CN202590974U - Separated water vacuum-pumping type ultrahigh-speed centrifugal dehydrator - Google Patents
Separated water vacuum-pumping type ultrahigh-speed centrifugal dehydrator Download PDFInfo
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- CN202590974U CN202590974U CN 201220248720 CN201220248720U CN202590974U CN 202590974 U CN202590974 U CN 202590974U CN 201220248720 CN201220248720 CN 201220248720 CN 201220248720 U CN201220248720 U CN 201220248720U CN 202590974 U CN202590974 U CN 202590974U
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- water
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Abstract
The utility model relates to a separated water vacuum-pumping type ultrahigh-speed centrifugal dehydrator, belonging to the technical field of ultrahigh-speed centrifugal dehydrators. The ultrahigh-speed centrifugal dehydrator comprises three layers of barrels sheathed from inside to outside: a material rotating barrel, a flow guide water barrel and an explosion-proof outer barrel, wherein an interlayer space between the material rotating barrel and the flow guide water barrel is a water storage interlayer for temporarily storing separated water; and air inlet pipe is arranged at the top of the water storage interlayer, a water outlet pipe is arranged at the bottom of the water storage interlayer, and a vacuum pump is connected on the pipe section of the water outlet pipe outside the explosion-proof outer barrel. The ultrahigh-speed centrifugal dehydrator has the advantages that no separated water is stored in the water storage interlayer, the separated water in the water storage interlayer is convenient to quickly flow out of the dehydrator from the water outlet pipe, and the dehydration working efficiency is increased; and a vacuum negative-pressure gas flow in the water storage interlayer has negative-pressure pumping effect on separated water in the material rotating barrel and is beneficial for the separated water in the material rotating barrel to quickly enter the water storage interlayer, and the dehydration working efficiency is increased.
Description
Technical field
The utility model belongs to ultrahigh speed centrifugal dehydrator technical field, and particularly the isolated water of ultrahigh speed centrifugal dehydrator can flow out from the ultrahigh speed centrifugal dehydrator rapidly, is not accumulated in the technology in the ultrahigh speed centrifugal dehydrator.
Background technology
Existing ultrahigh speed centrifugal dehydrator structure is from inside to outside to have three layers of tube: material rotating cylinder, water conservancy diversion water drum, explosion-proof urceolus.It is dried up that the rotating speed that the material rotating cylinder changes with per minute kind 15000 is deviate from composition to the water in the material, divides the dried up sieve aperture wall that passes the material rotating cylinder, enters into the mezzanine space of material rotating cylinder and water conservancy diversion water drum.Utilize the gravity effect, the branch in the mezzanine space is dried up to flow to downwards in the outlet pipe, and outlet pipe passes the steel wall of water conservancy diversion water drum and the steel wall of explosion-proof urceolus, and outlet pipe is the dried up ultrahigh speed centrifugal dehydrator of drawing of the branch in the mezzanine space.The shortcoming of this water-out manners of ultrahigh speed centrifugal dehydrator is: the superelevation of material rotating cylinder is rotated and is given and very big centrifugal force the branch in the mezzanine space is dried up; And the direction of centrifugal force becomes the angle of 90 degree with the direction that goes out water flows; Then dried up being difficult to of the branch in the mezzanine space flowed out from outlet pipe; Divide dried up long-pending full in mezzanine space after, the speed that from outlet pipe, flows out is also very slow.Divide dried up long-pending full problem topic maximum in mezzanine space to be: enter into the mezzanine space medium velocity after the water in the material of material rotating cylinder the inside is separated by centrifugal force and slow down greatly, then the operating efficiency of ultrahigh speed centrifugal dehydrator reduces greatly.
Summary of the invention
The purpose of the utility model provides the method that the water storage interlayer to the ultrahigh speed centrifugal dehydrator vacuumizes; Make that the branch in the mezzanine space is dried up between material rotating cylinder and the water conservancy diversion water drum can flow out fast from outlet pipe, the ultrahigh speed centrifugal dehydrator that the dehydration operating efficiency improves.
The structure of the utility model is:
Extract separation ability of swimming ultrahigh speed centrifugal dehydrator out with vacuum; Comprise three layers of tube that from inside to outside become suit: material rotating cylinder 1, water conservancy diversion water drum 2 and explosion-proof urceolus 3; Motor 4 is positioned at the appearance end face 5 of explosion-proof urceolus 3; The appearance end face 5 that explosion-proof urceolus 3 is passed in the rotating shaft 6 of motor 4 is connected with the end face of material rotating cylinder 1, and motor 4 drives material rotating cylinder 1 and rotates; The bottom of material rotating cylinder 1 is provided with feed pipe 13, feed pipe 13 pass material rotating cylinder 1 and explosion-proof urceolus 3 in the outside of explosion-proof urceolus 3 opening; Mezzanine space between material rotating cylinder 1 and the water conservancy diversion water drum 2 is that interim the storage divided dried up water storage interlayer 7; Bottom at water storage interlayer 7; Be that water conservancy diversion water drum bottom 8 is provided with outlet pipe 9; Outlet pipe 9 passes water conservancy diversion water drum 2 and explosion-proof urceolus 3 at explosion-proof urceolus 3 outside openings, and outlet pipe 9 is characterized in that the dried up outside that is drawn out to explosion-proof urceolus 3 of the branch in the water storage interlayer 7: at the top of water storage interlayer 7; Be that water conservancy diversion water drum top 10 is provided with air inlet pipe 11, air inlet pipe 11 is passed water conservancy diversion water drum 2 and explosion-proof urceolus 3 at explosion-proof urceolus 3 outside openings; Outlet pipe 9 is connected with vavuum pump 12 on the pipeline section of explosion-proof urceolus 3 outsides.
4 on motor drives material rotating cylinder 1 and rotates, and the rotating speed that material rotating cylinder 1 changes with per minute kind 15000 is deviate from the water in the material of material rotating cylinder 1 the inside dress, and the water of deviating from is that branch is dried up.Material rotating cylinder 1 is that the allowed water that macromolecule resin material is processed passes through, but the macromolecule resin sieve that does not allow material to pass through.Divide the dried up material rotating cylinder 1 macromolecule resin sieve that passes to enter into the water storage interlayer 7 between material rotating cylinder 1 and the water conservancy diversion water drum 2.The top of water storage interlayer 7, promptly water conservancy diversion water drum top 10 is provided with air inlet pipe 11, and air inlet pipe 11 is passed water conservancy diversion water drum 2 and explosion-proof urceolus 3 at explosion-proof urceolus 3 outside openings.Outlet pipe 9 is connected with vavuum pump 12 on the pipeline section of explosion-proof urceolus 3 outsides.Vavuum pump 12 extracts the air that enters into water storage interlayer 7 from air inlet pipe 11 through outlet pipe 9, simultaneously with the dried up extraction of the branch in the water storage interlayer 7.The pressure of body is given greater than material rotating cylinder 1 and is divided dried up centrifugal force because vavuum pump 12 is bled, and then the branch in the water storage interlayer 7 is dried up is taken out to outlet pipe 9 by the bleed pressure of body of vavuum pump 12.Divide dried up the storage no longer in a large number not in the water storage interlayer 7, body has enough pressure as long as vavuum pump 12 is bled, and divides dried up can not being stored in the water storage interlayer 7.And the negative pressure of vacuum gas in the water storage interlayer 7 stream has a negative pressure extracting effect to the branch in the material rotating cylinder 1 is dried up.So negative pressure of vacuum gas stream has two effects in the water storage interlayer 7: the firstth, make that not store branchs in the water storage interlayer 7 dried up, help that branch in the water storage interlayer 7 is dried up to flow out dewaterer fast from outlet pipe 9, improve the operating efficiency of dewatering; The secondth, negative pressure of vacuum gas in the water storage interlayer 7 stream has a negative pressure extracting effect to the branch in the material rotating cylinder 1 is dried up, also helps the dried up quick entering water storage interlayer 7 of branch in the material rotating cylinder 1, improves the dehydration operating efficiency.
The advantage of the utility model: the firstth, make that not store branch in the water storage interlayer dried up, help the dried up dewaterer that from outlet pipe, flows out fast of branch in the water storage interlayer, improve the dehydration operating efficiency; The secondth, negative pressure of vacuum gas in water storage interlayer stream has a negative pressure extracting effect to the branch in the material rotating cylinder is dried up, also helps the dried up quick entering water storage interlayer of branch in the material rotating cylinder, improves the dehydration operating efficiency.
Description of drawings
Fig. 1 is the new structural representation of this practicality.
1 is material rotating cylinder, the 2nd among the figure, water conservancy diversion water drum, the 3rd, explosion-proof urceolus, the 4th, motor, the 5th, appearance end face, the 6th, rotating shaft, the 7th, water storage interlayer, the 8th, water conservancy diversion water drum bottom, the 9th, outlet pipe, the 10th, water conservancy diversion water drum top, the 11st, air inlet pipe, the 12nd, vavuum pump, the 13rd, feed pipe.
The specific embodiment
Embodiment 1, extract out to separate ability of swimming ultrahigh speed centrifugal dehydrator with vacuum
Like Fig. 1; Extract separation ability of swimming ultrahigh speed centrifugal dehydrator out with vacuum and comprise three layers of tube that from inside to outside become suit: material rotating cylinder 1, water conservancy diversion water drum 2 and explosion-proof urceolus 3; Motor 4 is positioned at the appearance end face 5 of explosion-proof urceolus 3; The appearance end face 5 that explosion-proof urceolus 3 is passed in the rotating shaft 6 of motor 4 is connected with the end face of material rotating cylinder 1, and motor 4 drives material rotating cylinder 1 and rotates; The bottom of material rotating cylinder 1 is provided with feed pipe 13, feed pipe 13 pass material rotating cylinder 1 and explosion-proof urceolus 3 in the outside of explosion-proof urceolus 3 opening; Mezzanine space between material rotating cylinder 1 and the water conservancy diversion water drum 2 is that interim the storage divided dried up water storage interlayer 7; In the bottom of water storage interlayer 7, promptly water conservancy diversion water drum bottom 8 is provided with outlet pipe 9, and outlet pipe 9 passes water conservancy diversion water drum 2 and explosion-proof urceolus 3 at explosion-proof urceolus 3 outside openings, and outlet pipe 9 is the dried up outside that is drawn out to explosion-proof urceolus 3 of the branch in the water storage interlayer 7.At the top of water storage interlayer 7, promptly water conservancy diversion water drum top 10 is provided with air inlet pipe 11, and air inlet pipe 11 is passed water conservancy diversion water drum 2 and explosion-proof urceolus 3 at explosion-proof urceolus 3 outside openings; Outlet pipe 9 is connected with vavuum pump 12 on the pipeline section of explosion-proof urceolus 3 outsides.
4 on motor drives material rotating cylinder 1 and rotates, and the rotating speed that material rotating cylinder 1 changes with per minute kind 15000 is deviate from the water in the material of material rotating cylinder 1 the inside dress, and the water of deviating from is that branch is dried up.Material rotating cylinder 1 is that the allowed water that macromolecule resin material is processed passes through, but the macromolecule resin sieve that does not allow material to pass through.Divide the dried up material rotating cylinder 1 macromolecule resin sieve that passes to enter into the water storage interlayer 7 between material rotating cylinder 1 and the water conservancy diversion water drum 2.The top of water storage interlayer 7, promptly water conservancy diversion water drum top 10 is provided with air inlet pipe 11, and air inlet pipe 11 is passed water conservancy diversion water drum 2 and explosion-proof urceolus 3 at explosion-proof urceolus 3 outside openings.Outlet pipe 9 is connected with vavuum pump 12 on the pipeline section of explosion-proof urceolus 3 outsides.Vavuum pump 12 extracts the air that enters into water storage interlayer 7 from air inlet pipe 11 through outlet pipe 9, simultaneously with the dried up extraction of the branch in the water storage interlayer 7.The pressure of body is given greater than material rotating cylinder 1 and is divided dried up centrifugal force because vavuum pump 12 is bled, and then the branch in the water storage interlayer 7 is dried up is taken out to outlet pipe 9 by the bleed pressure of body of vavuum pump 12.Divide dried up the storage no longer in a large number not in the water storage interlayer 7, body has enough pressure as long as vavuum pump 12 is bled, and divides dried up can not being stored in the water storage interlayer 7.And the negative pressure of vacuum gas in the water storage interlayer 7 stream has a negative pressure extracting effect to the branch in the material rotating cylinder 1 is dried up.So negative pressure of vacuum gas stream has two effects in the water storage interlayer 7: the firstth, make that not store branchs in the water storage interlayer 7 dried up, help that branch in the water storage interlayer 7 is dried up to flow out dewaterer fast from outlet pipe 9, improve the operating efficiency of dewatering; The secondth, negative pressure of vacuum gas in the water storage interlayer 7 stream has a negative pressure extracting effect to the branch in the material rotating cylinder 1 is dried up, also helps the dried up quick entering water storage interlayer 7 of branch in the material rotating cylinder 1, improves the dehydration operating efficiency.
Claims (1)
1. extract out with vacuum and separate ability of swimming ultrahigh speed centrifugal dehydrator; Comprise three layers of tube that from inside to outside become suit: material rotating cylinder (1), water conservancy diversion water drum (2) and explosion-proof urceolus (3); Motor (4) is positioned at the appearance end face (5) of explosion-proof urceolus (3); The appearance end face (5) that explosion-proof urceolus (3) is passed in the rotating shaft (6) of motor (4) is connected with the end face of material rotating cylinder (1), and motor (4) drives material rotating cylinder (1) and rotates; The bottom of material rotating cylinder (1) is provided with feed pipe (13), and feed pipe (13) passes material rotating cylinder (1) and explosion-proof urceolus (3) the outside opening at explosion-proof urceolus (3); Mezzanine space between material rotating cylinder (1) and the water conservancy diversion water drum (2) is that interim the storage divided dried up water storage interlayer (7); Bottom in water storage interlayer (7); Be that water conservancy diversion water drum bottom (8) is provided with outlet pipe (9); Outlet pipe (9) passes water conservancy diversion water drum (2) and explosion-proof urceolus (3) opening outside explosion-proof urceolus (3); Outlet pipe (9) is the dried up outside that is drawn out to explosion-proof urceolus (3) of the branch in the water storage interlayer (7); It is characterized in that: the top in water storage interlayer (7), promptly water conservancy diversion water drum top (10) are provided with air inlet pipe (11), and air inlet pipe (11) is passed water conservancy diversion water drum (2) and explosion-proof urceolus (3) opening outside explosion-proof urceolus (3); Outlet pipe (9) is connected with vavuum pump (12) on the pipeline section of explosion-proof urceolus (3) outside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220248720 CN202590974U (en) | 2012-05-30 | 2012-05-30 | Separated water vacuum-pumping type ultrahigh-speed centrifugal dehydrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220248720 CN202590974U (en) | 2012-05-30 | 2012-05-30 | Separated water vacuum-pumping type ultrahigh-speed centrifugal dehydrator |
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| Publication Number | Publication Date |
|---|---|
| CN202590974U true CN202590974U (en) | 2012-12-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220248720 Expired - Fee Related CN202590974U (en) | 2012-05-30 | 2012-05-30 | Separated water vacuum-pumping type ultrahigh-speed centrifugal dehydrator |
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| CN (1) | CN202590974U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106607191A (en) * | 2015-10-21 | 2017-05-03 | 江苏华苏亚生物科技有限公司 | Horizontal type spiral filtering centrifuge for processing pleurotus eryngii |
| CN107587673A (en) * | 2017-09-23 | 2018-01-16 | 天津市盛泰建筑工程有限公司 | A kind of staircase structure and its construction method for building construction |
| CN111841903A (en) * | 2020-08-10 | 2020-10-30 | 广州大健康药业有限公司 | Centrifugal machine |
-
2012
- 2012-05-30 CN CN 201220248720 patent/CN202590974U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106607191A (en) * | 2015-10-21 | 2017-05-03 | 江苏华苏亚生物科技有限公司 | Horizontal type spiral filtering centrifuge for processing pleurotus eryngii |
| CN107587673A (en) * | 2017-09-23 | 2018-01-16 | 天津市盛泰建筑工程有限公司 | A kind of staircase structure and its construction method for building construction |
| CN111841903A (en) * | 2020-08-10 | 2020-10-30 | 广州大健康药业有限公司 | Centrifugal machine |
| CN111841903B (en) * | 2020-08-10 | 2021-10-26 | 广州大健康药业有限公司 | Centrifugal machine |
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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 |
Granted publication date: 20121212 Termination date: 20150530 |
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| EXPY | Termination of patent right or utility model |