CN204891498U - Powder collector of aerial fog powder manufacturing apparatus - Google Patents
Powder collector of aerial fog powder manufacturing apparatus Download PDFInfo
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- CN204891498U CN204891498U CN201520144347.3U CN201520144347U CN204891498U CN 204891498 U CN204891498 U CN 204891498U CN 201520144347 U CN201520144347 U CN 201520144347U CN 204891498 U CN204891498 U CN 204891498U
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- collection
- sump
- ball
- transition
- collection unit
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Abstract
The utility model relates to a powder collector of aerial fog powder manufacturing apparatus, it includes pipe connection portion, one collection, two ones collections, filter house, dewatering portion and air exhauster, it includes one transition, collection portion and passes through two ones to collect one, the inside of collection portion includes collection portion water inlet, one in sump, infiltration membrane, ball and suspension, and it is the same to collect two structures with collection portion, and during the use, the gas that is mixing with the powder carries out collection first time through the collection portion in one of collecting, carries out the collection second time through collecting two ones, carries out the collection third time through the filter screen in the filter house, is provided with super absorbent resin in the dewatering portion for get into the air current keep dry of hair -dryer. The utility model discloses simple structure, it is with low costs, with the powder process in -process, the farine of departure on the pipeline, through tertiary collection device, effective collection is got up.
Description
Technical field
The utility model relates to powder collecting device, is specifically related to a kind of powder collector of gas-atomized powder equipment.
Background technology
Gas-atomized powder has that powder sphericity is high, oxygen content is low and the advantage such as cooldown rate is large.Through for many years constantly bring forth new ideas and perfect, gas-atomized powder technology has developed into the main method of producing high-performance metal and alloy powder, but some superfines in the process of powder process, along with high velocity air flies out along pipeline, if do not processed, one is to environment, two is waste material, so must be reclaimed, because the particle diameter of superfines is very little, the particle of a small amount of nanoscale in fine powder, is even had to exist, so the how current most complex structure of powder collecting device, cost is high, and is difficult to superfines to be collected completely.
Summary of the invention
Technical problem to be solved in the utility model is to provide a kind of in pulverizing process, and the fine powder that can collection conduit fly out, by three grades of gathering-devices, effectively collects the low cost of superfines, the powder collector of the simple a kind of gas-atomized powder equipment of structure.
For achieving the above object, the technical solution of the utility model comprises pipe connection portion, collection one, collection two, filter house, dewater portion and air exhauster, described pipe connection portion is connected with the pipeline in gas-atomized powder equipment, described collection one comprises transition one, collection unit and transition two, described transition one and described transition two are separately positioned on the both sides of described collection unit, transition one and transition two are in cone barrel, most extra heavy pipe path portion is all connected with collection unit, transition one is threaded connection between the part that caliber is the thinnest and pipe connection portion, the thinnest part of transition two calibers communicates with collection two, the inside of collection unit comprises collection unit water inlet, one, sump, water-permeable membrane, ball and suspension, described collection unit water inlet is arranged on the outer surface of collection unit, one, sump arranges on the inwall of collection unit, the bottom even that sump is one is provided with circular hole, the inner surface that sump is one is provided with the water-permeable membrane covered on circular hole, described ball is positioned at immediately below the bottom circular aperture of one, sump, the diameter of ball is 1.4 times of Circularhole diameter, the surface of ball is crude, described suspension is L-type, two suspensions are symmetrical and be arranged on the both sides of ball in opposite directions, ball is made to be fixed on one, sump, diameter and transition two the thinnest section diameters of caliber of described collection two are identical, the inside of collecting two comprises collection two water inlets, two, sump, water-permeable membrane, ball and suspension, described collection two water inlets are arranged on the outer surface of collection two, two, sump arranges on the inwall of collection two, the bottom even that sump is two is provided with circular hole, the inner surface that sump is two is provided with the water-permeable membrane covered on circular hole, described ball is positioned at immediately below the bottom circular aperture of two, sump, the diameter of ball is 1.4 times of Circularhole diameter, the surface of ball is crude, described suspension is L-type, two suspensions are symmetrical and be arranged on the both sides of ball in opposite directions, ball is made to be fixed on two, sump, be threaded connection between described filter house and collection two, in filter house, be provided with filter screen, describedly to dewater between portion with filter house as being threaded, dewater on portion's outer wall and be provided with door, dewater portion inwall on be provided with except sump, the described sump surface uniform that removes is provided with hole, high hydroscopic resin is provided with except in sump, dewater in portion's pipeline and be provided with air flow valve, described air flow valve can control air force by Non-follow control, described air exhauster and the portion of dewatering are threaded connection.
The utility model good effect is as follows:
The powder collector of a kind of gas-atomized powder equipment that the utility model provides, comprise pipe connection portion, collect one, collect two, filter house, dewater portion and air exhauster, filtration system is collected by three grades, powder can be collected fully, particularly, the first order is collected and is completed by the collection unit of collecting in, described collection one comprises transition one, collection unit and transition two, collection unit plays the effect of collecting powder, transition one is the transition region of connecting pipe connecting portion and collection unit, because the caliber of transition one becomes large gradually by little, such design can make the wind speed entering collection unit reduce gradually, make separation more abundant, improve separative efficiency, the inside of collection unit comprises collection unit water inlet, one, sump, water-permeable membrane, ball and suspension, one, sump arranges on the inwall of collection unit, the bottom even that sump is one is provided with circular hole, the inner surface that sump is one is provided with the water-permeable membrane covered on circular hole, described ball is positioned at immediately below the bottom circular aperture of one, sump, the diameter of ball is 1.4 times of Circularhole diameter, the surface of ball is crude, ball is fixed on one, sump by suspension, before using, water is poured into from the collection unit water inlet of collection unit upper surface, water penetrates on ball under the effect of water-permeable membrane, after the ball of the gas being mingled with powder by surface attachment water layer, powder can stick on ball, complete first collection, the first order is collected and is completed by collecting two thus, the diameter collecting two is less than the diameter of collection unit, because collection unit diameter is larger, so fail to collect fully the powder of the gas be arranged in around pipe centerline, so after the first order is collected, to be collected further by the collection two that diameter is less, the structure collecting two is identical with collection unit, can collect powder further, completes the second level and collects, the third level is collected in filter house and completes, and last remaining powder can intercept by the filter screen in filter house, dewater in portion and be provided with high hydroscopic resin, can moisture in adsorbed gas, prevent moisture from entering air exhauster, the part in protection air exhauster does not make moist, after collection completes, first back out collection one, collect two and this entirety of filter house, filter house is downward, collect one upwards, water filling inside, the powder belt that ball adheres to down by water, falls on filter screen, and the hole of water in filter screen flows out, finally, filter screen have accumulated the powder collected, back out the portion of dewatering, replaceable except the high hydroscopic resin in sump, dewater portion
On be provided with valve, gases flow can be controlled at reduced levels.The utility model structure is simple, and cost is low, and separating effect is outstanding.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
In accompanying drawing, 1 pipe connection portion, 2 transition one, 3 collection units, 4 transition two, 5 collections two, 6 filter houses, 7 dewater portion, 8 air exhausters, 9 collection unit water inlets, one, 10 sump, 11 water-permeable membrane, 12 balls, 13 suspensions, 14 collections, two water inlets, two, 15 sump, 16 filter screens, 17 except sump, 18 high hydroscopic resins, 19 air flow valve, 20 doors.
Detailed description of the invention
As shown in Figure 1, the utility model comprises pipe connection portion 1, collection one, collection two 5, filter house 6, dewater portion 7 and air exhauster 8, described pipe connection portion 1 is connected with the pipeline in gas-atomized powder equipment, described collection one comprises transition one 2, collection unit 3 and transition two 4, described transition one 2 and described transition two 4 are separately positioned on the both sides of described collection unit 3, transition one 2 and transition two 4 are cone barrel, most extra heavy pipe path portion is all connected with collection unit 3, be threaded connection between the part that transition 2 calibers are the thinnest and pipe connection portion 1, this kind of structure can make the wind speed entering collection unit 3 reduce gradually, make separation more abundant, improve separative efficiency, the inside of collection unit 3 comprises collection unit water inlet 9, one 10, sump, water-permeable membrane 11, ball 12 and suspension 13, described collection unit 3 water inlet is arranged on the outer surface of collection unit 3, one 10, sump is arranged on the inwall of collection unit 3, the bottom even that sump is one 10 is provided with circular hole, the inner surface that sump is one 10 is provided with the water-permeable membrane 11 covered on circular hole, described ball 12 is positioned at immediately below the bottom circular aperture of one 10, sump, described suspension 13 is L-type, two suspensions 13 are symmetrical and be arranged on the both sides of ball 12 in opposite directions, ball 12 is made to be fixed on one 10, sump, during use, from collection unit water inlet 9, water is injected in one 10, sump, water enters the surface of ball 12 along water-permeable membrane 11, when great many of experiments finally determines that the diameter of ball 12 is 1.4 times of Circularhole diameter, in one 10, sump, water can just by all upper water layers of attachment of all balls 12 surface bottom one 10, sump, and be unlikely to have the globule to fall, when the gas being mingled with metal dust flows through collection unit 3 time, metal dust in gas can be attached on the water layer on ball 12 surface, the specific area of ball is maximum, can adsorb to the full extent, and ball 12 surface is crude, be conducive to the attachment that powder is more firm, thus, collection unit 3 completes the first order and collects, because the caliber of collection unit 3 is thicker, the gas of caliber centre line zone is made to fail fully to collect, so will second level collection be carried out, the thinnest part of transition two 4 calibers communicates with collection two 5, the diameter that described collection is two 5 and transition two the thinnest section diameters of 4 caliber are identical, the inside of collecting two 5 comprises collection two water inlets 14, two 15, sump, water-permeable membrane 11, ball 12 and suspension 13, described collection two water inlets 14 are arranged on the outer surface of collection two 5, two 15, sump arranges on the inwall of collection two 5, the bottom even that sump is two 15 is provided with circular hole, the inner surface that sump is two is provided with the water-permeable membrane 11 covered on circular hole, described ball 12 is positioned at immediately below the bottom circular aperture of two 15, sump, the diameter of ball 12 is 1.4 times of Circularhole diameter, the surface of ball 12 is crude, described suspension 13 is L-type, two suspensions 13 are symmetrical and be arranged on the both sides of ball 12 in opposite directions, ball 12 is made to be fixed on two 15, sump, gas is identical with the powder collection process in collection unit 3 collection two 5, because the diameter collecting two 5 is less, the basis can collected in the first order is collected further, in reduction collection process, some powder are by the probability leaked down, complete the second level thus to collect, described filter house 6 and collecting between two 5 is threaded connection, and is provided with filter screen 16 in filter house 6, and filter screen 16, as last one barrier collected, is used for the powder of filtration residue, completes third level collection thus, describedly to dewater between portion 7 with filter house 6 as being threaded, dewater on portion 7 outer wall and be provided with door 20, dewater portion 7 inwall on be provided with except sump 17, described sump 17 surface uniform that removes is provided with hole, high hydroscopic resin 18 is provided with except in sump 17, because gas is after collecting one and collection two 5, the humidity of gas increases, and these gases finally can enter air exhauster 8, moisture in gas can produce harmful effect to the parts in air exhauster 8, by the high hydroscopic resin in sump 17, steam is absorbed, the gas entering air exhauster 8 is kept dry, dewater in portion 7 pipeline and be provided with air flow valve 19, described air flow valve 19 can control air force by Non-follow control, in use want controlled wind speed at lower level run.
Collection unit water inlet 9 and collection two water inlets 14 are first filled water before using by the utility model, after whole ball 12 adheres to water layer, open air exhauster 8, regulate wind speed, be mingled with the gas of powder after above three grades of described collections, close air exhauster 8, by collection one, collect two 5 and filter house 6 integrally screws down, filter house 6 is downward, collect one upwards, toward collecting an interior water filling, the powder belt of attachment on ball 12 goes down by the water of flowing, fall on filter screen 16, the hole of water in filter screen 16 flows out, because metal dust is not dissolved in water, so last, filter screen 16 have accumulated the powder collected, then filter house 6 is backed out, the powder collected can be taken out, back out the portion of dewatering 7, open door 20 replaceable except the high hydroscopic resin 18 in sump 17.The utility model structure is simple, and cost is low, and separating effect is outstanding.
To the above-mentioned explanation of the disclosed embodiments, professional and technical personnel in the field are realized or uses the utility model.To be apparent for those skilled in the art to the multiple amendment of these embodiments, General Principle as defined herein when not departing from spirit or scope of the present utility model, can realize in other embodiments.Therefore, the utility model can not be restricted to these embodiments shown in this article, but will meet the widest scope consistent with principle disclosed herein and features of novelty.
Claims (1)
1. a powder collector for gas-atomized powder equipment, is characterized in that: it comprises pipe connection portion (1), collects one, collects two (5), filter house (6), the portion that dewaters (7) and air exhausters (8), described pipe connection portion (1) is connected with the pipeline in gas-atomized powder equipment, described collection one comprises transition one (2), collection unit (3) and transition two (4), described transition one (2) and described transition two (4) are separately positioned on the both sides of described collection unit (3), transition one (2) and transition two (4) are in cone barrel, most extra heavy pipe path portion is all connected with collection unit (3), be threaded connection between the part that transition (2) caliber is the thinnest and pipe connection portion (1), the thinnest part of transition two (4) calibers communicates with collection two (5), the inside of collection unit (3) comprises collection unit water inlet (9), one, sump (10), water-permeable membrane (11), ball (12) and suspension (13), described collection unit (3) water inlet is arranged on the outer surface of collection unit (3), one, sump (10) arranges on the inwall of collection unit (3), the bottom even of sump one (10) is provided with circular hole, the inner surface of sump one (10) is provided with the water-permeable membrane (11) covered on circular hole, described ball (12) is positioned at immediately below the bottom circular aperture of sump one (10), the diameter of ball (12) is 1.4 times of Circularhole diameter, the surface of ball (12) is crude, described suspension (13) is L-type, two suspensions (13) are symmetrical and be arranged on the both sides of ball (12) in opposite directions, ball (12) is made to be fixed on one, sump (10), diameter and transition two (4) the thinnest section diameters of caliber of described collection two (5) are identical, the inside of collecting two (5) comprises collection two water inlets (14), two, sump (15), water-permeable membrane (11), ball (12) and suspension (13), described collection two water inlets (14) are arranged on the outer surface of collection two (5), two, sump (15) arranges on the inwall of collection two (5), the bottom even of sump two (15) is provided with circular hole, the inner surface that sump is two is provided with the water-permeable membrane (11) covered on circular hole, described ball (12) is positioned at immediately below the bottom circular aperture of sump two (15), the diameter of ball (12) is 1.4 times of Circularhole diameter, the surface of ball (12) is crude, described suspension (13) is L-type, two suspensions (13) are symmetrical and be arranged on the both sides of ball (12) in opposite directions, ball (12) is made to be fixed on two, sump (15), be threaded connection between described filter house (6) and collection two (5), in filter house (6), be provided with filter screen (16), the described portion that dewaters (7) with between filter house (6) for being threaded, dewater on portion (7) outer wall and be provided with door (20), dewater portion (7) inwall on be provided with except sump (17), described sump (17) surface uniform that removes is provided with hole, except being provided with high hydroscopic resin (18) in sump, dewater in portion (7) pipeline and be provided with air flow valve (19), described air flow valve (19) can control air force by Non-follow control, described air exhauster (8) is threaded connection with the portion (7) that dewaters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520144347.3U CN204891498U (en) | 2015-03-16 | 2015-03-16 | Powder collector of aerial fog powder manufacturing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520144347.3U CN204891498U (en) | 2015-03-16 | 2015-03-16 | Powder collector of aerial fog powder manufacturing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204891498U true CN204891498U (en) | 2015-12-23 |
Family
ID=54913715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520144347.3U Expired - Fee Related CN204891498U (en) | 2015-03-16 | 2015-03-16 | Powder collector of aerial fog powder manufacturing apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204891498U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114472906A (en) * | 2022-01-19 | 2022-05-13 | 江苏威拉里新材料科技有限公司 | Dust exhauster for gas atomization powder making equipment and application method thereof |
-
2015
- 2015-03-16 CN CN201520144347.3U patent/CN204891498U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114472906A (en) * | 2022-01-19 | 2022-05-13 | 江苏威拉里新材料科技有限公司 | Dust exhauster for gas atomization powder making equipment and application method thereof |
| CN114472906B (en) * | 2022-01-19 | 2023-12-01 | 江苏威拉里新材料科技有限公司 | Dust exhauster for aerosolization powder making equipment and using method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151223 Termination date: 20170316 |