CN201091810Y - Auger convey discharge forcing ceramic filter - Google Patents

Auger convey discharge forcing ceramic filter Download PDF

Info

Publication number
CN201091810Y
CN201091810Y CNU2007201513378U CN200720151337U CN201091810Y CN 201091810 Y CN201091810 Y CN 201091810Y CN U2007201513378 U CNU2007201513378 U CN U2007201513378U CN 200720151337 U CN200720151337 U CN 200720151337U CN 201091810 Y CN201091810 Y CN 201091810Y
Authority
CN
China
Prior art keywords
ceramic filter
screw
pressurizing
filter
conveying discharging
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 - Lifetime
Application number
CNU2007201513378U
Other languages
Chinese (zh)
Inventor
高彬
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CNU2007201513378U priority Critical patent/CN201091810Y/en
Application granted granted Critical
Publication of CN201091810Y publication Critical patent/CN201091810Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Abstract

The utility model relates to a screw-conveying discharging style pressurizing ceramic filter, comprising a pressurizing cabin, a shaft sealing system, a ceramic filter, a feeding system, a vacuum and pressurizing system, a conveying discharging system, a filtered liquid draining and backwashing system, an automatic control and safety system, etc. The screw-conveying discharging style pressurizing ceramic filter is characterized in that a sealing style with a groove body, a filtering plate and the screw-conveying discharging system is adopted to reduce the pressurizing space required by the sealing the whole machine, and then material consumption and the weight of the whole machine are greatly reduced and the work energy consumption is reduced; simultaneously, screw vanes are arranged in the screw-conveying discharging system and materials are stacked on vanes and cavities, which is good for preserving air pressure; and a roller motor, a distributing valve and a pipeline system are arranged outside a pressure cabin, so as to reduce the failure of the system and to result in convenient maintenance. The utility model leads the ceramic filter to adapt to the filtering in high altitude areas and for materials with high viscosity, and then the production efficiency and capability of the ceramic filter are enhanced, and the energy conserving characteristic becomes distinct.

Description

Spiral Conveying Blowdown Type Pressure Ceramic Filter
Technical field
The utility model relates to a kind of working region sealing continous way pressure ceramic filter, specifically, relate to working region (cell body, filter and helical feed discharge system) sealed, with the micropore ceramics material is filter medium, and the pressure differential (can reach 0.6MPa) of utilizing compressed air (or compressed air and vacuum draw act on simultaneously) to be produced realizes the ceramic filter that filters.Be a kind of energy-efficient shape solid-liquid separating equipment, be applicable to fields such as black, non-ferrous metal ore, thin fine coal powder, chemical industry, food and sewage disposal.
Background technology
The vacuum ceramic filter is a kind of advanced person's a solid-liquid separating equipment, its capillarity of utilizing negative pressure of vacuum and micropore ceramics material to be had realizes filtering (its micro-pore diameter is about 1.5 μ m), it is advanced in performance to possess skills, energy-saving and cost-reducing, advantages such as clean environment firendly, at present, the trend of the high traditional filter cloth formula filter of progressively alternative energy consumption is arranged in applications that put it over of the Separation of Solid and Liquid of industries such as ore dressing, chemical industry, nonmetallic materials, metallurgy.But because vacuum filtration maximum filtering pressure reduction is an atmospheric pressure, make the use of vacuum ceramic filter be subjected to severely restricts, especially the regional vacuum of forcing down at the height above sea level atmosphere only is 0.06MPa.Filtering that solid contents is low, material thin and slip viscosity when big, having that production capacity is low, the high problem of filter cake moisture, having a strong impact on the expansion of ceramic filter application.
The described flotation concentrate pressing filter of ZL95217603.3 that Patent Office of the People's Republic of China (PRC) was authorized on March 13rd, 1996, be that traditional disk filter integral body is wrapped into pressurizing vessel, the very huge heaviness of complete machine, filter medium adopts stainless (steel) wire (weaving of employing filter cloth is also arranged in actual the enforcement), filter opening diameter big (>12 μ m), it is serious that thin material is worn filter, and the suspension content height must return production procedure and handles in the filtrate, increase the weight of the load of whole production flow process, increased the production run cost.
On July 19th, 2006, application number 200620124082.1 was to adopt ceramic filter integral body is wrapped into pressurizing vessel by the pressure ceramic filter patent of our company's application, and equipment volume is big, and high material consumption is used the energy consumption height, is unfavorable for Operation and Maintenance.
Summary of the invention
The objective of the invention is to adopt working region partial closure mode to dwindle the required pressurization space of complete machine sealing, reduced material consumption significantly and alleviated complete machine weight, reduced the work energy consumption, be convenient to Operation and Maintenance.The pressure that utilizes compressed air (or compressed air and vacuum draw act on simultaneously) to be produced is realized filtering, and comparable conventional vacuum ceramic filter improves nearly ten times of pressure differentials.With the micropore ceramics material is filter medium, makes the ceramic filter function adapt to the filtration of high altitude localities and various high-viscosity materials.It can increase substantially the production capacity of filter, reduces filter cake moisture, realizes disposable Separation of Solid and Liquid, reduces filter production run cost, improves the adaptive capacity of filter to material, expands its application.
For realizing purpose of the present invention, pressure ceramic filter provided by the invention comprises the pressurization storehouse, and the ore pulp cell body of ceramic filter, filter, stirring pendulous device place the pressurization storehouse; By the sealing movingly between axle sealing system realization pressurization storehouse and turning cylinder; The helical feed discharge system is arranged and is connected in pressurization storehouse outer setting, under the situation that keeps the storehouse internal pressure not leak, the solid material of conveying is discharged to outside the storehouse on the belt conveyor with the pressurization storehouse; The helical feed discharge system is equipped with helical blade, and solid accumulation more helps keeping air pressure in blade and cavity place.Middle trough is set, the slag stock pump is used for the filtration slip is fed the ceramic filter cell body with certain pressure; Moisture trap, vavuum pump and low pressure gasholder are set, air compressor machine provides power for filtration; Circulating pump, measuring pump and associated pipe, pipe fitting are set, are used for the backwash and the regular cleaning and regeneration of filtrate discharge, ceramic filter plate, to keep its production capacity; Automatic control system is set is used for complete machine control and failure warning automatically.
Description of drawings
Fig. 1. the main frame front view
Fig. 2. the host computer side view
Fig. 3. the interconnection front view
Fig. 4. the interconnection side view
Fig. 5. axle envelope form figure
Fig. 6. mass transport and discharge system figure
1 pressurization storehouse 2 envelopes, 3 agitating devices, 4 distributing valves, 5 cylinder 6 frames, 7 helical feed and discharge system 8 moisture traps
10 automatic controls of 9 vavuum pumps and security system 11 measuring pumps 12 circulating pumps 13 air compressor machines, low pressure gasholder 14 middle troughs 15 slag stock pumps 16 helical blades 17 on-the-spot cesspools 18 on-the-spot shurry pump ponds
The a storehouse sidewall b sealing gasket I c sealing clamp I d sealing gasket II e sealing clamp II that pressurizes
Embodiment
Pressure ceramic filter such as Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, shown in Figure 6, comprise pressurization storehouse (1), the compression system of being made up of air compressor machine and low pressure gasholder (13) is connected with pressurization storehouse (1) by pipeline, duration of work, pressurization storehouse (1) internal pressure is controlled at below the 0.6MPa, and keeps stable; Vavuum pump (9) communicates with ceramic filter plate by moisture trap (8), ceramic filter distributing valve (4), duration of work, and vacuum pressure is controlled at-0.05--0.098MPa according to working environment and material properties, also can not vacuumize; During the equipment operation, slip is by middle trough (14), the feeding system that slag stock pump (15) is formed is sent in the cell body of ceramic filter by pipeline with certain pressure, and be in suspended state under the agitating device in being arranged on cell body (3) stirring, under compressed air (or compressed air and vacuum draw while) effect, solids is adsorbed on the ceramic filter plate surface, under drum spindle drives, unload by the ceramic filter scraper, drop on the helical conveyer system (7), solid material is transmitted and discharges the pressurization storehouse by helical conveyer system (7), filtrate enters in the moisture trap (8) via ceramic filter intralamellar part and associated pipe, be disposed to setting ground by circulating pump (13), and a part of filtrate returned to ceramic filter plate, be used for the backwash after ceramic filter plate strikes off material, measuring pump (11) communicates with ceramic filter plate by pipeline, when regularly cleaning, cleaning fluid is carried out Chemical cleaning regeneration by this covering device to ceramic filter plate, meanwhile, the ultrasonic cleaning equipment that is arranged on ceramic filter inside carries out machinery to ceramic filter plate and cleans, and guarantees the regeneration effect of ceramic filter plate; Automatic control system (10) is used for complete machine automatically control and failure warning, comprises controller and related electric element, safety valve etc., is connected with motor, pneumatic element, realizes the Automatic Control of equipment, manually controls function, and guarantee the safety of equipment.

Claims (4)

1. Spiral Conveying Blowdown Type Pressure Ceramic Filter, it comprises pressurization storehouse, axle sealing system, ceramic filter, feeding system, vacuum and compression system, conveying discharge system, filtrate discharge and backwashing system, automatically control and security system is characterized in that cell body, filter and the helical feed discharge system of filter places in the pressurization storehouse.
2. Spiral Conveying Blowdown Type Pressure Ceramic Filter as claimed in claim 1 is characterized in that axle sealing system adopts rubber or ceramic wear-resisting material.
3. Spiral Conveying Blowdown Type Pressure Ceramic Filter as claimed in claim 1 is characterized in that the helical feed discharge system is equipped with helical blade.
4. Spiral Conveying Blowdown Type Pressure Ceramic Filter according to claim 1 is characterized in that filter medium adopts withstand voltage ceramic filter plate.
CNU2007201513378U 2007-07-10 2007-07-10 Auger convey discharge forcing ceramic filter Expired - Lifetime CN201091810Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2007201513378U CN201091810Y (en) 2007-07-10 2007-07-10 Auger convey discharge forcing ceramic filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2007201513378U CN201091810Y (en) 2007-07-10 2007-07-10 Auger convey discharge forcing ceramic filter

Publications (1)

Publication Number Publication Date
CN201091810Y true CN201091810Y (en) 2008-07-30

Family

ID=39899770

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2007201513378U Expired - Lifetime CN201091810Y (en) 2007-07-10 2007-07-10 Auger convey discharge forcing ceramic filter

Country Status (1)

Country Link
CN (1) CN201091810Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104481886A (en) * 2014-10-27 2015-04-01 攀枝花钢城集团瑞矿工业有限公司 Slurry pump sump
CN107351437A (en) * 2017-07-19 2017-11-17 上海诺辉工程科技发展有限公司 Auto purification type screw extrusion slag tapping equipment and its application method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104481886A (en) * 2014-10-27 2015-04-01 攀枝花钢城集团瑞矿工业有限公司 Slurry pump sump
CN107351437A (en) * 2017-07-19 2017-11-17 上海诺辉工程科技发展有限公司 Auto purification type screw extrusion slag tapping equipment and its application method

Similar Documents

Publication Publication Date Title
CN201076795Y (en) Press ceramic filter with confined working range
CA1119406A (en) Consolidation of coal slurry
CN206809873U (en) A kind of vacuum Dehydrator for Slurry
CN106731154A (en) A kind of vacuum Dehydrator for Slurry
CN201082371Y (en) Drum vacuum filter
CN201091810Y (en) Auger convey discharge forcing ceramic filter
CN204933745U (en) Centrifuge with cutter discharge of solid is filtered in a kind of horizontal siphon
CN104667612A (en) Novel ceramic filter device
CN100556497C (en) Pressure ceramic filter
CN201046363Y (en) Pressurization ceramic filter
CN208727696U (en) A kind of spiral squeezing type filter that filter effect is good
CN201105185Y (en) Sealed type pressurization ceramic vacuum filter device
CN105396702A (en) Fine coal centrifugal separation equipment capable of discharging materials continuously
CN208574321U (en) Ceramic filter scraper
CN87102662A (en) Mechanical extrusion type continuous filter press
US3378143A (en) Straining apparatus for paint and the like
CN101445316A (en) Tailing and tail mud treatment system and process method thereof
CN201701813U (en) Electrolyte blocking filter of vacuum pipeline
CN107648922B (en) Discharge device of pressure disk type filter
CN207445746U (en) The discharge device of pressurization disk filter
CN1104926C (en) Multifunctional enclosed continuous filter
CN2221998Y (en) Pressing filter machine for flotation ore concentrate
CN107540190A (en) A kind of drum-type dewaterer
CN208454778U (en) A kind of device purified for river and lake silt dehydration and drying and tail water
CN208212622U (en) A kind of automatic discharge filter device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: ANSHAN SPECIAL WEAR-RESISTING EQUIPMENT FACTORY

Assignor: Gao Bin

Contract fulfillment period: 2009.3.19 to 2017.6.14

Contract record no.: 2009210000038

Denomination of utility model: Auger convey discharge forcing ceramic filter

Granted publication date: 20080730

License type: Exclusive license

Record date: 20090320

LIC Patent licence contract for exploitation submitted for record

Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.3.19 TO 2017.6.14; CHANGE OF CONTRACT

Name of requester: ANSHAN CITY SPECIAL WEAR-RESISTING EQUIPMENT PLANT

Effective date: 20090320

EE01 Entry into force of recordation of patent licensing contract

Assignee: ANSHAN SPECIAL WEAR-RESISTING EQUIPMENT FACTORY

Assignor: Gao Bin

Contract fulfillment period: 2008.6.14 to 2017.6.13

Contract record no.: 2009210000038

Denomination of utility model: Auger convey discharge forcing ceramic filter

Granted publication date: 20080730

License type: Exclusive license

Record date: 20090320

LIC Patent licence contract for exploitation submitted for record

Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2008.6.14 TO 2017.6.13; CHANGE OF CONTRACT

Name of requester: ANSHAN CITY SPECIAL WEAR-RESISTING EQUIPMENT PLANT

Effective date: 20090320

CX01 Expiry of patent term

Granted publication date: 20080730

CX01 Expiry of patent term