CN205218056U - System for be used for handling oiliness metal powder - Google Patents
System for be used for handling oiliness metal powder Download PDFInfo
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- CN205218056U CN205218056U CN201521023825.1U CN201521023825U CN205218056U CN 205218056 U CN205218056 U CN 205218056U CN 201521023825 U CN201521023825 U CN 201521023825U CN 205218056 U CN205218056 U CN 205218056U
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- 239000002184 metal Substances 0.000 title claims abstract description 65
- 239000000843 powder Substances 0.000 title abstract description 17
- 239000000463 material Substances 0.000 claims abstract description 72
- 239000013527 degreasing agent Substances 0.000 claims abstract description 10
- 239000000428 dust Substances 0.000 claims description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 239000004744 fabric Substances 0.000 claims description 39
- 238000007599 discharging Methods 0.000 claims description 30
- 239000006148 magnetic separator Substances 0.000 claims description 28
- 238000002156 mixing Methods 0.000 claims description 15
- 229910000831 Steel Inorganic materials 0.000 claims description 13
- 239000010959 steel Substances 0.000 claims description 13
- 238000005406 washing Methods 0.000 claims description 12
- 238000004513 sizing Methods 0.000 claims description 10
- 239000011230 binding agent Substances 0.000 claims description 4
- -1 remove emergy device Substances 0.000 claims 1
- 239000000919 ceramic Substances 0.000 abstract description 25
- 239000012528 membrane Substances 0.000 abstract description 25
- 239000007788 liquid Substances 0.000 abstract description 20
- 239000002699 waste material Substances 0.000 abstract description 10
- 238000000926 separation method Methods 0.000 abstract description 9
- 229910052593 corundum Inorganic materials 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 abstract description 3
- 239000004576 sand Substances 0.000 abstract description 3
- 239000010431 corundum Substances 0.000 abstract 2
- 239000003921 oil Substances 0.000 description 53
- 239000012530 fluid Substances 0.000 description 34
- 238000000034 method Methods 0.000 description 29
- 238000004140 cleaning Methods 0.000 description 22
- 238000000227 grinding Methods 0.000 description 19
- 239000010808 liquid waste Substances 0.000 description 7
- 238000001914 filtration Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000012216 screening Methods 0.000 description 5
- 239000000839 emulsion Substances 0.000 description 4
- 238000007667 floating Methods 0.000 description 4
- 238000007885 magnetic separation Methods 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005453 pelletization Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 238000007873 sieving Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002569 water oil cream Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000010734 process oil Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000004506 ultrasonic cleaning Methods 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
- Centrifugal Separators (AREA)
Abstract
The utility model relates to a system for be used for handling oiliness metal powder. Include the degreaser, remove pulverized corundum device and waste liquid treatment device, the degreaser includes automatic feed centrifugal separator and ultrasonic wave stirred tank, go the pulverized corundum device to include wet -type rotary screen and full magnet separator against the current, waste liquid treatment device is ceramic membrane filter equipment. The utility model discloses metal powder is effectual for the separation oiliness, and the oil content in the metal powder oiliness material after the processing drops 0.5 percent to, and the impurity such as beautiful sand among the oiliness metal powder drop 0.5 percent to. Degree of automation is high, and is with low costs, reduces environmental pollution, and the resource is recycled.
Description
Technical field
The utility model belongs to the technical field of process oil-containing metal dust, is specifically related to a kind of system for the treatment of oil-containing metal dust.
Background technology
Usually containing the impurity such as oil plant and emergy in metal dust, if do not processed, subsequent technique process can be affected, and reduce metal dust quality.Some waste liquids can be produced in process metal dust process, need to process, otherwise pollute the environment.
Existing separating metal powder has following three kinds with the method for oil: first method is for artificial reinforced in centrifuge housing, and fluid gets rid of to cavity pocket of outer cover through filter bag gap and drum wall aperture, and fluid is discharged by outage.Second method is heating means, and be placed in a large still by metal dust and oil plant and add water, electricity consumption or other mode of heatings heat it, and oil gently can swim on water surface, come separating oil and metal dust.The third method is lighted by the metal dust containing oil plant, burns the rear Footwall drift powder of oil.There is contaminated environment in above three kinds of methods, metal recovery rate is low, and wastes time and energy, and working strength is high, cannot realize automated production, and oil plant is separated not thorough.
The method of existing separating metal powder and emergy has following three kinds: the first is after sieve is put into water, manually rocks sieve and screens; The second adopts Wet oscillating screen, and the material that sieve is put into sieve, opens vibratory sieve.Above two kinds of methods, waste time and energy, working strength is high, automaticity is low, and sieving rate are extremely low.The third is Magnetic Separation Technology: when direct magnetic separator is separated, and the powder of this part pelletizing shape is separated owing to presenting magnetic pelletizing, thus affects the impurity content of grinding metal dust, does not far reach impure standard volume.
Can produce some waste liquids in process metal dust process, as scrapped cleaning fluid, water surface has micro-oil slick, oil-water emulsion.If these liquid do not process, only excluding of can not re-using aborning, just pollute the environment if drained, this is unallowed, but absorption method, the precipitation method, the method major parts such as neutralisation and diatomite process are disposable, can not Reusability, inapplicable with this production process.
Summary of the invention
In view of the defect that prior art exists, the utility model provides a kind of system for the treatment of oil-containing metal dust, improves metal dust quality, reduces environmental pollution, improve the object for the treatment of effeciency to reach.
For achieving the above object, the technical scheme that the utility model adopts is a kind of system for the treatment of oil-containing metal dust, and it comprises degreaser, removes emergy device and liquid waste treating apparatus; Degreaser comprises Automatic-feeding centrifuge and ultrasonic wave stirred tank; Emergy device is gone to comprise wet type rotary screen and full counter-current magnetic separator; Liquid waste treating apparatus is ceramic membrane filter device.Ultrasonic wave stirred tank, wet type rotary screen and full counter-current magnetic separator is connected successively according to technological process after centrifuge.
Described Automatic-feeding centrifuge comprises centrifuge housing, feed pipe, centrifuge shurry pump, centrifuge paddle, tank of sizing mixing, buncher, pipette and suction pumps, feed pipe one end extend in centrifuge housing, the feed pipe other end is connected with centrifuge shurry pump, centrifuge shurry pump is connected with tank of sizing mixing, centrifuge paddle is arranged in tank of sizing mixing, and centrifuge paddle upper end connects buncher; Pipette one end extend in centrifuge housing, and the pipette other end connects suction pumps.
Described ultrasonic wave stirred tank comprises the frequency modulation motor of ultrasonic wave stirred tank, ultrasonator, shaft, paddle, ultrasonic equipment tank body, recoil tube, shurry pump, filter washing water inlet and material inlet; Ultrasonic equipment tank body stretches into a shaft, shaft upper end is provided with the frequency modulation motor of ultrasonic wave stirred tank, shaft lower end is provided with paddle, ultrasonic equipment tank body lower part binder stock pump, shurry pump connects discharge pipe, ultrasonic equipment tank body top is provided with filter washing water inlet and material inlet, evenly installs six ultrasonators around ultrasonic equipment tank body.
Described ceramic membrane separation device is applied to the filtration of used wiping solution, emulsion and the floating oil-water fluid produced in Automatic-feeding centrifuge and ultrasonic wave stirred tank, and ceramic membrane filter device comprises multistage pump, fluid reservoir, purpose ceramic-film filter, circulation line, goes out clear liquid mouth and fluid reservoir charging aperture; Described fluid reservoir, multistage pump, purpose ceramic-film filter connect into closed circuit by circulation line successively, fluid reservoir is provided with fluid reservoir charging aperture, purpose ceramic-film filter is provided with out clear liquid mouth, purpose ceramic-film filter is provided with ceramic membrane, the micropore of 50 ~ 80 nanometers that ceramic membrane tube wall gathers.
Described wet type rotary screen comprises screen cloth, sieve main frame square steel frame, material screen discharging collecting box, frequency modulation motor, sift out material and collect agitator tank and sieve charging collection agitator tank, screen cloth is arranged on above sieve main frame square steel frame, in sieve main frame square steel frame, material screen discharging collecting box is set, screen cloth is horizontal cylinder shape, screen cloth connects frequency modulation motor, frequency modulation motor drives screen cloth to rotate, at screen cloth feed end and material screen discharging collecting box side arrange sieve charging collect agitator tank, arrange in any in addition side of material screen discharging collecting box and sift out material collection agitator tank, water is added in material screen discharging collecting box inside, screen cloth rotates in water, described material screen discharging collecting box inside arranges inclined-plane, and material screen discharging slips into along inclined-plane sifts out material collection agitator tank.
Described wet type rotary screen and full counter-current magnetic separator arrange as a whole.
System work process:
The process of deoiling be divided into once deoil and secondary deoil.
Once deoil: what oil and oil-containing metal powder in certain ratio were added to Automatic-feeding centrifuge sizes mixing in tank, after regulating, ratio is that oil accounts for 35 ~ 55%, and metal dust accounts for 65 ~ 45%, is stirred by paddle, make oil and metal dust Homogeneous phase mixing, have certain mobility.The slurry that this method adjusts is placed and also can not be precipitated for 12 hours, is convenient to the conveying of centrifuge shurry pump.The oil-containing metal dust regulated; be transported in the device of the separation oil-containing metal dust of certain rotating speed (rotating speed about 200 revs/min) with shurry pump; rotary drum rotating speed is 2300 ~ 3000 revs/min, starts oil plant and is separated, during shutdown; metal dust can be close on drum inner wall cloth bag; unnecessary oil is just separated, and oil accumulates in centrifuge housing bottom of the drum in cloth bag, and pipette is advanced oil reservoir position by propeller under compressed air effect; by pipette by oily sucking-off, reach separation object.In the remaining oil-containing metal dust be attached on drum inner wall cloth bag, add water, furnishing slip, the volume adding water is greater than the volume of oil, and centrifuge shell intracoelomic cavity rotary drum when rotated, can keep apart by water by oil and metal dust.When rotary drum stops operating, the grinding metal dust in centrifuge housing is close on drum inner wall cloth bag, and water and replaced oil out amass in bottom of the drum, reach separation object.Afterwards by twice propelling of pipette, first by oily sucking-off, then by water sucking-off.
Secondary deoils: the inwall cloth bag taking out Automatic-feeding centrifuge with crane, wherein grinding metal dust is slowly sent in ultrasonic equipment tank body by the material inlet of ultrasonic wave stirred tank, simultaneously, cleaning liquid is squeezed in ultrasonic equipment tank body from filter washing water inlet, the frequency modulation motor opening ultrasonic wave stirred tank makes shaft drive frame type agitating blade slow circumvolve, open ultrasonator, frequency modulation is carried out to the frequency modulation motor of ultrasonic wave stirred tank, the frequency modulation motor faster rotational speed of ultrasonic wave stirred tank, substrate material is uniformly distributed to be suspended in cleaning liquid, grinding metal dust carries out comprehensive cleaning under being repeatedly reversed in washing agent and ultrasonator effect under paddle effect in cleaning fluid again.Scavenging period is how many depending on substrate material.Cleaned material is squeezed in centrifuge by the shurry pump of ultrasonic wave stirred tank, the micro oil metal dust that contains after deoiling is separated with cleaning fluid.
Go emergy process:
Agitator tank is collected in the sieve charging of inserting wet type rotary screen through the isolated metal dust (metal dust containing 0.5% oil) containing micro oil of centrifuge, the water collected in agitator tank with the sieve charging of wet type rotary screen stirs, under the effect of pump, material enters screen cloth by sieving charging collection agitator tank, screen cloth is rotated in water, rotating speed is 15 ~ 20 revs/min and is with certain angle of inclination (2 ~ 5 °), the material that sifts out sieved falls into material screen discharging collecting box, automatically slipped into by the inclined-plane of material screen discharging collecting box and sift out material collection agitator tank, enter full counter-current magnetic separator by the material sifting out the outflow of material collection agitator tank and carry out magnetic separation, by the discharging of magnetic separator discharge nozzle.
Waste treatment process:
The waste liquid (used wiping solution, the emulsion that produce in process of deoiling, floating oil-water fluid) enter in ceramic membrane separation device fluid reservoir, through circulation line, waste liquid is squeezed into purpose ceramic-film filter by multistage pump, by certain pressure effect micromolecular water permeation ceramic membrane by filtering, being passed through clear liquid mouth by the water of filtering enters on production line, does not have the liquid of permeation ceramic membrane to get back to again in fluid reservoir and continues circulating filtration.
The beneficial effects of the utility model:
Utilize Automatic-feeding centrifuge, equipment operating is easy, cost is low, can Automatic-feeding, reduce use manpower, working strength is low, automaticity is high, it is effective to be separated oil-containing metal dust, the metal dust after process is down to 1.2% containing the oil content in oil plant.
Ultrasonic wave stirred tank, is applied to cleaning oil-containing grinding metal dust field when being differed greatly by the oil-containing grinding metal dust density of cleaning and fluid density, still can realizes without dead angle high-efficiency washing by ultrasonic equipment.Clean the metal dust by the oil content about 1.2% of Automatic-feeding centrifuge, the grinding metal dust oil content after cleaning is 0.5%.The bottommost of bottom segment is provided with shutdown recoiling device, enters subsequent processing, without the need to labor cleaning with shurry pump by by the oil-containing grinding metal dust cleaned.This equipment is circular vertical body, and floor space is reasonable, and manual operation is convenient, and a people can operate several this kind of equipment, and operating efficiency is high, can use continuously and also can intermittently use.
Six pieces of ultrasonators are evenly distributed on cylinder periphery, and the wave of oscillation that oscillator produces interts with netted intersection, and ultrasonic wave can act on every by the grinding metal powder granulates washed on the surface, reaches cleaning performance.Adopt drum type brake ultrasonic cleaning design concept, production capacity and maximum unit output can be improved like this.Adopt speed changing type driven by motor paddle to stir and cleaned to obtain grinding metal powder material, grinding metal powder material particle is repeatedly reversed in cleaning fluid, the energy that ultrasonator produces can excessively comprehensively act on the surface of each particle, reaches the object of cleaning.
Adopt transport pump and pump grinding metal dust material, production capacity, convenient operation and automated production can be improved like this.Cleaned grinding metal powder material pump can be pumped out to subsequent processing (entering centrifuge) together with cleaning fluid, reach the object except material.
Wet type rotary screen and full counter-current magnetic separator arrange as a whole, emergy powder is nonmagnetic and the magnetic principle of grinding metal dust, and wet type rotary screen is combined with full counter-current magnetic separator, realize automation screening and magnetic separation, and emergy content in oil-containing grinding metal dust directly can be reduced to 0.5% by 3.5%, reach the standard volume that grinding metal dust is impure.Achieve automation screening and magnetic separation, cost low and easy and simple to handle, reduce working strength, use manpower and material resources sparingly, cleaning screen spray group is set, can automatically cleans, without the need to manual cleaning.
Adopt ceramic membrane filter device, effectively environmental protect, accomplish without discharge, or micro-discharge, improve huge liquid waste treatment system, reduce the consumption reducing water.Take up an area few, practicable unattended.By used cleaning fluid by ceramic membrane filter, cleaner liquid can reclaim and reuse.The removing of oil-water emulsion and water surface oil film, can make water after treatment reuse, and reaches the object without discharge or micro-discharge.The utility model utilizes ceramic membrane to be namely acidproofly have alkaline-resisting alundum (Al2O3) material to make, the aperture of ceramic membrane can be selected, select suitable ceramic membrane aperture 50 to 80 nanoscale, facility compact, floor space is little, and can realize automation mechanized operation, keep an eye on without special messenger, cost is low, can Reusability, long service life.
Oil-containing metal dust oil content can be down to 0.5% by 15% by a kind of system for the treatment of oil-containing metal dust, wherein emergy amount will be down to 0.5% by 3.5%, and the used wiping solution, emulsion and the floating oil-water fluid that produce in process separating metal powder oil-containing powder process are carried out circulating filtration process, reach and improve metal dust quality, reduce the object of environmental pollution.
Accompanying drawing explanation
Fig. 1 is the structural representation of utility model;
Fig. 2 is the structural representation of Automatic-feeding centrifuge;
Fig. 3 is the pipette oil suction state partial schematic diagram of Automatic-feeding centrifuge;
Fig. 4 is the pipette water suction state partial schematic diagram of Automatic-feeding centrifuge;
Fig. 5 is ultrasonic wave stirred tank schematic diagram;
Fig. 6 be wet type rotary screen and full counter-current magnetic separator as a whole time front view;
Fig. 7 be wet type rotary screen and full counter-current magnetic separator as a whole time top view;
Fig. 8 be wet type rotary screen and full counter-current magnetic separator as a whole time side view;
Fig. 9 is the structural representation of ceramic membrane filter device;
In figure: 1, Automatic-feeding centrifuge, 1.1, drum inner wall, 1.2, metal dust, 1.3, the oil separated, 1.4, water, 1.5, centrifuge shurry pump, 1.6, centrifuge paddle, 1.7, buncher, 1.8, to size mixing tank, 1.9, slip, 1.10, pipette, 1.11, suction pumps, 1.12, feed pipe, 2, ultrasonic wave stirred tank, 2.1, the frequency modulation motor of ultrasonic wave stirred tank, 2.2, ultrasonator, 2.3, shaft, 2.4, paddle, 2.5, ultrasonic equipment tank body, 2.6, substrate material and cleaning fluid, 2.7, recoil tube, 2.8, shurry pump, 2.9, discharge pipe, 2.10, filter washing water inlet, 2.11, material inlet, 3, centrifuge, 4, wet type rotary screen, 4.1, screen cloth, 4.2, sieve main frame square steel frame, 4.3, material screen discharging collecting box, 4.4, frequency modulation motor, 4.5, sift out material and collect agitator tank, 4.6, agitator tank is collected in sieve charging, 4.7, cleaning screen spray group, 4.8, magnetic separator discharge nozzle, 4.9, inclined-plane, 5, full counter-current centrifuge, 6, ceramic membrane separation device, 6.1, multistage pump, 6.2, fluid reservoir, 6.3, purpose ceramic-film filter, 6.4, circulation line, 6.5, go out clear liquid mouth, 6.6, sewage draining exit, 6.7, fluid reservoir charging aperture, 7, oil water separator.
Detailed description of the invention
Embodiment 1
For the treatment of a system for oil-containing metal dust, it comprises degreaser, removes emergy device and liquid waste treating apparatus; Degreaser comprises Automatic-feeding centrifuge 1 and ultrasonic wave stirred tank 2; Beautiful sand device is gone to comprise wet type rotary screen 4 and full counter-current magnetic separator 5; Liquid waste treating apparatus is ceramic membrane filter device 6.
Automatic-feeding centrifuge, comprise centrifuge housing, feed pipe 1.12, centrifuge shurry pump 1.5, centrifuge paddle 1.6, size mixing tank 1.8 and buncher 1.7, feed pipe 1.12 one end extend in centrifuge housing, feed pipe 1.12 other end is connected with centrifuge shurry pump 1.5, centrifuge shurry pump 1.5 is connected with tank 1.8 of sizing mixing, centrifuge paddle 1.6 is arranged in tank 1.8 of sizing mixing, and centrifuge paddle 1.6 upper end connects buncher 1.7.Also comprise pipette 1.10 and suction pumps 1.11, pipette 1.10 one end extend in centrifuge housing, and pipette 1.10 other end connects suction pumps 1.11.
Ultrasonic wave stirred tank 2 comprises the frequency modulation motor 2.1 of ultrasonic wave stirred tank, ultrasonator 2.2, shaft 2.3, paddle 2.4, ultrasonic equipment tank body 2.5, recoil tube 2.7, shurry pump 2.8, filter washing water inlet 2.10 and material inlet 2.11; Ultrasonic equipment tank body 2.5 stretches into a shaft 2.3, shaft 2.3 upper end is provided with the frequency modulation motor 2.1 of ultrasonic wave stirred tank, shaft 2.3 lower end is provided with paddle 2.4, ultrasonic equipment tank body 2.5 bottom binder stock pump 2.8, shurry pump 2.8 connects discharge pipe 2.9, ultrasonic equipment tank body top is provided with filter washing water inlet 2.10 and material inlet 2.11, evenly installs six ultrasonators 2.2 around ultrasonic equipment tank body 2.5.
Ceramic membrane separation device is applied to the filtration of used wiping solution, emulsion and the floating oil-water fluid produced in Automatic-feeding centrifuge 1 and ultrasonic wave stirred tank 2.Ceramic membrane filter device 6 comprises multistage pump 6.1, fluid reservoir 6.2, purpose ceramic-film filter 6.3, circulation line 6.4, goes out clear liquid mouth 6.5 and fluid reservoir charging aperture 6.7; Described fluid reservoir 6.2, multistage pump 6.1 and purpose ceramic-film filter 6.3 connect into closed circuit by circulation line 6.4 successively, fluid reservoir 6.2 are provided with fluid reservoir charging aperture 6.7, purpose ceramic-film filter 6.3 are provided with out clear liquid mouth 6.5.Purpose ceramic-film filter 6.3 is provided with ceramic membrane, the micropore of 50 ~ 80 nanometers that ceramic membrane tube wall gathers.
Wet type rotary screen 4 comprises screen cloth 4.1, sieve main frame square steel frame 4.2, material screen discharging collecting box 4.3, frequency modulation motor 4.4, sift out material and collect agitator tank 4.5 and sieve charging collection agitator tank 4.6, screen cloth 4.1 is arranged on above sieve main frame square steel frame 4.2, in sieve main frame square steel frame 4.2, material screen discharging collecting box 4.3 is set, screen cloth 4.1 is horizontal cylinder shape, screen cloth 4.1 connects frequency modulation motor 4.4, frequency modulation motor 4.4 drives screen cloth 4.1 to rotate, at screen cloth 4.1 feed end and material screen discharging collecting box 4.3 side arrange sieve charging collect agitator tank 4.6, arrange in any in addition side of material screen discharging collecting box 4.3 and sift out material collection agitator tank 4.5, water is added in material screen discharging collecting box 4.3 inside, screen cloth 4.1 rotates in water.Material screen discharging collecting box 4.3 inside arranges inclined-plane 4.9, and material screen discharging slips into along inclined-plane sifts out material collection agitator tank 4.5.
Full counter-current magnetic separator 5 is counter-current magnetic separator, and it is connected with wet type rotary screen 4.
Embodiment 2
For the treatment of a system for oil-containing metal dust, it comprises degreaser, removes emergy device and liquid waste treating apparatus; Degreaser comprises Automatic-feeding centrifuge 1 and ultrasonic wave stirred tank 2; Go beautiful sand device to comprise wet type rotary screen 4 and full counter-current magnetic separator 5(wet type rotary screen 4 and full counter-current magnetic separator 5 and be set to one, also known as screening magnetic separator); Liquid waste treating apparatus is ceramic membrane filter device 6.
Automatic-feeding centrifuge, comprise centrifuge housing, feed pipe 1.12, centrifuge shurry pump 1.5, centrifuge paddle 1.6, size mixing tank 1.8 and buncher 1.7, feed pipe 1.12 one end extend in centrifuge housing, feed pipe 1.12 other end is connected with centrifuge shurry pump 1.5, centrifuge shurry pump 1.5 is connected with tank 1.8 of sizing mixing, centrifuge paddle 1.6 is arranged in tank 1.8 of sizing mixing, and centrifuge paddle 1.6 upper end connects buncher 1.7.Also comprise pipette 1.10 and suction pumps 1.11, pipette 1.10 one end extend in centrifuge housing, and pipette 1.10 other end connects suction pumps 1.11.Arrange cloth bag in centrifuge housing, oil-containing metal dust loads in cloth bag, is separated.The rotary drum of centrifuge housing is vertical.
For cleaning the ultrasonic wave stirred tank of oil-containing grinding metal dust, it comprises the frequency modulation motor 2.1 of ultrasonic wave stirred tank, ultrasonator 2.2, shaft 2.3, paddle 2.4, ultrasonic equipment tank body 2.5, recoil tube 2.7, shurry pump 2.8, filter washing water inlet 2.10 and material inlet 2.11; Ultrasonic equipment tank body 2.5 stretches into a shaft 2.3, shaft 2.3 upper end is provided with the frequency modulation motor 2.1 of ultrasonic wave stirred tank, shaft 2.3 lower end is provided with paddle 2.4, ultrasonic equipment tank body 2.5 bottom binder stock pump 2.8, shurry pump 2.8 connects discharge pipe 2.9, ultrasonic equipment tank body 2.5 top is provided with filter washing water inlet 2.10 and material inlet 2.11, evenly installs six ultrasonators 2.2 around ultrasonic equipment tank body 2.5, and ultrasonator 2.2 angle that distributes is 60 °.Described ultrasonic equipment tank body 2.5 is bottoms is hemispheric cylindrical structure.
Described paddle 2.4 rotating speed is enough to the oil-containing grinding metal dust by cleaning is suspended.
Described paddle 2.4 adopts frame type agitating blade.
Recoil tube 2.7 is provided with bottom described ultrasonic equipment tank body 2.5.
For the screening magnetic separator of oil-containing grinding metal dust, it is that wet type rotary screen and full counter-current magnetic separator arrange as a whole situation.It comprises screen cloth 4.1, sieve main frame square steel frame 4.2, material screen discharging collecting box 4.3, frequency modulation motor 4.4, sifts out material collection agitator tank 4.6, sieve charging collection agitator tank 4.6, full counter-current magnetic separator 5, magnetic separator discharge nozzle 4.8; Screen cloth 4.1 is placed on described sieve main frame square steel frame 4.2 top, material screen discharging collecting box 4.3 is placed in sieve main frame square steel frame 4.2 bottom, material screen discharging collecting box 4.3 side is arranged sifts out material collection agitator tank 4.5, described screen cloth 1 arranges frequency modulation motor 4.4, and the feed end of screen cloth 1 arranges sieve charging and collects agitator tank 4.6; The described material collection agitator tank 4.5 that sifts out connects full counter-current magnetic separator 5, and full counter-current magnetic separator 5 arranges magnetic separator discharge nozzle 4.8.Described material screen discharging collecting box 3 inside arranges inverted trapezoidal inclined-plane 4.8, and material screen discharging can slip into automatically along inclined-plane 4.9 sifts out material collection agitator tank 4.6.Described screen cloth 4.1 side arranges cleaning screen spray group 4.7.
Sifting out material collection agitator tank 4.5 arranges as a whole with full counter-current magnetic separator 5.
Preferred screen cloth 4.1 is drum-type, and frequency modulation motor 4.5 drives screen cloth 4.1 to rotate, and the screening of screen cloth 4.1 is carried out in water.
For the ceramic membrane separation device that waste liquid circulation filters, it comprises multistage pump 6.1, fluid reservoir 6.2, purpose ceramic-film filter 6.3, circulation line 6.4, goes out clear liquid mouth 6.5 and fluid reservoir charging aperture 6.7; Described fluid reservoir 6.2, multistage pump 6.1 and purpose ceramic-film filter 6.3 connect into closed circuit by circulation line 6.4 successively, fluid reservoir 6.2 is provided with fluid reservoir charging aperture 6.7, purpose ceramic-film filter 6.1 is provided with out clear liquid mouth 6.5, the circulation line between purpose ceramic-film filter 6.3 and fluid reservoir 6.2 is arranged sewage draining exit 6.6.Described purpose ceramic-film filter 6.3 is provided with ceramic membrane, and ceramic membrane tube wall gathers micropore.The hole of described micropore is in 50 ~ 80 nanometers.
Claims (3)
1. for the treatment of a system for oil-containing metal dust, it is characterized in that: comprise degreaser, remove emergy device, degreaser comprises Automatic-feeding centrifuge and ultrasonic wave stirred tank, emergy device is gone to comprise wet type rotary screen and full counter-current magnetic separator, described Automatic-feeding centrifuge comprises centrifuge housing, feed pipe, centrifuge shurry pump, centrifuge paddle, tank of sizing mixing, buncher, pipette and suction pumps, feed pipe one end extend in centrifuge housing, the feed pipe other end is connected with centrifuge shurry pump, centrifuge shurry pump is connected with tank of sizing mixing, centrifuge paddle is arranged in tank of sizing mixing, centrifuge paddle upper end connects buncher, pipette one end extend in centrifuge housing, and the pipette other end connects suction pumps, ultrasonic wave stirred tank comprises the frequency modulation motor of ultrasonic wave stirred tank, ultrasonator, shaft, paddle, ultrasonic equipment tank body, recoil tube, shurry pump, filter washing water inlet and material inlet, ultrasonic equipment tank body stretches into a shaft, shaft upper end is provided with the frequency modulation motor of ultrasonic wave stirred tank, shaft lower end is provided with paddle, ultrasonic equipment tank body lower part binder stock pump, shurry pump connects discharge pipe, ultrasonic equipment tank body top is provided with filter washing water inlet and material inlet, evenly installs six ultrasonators around ultrasonic equipment tank body, described wet type rotary screen comprises screen cloth, sieve main frame square steel frame, material screen discharging collecting box, frequency modulation motor, sift out material and collect agitator tank and sieve charging collection agitator tank, screen cloth is arranged on above sieve main frame square steel frame, in sieve main frame square steel frame, material screen discharging collecting box is set, screen cloth is horizontal cylinder shape, screen cloth connects frequency modulation motor, frequency modulation motor drives screen cloth to rotate, at screen cloth feed end and material screen discharging collecting box side arrange sieve charging collect agitator tank, arrange in any in addition side of material screen discharging collecting box and sift out material collection agitator tank, water is added in material screen discharging collecting box inside, screen cloth rotates in water.
2. a kind of system for the treatment of oil-containing metal dust according to claim 1, is characterized in that: described material screen discharging collecting box inside arranges inclined-plane, and material screen discharging slips into along inclined-plane sifts out material collection agitator tank.
3. a kind of system for the treatment of oil-containing metal dust according to claim 2, is characterized in that: described wet type rotary screen and full counter-current magnetic separator arrange as a whole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521023825.1U CN205218056U (en) | 2015-12-11 | 2015-12-11 | System for be used for handling oiliness metal powder |
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| CN201521023825.1U CN205218056U (en) | 2015-12-11 | 2015-12-11 | System for be used for handling oiliness metal powder |
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