry that described one section of HC Cleaner 20 is separated enters described discharging tower
In 4, tailings enters in described collection slag ladle 21；Described collection slag ladle 21 is used for separating described one section high
Fiber in dense scummer 20 tailings and heavy seeds, described two-stage nitration HC Cleaner 3 is from described collection slag
The extraction of tank 21 top eliminates the slurry of heavy seeds, and removes the gred slurry, and good slurry enters into institute
Stating in discharging tower 4, defective slurry returns in described pulper 1.
Specifically, described collection slag ladle 21 bottom is additionally provided with automatic discharge system 22, described automatic row
The heavy seeds that described collection slag ladle 21 is separated by slag system 22 discharges system.
Wastepaper as raw material is carried out broken by the described pulper 1 at high concentration slag removing system of the present utility model
Solving, accepted stock is pumped in described one section of highly concentrated deslagging device 2 by discharging pump and carries out at slagging-off
Reason.Described one section of HC Cleaner 20 utilizes centrifugal slagging-off principle to remove the heavy seeds in slurry
Removing, good slurry enters in described discharging tower 4, and tailings enters into and described one section of HC Cleaner 20
The collection slag ladle 21 that is connected of afterbody in, described collection slag ladle 21 utilizes the principle of centrifugal force to remove described
Heavy seeds in tailings, the slurry removing heavy seeds enters in two-stage nitration scummer 3.Described two-stage nitration
The good slurry of scummer 3 enters in described discharging tower 4, and accepted stock returns in described pulper 1.
Preferably, heavy seeds is discharged system by auto-programming timing by described automatic slag discharge device 22.
The high concentration slag removing system that this utility model provides, on the premise of ensureing stock quality, improves
Slurrying production capacity, simultaneously also because decreasing the circulation of slurry, reduces power consumption.
It should be noted that, in this article, the relational terms of such as first and second or the like is only
It is used for separating an entity or operation with another entity or operating space, and not necessarily requires
Or imply relation or the order that there is any this reality between these entities or operation.And,
Term " includes ", " comprising " or its any other variant are intended to comprising of nonexcludability,
So that include that the process of a series of key element, method, article or equipment not only include that those are wanted
Element, but also include other key elements being not expressly set out, or also include for this process,
The key element that method, article or equipment are intrinsic.In the case of there is no more restriction, by statement
The key element that " including one ... " limits, it is not excluded that include the process of described key element, method,
Article or equipment there is also other identical element.
Last it is noted that obvious, above-described embodiment is only new for clearly demonstrating this practicality
Type example, and not restriction to embodiment.Ordinary skill people for art
For Yuan, can also make other changes in different forms on the basis of the above description.
Here without also cannot all of embodiment be given exhaustive.And thus amplified out aobvious and easy
The change seen or variation still in protection domain of the present utility model among.
Claims (4)
1. a high concentration slag removing system, described high concentration slag removing system includes:
Pulper, described pulper is used for size degradation slurry；
One section of highly concentrated deslagging device, one section of highly concentrated deslagging device is connected with described pulper, is used for connecing
Receive the accepted stock after described pulper size degradation；
Two-stage nitration HC Cleaner, described two-stage nitration HC Cleaner and described one section of highly concentrated deslagging device phase
Even；And
Discharging tower, described discharging tower is connected with described two-stage nitration HC Cleaner.
High concentration slag removing system the most according to claim 1, it is characterised in that described one section high
Dense deslagging device includes one section of HC Cleaner and the collection being connected with described one section of HC Cleaner afterbody
Slag ladle；Described one section of HC Cleaner is connected with described discharging tower, and described one section of HC Cleaner divides
The good slurry separated out enters in described discharging tower, and tailings enters described collection slag ladle；Described collection slag ladle with
Described two-stage nitration HC Cleaner is connected, and described collection slag ladle is used for separating described one section of HC Cleaner tail
Fiber in slag and heavy seeds, described two-stage nitration HC Cleaner is from the extraction removal of described collection slag ladle top
The slurry of heavy seeds.
High concentration slag removing system the most according to claim 2, it is characterised in that described collection slag ladle
Bottom is additionally provided with automatic discharge system, and described collection slag ladle is separated by described automatic discharge system
Heavy seeds discharges system.
High concentration slag removing system the most according to claim 1, it is characterised in that described two-stage nitration is high
Dense scummer is connected with pulper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620296776.7U CN205576620U (en) | 2016-04-12 | 2016-04-12 | High concentration deslagging system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620296776.7U CN205576620U (en) | 2016-04-12 | 2016-04-12 | High concentration deslagging system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205576620U true CN205576620U (en) | 2016-09-14 |
Family
ID=56865289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620296776.7U Active CN205576620U (en) | 2016-04-12 | 2016-04-12 | High concentration deslagging system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205576620U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107503212A (en) * | 2016-12-31 | 2017-12-22 | 天津市宝坻区发达造纸有限公司 | A kind of waste paper recycling pulping process |
| CN109098027A (en) * | 2018-09-04 | 2018-12-28 | 马丽芬 | Two sections of continous way HC Cleaner devices of level-one |
| CN111636232A (en) * | 2020-06-03 | 2020-09-08 | 玖龙纸业（东莞）有限公司 | Two-section type high-concentration slag separator, pulp inlet concentration control method thereof and storage medium |
-
2016
- 2016-04-12 CN CN201620296776.7U patent/CN205576620U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107503212A (en) * | 2016-12-31 | 2017-12-22 | 天津市宝坻区发达造纸有限公司 | A kind of waste paper recycling pulping process |
| CN109098027A (en) * | 2018-09-04 | 2018-12-28 | 马丽芬 | Two sections of continous way HC Cleaner devices of level-one |
| CN111636232A (en) * | 2020-06-03 | 2020-09-08 | 玖龙纸业（东莞）有限公司 | Two-section type high-concentration slag separator, pulp inlet concentration control method thereof and storage medium |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205576620U (en) | High concentration deslagging system | |
| CN102041750B (en) | Manufacture process of all waste paper dried noodle cardboard paper | |
| CN106930139A (en) | The preparation technology of environmentally friendly liner board | |
| CN105780568A (en) | Pulp making technology through performing biological enzyme softening lignin removal twice combined with mechanical method | |
| CN105586797A (en) | Wastepaper recycling regeneration paperboard process | |
| CN204622250U (en) | A kind of log is chipped production line | |
| CN103433123A (en) | Process for ore pulp desliming and ore slurry dehydration | |
| AU2021100676A4 (en) | Efficient desliming and separating method | |
| CN202129156U (en) | Three-product autogenous medium cyclone for coarse coal slime separation | |
| CN205182354U (en) | Coal slime water processing system | |
| CN207605861U (en) | A kind of fine coal slurry desliming drop apparatus for ash | |
| CN106622672A (en) | Float fine coal cell distribution treatment technique | |
| CN104437832A (en) | Dry-method fines removal dense medium sorting process for slack coal flip-flow screen | |
| CN108277670B (en) | Steam explosion pulping system for salix psammophila pulping | |
| CN102603900B (en) | High-potential-difference potato starch-residue separation system | |
| CN204317475U (en) | Papermaking-method reconstituted tobaccos coating fluid cleaning system | |
| CN110523522A (en) | Separation of coarse slime method and its equipment | |
| US2310651A (en) | Starch manufacturing process | |
| CN107237192B (en) | A kind of regenerated newsprint and preparation method thereof | |
| CN109594385A (en) | A kind of useless slurrying production method in the single process whole nation of lightweight paper | |
| CN105386351B (en) | A kind of fast-growing willow pulping process | |
| CN105821696B (en) | Application of the centrifuge on papermaking pulping system | |
| CN209144574U (en) | A kind of closed addition in pulp equipment | |
| CN204563781U (en) | A kind of two-stage dust removal device of producd fibers plate | |
| CN106948199A (en) | The system that a kind of use floatation handles waste paper pulp sicker |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 063500, 88 West Road, Chengguan County, Hebei, Luannan Patentee after: Nine dragon paper (Hebei) Co., Ltd. Address before: 063500, 88 West Road, Chengguan County, Hebei, Luannan Patentee before: Hebei Yongxin Paper Co., Ltd. |
|
| CP01 | Change in the name or title of a patent holder |