CN202610041U - Centrifugal self-absorption hybrid type inversed umbrella shaped aeration machine - Google Patents
Centrifugal self-absorption hybrid type inversed umbrella shaped aeration machine Download PDFInfo
- Publication number
- CN202610041U CN202610041U CN201220136651XU CN201220136651U CN202610041U CN 202610041 U CN202610041 U CN 202610041U CN 201220136651X U CN201220136651X U CN 201220136651XU CN 201220136651 U CN201220136651 U CN 201220136651U CN 202610041 U CN202610041 U CN 202610041U
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- Prior art keywords
- phase mixing
- mixing head
- iii
- guide shell
- trap
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- 238000005273 aeration Methods 0.000 title abstract description 9
- 238000010521 absorption reaction Methods 0.000 title abstract 2
- 238000005276 aerator Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000010865 sewage Substances 0.000 description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000007787 solid Substances 0.000 description 5
- 239000012530 fluid Substances 0.000 description 4
- 230000001580 bacterial effect Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 230000036284 oxygen consumption Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000006213 oxygenation reaction Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Structures Of Non-Positive Displacement Pumps (AREA)
Abstract
The utility model discloses a centrifugal self-absorption hybrid type inversed umbrella shaped aeration machine. A plurality of three-phase hybrid pipe bundles are distributed on the surface of an impeller body (1), each three-phase hybrid pipe bundle comprises a plurality of three-phase hybrid pipes, the plurality of three-phase hybrid pipes are distributed on the surface of the impeller body (1) in a scattered way, a plurality of diversion cylinders downwards extend from the bottom of the impeller body (1) and are concentrically arranged, a plurality of vertical siphon pipes are distributed on the inner walls of the diversion cylinders, the number of the siphon pipes distributed in each layer of diversion cylinders is equal to the number of three-phase hybrid pipes in the corresponding three-phase hybrid pipe bundle, one end of each three-phase hybrid pipe is attached to the edge of the impeller body (1), the other end of each three-phase hybrid pipe is communicated with each siphon pipe, and a negative pressure air suction pipe is arranged at a joint of each siphon pipe and each three-phase hybrid pipe.
Description
Technical field
The utility model relates to the hybrid inversed umbrella type aerator of a kind of centrifugal self-priming.
Background technology
All there is a fatal defective in all similar inversed umbrella type surface aeration machines in the world; In the dark pond of 4～6m, carry out aeration; Can only carry out aeration to sewage and can not deep water be carried out aeration aerating apart from the water surface 2～3m; And gas, liquid, solid are carried out fully effectively mixing, the energy consumption of WWT strengthens, expense increases so make.
Summary of the invention
The utility model provides a kind of centrifugal self-priming hybrid inversed umbrella type aerator; It not only makes the sewage that gets each aspect in the pond all get a promotion; The aquosity of circulation makes no longer to have the oxygenation blind area in the pond up and down, and airborne oxygen is constantly brought into sewage lagoon; And the organism in the sewage carried out effective oxidation, for the oxygen consumption bacterial classification life source is provided simultaneously.
The utility model has adopted following technical scheme: the hybrid inversed umbrella type aerator of a kind of centrifugal self-priming; It comprises the inversed umbrella type impeller body; On impeller body, be distributed with blade, the surface arrangement of described impeller body has some three-phase mixing head groups, and each three-phase mixing head group comprises some three-phase mixing heads; Some three-phase mixing heads are the surface that divergent shape is distributed in impeller body; Be extended with the guide shell that several layers is provided with one heart in the bottom of impeller body downwards, on the inwall of every layer of guide shell, be distributed with some vertical U traps, each three-phase mixing head group is corresponding with every layer of guide shell; The siphonal quantity of every layer of interior distribution of guide shell is identical with the three-phase mixing head quantity in the corresponding three-phase mixing head group; Each three-phase mixing head one end invests the edge of impeller body, and the other end of each three-phase mixing head is connected with each U trap, and the junction of each U trap and each three-phase mixing head is provided with negative pressure suction tube; One end of negative pressure suction tube vertically points to the outside and the atmosphere of impeller body, and the other end of negative pressure suction tube stretches in the three-phase mixing head consistent with the direction of water flow jet in the three-phase mixing head.
The surface of described impeller body is evenly distributed with three-phase mixing head group I, three-phase mixing head group II and three-phase mixing head group III; Include some three-phase mixing head I, some three-phase mixing head II and some three-phase mixing head III in three-phase mixing head group I, three-phase mixing head group II and the three-phase mixing head group III respectively; Each three-phase mixing head III space in each three-phase mixing head I in the three-phase mixing head group I, the three-phase mixing head group II in each three-phase mixing head II and the three-phase mixing head group III is distributed in the surface of impeller body; The bottom of described impeller body is provided with guide shell I, guide shell II and the guide shell III of concentric setting; The caliber of guide shell I is greater than the caliber of guide shell II; The caliber of guide shell II is greater than the caliber of guide shell III; Guide shell I, guide shell II and guide shell III are extended stepped arrangement straight down according to the descending order of barrel dliameter; Be evenly distributed with some U trap I, some U trap II and some U trap III on the inwall of guide shell I, guide shell II and guide shell III respectively, every U trap I is connected with every three-phase mixing head I respectively, is provided with the negative pressure suction tube I in the junction of U trap I and three-phase mixing head I; Every U trap II is connected with every three-phase mixing head II respectively; Junction in U trap II and three-phase mixing head II is provided with the negative pressure suction tube II, and every U trap III is connected with every three-phase mixing head III respectively, is provided with the negative pressure suction tube III in the junction of U trap III and three-phase mixing head III.
Described guide shell I, guide shell II and guide shell III are extended stepped arrangement straight down according to the descending order of barrel dliameter.Said three-phase mixing head I cross section is rectangle, circle, trilateral or Polygons, and three-phase mixing head II cross section is rectangle, circle, trilateral or Polygons, and the cross section of three-phase mixing head III is rectangle, circle, trilateral or Polygons.The cross section of said U trap I, U trap II and U trap III is rectangle, circle, trilateral or Polygons.Described three-phase mixing head group I, three-phase mixing head group II and three-phase mixing head group III are distributed in the upper surface or the lower surface of impeller body.
The utlity model has following beneficial effect: it is different that the bottom of the utility model impeller body is provided with length; Can reach some guide shells of different depths in the sewage lagoon respectively; Be provided with some U traps in the guide shell; The upper surface of aeration machine impeller body or lower surface are provided with the three-phase mixing head; The cf-that when aeration impeller rotates, is produced just can be promoted to the fluid in the deep mixed U trap in the gas-liquid-solid three-phase mixing head and constantly spray to periphery; The fluid of each aspect just can not promote naturally through cf-and continuously form circulation, ambient radiation up and down in the sewage lagoon as long as impeller does not stop the rotation, and makes the fluid and the air thorough mixing of each aspect.The junction back segment of U trap and three-phase mixing head is provided with negative pressure suction tube; When fluid sprays through the cf-hoop; Will inevitably make and produce bigger negative pressure in the three-phase mixing head; Air just by the negative pressure pipe constantly sucked three-phase mixing head and solid-liquid in the sewage mix mutually form water, solid, gas three-phase mixtinite is spurted into the pond, the oxygen that is contained in the air just can carry out effective oxidation to the organism in the sewage effectively, for the oxygen consumption bacterial classification life source is provided simultaneously.
Description of drawings
Fig. 1 is that the embodiment one of the utility model gets structural representation.
Fig. 2 is the upward view of Fig. 1.
Fig. 3 is the synoptic diagram that the utility model embodiment U trap III is connected with three-phase mixing head III.
Fig. 4 is the synoptic diagram that the utility model embodiment U trap I is connected with three-phase mixing head I and the U trap II is connected with three-phase mixing head II.
Embodiment
Embodiment one, and in Fig. 1 and Fig. 2, the utility model provides a kind of centrifugal self-priming hybrid inversed umbrella type aerator; It comprises inversed umbrella type impeller body 1; On impeller body 1, be distributed with blade 2, the surface arrangement of described impeller body 1 has three-phase mixing head group I, three-phase mixing head group II and three-phase mixing head group III, and three-phase mixing head group I, three-phase mixing head group II and three-phase mixing head group III are distributed in the upper surface or the lower surface of impeller body 1; Include eight three-phase mixing head I 3, eight three-phase mixing head II 4 and eight three-phase mixing head III 5 in three-phase mixing head group I, three-phase mixing head group II and the three-phase mixing head group III respectively; The cross section of three-phase mixing head I 3, three-phase mixing head II 4 and three-phase mixing head III 5 is rectangle, circle, trilateral or Polygons, and each three-phase mixing head III 5 space in each the three-phase mixing head I 3 in the three-phase mixing head group I, the three-phase mixing head group II in each three-phase mixing head II 4 and the three-phase mixing head group III are distributed in the surface of impeller body 1, and each the three-phase mixing head I 3 in the three-phase mixing head group I is the surface that divergent shape is distributed in impeller body 1; Each three-phase mixing head II 4 in the three-phase mixing head group II is the surface that divergent shape is distributed in impeller body 1; Each three-phase mixing head III 5 in the three-phase mixing head group III is the surface that divergent shape is distributed in impeller body 1, is provided with guide shell I 6, guide shell II 7 and guide shell III 8 in the bottom of impeller body 1, and the caliber of guide shell I 6 is greater than the caliber of guide shell II 7; The caliber of guide shell II 7 is greater than the caliber of guide shell III 8; Guide shell I 6, guide shell II 7 and guide shell III 8 are extended stepped arrangement straight down according to the descending order of barrel dliameter, are evenly distributed with 14, eight vertical U trap II 12 of eight vertical U trap I and eight vertical U trap III 10 on the inwall of guide shell I 6, guide shell II 7 and guide shell III 8 respectively; Each three-phase mixing head group is corresponding with every layer of guide shell; The interior three-phase mixing head quantity of the siphonal quantity that distributes in each guide shell and corresponding three-phase mixing head group is identical, and every three-phase mixing head I 3, every three-phase mixing head II 4 and every three-phase mixing head III 5 one end all invest the edge of impeller body 1, in Fig. 3; Every U trap I 14 is connected with every three-phase mixing head I 3 respectively; Junction in U trap I 14 and three-phase mixing head I 3 is provided with negative pressure suction tube I 13, and an end of negative pressure suction tube I 13 vertically points to the outside and the atmosphere of impeller body 1, and the other end of negative pressure suction tube I 13 stretches in the three-phase mixing head I 3 consistent with the directions of water flow jets in the three-phase mixing head I 3; In Fig. 4; Every U trap II 12 of present embodiment is connected with every three-phase mixing head II 4 respectively, and U trap II 12 is provided with negative pressure suction tube II 11 with the junction of three-phase mixing head II 4, and the outside that an end of negative pressure suction tube II 11 vertically points to impeller body 1 communicates with the outside of impeller body 1 mutually; The other end of negative pressure suction tube II 11 stretches in the three-phase mixing head II 4 consistent with the direction of water flow jet in the three-phase mixing head II 4; In Fig. 4, every U trap III 10 of present embodiment is connected with every three-phase mixing head III 5 respectively, is provided with negative pressure suction tube III 9 in 5 junctions of U trap III 10 and three-phase mixing head III; The outside that one end of negative pressure suction tube III 9 vertically points to impeller body 1 communicates with the outside of impeller body 1, and the other end of negative pressure suction tube III 9 stretches in the three-phase mixing head III 5 consistent with the direction of water flow jet in the three-phase mixing head III 5.
When the inverted umbrella-shaped aeration machine rotary work, under action of centrifugal force, the sewage of each aspect is promoted continuously to be transported in the every solid three-phase mixing head of gas-liquid and by hoop by U trap and throws away in the pond; Produce bigger negative pressure in the gas-liquid-solid three-phase mixing head this moment; The air suction pipe that is located on the three-phase mixing head just constantly sucks a large amount of air, and sewage and airborne oxygen ceaselessly collide, stir in the three-phase mixing head, reaches fully to mix; Sewage at the not end of three-phase mixing head again with the formal ring of water sheet, water droplet to ejecting; Contact and accomplish the transfer of oxygen aloft again with airborne oxygen fully, finally fall into the pond, each aspect all gets a promotion in the pond like this; The aquosity of circulation makes and no longer has the oxygenation blind area in the pond up and down; Airborne oxygen is constantly brought into sewage lagoon, and the organism in the sewage is carried out effective oxidation, for the oxygen consumption bacterial classification life source is provided simultaneously.
Claims (6)
1. hybrid inversed umbrella type aerator of centrifugal self-priming; It comprises inversed umbrella type impeller body (1); On impeller body (1), be distributed with blade (2), it is characterized in that the surface arrangement of described impeller body (1) has some three-phase mixing head groups, each three-phase mixing head group comprises some three-phase mixing heads; Some three-phase mixing heads are the surface that divergent shape is distributed in impeller body (1); Be extended with the guide shell that several layers is provided with one heart in the bottom of impeller body (1) downwards, on the inwall of every layer of guide shell, be distributed with some vertical U traps, each three-phase mixing head group is corresponding with every layer of guide shell; The siphonal quantity of every layer of interior distribution of guide shell is identical with the three-phase mixing head quantity in the corresponding three-phase mixing head group; Each three-phase mixing head one end invests the edge of impeller body (1), and the other end of each three-phase mixing head is connected with each U trap, and the junction of each U trap and each three-phase mixing head is provided with negative pressure suction tube; One end of negative pressure suction tube vertically points to the outside and the atmosphere of impeller body (1), and the other end of negative pressure suction tube stretches in the three-phase mixing head consistent with the direction of water flow jet in the three-phase mixing head.
2. according to the hybrid inversed umbrella type aerator of the centrifugal self-priming described in the claim 1; The surface that it is characterized in that described impeller body (1) is evenly distributed with three-phase mixing head group I, three-phase mixing head group II and three-phase mixing head group III; Include some three-phase mixing head I (3), some three-phase mixing head II (4) and some three-phase mixing head III (5) respectively in three-phase mixing head group I, three-phase mixing head group II and the three-phase mixing head group III; Each three-phase mixing head III (5) space in each three-phase mixing head I (3) in the three-phase mixing head group I, the three-phase mixing head group II in each three-phase mixing head II (4) and the three-phase mixing head group III is distributed in the surface of impeller body (1); The bottom of described impeller body is provided with guide shell I (6), guide shell II (7) and the guide shell III (8) of concentric setting; The caliber of guide shell I (6) is greater than the caliber of guide shell II (7); The caliber of guide shell II (7) is greater than the caliber of guide shell III (8); Guide shell I (6), guide shell II (7) and guide shell III (8) are extended stepped arrangement straight down according to the descending order of barrel dliameter; Be evenly distributed with some U trap I (14), some U trap II (12) and some U trap III (10) on the inwall of guide shell I (6), guide shell II (7) and guide shell III (8) respectively; Every U trap I (14) is connected with every three-phase mixing head I (3) respectively; Junction in U trap I (14) and three-phase mixing head I (3) is provided with negative pressure suction tube I (13); Every U trap II (12) is connected with every three-phase mixing head II (4) respectively; Junction in U trap II (12) and three-phase mixing head II (4) is provided with negative pressure suction tube II (11), and every U trap III (10) is connected with every three-phase mixing head III (5) respectively, is provided with negative pressure suction tube III (9) in (5) junction of U trap III (10) and three-phase mixing head III.
3. the hybrid inversed umbrella type aerator of centrifugal self-priming according to claim 2 is characterized in that described guide shell I (6), guide shell II (7) and guide shell III (8) extend stepped arrangement straight down according to the descending order of barrel dliameter.
4. the hybrid inversed umbrella type aerator of centrifugal self-priming according to claim 2; It is characterized in that said three-phase mixing head I (3) cross section is rectangle, circle, trilateral or Polygons; Three-phase mixing head II (4) cross section is rectangle, circle, trilateral or Polygons, and the cross section of three-phase mixing head III (5) is rectangle, circle, trilateral or Polygons.
5. the hybrid inversed umbrella type aerator of centrifugal self-priming according to claim 2 is characterized in that the cross section of said U trap I (14), U trap II (12) and U trap III (10) is rectangle, circle, trilateral or Polygons.
6. the hybrid inversed umbrella type aerator of centrifugal self-priming according to claim 2 is characterized in that described three-phase mixing head group I, three-phase mixing head group II and three-phase mixing head group III are distributed in the upper surface or the lower surface of impeller body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220136651XU CN202610041U (en) | 2012-04-01 | 2012-04-01 | Centrifugal self-absorption hybrid type inversed umbrella shaped aeration machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220136651XU CN202610041U (en) | 2012-04-01 | 2012-04-01 | Centrifugal self-absorption hybrid type inversed umbrella shaped aeration machine |
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| Publication Number | Publication Date |
|---|---|
| CN202610041U true CN202610041U (en) | 2012-12-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220136651XU Expired - Lifetime CN202610041U (en) | 2012-04-01 | 2012-04-01 | Centrifugal self-absorption hybrid type inversed umbrella shaped aeration machine |
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| Country | Link |
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| CN (1) | CN202610041U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102730854A (en) * | 2012-04-01 | 2012-10-17 | 张鑫珩 | Centrifugal self-suction mixing inverted umbrella-type aerator |
| CN106277382A (en) * | 2016-08-15 | 2017-01-04 | 亚太水处理(天长)有限公司 | A kind of Double-conical-surface surface aerating machine of inverted umbrella |
-
2012
- 2012-04-01 CN CN201220136651XU patent/CN202610041U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102730854A (en) * | 2012-04-01 | 2012-10-17 | 张鑫珩 | Centrifugal self-suction mixing inverted umbrella-type aerator |
| WO2013149557A1 (en) * | 2012-04-01 | 2013-10-10 | 中冶华天工程技术有限公司 | Centrifugal, self-aspirating, mixing inverse umbrella aeration machine |
| CN102730854B (en) * | 2012-04-01 | 2013-11-06 | 中冶华天工程技术有限公司 | Centrifugal self-suction mixing inverted umbrella-type aerator |
| US9382720B2 (en) | 2012-04-01 | 2016-07-05 | Huatian Engineering & Technology Corporation, Mcc | Centrifugal self-priming mixed and inverted-umbrella shaped aerator |
| CN106277382A (en) * | 2016-08-15 | 2017-01-04 | 亚太水处理(天长)有限公司 | A kind of Double-conical-surface surface aerating machine of inverted umbrella |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Free format text: FORMER OWNER: WANG YUEPING Effective date: 20130715 Owner name: ZHONGYE HUATIAN ENGINEERING TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: ZHANG XINHENG Effective date: 20130715 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 225400 TAIZHOU, JIANGSU PROVINCE TO: 243005 MAANSHAN, ANHUI PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130715 Address after: 243005 No. 25, Hunan Road, Anhui, Ma'anshan Patentee after: Zhongye Huatian Engineering Technology Co., Ltd. Address before: 225400, room 26, building seven, 104 National Day Village, Taixing, Jiangsu, Taizhou Patentee before: Zhang Xinhang Patentee before: Wang Yueping |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20121219 Effective date of abandoning: 20131106 |
|
| RGAV | Abandon patent right to avoid regrant |