CN2841749Y - Paper pulp lightweight scummer - Google Patents

Paper pulp lightweight scummer Download PDF

Info

Publication number
CN2841749Y
CN2841749Y CN 200520086019 CN200520086019U CN2841749Y CN 2841749 Y CN2841749 Y CN 2841749Y CN 200520086019 CN200520086019 CN 200520086019 CN 200520086019 U CN200520086019 U CN 200520086019U CN 2841749 Y CN2841749 Y CN 2841749Y
Authority
CN
China
Prior art keywords
scummer
tube
lightweight
paper pulp
eddy flow
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.)
Expired - Fee Related
Application number
CN 200520086019
Other languages
Chinese (zh)
Inventor
贾来恩
王东军
李光亮
卞绍华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ANQIU CITY TIANLI MACHINERY MANUFACTURING Co Ltd
Original Assignee
ANQIU CITY TIANLI MACHINERY MANUFACTURING Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ANQIU CITY TIANLI MACHINERY MANUFACTURING Co Ltd filed Critical ANQIU CITY TIANLI MACHINERY MANUFACTURING Co Ltd
Priority to CN 200520086019 priority Critical patent/CN2841749Y/en
Application granted granted Critical
Publication of CN2841749Y publication Critical patent/CN2841749Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Paper (AREA)

Abstract

The utility model discloses a kind of paper pulp lightweight scummer, comprise the scummer housing, described scummer housing middle and upper part is the upper conical-tube of tapered diameter, and the bottom is the gradually big slower conical tube of diameter; At the top of upper conical-tube oral area the eddy flow that reaches down in the scummer housing inner chamber is installed and forms device, the top that eddy flow forms device is equipped with upper cover, and upper cover is provided with stock inlet; Be provided with capping down in the bottom of slower conical tube, lower seal covers and is provided with good slurry pipe, descends the center of capping that the scum pipe that reaches the slower conical tube bottom also is installed certainly.It is simple in structure, power consumption is few, and is easy for installation, and the system maintenance expense is low, can effectively remove the various light impurities in the paper pulp, adapts to concentration is removed light slag in slurries such as the various secondary stocks below 1%, chemical pulp, Straw Pulp requirement.

Description

Paper pulp lightweight scummer
Technical field
The utility model relates to a kind of pulp processing equipment, especially a kind of paper pulp lightweight scummer.
Background technology
At present, in pulp production, scummer is to be used widely, and scummer generally is divided into heavy scummer and lightweight scummer, the slagging-off effect of heavy scummer is very good, but the processing of light impurity is a great problem of domestic paper-making industry always, and existing lightweight scummer separates not thorough, the slagging-off weak effect, the fibre stream vector is big, and advance to starch concentration and generally be not more than 0.5%, cause great lot of water resources and power waste, have a strong impact on the quality of the especially high-grade paper of paper.
Summary of the invention
The technical problems to be solved in the utility model provide a kind of simple in structure, power consumption is few, can effectively remove the paper pulp lightweight scummer of various light impurities.
For solving the problems of the technologies described above, the utility model comprises the scummer housing, and its design feature is that described scummer housing middle and upper part is the upper conical-tube of tapered diameter, and the bottom is the gradually big slower conical tube of diameter; At the top of upper conical-tube oral area the eddy flow that reaches down in the scummer housing inner chamber is installed and forms device, the top that eddy flow forms device is equipped with upper cover, and upper cover is provided with stock inlet; Be provided with capping down in the bottom of slower conical tube, lower seal covers and is provided with good slurry pipe, descends the center of capping that the scum pipe that reaches the slower conical tube bottom also is installed certainly.
Described eddy flow forms device and has discoid base plate, is provided with down the deflection cone of stretching from the centre of base plate; Top being equipped with opposed to each other by two approximate semiorbicular sidewalls of base plate constitutes chamber, and the two side is at the interlaced formation guiding gutter of radial direction, and the guiding gutter top is provided with closure plate, is provided with the deflector that tilts to extend to base plate along guiding gutter export department.
Described stock inlet is mounted obliquely within on the upper cover, and the stock inlet direction is pointed to the center line of chamber.
The diameter of described scum pipe hypomere is greater than the diameter of its epimere.
After adopting said structure, because being installed, the eddy flow that reaches in the scummer housing inner chamber down forms device in upper conical-tube, make slurry in scummer housing inner chamber, form stable spiral eddy flow, slurry time of staying in scummer is longer, separation for light impurity is more thorough, because of light impurity proportion low weight, in with the slurry rotary course, gather the center gradually, from the deslagging mozzle, discharge, and slurry is bigger owing to proportion, is thrown toward wall and edge good slurry pipe discharge, the fibre stream vector reduces greatly, and it is simple in structure, power consumption is few, and is easy for installation, and the system maintenance expense is low.Experiment showed, and use this structure, pressure can form stable spiral eddy flow when 190Kpa, under equal conditions, and the more existing scummer 5-8% that cuts down the consumption of energy.The utility model can adapt to concentration is removed light slag in slurries such as the various secondary stocks below 1%, chemical pulp, Straw Pulp requirement.
Description of drawings
Below in conjunction with accompanying drawing the specific embodiment of the present utility model is described in further detail:
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the structural representation that eddy flow forms device among Fig. 1;
Fig. 3 is the A-A cross-sectional view of Fig. 2;
Fig. 4 forms the perspective view of device for eddy flow.
The specific embodiment
With reference to accompanying drawing, this paper pulp lightweight scummer has the scummer housing, and scummer housing middle and upper part is the upper conical-tube 4 of tapered diameter, and the bottom is the gradually big slower conical tube of diameter 7.At the top of upper conical-tube 4 oral area the eddy flow that reaches down in the scummer housing inner chamber is installed and forms device 3, this eddy flow forms device 3 and has discoid base plate 14, is provided with down the deflection cone of stretching 15 from the centre of base plate 14; Top being equipped with opposed to each other by two approximate semiorbicular sidewalls of base plate 14 constitutes chamber 12, the two side is at the interlaced formation guiding gutter of radial direction (16,17), the guiding gutter top is provided with closure plate 11, be provided with the deflector 13 that tilts to extend to base plate 14 along guiding gutter export department, guiding gutter designs for axial symmetry, guarantee upper conical-tube 4 inner chamber stress balances, make slurry form the spiral eddy flow of steady ordered, under the effect of deflection cone 15, eddy flow is more stable, use deflector 13, avoid occurring turbulent phenomenon.The top of eddy flow formation device 3 and the top oral area of upper conical-tube 4 are integrally welded.The middle part of upper conical-tube 4 is provided with fastener 5, and the top that eddy flow forms device 3 is equipped with upper cover 2, and upper cover 2 is provided with stock inlet 1, and stock inlet 1 is mounted obliquely within on the upper cover 2, and the stock inlet direction is pointed to the center line of chamber 12, in order to strengthen flow velocity.Be provided with capping 9 down in the bottom of slower conical tube 7, following capping 9 is provided with good slurry pipe 10, center from capping 9 down also is equipped with the scum pipe 6 that reaches slower conical tube 7 bottoms, it is the top that extends upper conical-tube 4 and slower conical tube 7 connecting portions on the scum pipe 6, the diameter of scum pipe 6 hypomeres can avoid light slag to stop up scum pipe, and slower conical tube 7 is the gradually big shape of lower diameter greater than the diameter of its epimere, assurance has enough spaces that the good slurry slurry pipe 10 of getting married and start a new life is discharged, and reduces fiber loss.

Claims (4)

1, a kind of paper pulp lightweight scummer comprises the scummer housing, it is characterized in that described scummer housing middle and upper part is the upper conical-tube (4) of tapered diameter, and the bottom is the gradually big slower conical tube of diameter (7); Top oral area at upper conical-tube (4) is equipped with the eddy flow formation device (3) that reaches down in the scummer housing inner chamber, and the top that eddy flow forms device (3) is equipped with upper cover (2), and upper cover (2) is provided with stock inlet (1); Be provided with capping (9) down in the bottom of slower conical tube (7), following capping (9) is provided with good slurry pipe (10), descends the center of capping (9) that the scum pipe (6) that reaches slower conical tube (7) bottom also is installed certainly.
2, paper pulp lightweight scummer according to claim 1 is characterized in that described eddy flow forms device (3) and has discoid base plate (14), is provided with down the deflection cone of stretching (15) from the centre of base plate (14); Top being equipped with opposed to each other by two approximate semiorbicular sidewalls of base plate (14) constitutes chamber (12), the two side is at the interlaced formation guiding gutter of radial direction (16,17), the guiding gutter top is provided with closure plate (11), is provided with the deflector (13) that tilts to extend to base plate (14) along guiding gutter export department.
3, paper pulp lightweight scummer according to claim 2 is characterized in that described stock inlet (1) is mounted obliquely within on the upper cover (2), and the stock inlet direction is pointed to the center line of chamber (12).
4, paper pulp lightweight scummer according to claim 1 is characterized in that the diameter of the diameter of described scum pipe (6) hypomere greater than its epimere.
CN 200520086019 2005-08-07 2005-08-07 Paper pulp lightweight scummer Expired - Fee Related CN2841749Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200520086019 CN2841749Y (en) 2005-08-07 2005-08-07 Paper pulp lightweight scummer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200520086019 CN2841749Y (en) 2005-08-07 2005-08-07 Paper pulp lightweight scummer

Publications (1)

Publication Number Publication Date
CN2841749Y true CN2841749Y (en) 2006-11-29

Family

ID=37445636

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200520086019 Expired - Fee Related CN2841749Y (en) 2005-08-07 2005-08-07 Paper pulp lightweight scummer

Country Status (1)

Country Link
CN (1) CN2841749Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018058219A1 (en) * 2016-09-30 2018-04-05 Oxitec Participação E Gestão De Ativos Não Financeiros Ltda. Process for treating dregs, treated dregs, use thereof, process for vulcanizing rubber, and vulcanized rubber

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018058219A1 (en) * 2016-09-30 2018-04-05 Oxitec Participação E Gestão De Ativos Não Financeiros Ltda. Process for treating dregs, treated dregs, use thereof, process for vulcanizing rubber, and vulcanized rubber
US11306436B2 (en) 2016-09-30 2022-04-19 OXITEC Participaçäo e Gesto de Ativos näo Financeiros Ltda. Process for treating dregs, treated dregs, use thereof, process for vulcanizing rubber, and vulcanized rubber
US11767636B2 (en) 2016-09-30 2023-09-26 Oxitec Participação E Gestão De Ativos Não Financeiros Ltda. Process for treating dregs, treated dregs, use thereof, process for vulcanizing rubber, and vulcanized rubber

Similar Documents

Publication Publication Date Title
CN209631429U (en) A kind of twin-stage cyclone separator
EP2716342A1 (en) Clarifier with feedwell and methods of clarifying liquids
CN2841749Y (en) Paper pulp lightweight scummer
CN203222698U (en) Scummer used for purifying low-concentration paper pulp
CN201713366U (en) Flow guide type tapered sedimentation tank
CN207483404U (en) A kind of oil water separator based on Bubble-floating Method
CN203021862U (en) Sediment tank of high-concentration slag separator
CN2808309Y (en) Stratification ore concentrator
CN206965950U (en) A kind of concentration-type cyclone
CN203021857U (en) High-concentration slag separator
CN205815944U (en) A kind of novel wear resistant heavy medium cyclone
CN101678369B (en) Cyclone separator and method for separating matter from a gas flow
CN2771272Y (en) Pulp light-impurity deslagging device
CN210474282U (en) Device for grading aluminum hydroxide
CN210302985U (en) Water-gas separator for compressed air treatment
CN203021860U (en) Cone inner core of high-concentration slag separator
CN2658145Y (en) Desulfurization dust removal device for smoke of glass smelting kiln
CN203174427U (en) Efficient and energy-saving internally-flowing pressure screen
CN201447633U (en) Fiber separator
CN212576563U (en) Column type large diameter centrifugal catcher
CN218357965U (en) Centrifugal gas-liquid separator
CN213867060U (en) Compound multi-functional scummer
CN211772398U (en) Pressure screen provided with heightening weir cylinder
CN213708964U (en) High-performance slag separator for producing antibacterial environment-friendly fruit bag outer bag paper
CN219210293U (en) Cyclone separator with high-efficient purification

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee