CN2234315Y - Vibration reverse divided type air heavy-media separator - Google Patents

Vibration reverse divided type air heavy-media separator Download PDF

Info

Publication number
CN2234315Y
CN2234315Y CN 94221391 CN94221391U CN2234315Y CN 2234315 Y CN2234315 Y CN 2234315Y CN 94221391 CN94221391 CN 94221391 CN 94221391 U CN94221391 U CN 94221391U CN 2234315 Y CN2234315 Y CN 2234315Y
Authority
CN
China
Prior art keywords
heavy
separator
media
air
outlet
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 94221391
Other languages
Chinese (zh)
Inventor
张济宇
刘有智
陈荣耀
张碧江
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.)
Shanxi Institute of Coal Chemistry of CAS
Original Assignee
Shanxi Institute of Coal Chemistry of CAS
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 Shanxi Institute of Coal Chemistry of CAS filed Critical Shanxi Institute of Coal Chemistry of CAS
Priority to CN 94221391 priority Critical patent/CN2234315Y/en
Application granted granted Critical
Publication of CN2234315Y publication Critical patent/CN2234315Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The utility model belongs to a high-efficiency separator for solid mixtures, particularly relating to a vibration reverse divided type air heavy-media separator. The vibration reverse divided type air heavy-media separator is composed of an air inlet, raw materials and a heavy media inlet, floats and a heavy media outlet, sinking objects and a heavy media outlet, dust gas outlet, a multi-air chamber distributing device, and a fluidized bed. The utility model is characterized in that the fluidized bed is provided with a vibrator, the floats and the heavy media outlet and the sinking objects and the heavy media outlet are respectively provided with baffles. The utility model avoids the shortcomings of the wear of a general-purpose machine conveying type heavy-media separator, the complicated equipment, etc.

Description

Vibrate reverse shunting air dense medium separator
The utility model is a kind of efficient cyclone of solid mixture, is specifically related to the reverse shunting air dense medium of a kind of vibration separator.
Air---the principle of dense medium separation technology is: utilize dispersion and the suspension of dense media particulate in air-flow, under optimum conditions, can form a desirable fluidized-bed layer that is similar to liquid homogeneous density, difference according to solid mixture and bed density, light thing floats on the surface, weight is sunken to the bottom, uses different means and device respectively light, heavy material to be removed from bed then, thereby finishes effective separation of solid mixture.
Technology maturation and very representational device in air----the dense media method sorting process, " adverse current tandem " fluid bed cleaning unit (Counter-Current FluidizedCascads that Beeckmans is abroad arranged, Beeckmans, J.M.and Goransson, M., CIM Builetin, 75 (839), 184 (1982)); " the reverse conveying-type of scraper plate " air dense medium fluid bed dry coal preparation device that the domestic Chen Qingru of having professor is proposed (Chen Qingru, Yang Yi, Yu Zhimin, Liu Huansheng, Li Jianming, the 5th national fluidization proceeding, 1990, P345) as shown in Figure 1:
1 is inlet, 2 medium inlets of attaching most importance to, 3 are the dusty gas outlet, and 4 is the up scraper plate of drag conveyor, and 5 is float coal and dense media outlet, 6 are the multilayer multihole distributor of weaving cotton cloth, 7 is gas diffluence room, and 8 is total air intake, and 9 is rectangle slot type air dense medium fluid bed, 10 is the descending scraper plate of drag conveyor, and 11 is hypostasis and dense media outlet.
For the light thing that will float on the surface separates with the weight that is sunken to the bottom, above-mentioned two kinds of devices have all adopted baroque, mechanical drag conveyor, thereby following tangible deficiency occurred:
(1) adding of drag conveyor all brings direct influence to the control of the even suspended state of air dense medium fluid bed and the adjusting of operating condition;
(2) the reasonably combined adjustable extent of scraper plate transporting velocity and air dense medium sorting condition has limited the production intensity of this sorting unit;
(3) mechanical wear in the equipment of scraper plate machine and the running thereof increases screening installation complex structure and cost.
The purpose of this utility model is to develop a kind of floating thing and separates the reverse shunting air dense medium of easy vibration separator with hypostasis.
Described separator is made up of raw material and dense media inlet, floating thing and dense media outlet, hypostasis and dense media outlet, ash-laden gas outlet, many air chambers distributor, air intake and fluid bed, it is characterized in that the outlet of described floating thing and dense media outlet and hypostasis and dense media is respectively equipped with plate washer, be used for regulating the fluidized-bed layer height, and make hypostasis and the dense media can be from the stable discharge of an end.Described fluid bed has vibrator, can form the air dense medium fluid bed of the oscillatory type with certain gradient.The distribution grid of described fluid bed can be the multihole distributor that many air chambers, multilayer are weaved cotton cloth.Described fluid bed can be the rectangle slot type, can carry out a plurality of parallel combinations, produces load so that increase.
Principle schematic of the present utility model is as shown in Figure 2: 1 is inlet, 2 medium inlets of attaching most importance to, 3 are the ash-laden gas outlet, 5 are floating thing and dense media outlet, and 6 is distribuor of fluidized bed, and 7 is gas diffluence room, 8 is total air intake, 9 is rectangle slot type air dense medium partition fluidized bed, and 11 is hypostasis and dense media outlet, and 12 is vibrator.
The solid mixture material adds from top, the middle part charge door 1 that is positioned at rectangle slot type partition fluidized bed 9, air sprays into through distribution grid 6, the dense media particulate disperses in air-flow and suspends, form the fluidized-bed layer of the homogeneous density of similar liquid state, less floating the formation thereon of solid of proportion floats thing in the raw material, moving right exports 5 places to floating thing and dense media and discharges, and the solid that proportion is bigger in the raw material sinks to it and forms hypostasis down and be moved to the left, to hypostasis and dense media outlet 11 discharges.Vibrator in the fluid bed plays the effect of the reverse shunting of vibration.
The advantage that the utility model " vibrates reverse shunting " is conspicuous:
1. the introducing of vibrational energy helps the fragmentation of bubble in the air dense medium fluid bed and the evenly formation of suspension density, and opereating specification is widened, and handles the intensity increase, thereby more helps the efficient separation of granulate mixture.
2. hypostasis is discharged to an end by vibration great-jump-forward ground in air dense medium fluid bed bottom, and causes the reverse convective motion of floating thing, need not machinery to carry, thereby makes equipment simple, and processing ease and cost reduce.
The utility model can be used for real processes such as ore dressing, coal separation, the processing of industrial solid waste residue, industrial residue mixture with the processing Taiyuan Chemical Fertilizer Factory is an example, processing through the utility model air dense medium separator that " vibrates reverse shunting ", cinder mixture to two kinds of thickness granularities all can be separated fully, and detailed results is listed in table 1.
Table 1: industrial cinder mixture separation results
Cinder mixture (coke content 10-30%) After the separation
Heavy (the Kg/m of coke ratio 3) Heavy (the Kg/m of slag ratio 3) Coke content % in the slag
Coarseness 50-13mm 1778 2661 <5%
Fine granularity 13-3mm 1771 2148 <5%
Jiao after the separation, wherein dregginess<5% can be used to gas making and does other fuel use; Cinder after the separation, wherein coke content all<5% can be made ground and the building materials of paving the way.Be not difficult to find out that the utility model has obvious social, environmental benefit and economic benefit for solving cinder separation utilization and reducing problem of environmental pollution and opened up a new way.
The utility model can be widely used in the efficient separation process of multiple solid mixture, simple, the processing ease of equipment, and small investment, cost is low, floor space is little, more need not water, and very strong prospects for commercial application and huge market competition potentiality are arranged.

Claims (4)

1. one kind is vibrated reverse shunting air dense medium separator, formed by air intake, feed(raw material)inlet, dense media inlet, floating thing and dense media outlet, ash-laden gas outlet, many air chambers distribution grid and fluid bed, be it is characterized in that described fluid bed has vibrator.
2. separator as claimed in claim 1 is characterized in that floating thing and dense media outlet and hypostasis and dense media outlet are respectively equipped with the plate washer of adjustment height.
3. separator as claimed in claim 1 or 2 is characterized in that described fluid bed is that the rectangle slot type also can a plurality of parallel combinations.
4. separator as claimed in claim 3, the distribution grid that it is characterized in that described flow point bed are that multilayer is weaved cotton cloth.
CN 94221391 1994-09-22 1994-09-22 Vibration reverse divided type air heavy-media separator Expired - Fee Related CN2234315Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 94221391 CN2234315Y (en) 1994-09-22 1994-09-22 Vibration reverse divided type air heavy-media separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 94221391 CN2234315Y (en) 1994-09-22 1994-09-22 Vibration reverse divided type air heavy-media separator

Publications (1)

Publication Number Publication Date
CN2234315Y true CN2234315Y (en) 1996-09-04

Family

ID=33835705

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 94221391 Expired - Fee Related CN2234315Y (en) 1994-09-22 1994-09-22 Vibration reverse divided type air heavy-media separator

Country Status (1)

Country Link
CN (1) CN2234315Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104043519A (en) * 2014-06-18 2014-09-17 孙玉平 Internal-lift-type conical heavy medium separator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104043519A (en) * 2014-06-18 2014-09-17 孙玉平 Internal-lift-type conical heavy medium separator

Similar Documents

Publication Publication Date Title
CN110328140B (en) Method for improving fluidization quality and separation density stability of particles and matched device
CN105289985A (en) Full-fraction dry method separation clean technology and method for coal
CN205110130U (en) Clean system is selected separately to coal wholegrain level dry process
WO2020098707A1 (en) Air dry sand coal sorting system
CN105536974A (en) Dry-method sand manufacturing system
CN211838464U (en) Segmentation dry-type magnetic separation device for powdery magnetic materials
CN104475231A (en) Dry method dense medium separation bed
CN101318182A (en) Modular coal preparation process and equipment based on gas-solid diphasic stream
CN105381950A (en) Large dry dense medium fluidized bed separation machine and separation system
CN108465563B (en) Dry sorting device and method for solid materials
CN105834011B (en) Flotation column intensified sorting device and method for separating with filling-material structure
CN107185830A (en) It is a kind of to fluidize bed dry coal dressing machine from medium gas-particle two-phase
CN2234315Y (en) Vibration reverse divided type air heavy-media separator
CN1597147A (en) Dry grading method of powdered coal and its equipment
CN214809557U (en) Multi-point position dust collecting and removing system of ceramic tile production line
CN213792827U (en) Novel gas-solid fluidized bed sorting device
CN201263935Y (en) Ash bucket
CN207600146U (en) A kind of wet-discharged coal ash suspended state cycle drying and separation system
CN87101056A (en) The dressing coal with dry fluidized bed method and apparatus
CN207805980U (en) A kind of medium recovery device from the gas-solid fluidized bed coal picker of medium
CN110801936B (en) Sectional dry magnetic separation device for powdery magnetic materials and application method of sectional dry magnetic separation device
CN110465403A (en) A kind of three phase fluidized bed mineral grain sorting unit
CN202605937U (en) System for reducing discharge of ultrafine particles in ash-laden gas
CN214916989U (en) Quartz tailing sand-mud separation device
CN209138255U (en) A kind of dust pelletizing system of efficient thermal insulation material

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