CN205650134U - Be used for producing lithodomous mixed agitated vessel - Google Patents
Be used for producing lithodomous mixed agitated vessel Download PDFInfo
- Publication number
- CN205650134U CN205650134U CN201620484391.3U CN201620484391U CN205650134U CN 205650134 U CN205650134 U CN 205650134U CN 201620484391 U CN201620484391 U CN 201620484391U CN 205650134 U CN205650134 U CN 205650134U
- Authority
- CN
- China
- Prior art keywords
- housing
- material baffle
- mix
- casing
- jet pipeline
- 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
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- 239000000463 material Substances 0.000 claims abstract description 44
- 239000000203 mixture Substances 0.000 claims abstract description 31
- 238000003756 stirring Methods 0.000 claims abstract description 18
- 241000143392 Oar Species 0.000 claims description 23
- 229910003460 diamond Inorganic materials 0.000 claims description 16
- 239000010432 diamond Substances 0.000 claims description 16
- 239000004744 fabric Substances 0.000 claims description 9
- 238000010298 pulverizing process Methods 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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4yIEwgMTY0LjksMTQ3LjMgTCAxNjUuMCwxNDcuNSBMIDE2NS4xLDE0Ny42IEwgMTY1LjMsMTQ3LjcgTCAxNjUuNCwxNDcuOCBMIDE2NS42LDE0Ny44IEwgMTY1LjcsMTQ3LjkgTCAxNjUuOSwxNDcuOSBMIDE2Ni4xLDE0OC4wIEwgMTY2LjIsMTQ4LjAgTCAxNjYuNCwxNDguMCBMIDE2Ni42LDE0OC4wIEwgMTY2LjcsMTQ4LjAgTCAxNjYuOSwxNDcuOSBMIDE2Ny4xLDE0Ny45IEwgMTY3LjIsMTQ3LjggTCAxNjcuNCwxNDcuNyBMIDE2Ny41LDE0Ny42IEwgMTY3LjcsMTQ3LjUgTCAxNjcuOCwxNDcuNCBMIDE2Ny45LDE0Ny4zIEwgMTY4LjAsMTQ3LjEgTCAxNjguMSwxNDcuMCBMIDE2OC4yLDE0Ni44IEwgMTY4LjIsMTQ2LjcgTCAxNjguMywxNDYuNSBMIDE2OC4zLDE0Ni4zIEwgMTY4LjQsMTQ2LjIgTCAxNjguNCwxNDYuMCBMIDE2Ni40LDE0Ni4wIFonIHN0eWxlPSdmaWxsOiMwMDAwMDA7ZmlsbC1ydWxlOmV2ZW5vZGQ7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOiMwMDAwMDA7c3Ryb2tlLXdpZHRoOjAuMHB4O3N0cm9rZS1saW5lY2FwOmJ1dHQ7c3Ryb2tlLWxpbmVqb2luOm1pdGVyO3N0cm9rZS1vcGFjaXR5OjE7JyAvPgo8cGF0aCBkPSdNIDE2OC40LDE1NC4wIEwgMTY4LjQsMTUzLjggTCAxNjguMywxNTMuNyBMIDE2OC4zLDE1My41IEwgMTY4LjIsMTUzLjMgTCAxNjguMiwxNTMuMiBMIDE2OC4xLDE1My4wIEwgMTY4LjAsMTUyLjkgTCAxNjcuOSwxNTIuNyBMIDE2Ny44LDE1Mi42IEwgMTY3LjcsMTUyLjUgTCAxNjcuNSwxNTIuNCBMIDE2Ny40LDE1Mi4zIEwgMTY3LjIsMTUyLjIgTCAxNjcuMSwxNTIuMSBMIDE2Ni45LDE1Mi4xIEwgMTY2LjcsMTUyLjAgTCAxNjYuNiwxNTIuMCBMIDE2Ni40LDE1Mi4wIEwgMTY2LjIsMTUyLjAgTCAxNjYuMSwxNTIuMCBMIDE2NS45LDE1Mi4xIEwgMTY1LjcsMTUyLjEgTCAxNjUuNiwxNTIuMiBMIDE2NS40LDE1Mi4yIEwgMTY1LjMsMTUyLjMgTCAxNjUuMSwxNTIuNCBMIDE2NS4wLDE1Mi41IEwgMTY0LjksMTUyLjcgTCAxNjQuOCwxNTIuOCBMIDE2NC43LDE1Mi45IEwgMTY0LjYsMTUzLjEgTCAxNjQuNSwxNTMuMiBMIDE2NC41LDE1My40IEwgMTY0LjQsMTUzLjYgTCAxNjQuNCwxNTMuNyBMIDE2NC40LDE1My45IEwgMTY0LjQsMTU0LjEgTCAxNjQuNCwxNTQuMyBMIDE2NC40LDE1NC40IEwgMTY0LjUsMTU0LjYgTCAxNjQuNSwxNTQuOCBMIDE2NC42LDE1NC45IEwgMTY0LjcsMTU1LjEgTCAxNjQuOCwxNTUuMiBMIDE2NC45LDE1NS4zIEwgMTY1LjAsMTU1LjUgTCAxNjUuMSwxNTUuNiBMIDE2NS4zLDE1NS43IEwgMTY1LjQsMTU1LjggTCAxNjUuNiwxNTUuOCBMIDE2NS43LDE1NS45IEwgMTY1LjksMTU1LjkgTCAxNjYuMSwxNTYuMCBMIDE2Ni4yLDE1Ni4wIEwgMTY2LjQsMTU2LjAgTCAxNjYuNiwxNTYuMCBMIDE2Ni43LDE1Ni4wIEwgMTY2LjksMTU1LjkgTCAxNjcuMSwxNTUuOSBMIDE2Ny4yLDE1NS44IEwgMTY3LjQsMTU1LjcgTCAxNjcuNSwxNTUuNiBMIDE2Ny43LDE1NS41IEwgMTY3LjgsMTU1LjQgTCAxNjcuOSwxNTUuMyBMIDE2OC4wLDE1NS4xIEwgMTY4LjEsMTU1LjAgTCAxNjguMiwxNTQuOCBMIDE2OC4yLDE1NC43IEwgMTY4LjMsMTU0LjUgTCAxNjguMywxNTQuMyBMIDE2OC40LDE1NC4yIEwgMTY4LjQsMTU0LjAgTCAxNjYuNCwxNTQuMCBaJyBzdHlsZT0nZmlsbDojMDAwMDAwO2ZpbGwtcnVsZTpldmVub2RkO2ZpbGwtb3BhY2l0eToxO3N0cm9rZTojMDAwMDAwO3N0cm9rZS13aWR0aDowLjBweDtzdHJva2UtbGluZWNhcDpidXR0O3N0cm9rZS1saW5lam9pbjptaXRlcjtzdHJva2Utb3BhY2l0eToxOycgLz4KPC9zdmc+Cg== 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 [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 17
- 229910002804 graphite Inorganic materials 0.000 abstract description 17
- 239000010439 graphite Substances 0.000 abstract description 17
- 238000000034 method Methods 0.000 abstract description 3
- 238000003892 spreading Methods 0.000 abstract description 3
- 238000010521 absorption reaction Methods 0.000 abstract description 2
- 238000004513 sizing Methods 0.000 abstract 3
- 239000007921 spray Substances 0.000 abstract 3
- 239000008187 granular material Substances 0.000 description 7
- 239000000843 powder Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000007664 blowing Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The utility model discloses a be used for producing lithodomous mixed agitated vessel, it is the columniform casing, the top of casing is equipped with agitator motor and charge door, the middle part of casing is equipped with the sizing screen net, the crushing district on upper portion and the receipts material district of lower part are separated into with the casing to the sizing screen net, the upper portion of smashing the district is equipped with curved material baffle that hinders, it is linked together with the charge door through drawing the material pipe to hinder the material baffle, it is equipped with round annular gap between with the casing to hinder the material baffle, be equipped with one yuan of annular gas spray pipeline in the circle annular gap, gas spray pipeline's below all has to distribute there are a plurality of air jets, the utility model discloses a have the agitated vessel of sizing screen net, accomplish smashing and stirring work of powdered graphite in one set of device, through its inside combination that hinders material baffle and gas spray pipeline, avoid the powdered graphite on the inner wall of absorption at the casing of stirring and crushing in -process in the very big degree, avoid spreading, make things convenient for the collection of material, the agitated vessel's of being convenient for aftertreatment and maintenance.
Description
Technical field
This utility model relates to the production apparatus field of diamond, diamond, particularly relates to a kind of mix and blend equipment for producing diamond.
Background technology
Powdered graphite is as producing diamond and the primary raw material of diamond；Before processing, raw graphite powder needs through screening and stirring, to filter out the granule of different regulation size, mix with the auxiliary agent participating in production simultaneously, to reach to produce high quality diamond or the purpose of diamond.
For common mix and blend equipment, due to the lighter weight of powdered graphite own, it readily diffuses into each corner of mixing plant in mixing and whipping process, these lightweight powder are liable to stick on each position of inner walls, cause raw material finally can not get rid of completely, and then can cause component in raw material that certain change occurs, not only result in the waste of raw material, affect the subsequent production of mixing plant, even can affect the quality of final products；The biggest puzzlement is caused to enterprise.
Utility model content
For the problem of above-mentioned existence, this utility model purpose is to provide a kind of simple in construction, convenient pulverizing and married operation, prevents powder particle from remaining, and facilitates the mix and blend equipment being applicable to produce diamond of post processing.
In order to achieve the above object, the technical solution adopted in the utility model is as follows: a kind of mix and blend equipment for producing diamond, described mix and blend equipment is cylindrical housing, the top of housing is provided with stirring motor and charge door, the bottom of housing is provided with discharging opening, the middle part of described housing is provided with sub-material screen cloth, housing is separated into the disintegrating area on top and the receiving section of bottom by sub-material screen cloth, the top of disintegrating area is provided with the resistance material baffle plate of arc, described resistance material baffle plate is connected with charge door by material guiding tube, described resistance material baffle plate annular gap together with being provided with between housing, the jet pipeline of one annular it is provided with in described annular gap, the lower section of jet pipeline is all distributed multiple puff prot, described jet pipeline is connected to case top by connecting tube.
As a kind of improvement of the present utility model, the inside of described housing is provided with Double-layer stirring paddle, and described Double-layer stirring paddle includes pulverizing oar and mixing oar, pulverizes oar and is arranged on disintegrating area, mixes oar and be arranged on receiving section；Completing different work by Double-layer stirring paddle, pulverize oar and be mainly used in the crushing operation to bulky grain graphite granule, mixing oar is mainly used in the married operation of material.
As a kind of improvement of the present utility model, described puff prot is movably arranged on jet pipeline, and the angle between puff prot and jet pipeline is adjustable；By movable adjustable puff prot, convenient to carrying out blowing operation on each position below resistance material baffle plate, prevent powdered graphite to be attached on the inwall of housing and resistance material baffle plate.
As a kind of improvement of the present utility model, the setting height(from bottom) of described jet pipeline is higher than the setting height(from bottom) 5～8cm of resistance material baffle plate；Resistance material baffle plate is under the compound action of jet pipeline, and both are mainly used in preventing powdered graphite granule from spreading to housing upper, are worked by the internal cleaning of jet pipeline finishing device simultaneously, prevent powder from remaining.
A kind of improve as of the present utility model, described pulverize oar by how with the blade that length is different is formed；Pulverize oar by how with length difference from multiple angles, graphite granule to be pulverized, it is provided that crush efficiency, facilitate powdered graphite to pass through sub-material screen cloth.
The utility model has the advantage of: this utility model is by the mixing plant with sub-material screen cloth, pulverizing and the stirring work of powdered graphite is completed in set of device, simultaneously by its internal resistance material baffle plate and the combination of jet pipeline, avoid powdered graphite absorption in stirring and crushing process largely on the inwall of housing, avoid its large-area diffusion, facilitate the collection completely of a batches, it is simple to the post processing of mixing plant and maintenance, improve the production efficiency of enterprise.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation；
Fig. 2 is the plan structure figure of resistance material baffle plate of the present utility model and jet pipeline；
Wherein, 1 housing, 2 sub-material screen clothes, 3 disintegrating areas, 4 receiving sections, 5 stirring paddles, 5-1 pulverizes oar, 5-2 mixing oar, 6 charge doors, 7 discharging openings, 8 material guiding tubes, 9 resistance material baffle plates, 10 jet pipelines, 11 puff prots, 12 connecting tubes, 13 stirring motors.
Detailed description of the invention
This utility model is described in further detail by explanation and detailed description of the invention below in conjunction with the accompanying drawings.
Embodiment 1:A kind of mix and blend equipment for producing diamond as illustrated in fig. 1 and 2, described mix and blend equipment is cylindrical housing 1, the top of housing 1 is provided with stirring motor 13 and charge door 6, the bottom of housing 1 is provided with discharging opening 7, the middle part of described housing 1 is provided with sub-material screen cloth 2, housing 1 is separated into the disintegrating area 3 on top and the receiving section 4 of bottom by sub-material screen cloth 2, the top of disintegrating area 3 is provided with the resistance material baffle plate 9 of arc, described resistance material baffle plate 9 is connected with charge door 6 by material guiding tube 8, described resistance material baffle plate 9 is annular gap together with being provided with between housing 1, the jet pipeline 10 of one annular it is provided with in described annular gap, the lower section of jet pipeline 10 is all distributed multiple puff prot 11, described jet pipeline 10 is connected to the top of housing 1 by connecting tube 12.
Embodiment 2:As illustrated in fig. 1 and 2, the inside of housing 1 is provided with Double-layer stirring paddle 5, and described Double-layer stirring paddle 5 includes pulverizing oar 5-1 and mixing oar 5-2, pulverizes oar 5-1 and is arranged on disintegrating area 3, and mixing oar 5-2 is arranged on receiving section 4；Completing different work by Double-layer stirring paddle 5, pulverize oar 5-1 and be mainly used in the crushing operation to bulky grain graphite granule, mixing oar 5-2 is mainly used in the married operation of material.
Embodiment 3:As illustrated in fig. 1 and 2, puff prot 11 is movably arranged on jet pipeline 10, and the angle between puff prot 11 and jet pipeline 10 is adjustable；By movable adjustable puff prot 11, convenient to carrying out blowing operation on each position below resistance material baffle plate 9, prevent powdered graphite to be attached on the inwall of housing 1 and resistance material baffle plate 9.
Embodiment 4:As illustrated in fig. 1 and 2, the setting height(from bottom) of jet pipeline 10 is higher than the setting height(from bottom) 5～8cm of resistance material baffle plate 9；Resistance material baffle plate 9 is under the compound action of jet pipeline 10, and both are mainly used in preventing powdered graphite granule from spreading to the top of housing 1, are worked by the internal cleaning of jet pipeline 10 finishing device simultaneously, prevent powder from remaining.
Embodiment 5:As illustrated in fig. 1 and 2, oar 5-1 is pulverized by how with the blade that length is different is formed；Pulverize oar by how with length difference from multiple angles, graphite granule to be pulverized, it is provided that crush efficiency, facilitate powdered graphite to pass through sub-material screen cloth 2.
Being only preferred embodiment of the present utility model it should be noted that above-mentioned, be not used for limiting protection domain of the present utility model, equivalents done on the basis of above-described embodiment belongs to protection domain of the present utility model.
Claims (5)
1. the mix and blend equipment being used for producing diamond, described mix and blend equipment is cylindrical housing, the top of housing is provided with stirring motor and charge door, the bottom of housing is provided with discharging opening, it is characterized in that, the middle part of described housing is provided with sub-material screen cloth, housing is separated into the disintegrating area on top and the receiving section of bottom by sub-material screen cloth, the top of disintegrating area is provided with the resistance material baffle plate of arc, described resistance material baffle plate is connected with charge door by material guiding tube, described resistance material baffle plate annular gap together with being provided with between housing, the jet pipeline of one annular it is provided with in described annular gap, the lower section of jet pipeline is all distributed multiple puff prot, described jet pipeline is connected to case top by connecting tube.
Mix and blend equipment for producing diamond the most according to claim 1, it is characterized in that, the inside of described housing is provided with Double-layer stirring paddle, and described Double-layer stirring paddle includes pulverizing oar and mixing oar, pulverizing oar and be arranged on disintegrating area, mixing oar is arranged on receiving section.
Mix and blend equipment for producing diamond the most according to claim 1, it is characterised in that described puff prot is movably arranged on jet pipeline, the angle between puff prot and jet pipeline is adjustable.
4. according to the mix and blend equipment for producing diamond described in claim 1 or 3, it is characterised in that the setting height(from bottom) of described jet pipeline is higher than the setting height(from bottom) 5～8cm of resistance material baffle plate.
Mix and blend equipment for producing diamond the most according to claim 2, it is characterised in that described pulverize oar by how with the blade that length is different is formed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620484391.3U CN205650134U (en) | 2016-05-25 | 2016-05-25 | Be used for producing lithodomous mixed agitated vessel |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620484391.3U CN205650134U (en) | 2016-05-25 | 2016-05-25 | Be used for producing lithodomous mixed agitated vessel |
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| CN205650134U true CN205650134U (en) | 2016-10-19 |
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| CN201620484391.3U Expired - Fee Related CN205650134U (en) | 2016-05-25 | 2016-05-25 | Be used for producing lithodomous mixed agitated vessel |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106390904A (en) * | 2016-12-05 | 2017-02-15 | 南京东擎科技有限公司 | Integrated reaction device capable of crushing and screening materials |
| CN108095165A (en) * | 2017-12-27 | 2018-06-01 | 吴烨程 | A kind of feed crushing and screening device of intermittent feeding |
| CN108187528A (en) * | 2017-12-12 | 2018-06-22 | 芜湖市诺康生物科技有限公司 | A kind of liquid dispensing tank arrangement |
| CN109173805A (en) * | 2018-09-19 | 2019-01-11 | 江苏金曼科技有限责任公司 | A kind of continuous discharge agitating device |
| CN113082988A (en) * | 2021-04-09 | 2021-07-09 | 冯瑞强 | Desulfurization and denitrification treatment equipment and method for industrial pollution emission waste gas |
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2016
- 2016-05-25 CN CN201620484391.3U patent/CN205650134U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106390904A (en) * | 2016-12-05 | 2017-02-15 | 南京东擎科技有限公司 | Integrated reaction device capable of crushing and screening materials |
| CN106390904B (en) * | 2016-12-05 | 2018-09-21 | 山东凌凯药业有限公司 | It is a kind of can grinding screen material integrated reacting device |
| CN108187528A (en) * | 2017-12-12 | 2018-06-22 | 芜湖市诺康生物科技有限公司 | A kind of liquid dispensing tank arrangement |
| CN108095165A (en) * | 2017-12-27 | 2018-06-01 | 吴烨程 | A kind of feed crushing and screening device of intermittent feeding |
| CN109173805A (en) * | 2018-09-19 | 2019-01-11 | 江苏金曼科技有限责任公司 | A kind of continuous discharge agitating device |
| CN113082988A (en) * | 2021-04-09 | 2021-07-09 | 冯瑞强 | Desulfurization and denitrification treatment equipment and method for industrial pollution emission waste gas |
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