CN220398276U - Steam condensation recycling system - Google Patents
Steam condensation recycling system Download PDFInfo
- Publication number
- CN220398276U CN220398276U CN202321688853.XU CN202321688853U CN220398276U CN 220398276 U CN220398276 U CN 220398276U CN 202321688853 U CN202321688853 U CN 202321688853U CN 220398276 U CN220398276 U CN 220398276U
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- Prior art keywords
- gas
- liquid separation
- pipeline
- separation tank
- steam
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- 238000004064 recycling Methods 0.000 title claims abstract description 21
- 238000009833 condensation Methods 0.000 title claims abstract description 18
- 230000005494 condensation Effects 0.000 title claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 102
- 238000000926 separation method Methods 0.000 claims abstract description 87
- 230000017525 heat dissipation Effects 0.000 claims abstract description 22
- 238000002955 isolation Methods 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000007599 discharging Methods 0.000 claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims description 13
- 125000006850 spacer group Chemical group 0.000 claims description 3
- 238000001816 cooling Methods 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 238000001035 drying Methods 0.000 abstract description 6
- 239000002994 raw material Substances 0.000 abstract description 5
- 239000012153 distilled water Substances 0.000 abstract description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- QHPQWRBYOIRBIT-UHFFFAOYSA-N 4-tert-butylphenol Chemical compound CC(C)(C)C1=CC=C(O)C=C1 QHPQWRBYOIRBIT-UHFFFAOYSA-N 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000008234 soft water Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to the technical field of steam condensation recycling, in particular to a steam condensation recycling system. The steam condensation recycling system comprises a reaction kettle, a gas-liquid separation tank, a wind cooler and a condensate collecting tank, wherein the reaction kettle is connected with the gas-liquid separation tank through a gas inlet-liquid separation tank pump, the gas-liquid separation tank is connected with the wind cooler through a gas-liquid separation tank discharging pump, the wind cooler is connected with the condensate collecting tank through a pipeline, a separation disc is arranged in the gas-liquid separation tank, and a U-shaped heat dissipation pipeline is arranged in the wind cooler. Through the arrangement of the isolation disc, gas and liquid can be physically separated, and distilled water below can play a role in preserving heat for steam above; the energy of the residual steam is used for drying the raw materials through the arrangement of the dryer, so that the drying cost is greatly reduced; through the setting of wind-force cooler, the speed of comdenstion water cooling has been accelerated for the comdenstion water after the cooling can be used for production rapidly, has improved production efficiency.
Description
Technical Field
The utility model relates to the technical field of steam condensation recycling, in particular to a steam condensation recycling system.
Background
In the process of producing p-tert-butylphenol in workshops, a large amount of steam is required to supply heat for the whole reaction so as to improve the reaction efficiency. After a large amount of steam exchanges heat, a large amount of condensed water is generated, and the heat exchange efficiency is not influenced.
In the existing workshop production, condensate is only recovered, but huge heat energy existing in a mixture of condensate and steam is ignored, so that not only is energy wasted, but also the production cost of enterprises is greatly increased. In particular, the condensed water can be directly used as soft water for production after being cooled.
Disclosure of Invention
According to the defects in the prior art, the utility model aims to provide a steam condensation recycling system, gas and liquid are physically separated through the arrangement of the isolation disc, and distilled water below can play a role in heat preservation of steam above; the energy of the residual steam is used for drying the raw materials through the arrangement of the dryer, so that the drying cost is greatly reduced; through the setting of wind-force cooler, the speed of comdenstion water cooling has been accelerated for the comdenstion water after the cooling can be used for production rapidly, has improved production efficiency.
The utility model is realized by adopting the following technical scheme:
the steam condensation recycling system comprises a reaction kettle, a gas-liquid separation tank, a wind cooler and a condensate collecting tank, wherein the reaction kettle is connected with the gas-liquid separation tank through a gas inlet-liquid separation tank pump, the gas-liquid separation tank is connected with the wind cooler through a gas-liquid separation tank discharging pump, the wind cooler is connected with the condensate collecting tank through a pipeline, a separation disc is arranged in the gas-liquid separation tank, and a U-shaped heat dissipation pipeline is arranged in the wind cooler.
The gas-liquid separation tank is used for separating gas and liquid, the gas-liquid is physically isolated through the isolating disc, the wind power cooler is used for cooling condensate, the condensate collecting tank is used for temporarily storing condensate, and the U-shaped heat dissipation pipeline is used for increasing heat exchange area.
The reaction kettle is internally provided with a heating coil, one end of the heating coil is connected with a steam inlet pipeline, and one end of the heating coil is connected with an inlet liquid separation tank pump through a pipeline.
The gas-liquid separation tank is connected with the dryer through a dryer inlet pipeline, the dryer is connected with the steam trap through a pipeline, and the liquid outlet end of the steam trap is connected with the gas-liquid separation tank through a steam trap liquid outlet pipeline.
The dryer is internally provided with a dryer guide plate, the dryer is provided with a dryer gas-liquid outlet, and the gas outlet end of the steam trap is connected with a water separator gas outlet pipeline. The dryer deflector is used for guiding the generated condensate.
The isolation disc is arranged in a concave mode, the one-way valve is arranged in the center of the isolation disc, and the isolation disc is provided with isolation disc guide edges.
The gas-liquid separation tank discharging pump is connected with a gas-liquid separation tank discharging pump pipeline between the gas-liquid separation tank discharging pump and the wind power cooler, the gas-liquid separation tank discharging pump pipeline is connected with a heat inlet exchanger pipeline through a tee joint, the heat inlet exchanger pipeline is connected with a heat exchanger, and the heat exchanger is connected with the gas-liquid separation tank through a heat outlet exchanger pipeline. The heat exchanger is used for heating tap water, and the heated tap water can be used for bathing.
The discharging pump pipeline of the gas-liquid separation tank is connected with a U-shaped heat dissipation pipeline, a heat dissipation plate is arranged on the U-shaped heat dissipation pipeline, and heat dissipation holes are formed in the heat dissipation plate.
The wind cooler is connected with an air inlet pipeline, and an air outlet is arranged on the wind cooler.
The working principle of the utility model is as follows:
the steam enters a heating coil pipe through a steam inlet pipeline to heat the reaction raw materials, then enters a gas-liquid separation tank through a gas inlet-liquid separation tank pump, liquid enters the lower part of the gas-liquid separation tank along a guide edge of a separation disc under the action of gravity, and gas is left at the upper part of the gas-liquid separation tank; the gas at the upper part of the gas-liquid separation tank enters a dryer through a dryer inlet pipeline, enters a steam trap after heat exchange of the dryer, enters a next device through a steam trap outlet pipeline, and returns liquid to the gas-liquid separation tank through a steam trap outlet pipeline; part of condensate in the gas-liquid separation tank enters a heat exchanger through a discharge pump of the gas-liquid separation tank, and returns to the gas-liquid separation tank through a pipeline of the heat exchanger after heat exchange is completed; part of condensate in the gas-liquid separation tank enters the wind cooler through a discharge pump of the gas-liquid separation tank, and cooled condensate enters a condensate collecting tank for storage. The gas-liquid separation tank is used for separating gas and liquid, the gas-liquid physical separation is realized through the separation disc, the wind power cooler is used for cooling condensate, the condensate collection tank is used for temporarily storing condensate, and the U-shaped heat dissipation pipeline is used for increasing heat exchange area.
Compared with the prior art, the utility model has the beneficial effects that:
by adopting the steam condensation recycling system, the gas and the liquid can be physically separated through the arrangement of the isolation disc, and the distilled water below can play a role in preserving heat for the steam above; the energy of the residual steam is used for drying the raw materials through the arrangement of the dryer, so that the drying cost is greatly reduced; through the setting of wind-force cooler, the speed of comdenstion water cooling has been accelerated for the comdenstion water after the cooling can be used for production rapidly, has improved production efficiency.
Drawings
FIG. 1 is a schematic diagram of a vapor condensation recycling system of the present utility model;
FIG. 2 is a schematic diagram of the structure of the spacer disc of the present utility model;
FIG. 3 is a schematic diagram of a heat sink according to the present utility model;
in the figure: 1. a reaction kettle; 2. a gas-liquid separation tank; 3. a wind cooler; 4. a condensate collection tank; 5. a dryer; 6. a heat exchanger; 7. a steam trap; 8. a heating coil; 9. steam enters the pipeline; 10. an inlet gas-liquid separation tank pump; 11. a spacer disc; 12. a dryer inlet conduit; 13. a dryer baffle; 14. a dryer gas-liquid outlet; 15. a steam trap liquid outlet pipeline; 16. an air outlet pipeline of the water separator; 17. a gas-liquid separation tank discharge pump; 18. a discharge pump pipeline of the gas-liquid separation tank; 19. a heat exchanger inlet pipe; 20. a heat exchanger outlet pipe; 21. u-shaped heat dissipation pipelines; 22. a heat sink; 23. an air outlet; 24. an air inlet pipeline; 25. guide ribs of the isolating disc; 26. a heat radiation hole; 27. a one-way valve.
Detailed Description
The present utility model will be described in further detail with reference to the accompanying drawings, in order to make the objects and technical solutions of the present utility model more apparent.
Example 1
As shown in fig. 1-3, the steam condensation recycling system comprises a reaction kettle 1, a gas-liquid separation tank 2, a wind cooler 3 and a condensate collecting tank 4, wherein the reaction kettle 1 is connected with the gas-liquid separation tank 2 through a gas inlet-liquid separation tank pump 10, the gas-liquid separation tank 2 is connected with the wind cooler 3 through a gas-liquid separation tank discharging pump 17, the wind cooler 3 is connected with the condensate collecting tank 4 through a pipeline, a separation disc 11 is arranged in the gas-liquid separation tank 2, and a U-shaped heat dissipation pipeline 21 is arranged in the wind cooler 3. The gas-liquid separation tank 2 is used for separating gas and liquid, the gas-liquid physical separation is carried out through the separation disc 11, the wind power cooler 3 is used for cooling condensate, the condensate collecting tank 4 is used for temporarily storing condensate, the heating coil 8 is arranged in the reaction kettle 1, one end of the heating coil 8 is connected with a steam inlet pipeline 9, and one end of the heating coil 8 is connected with the gas-liquid separation tank pump 10 through the pipeline. The gas-liquid separation tank 2 is connected with the dryer 5 through a dryer inlet pipeline 12, the dryer 5 is connected with the steam trap 7 through a pipeline, and the liquid outlet end of the steam trap 7 is connected with the gas-liquid separation tank 2 through a steam trap liquid outlet pipeline 15. The dryer 5 is internally provided with a dryer guide plate 13, the dryer 5 is provided with a dryer gas-liquid outlet 14, and the air outlet end of the steam trap 7 is connected with a water separator air outlet pipeline 16. The isolation disc 11 is arranged in a concave mode, the center of the isolation disc 11 is provided with a one-way valve 27, and the isolation disc 11 is provided with an isolation disc guide rib 25. A gas-liquid separation tank discharge pump pipeline 18 is connected between the gas-liquid separation tank discharge pump 17 and the wind power cooler 3, a heat inlet exchanger pipeline 19 is connected to the gas-liquid separation tank discharge pump pipeline 18 through a tee joint, a heat exchanger 6 is connected to the heat inlet exchanger pipeline 19, and the heat exchanger 6 is connected with the gas-liquid separation tank 2 through a heat outlet exchanger pipeline 20. The discharging pump pipeline 18 of the gas-liquid separation tank is connected with a U-shaped heat dissipation pipeline 21, a heat dissipation plate 22 is arranged on the U-shaped heat dissipation pipeline 21, and a heat dissipation hole 26 is arranged on the heat dissipation plate 22. The wind cooler 3 is connected with an air inlet pipeline 24, and the wind cooler 3 is provided with an air outlet 23.
The steam condensation recycling system comprises the following steps when in operation:
(1) The steam enters a heating coil 8 through a steam inlet pipeline 9 to heat the reaction raw materials, then enters a gas-liquid separation tank 2 through an air inlet-liquid separation tank pump 10, liquid enters the lower part of the gas-liquid separation tank 2 along a separation disc guide rib 25 under the action of gravity, and gas is left at the upper part of the gas-liquid separation tank 2; (2) The gas at the upper part of the gas-liquid separation tank 2 enters the dryer 5 through a dryer inlet pipeline 12, enters the steam trap 7 after heat exchange of the dryer 5, enters the next device through a steam trap outlet pipeline 16, and returns the liquid to the gas-liquid separation tank 2 through a steam trap outlet pipeline 15; (3) Part of condensate in the gas-liquid separation tank 2 enters the heat exchanger 6 through the gas-liquid separation tank discharge pump 17, and returns to the gas-liquid separation tank 2 through the heat exchanger outlet pipeline 20 after heat exchange is completed; (4) Part of condensate in the gas-liquid separation tank 2 enters the wind cooler 3 through the gas-liquid separation tank discharge pump 17, and cooled condensate enters the condensate collection tank 4 for storage.
Claims (8)
1. The utility model provides a steam condensation recycling system, a serial communication port, including reation kettle (1), gas-liquid separation jar (2), wind-force cooler (3), condensate collection tank (4), reation kettle (1) link to each other with gas-liquid separation jar (2) through inlet air liquid separation jar pump (10), gas-liquid separation jar (2) link to each other with wind-force cooler (3) through gas-liquid separation jar discharging pump (17), wind-force cooler (3) link to each other with condensate collection tank (4) through the pipeline, be equipped with spacer disc (11) in gas-liquid separation jar (2), be equipped with U type heat dissipation pipeline (21) in wind-force cooler (3).
2. The steam condensation recycling system according to claim 1, wherein a heating coil (8) is arranged in the reaction kettle (1), one end of the heating coil (8) is connected with a steam inlet pipeline (9), and one end of the heating coil (8) is connected with an air inlet liquid separation tank pump (10) through a pipeline.
3. The steam condensing and recycling system according to claim 1, wherein the gas-liquid separation tank (2) is connected with the dryer (5) through a dryer inlet pipeline (12), the dryer (5) is connected with the steam trap (7) through a pipeline, and the liquid outlet end of the steam trap (7) is connected with the gas-liquid separation tank (2) through a steam trap liquid outlet pipeline (15).
4. A steam condensing, recycling and reusing system according to claim 3, characterized in that a dryer guide plate (13) is arranged in the dryer (5), a dryer gas-liquid outlet (14) is arranged on the dryer (5), and the air outlet end of the steam trap (7) is connected with a water separator air outlet pipeline (16).
5. The steam condensing, recycling and reusing system according to claim 1, wherein the isolation disc (11) is arranged in a concave manner, a one-way valve (27) is arranged in the center of the isolation disc (11), and an isolation disc guide rib (25) is arranged on the isolation disc (11).
6. The steam condensation recycling system according to claim 1, wherein a gas-liquid separation tank discharging pump pipeline (18) is connected between the gas-liquid separation tank discharging pump (17) and the wind power cooler (3), a gas-liquid separation tank discharging pump pipeline (18) is connected with a heat inlet pipeline (19) through a tee joint, a heat exchanger (6) is connected to the heat inlet pipeline (19), and the heat exchanger (6) is connected with the gas-liquid separation tank (2) through a heat outlet pipeline (20).
7. The vapor condensation recycling system according to claim 6, wherein the discharging pump pipeline (18) of the vapor-liquid separation tank is connected with a U-shaped heat dissipation pipeline (21), the U-shaped heat dissipation pipeline (21) is provided with heat dissipation fins (22), and the heat dissipation fins (22) are provided with heat dissipation holes (26).
8. The steam condensation recycling system according to claim 1, wherein the wind cooler (3) is connected with an air inlet pipeline (24), and an air outlet (23) is arranged on the wind cooler (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321688853.XU CN220398276U (en) | 2023-06-30 | 2023-06-30 | Steam condensation recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321688853.XU CN220398276U (en) | 2023-06-30 | 2023-06-30 | Steam condensation recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220398276U true CN220398276U (en) | 2024-01-26 |
Family
ID=89602592
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321688853.XU Active CN220398276U (en) | 2023-06-30 | 2023-06-30 | Steam condensation recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220398276U (en) |
-
2023
- 2023-06-30 CN CN202321688853.XU patent/CN220398276U/en active Active
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