CN221207172U - Steam-water separator - Google Patents
Steam-water separator Download PDFInfo
- Publication number
- CN221207172U CN221207172U CN202322959700.0U CN202322959700U CN221207172U CN 221207172 U CN221207172 U CN 221207172U CN 202322959700 U CN202322959700 U CN 202322959700U CN 221207172 U CN221207172 U CN 221207172U
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- water
- tank
- steam
- air inlet
- pipe
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 103
- 229910000831 Steel Inorganic materials 0.000 claims description 9
- 239000010959 steel Substances 0.000 claims description 9
- 230000000149 penetrating effect Effects 0.000 claims description 8
- 230000000903 blocking effect Effects 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims 2
- 239000002351 wastewater Substances 0.000 abstract description 25
- 239000007921 spray Substances 0.000 abstract description 18
- 230000000694 effects Effects 0.000 abstract description 17
- 230000000630 rising effect Effects 0.000 abstract description 15
- 238000000926 separation method Methods 0.000 abstract description 13
- 239000010802 sludge Substances 0.000 abstract description 11
- 238000005381 potential energy Methods 0.000 abstract description 8
- 230000002035 prolonged effect Effects 0.000 abstract description 6
- 239000012535 impurity Substances 0.000 abstract description 4
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006557 surface reaction Methods 0.000 description 1
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- Removal Of Floating Material (AREA)
Abstract
The utility model discloses a steam-water separator, which belongs to the technical field of wastewater treatment equipment and comprises a tank body, an end socket and a tank bottom, wherein the end socket and the tank bottom are respectively and fixedly connected to the top and the bottom of the tank body, an air outlet pipe is in through connection with the top center position of the end socket, a water return pipe is in through connection with the bottom center position of the tank bottom, a spray pipe is fixedly arranged on the inner wall of the tank body through a fixed bracket, the upper end of the spray pipe extends to the position right below the air outlet pipe, an upper water baffle plate, a lower water baffle plate and a water baffle cover can be matched by an upper air inlet pipe and a lower air inlet pipe, so that wastewater mixed in rising gas can be gradually separated, waste water potential energy is weakened, better and more efficient gas-water separation effects can be achieved, meanwhile, the spray pipe and a large-area high-pressure spray nozzle are additionally arranged, the inside the tank body can be sprayed at regular high pressure, the sludge impurity structure is prevented from being detained, and the service life of the steam-water separator is prolonged.
Description
Technical Field
The utility model relates to the technical field of wastewater treatment equipment, in particular to a steam-water separator.
Background
After mixing anaerobic sludge and wastewater in the anaerobic reactor, organic matters in the wastewater are decomposed into small molecular substances such as CH 4、CO2、H2 O and the like. CH 4 and CO 2 are in a gas state in a normal state, under the separation effect of a three-phase separator which is a component in the anaerobic reactor, the generated air pressure is larger because of larger biogas yield, CH 4 and CO 2 carry wastewater and a small amount of sludge to rush out upwards at a fast speed, if necessary measures are not taken for further separating the gas from the water, the gushing of the wastewater and the anaerobic sludge can pollute the environment, cause sense discomfort, damage equipment and reduce the service life of the anaerobic reactor.
Based on the above, the present inventors found that: on the basis of the separation of the three-phase separator of the traditional anaerobic reactor, a plurality of process designers can set one or more steam-water separators at the top of the anaerobic reactor to prevent the occurrence of the conditions, and meanwhile, the waste water separated by the steam-water separators is discharged along with the direct current of a return pipe, so that the stirring effect of the water distributor at the bottom of the anaerobic reactor is enhanced, the mud-water mixing effect is ensured, and the degradation effect of organic matters in an anaerobic tank is further ensured, but the traditional steam-water separators are simple in internal structure and poor in separation effect, and along with the time, anaerobic sludge on CH 4 and CO 2 is easily attached to the tank wall of the steam-water separators, thereby causing the influence of tank corrosion and volume reduction. The separated gas still brings a large amount of water and sludge, which is unfavorable for the operation of the anaerobic reactor, so that the prior structure is researched and improved for the reason, and the steam-water separator is provided for achieving the purpose of higher practical value.
Disclosure of utility model
1. Technical problem to be solved
Aiming at the problems existing in the prior art, the utility model aims to provide the steam-water separator, which can utilize an upper air inlet pipe, a lower air inlet pipe, an upper water baffle, a lower water baffle and a water baffle cover to gradually separate waste water mixed in rising air, weaken potential energy of the waste water so as to achieve better and more efficient gas-water separation effect, and meanwhile, a spray pipe and a large-area high-pressure spray nozzle are additionally arranged, so that the inside of a tank body can be sprayed at high pressure regularly, the structure of sludge impurities is prevented from being detained, and the service life of the steam-water separator is prolonged.
2. Technical proposal
In order to solve the problems, the utility model adopts the following technical scheme.
The utility model provides a steam-water separator, includes the jar body, head and tank bottoms are fixedly connected with in the top and the bottom of the jar body respectively, the top central point of head puts through-connection has the outlet duct, the bottom central point of tank bottoms puts through-connection has the water reflux pipe, the inner wall of the jar body has the shower through fixed bolster fixed mounting, the upper end of shower extends to under the outlet duct, the lower extreme of shower extends to the outside of the jar body to fixed mounting has the shower nozzle, the upper water baffle and the lower floor water baffle of fixedly connected with respectively of jar body both sides inner wall, the upper water baffle sets up in the top position of lower floor water baffle.
Further, the jar body is cylindrical barrel form structure, the head is butterfly-shaped structure, the tank bottoms is the toper structure, the periphery through-connection of the jar body has the scraper sight glass that two symmetries set up, the top edge position through-connection of head has the blow-down pipe.
Further, the upper water baffle and the lower water baffle are both lifted by an angle of 30 degrees at one end close to the middle part of the tank body, and the enclosing and blocking angles are 180 degrees.
Further, the both sides of the jar body are respectively through-connected with upper intake pipe and lower floor's intake pipe, upper intake pipe is located the below of upper water baffle, lower floor's intake pipe is located the below of lower water baffle.
Further, the upper layer air inlet pipe and the lower layer air inlet pipe are arranged at an angle of 45 degrees downwards at one end of the tank body.
Further, the inside of head is through connecting piece fixedly connected with manger plate cover, manger plate cover is located under the outlet duct.
Further, four steel pipe supports are fixedly connected to the bottom of the tank bottom and are uniformly distributed, and a bottom plate is fixedly connected to the bottom end of each steel pipe support.
3. Advantageous effects
Compared with the prior art, the utility model has the advantages that:
(1) According to the scheme, the upper water baffle and the lower water baffle are matched through the upper air inlet pipe and the lower air inlet pipe, the rotational flow formed by the two air and water mixtures can be refracted through the reaction of the upper water baffle and the lower water baffle in the rising process, the pressure is released, the waste water potential energy is gradually separated, and the waste water potential energy can be further prevented from rising continuously. And the gas can not weaken the continuous rising capability of the gas, so that better and more efficient gas-water separation effect is achieved, meanwhile, the water retaining cover is additionally arranged, and the residual wastewater in the rising gas is finally cut and separated, so that the best gas-water separation effect is achieved.
(2) According to the scheme, through the additionally arranged spray pipe and the large-area high-pressure spray nozzle, the inside of the tank body can be sprayed and washed at regular intervals, the sludge impurity structure is prevented from being detained, and the service life of the steam-water separator is prolonged.
Drawings
FIG. 1 is a schematic perspective view of the present utility model;
FIG. 2 is a schematic view of the bottom view of the present utility model;
FIG. 3 is a schematic view of a partial cross-sectional structure of the present utility model;
fig. 4 is a schematic view of the internal structure of the present utility model.
The reference numerals in the figures illustrate:
1. A tank body;
2. A seal head;
3. a tank bottom;
4. An air outlet pipe;
5. a water return pipe;
6. A fixed bracket;
7. A shower pipe;
8. A spray head;
9. an upper water baffle;
10. A lower water baffle;
11. Scraper view mirror;
12. Blow-down pipe;
13. an upper layer air inlet pipe;
14. A lower air inlet pipe;
15. A connecting piece;
16. A water retaining cover;
17. Supporting a steel pipe;
18. A bottom plate.
Detailed Description
The technical solutions in the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model; it is apparent that the described embodiments are only some embodiments of the present utility model, not all embodiments, and that all other embodiments obtained by persons of ordinary skill in the art without making creative efforts based on the embodiments in the present utility model are within the protection scope of the present utility model.
Examples:
Referring to fig. 1-4, a steam-water separator comprises a tank body 1, an end socket 2 and a tank bottom 3, wherein the end socket 2 and the tank bottom 3 are respectively and fixedly connected to the top and the bottom of the tank body 1, the air outlet pipe 4 is connected to the central position of the top of the end socket 2 in a penetrating way, the water return pipe 5 with a large pipe diameter is connected to the central position of the bottom of the tank bottom 3 in a penetrating way, waste water can quickly and rapidly descend to the bottom of an anaerobic reactor without resistance through the water return pipe 5 with a large pipe diameter, the waste water is prevented from accumulating, the bottom stirring effect is realized, the whole system can smoothly and efficiently run, the aim of efficiently degrading organic matters of the anaerobic reactor is realized, the inner wall of the tank body 1 is fixedly provided with a spray pipe 7 through a fixed support 6, the upper end of the spray pipe 7 extends to the lower part of the air outlet pipe 4, the lower end of the spray pipe 7 extends to the outer part of the tank body 1, a spray pipe 8 is fixedly provided with a spray pipe 8 through the cooperation of the spray pipe 7 and the high pressure spray pipe 8, the inside of the tank body 1 can be regularly sprayed at a high pressure, the structure of the waste water is prevented, the service life of the steam-water separator is prolonged, the upper water baffle 10 and the lower water baffle are respectively fixedly arranged on the two inner walls of the tank body 1.
Referring to fig. 1 and 2, the tank 1 is in a cylindrical barrel-shaped structure, the seal head 2 is in a butterfly-shaped structure, the tank bottom 3 is in a conical structure, two scraper view mirrors 11 which are symmetrically arranged are connected with the periphery of the tank 1 in a penetrating manner, a blow-down pipe 12 is connected with the top edge position of the seal head 2 in a penetrating manner, when the tank is in a cylindrical barrel shape, the size of the tank 1 is 2.2m in diameter, the height of the tank is 2.2m, the height-diameter ratio is 1:1, the requirement of the running perimeter path of the linear speed in the circular arc direction is met, the height requirement of upward running of gas in the vertical direction and the height requirement of downward backflow of mud water are met, and the mud water separation effect is enhanced. Secondly, the design of the cone-shaped tank bottom 3 is very beneficial to the falling and collecting and flowing out of the muddy water, and the adhesion of the accumulated water and the sludge in the tank is ensured. Finally, the butterfly-shaped seal head 2 is designed, and the smooth arc shape is helpful for slowing down the pressure of the gas. When gas upwards gushes out, the cambered surface reaction force can effectively slow down vibration in the tank, the area is larger than that of a horizontal plane, the waste water and the sludge are scattered and fall back at a slower speed while the gas pressure is dispersed, and the gas-water separation effect is enhanced. The outlet duct 4 sets up the highest point at butterfly head 2, and the gaseous rising and the output of being convenient for, and the gaseous coming of production is then gone out, does not have the phenomenon of deposit, simultaneously, two scraper sight glass 11 that set up can be convenient for observe the running situation in the vapour and water separator jar, and then through the running situation of producing the gas state analysis anaerobic reactor.
Referring to fig. 3 and 4, the upper water baffle 9 and the lower water baffle 10 are both raised at an angle of 30 degrees at one end close to the middle of the tank body 1, and the enclosing and blocking angles are 180 degrees, when the tank is used, after the gas such as methane is introduced into the tank through the arrangement of the upper water baffle 9 and the lower water baffle 10, the two gas and water mixtures form rotational flow, and the rotational flow is refracted through the reaction of the upper water baffle 9 and the lower water baffle 10 in the rising process, so that the pressure is released, the waste water potential energy is gradually separated, and the waste water potential energy is weakened, so that the continuous rising of the waste water can be prevented. And the gas can not weaken the continuous rising capability of the gas, so that better and more efficient gas-water separation effect is achieved.
Referring to fig. 3 and 4, two sides of the tank 1 are respectively connected with an upper air inlet pipe 13 and a lower air inlet pipe 14 in a penetrating manner, the upper air inlet pipe 13 is located below the upper water baffle 9, the lower air inlet pipe 14 is located below the lower water baffle 10, one ends of the upper air inlet pipe 13 and the lower air inlet pipe 14 located in the tank 1 are all inclined downwards by 45 degrees, and when the three-phase separator is used, release of different gas pressures of the upper three-phase separator and the lower three-phase separator can be met through the upper air inlet pipe 13 and the lower air inlet pipe 14 with inconsistent heights. The release positions of the inner tank openings of the upper air inlet pipe 13 and the lower air inlet pipe 14 are inclined downwards by an angle of 45 degrees, firstly, waste water is released to the tank bottom 3 conveniently, secondly, a rotational flow state is formed in the tank, the gas-water release path is prolonged, and the gas state and the liquid state are better separated.
Referring to fig. 4, the inside of the seal head 2 is fixedly connected with a water retaining cover 16 through a connecting piece 15, the water retaining cover 16 is located under the air outlet pipe 4, and when in use, residual wastewater in rising air can be finally cut and separated through the arranged water retaining cover 16 located under the pipe orifice of the air outlet pipe 4, so that the best air-water separation effect is achieved.
Referring to fig. 2, four steel pipe supports 17 are fixedly connected to the bottom of the tank bottom 3, the four steel pipe supports 17 are uniformly distributed, and a bottom plate 18 is fixedly connected to the bottom end of the steel pipe supports 17.
When in use: after gas such as methane enters the steam-water separator through the upper air inlet pipe 13 and the lower air inlet pipe 14, the upper water baffle 9 and the lower water baffle 10 are arranged, after the gas such as methane is introduced into the steam-water separator, the two gas and water mixtures form rotational flow, and the rotational flow is refracted through the reaction of the upper water baffle 9 and the lower water baffle 10 in the rising process, so that the pressure is released, the waste water potential energy is gradually separated, and the waste water potential energy is weakened, so that the waste water can be prevented from rising continuously. The gas can not weaken the continuous rising capability of the gas, so that better and more efficient gas-water separation effect is achieved, meanwhile, the water retaining cover 16 is additionally arranged, residual wastewater in rising gas is finally cut and separated, the best gas-water separation effect is achieved, then the lower end of the spray pipe 7 is connected with an external water source, under the matched use of the large-area high-pressure spray head 8, the inside of the tank body 1 can be sprayed and washed at high pressure regularly, the sludge impurity structure is prevented from being detained, and the service life of the steam-water separator is prolonged.
Finally, it should be noted that: in the description of the present utility model, it should be noted that the azimuth or positional relationship indicated by the terms "vertical", "upper", "lower", "horizontal", etc. are based on the azimuth or positional relationship shown in the drawings, and are merely for convenience of describing the present utility model and simplifying the description, and do not indicate or imply that the apparatus or element referred to must have a specific azimuth, be constructed and operated in a specific azimuth, and thus should not be construed as limiting the present utility model.
In the description of the present utility model, it should also be noted that, unless explicitly specified and limited otherwise, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present utility model can be understood by those of ordinary skill in the art according to the specific circumstances.
The above description is only of the preferred embodiments of the present utility model; the scope of the utility model is not limited in this respect. Any person skilled in the art, within the technical scope of the present disclosure, may apply to the present utility model, and the technical solution and the improvement thereof are all covered by the protection scope of the present utility model.
Claims (7)
1. The utility model provides a steam-water separator, includes jar body (1), head (2) and tank bottoms (3), its characterized in that: the utility model discloses a jar of jar, including jar body (1) and bottom, head (2) and tank bottoms (3) are fixed connection respectively, the top central point of head (2) puts through-connection has outlet duct (4), the bottom central point of tank bottoms (3) puts through-connection has water back flow (5), the inner wall of jar body (1) has shower (7) through fixed bolster (6) fixed mounting, the upper end of shower (7) extends to under outlet duct (4), the lower extreme of shower (7) extends to the outside of jar body (1) to fixed mounting has shower nozzle (8), the upper water baffle (9) and lower floor water baffle (10) of jar body (1) both sides inner wall fixedly connected with respectively, upper water baffle (9) set up in the top position of lower floor water baffle (10).
2. The steam-water separator according to claim 1, wherein: the novel energy-saving tank is characterized in that the tank body (1) is of a cylindrical barrel-shaped structure, the sealing head (2) is of a butterfly-shaped structure, the tank bottom (3) is of a conical structure, two scraper sight glass (11) which are symmetrically arranged are connected with the periphery of the tank body (1) in a penetrating manner, and a blow-down pipe (12) is connected with the edge of the top of the sealing head (2) in a penetrating manner.
3. The steam-water separator according to claim 1, wherein: the upper water baffle (9) and the lower water baffle (10) are raised by an angle of 30 degrees at one end close to the middle of the tank body (1), and the enclosing and blocking angles are 180 degrees.
4. The steam-water separator according to claim 1, wherein: the two sides of the tank body (1) are respectively connected with an upper air inlet pipe (13) and a lower air inlet pipe (14) in a penetrating way, the upper air inlet pipe (13) is positioned below the upper water baffle (9), and the lower air inlet pipe (14) is positioned below the lower water baffle (10).
5. The steam-water separator as set forth in claim 4, wherein: the upper layer air inlet pipe (13) and the lower layer air inlet pipe (14) are arranged at an angle of 45 degrees downwards at one end of the tank body (1).
6. The steam-water separator according to claim 1, wherein: the inside of head (2) is through connecting piece (15) fixedly connected with manger plate cover (16), manger plate cover (16) are located under outlet duct (4).
7. The steam-water separator according to claim 1, wherein: the bottom of the tank bottom (3) is fixedly connected with four steel pipe supports (17), the four steel pipe supports (17) are uniformly distributed, and the bottom end of each steel pipe support (17) is fixedly connected with a bottom plate (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322959700.0U CN221207172U (en) | 2023-11-02 | 2023-11-02 | Steam-water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322959700.0U CN221207172U (en) | 2023-11-02 | 2023-11-02 | Steam-water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221207172U true CN221207172U (en) | 2024-06-25 |
Family
ID=91565252
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322959700.0U Active CN221207172U (en) | 2023-11-02 | 2023-11-02 | Steam-water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221207172U (en) |
-
2023
- 2023-11-02 CN CN202322959700.0U patent/CN221207172U/en active Active
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant |