CN219157852U - Bitter water direct drinking and heat supply dual-supply integrated system - Google Patents
Bitter water direct drinking and heat supply dual-supply integrated system Download PDFInfo
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- CN219157852U CN219157852U CN202223493491.7U CN202223493491U CN219157852U CN 219157852 U CN219157852 U CN 219157852U CN 202223493491 U CN202223493491 U CN 202223493491U CN 219157852 U CN219157852 U CN 219157852U
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Abstract
The utility model relates to the technical field of brackish water heat supply, in particular to a brackish water direct drinking and heat supply dual-supply integrated system, which comprises a high-level water tank, wherein a water inlet end of the high-level water tank is provided with a first water pump, a water outlet end of the first water pump is provided with an exchanger, one end of the exchanger is provided with a separator A and a separator B respectively, and one ends of the separator A and the separator B are connected with a heat supply furnace; when the water temperature of the separator A reaches a certain temperature, the high-level water tank supplements water for the separator B through the exchanger, and after the steam is cooled through the exchanger, part of condensate is filtered through the PP filter and enters the direct-drinking water tank. And part of the condensate enters a heat storage box, and the heat storage box is used for heat preservation by supplying heat to a heat furnace to perform night heating or perform heating to an ecological pool. The separator A evaporates to a certain extent, the concentrated water is pumped into the greenhouse by the water pump to heat the greenhouse, and the greenhouse enters the airing pool for airing after heat exchange is finished. Finally, coarse salt is formed.
Description
Technical Field
The utility model relates to the technical field of brackish water heat supply, in particular to a brackish water direct drinking and heat supply dual-supply integrated system.
Background
In the alpine regions of China, such as Xinjiang, tibet, inner Mongolia and the like, the ground water is brackish water generally, and the state of electricity deficiency and coal deficiency is also realized, and in the remote alpine regions, some sentry posts, scenic spots and the like, water drinking and heating are difficult problems. In alpine regions, reverse osmosis desalination systems cannot be used due to the fact that the weather is too cold. The heating problem is not solved because of the lack of fresh water. The system solves the problems of direct drinking and heating of brackish water under the current situation of electricity deficiency and coal deficiency.
Disclosure of Invention
In order to solve the technical problems in the background art, the utility model provides a brackish water direct drinking and heat supply dual integrated system, which comprises a high-level water tank, wherein a first water pump is arranged at the water inlet end of the high-level water tank, an exchanger is arranged at the water outlet end of the first water pump, a separator A and a separator B are respectively arranged at one end of the exchanger, a heat supply furnace is respectively connected at one ends of the separator A and the separator B, a PP filter and a heat storage tank are respectively arranged at the other ends of the exchanger, a direct drinking water tank is arranged at one end of the PP filter, one end of the heat storage tank is connected with the heat supply furnace, a second water pump is arranged at one end of the heat storage tank, a third water pump is arranged at the other ends of the separator A and the separator B, and the water outlet end of the third water pump is connected with a greenhouse.
Preferably, the structure of the separator A and the structure of the separator B are the same, the separator A comprises a heat conducting oil layer, the heat conducting oil layer is sleeved on the outer wall of the separator A, the outer wall of the heat conducting oil layer is sleeved with an insulating layer, a water inlet is arranged on one side of the outer wall of the separator A, the water inlet is connected with the exchanger, a water outlet is arranged at the bottom of the separator A, a heat conducting oil inlet is arranged on one side of the bottom of the separator A, the heat conducting oil inlet is connected with one end of the heat supply furnace, a heat conducting oil outlet is arranged on one side of the top of the heat conducting oil layer, the heat conducting oil outlet is connected with the other end of the heat supply furnace, a steam outlet is arranged on one side of the top of the separator A, an exhaust port is arranged on the other side of the top of the separator A, and a heat conducting oil outlet is arranged on the other side of the top of the heat conducting oil layer.
Preferably, the top of the separator A and the top of the separator B are also provided with a pressure gauge port and a safety valve port, and the bottom and the top of the inner sides of the separator A and the separator B are respectively provided with a water level gauge.
Preferably, the separator A evaporates to a certain extent, the concentrated water is pumped to the greenhouse by the third water pump to heat the greenhouse, and the concentrated water enters the airing pool for airing after heat exchange is finished to form coarse salt.
Preferably, the heat supply furnace adopts coal or other solid fuel, the heating mode adopts heat conduction oil, the external supply temperature of the heat conduction oil is adjustable, and the temperature is required to be less than 175 ℃.
Preferably, the separator A and the separator B are titanium alloy evaporation exchangers, and 2 separators are arranged in total and alternately operated.
Preferably, the PP filter accuracy is required to be less than 5um.
Preferably, the ratio of evaporated fresh water to concentrated water during evaporation in the separator a and the separator B cannot exceed: 6:4.
Preferably, the height of the head tank is required to be > 6m in order to supply water to the exchanger and separator a and the separator B.
Preferably, the airing pool needs to be subjected to anti-corrosion and anti-seepage operation.
Compared with the prior art, the technical scheme provided by the utility model has the following beneficial technical effects: the utility model relates to a heat supply furnace, a separator A, a separator B, an exchanger, a PP filter, a direct drinking water tank, a heat storage tank, a high-level water tank, a greenhouse and a drying pool. When the system is operated, the brackish water is lifted to the high-level water tank from the inside of the well by a water pump. As a make-up water source for separator A and separator B, and as a cold source for the exchanger. The high-level water tank is used for supplementing water to one of the separators A, after supplementing water to a certain water level, the hot furnace is started to heat the separator A, the hot furnace adopts coal or other solid fuels, the heating mode adopts heat conduction oil, the external supply temperature of the heat conduction oil is adjustable, the requirement is less than 175 ℃, when the water temperature of the separator A reaches a certain temperature, the high-level water tank is used for supplementing water to the separator B through the exchanger, and after the steam is cooled through the exchanger, a part of condensate is filtered through the PP filter and enters the direct-drinking water tank. And part of the condensate enters a heat storage box, and the heat storage box is used for heat preservation by supplying heat to a heat furnace to perform night heating or perform heating to an ecological pool. The separator A evaporates to a certain extent, the concentrated water is pumped into the greenhouse by the water pump to heat the greenhouse, and the greenhouse enters the airing pool for airing after heat exchange is finished. Finally, coarse salt is formed.
Drawings
FIG. 1 is a schematic diagram of the overall flow of the first embodiment;
fig. 2 is a schematic diagram of the structure of the separator a according to the present utility model.
Reference numerals: 1. a high level water tank; 2. a first water pump; 3. a separator A; 31. a thermally conductive oil layer; 32. a heat preservation layer; 33. a water inlet; 34. a water outlet; 35. a conduction oil inlet; 36. a heat transfer oil outlet; 37. a steam outlet; 38. an exhaust port; 39. a conduction oil exhaust port; 4. a separator B; 5. an exchanger; 6. a heat supply furnace; 7. a PP filter; 8. a direct-drinking water tank; 9. a heat storage tank; 10. a second water pump; 11. a third water pump; 12. a greenhouse; 13. and (5) airing the pond.
Detailed Description
Example 1
As shown in fig. 1, the brackish water direct drinking and heat supply integrated system provided by the utility model comprises a high-level water tank 1, wherein the height requirement of the high-level water tank 1 is more than 6m so as to supply water to an exchanger 5 and a separator A3 and a separator B4, a first water pump 2 is arranged at the water inlet end of the high-level water tank 1, an exchanger 5 is arranged at the water outlet end of the first water pump 2, a separator A3 and a separator B4 are respectively arranged at one end of the exchanger 5, the separator A3 and the separator B4 are titanium alloy evaporation exchangers, 2 separators are arranged in total for the separator A3 and the separator B4, and the ratio of evaporated fresh water to concentrated water cannot exceed in the evaporation process of the separator A3 and the separator B4: 6:4, the one end of separator A3 and separator B4 all is connected with heat supply stove 6, PP filter 7 and heat accumulation case 9 are installed respectively to the other end of exchanger 5, PP filter 7 precision requirement < 5um, direct drinking water tank 8 is installed to the one end of PP filter 7, the one end of heat accumulation case 9 is connected with heat supply stove 6, and second water pump 10 is installed to the one end of heat accumulation case 9, third water pump 11 is installed to the other end of separator A3 and separator B4, the play water end of third water pump 11 is connected with greenhouse 12.
In this embodiment, the heat supply furnace 6, the separator A3, the separator B4, the exchanger 5, the PP filter 7, the direct drinking water tank 8, the heat storage tank 9, the head tank 1, the greenhouse 12, and the airing pool 13. When the system is in operation, the first water pump 2 is required to lift the brackish water from the well to the high-level water tank 1. As a make-up water source for separator A3 and separator B4, and at the same time as a cold source for exchanger 5. One of the separators A3 is supplemented with water by the high-level water tank 1, after the water is supplemented to a certain water level, the heat furnace 6 is started to heat the separator A3, the heat furnace 6 adopts fire coal or other solid fuels, the heating mode adopts heat conduction oil, the external supply temperature of the heat conduction oil is adjustable, the requirement is less than 175 ℃, when the water temperature of the separator A3 reaches a certain temperature, the high-level water tank 1 supplements water for the separator B4 through the exchanger 5, after the steam is cooled through the exchanger 5, a part of condensate is filtered by the PP filter 7, and then enters the direct drinking water tank 8. Part of the condensate enters a heat storage tank 9, and the heat storage tank 9 is used for heat preservation by supplying heat to the heat furnace 6, so as to perform night heating or perform heating on the ecological pool. The separator A3 evaporates to a certain extent, the concentrated water is pumped into the greenhouse 12 by the third water pump 11 to heat the greenhouse 12, and enters the airing pool 13 for airing after heat exchange is finished. Finally, coarse salt is formed.
Example two
As shown in fig. 1-2, compared with the first embodiment, the present utility model further includes a separator A3 and a separator B4 having the same structure, the separator A3 includes a heat conducting oil layer 31, the heat conducting oil layer 31 is sleeved on an outer wall of the separator A3, the outer wall of the heat conducting oil layer 31 is sleeved with an insulating layer 32, a water inlet 33 is installed on one side of the outer wall of the separator A3, the water inlet 33 is connected with the exchanger 5, a water outlet 34 is installed at the bottom of the separator A3, a heat conducting oil inlet 35 is installed on one side of the bottom of the separator A3, the heat conducting oil inlet 35 is connected with one end of the heat supply furnace 6, a heat conducting oil outlet 36 is installed on one side of the top of the heat conducting oil layer 31, the heat conducting oil outlet 36 is connected with the other end of the heat supply furnace 6, a steam outlet 37 is installed on one side of the top of the separator A3, a steam outlet 37 is connected with the exchanger 5, a vent 38 is installed on the other side of the top of the separator A3, and a heat conducting oil vent 39 is installed on the other side of the top of the heat conducting oil layer 31.
In this embodiment, the tops of separator A3 and separator B4 are also provided with a pressure gauge port and a safety valve port, the bottoms and tops of the insides of separator A3 and separator B4 are respectively provided with a water level gauge, separator A3 evaporates to a certain extent, concentrated water is pumped to greenhouse 12 by third water pump 11 to heat greenhouse 12, after heat exchange is completed, the concentrated water enters sun-drying pool 13, sun-drying pool 13 needs to perform anti-corrosion and anti-seepage operation to perform sun-drying, and coarse salt is formed.
The embodiments of the present utility model have been described in detail with reference to the drawings, but the present utility model is not limited thereto, and various changes can be made within the knowledge of those skilled in the art without departing from the spirit of the present utility model.
Claims (10)
1. The utility model provides a bitter water direct drinking and heat supply integrated system suitable for alpine region, its characterized in that, including high-level water tank (1), first water pump (2) are installed to the water inlet end of high-level water tank (1), exchanger (5) are installed to the play water end of first water pump (2), separator A (3) and separator B (4) are installed respectively to the one end of exchanger (5), the one end of separator A (3) and separator B (4) all is connected with heat supply stove (6), PP filter (7) and heat accumulation case (9) are installed respectively to the other end of exchanger (5), direct drinking water tank (8) are installed to the one end of PP filter (7), the one end of heat accumulation case (9) with heat supply stove (6) are connected, just second water pump (10) are installed to the one end of heat accumulation case (9), third water pump (11) are installed to the other end of separator A (3) and separator B (4), water outlet end (12) of third water pump (11) are connected with greenhouse.
2. The bitter water direct drinking and heat supply integrated system suitable for alpine regions according to claim 1, wherein the structure of the separator A (3) is the same as that of the separator B (4), the separator A (3) comprises a heat conducting oil layer (31), the heat conducting oil layer (31) is sleeved on the outer wall of the separator A (3), the outer wall of the heat conducting oil layer (31) is sleeved with an insulating layer (32), one side of the outer wall of the separator A (3) is provided with a water inlet (33), the water inlet (33) is connected with the heat exchanger (5), the bottom of the separator A (3) is provided with a water outlet (34), one side of the bottom of the separator A (3) is provided with a heat conducting oil inlet (35), the heat conducting oil inlet (35) is connected with one end of the heat supply furnace (6), one side of the top of the heat conducting oil layer (31) is provided with a heat conducting outlet (36), the heat conducting oil outlet (36) is connected with the other end of the heat supply furnace (6), one side of the separator A (3) is provided with a heat conducting oil outlet (37), the other side of the separator A (37) is provided with a steam outlet (37), and a heat conduction oil exhaust port (39) is arranged on the other side of the top of the heat conduction oil layer (31).
3. The bitter water direct drinking and heat supply integrated system suitable for the alpine region according to claim 1, wherein the tops of the separator A (3) and the separator B (4) are also provided with a pressure gauge port and a safety valve port, and the bottoms and the tops of the inner sides of the separator A (3) and the separator B (4) are respectively provided with a water level gauge.
4. The brackish water direct drinking and heat supply integrated system suitable for the alpine region according to claim 1, wherein the separator A (3) evaporates to a certain extent, concentrated water is pumped to the greenhouse (12) by the third water pump (11) to heat the greenhouse (12), and enters the airing pool (13) for airing after heat exchange is finished to form coarse salt.
5. The integrated system for direct drinking of brackish water and heat supply and dual supply suitable for alpine regions according to claim 1, wherein the heat supply furnace (6) adopts coal or solid fuel, the heating mode adopts heat conduction oil, the external supply temperature of the heat conduction oil is adjustable, and the temperature is required to be less than 175 ℃.
6. The bitter water direct drinking and heat supply integrated system suitable for the alpine region according to claim 1, wherein the separator A (3) and the separator B (4) are titanium alloy evaporation exchangers, and 2 separators are arranged in total for the separator A (3) and the separator B (4) and run alternately.
7. The brackish water direct drinking and heat supply integrated system suitable for alpine regions according to claim 1, wherein the accuracy requirement of the PP filter (7) is less than 5um.
8. The integrated brackish water direct drinking and heat supply system suitable for alpine regions according to claim 1, wherein the ratio of evaporated fresh water to concentrated water in the evaporation process of the separator a (3) and the separator B (4) cannot be exceeded: 6:4.
9. The brackish water direct drinking and heating integrated system suitable for alpine regions according to claim 1, wherein the high level water tank (1) has a height requirement of > 6m for supplying water to the exchanger (5) and separator a (3) and separator B (4).
10. The integrated system for direct drinking of brackish water and heat supply, which is suitable for alpine regions, according to claim 4, wherein the airing pool (13) needs to perform anti-corrosion and anti-seepage operations.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223493491.7U CN219157852U (en) | 2022-12-27 | 2022-12-27 | Bitter water direct drinking and heat supply dual-supply integrated system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223493491.7U CN219157852U (en) | 2022-12-27 | 2022-12-27 | Bitter water direct drinking and heat supply dual-supply integrated system |
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| Publication Number | Publication Date |
|---|---|
| CN219157852U true CN219157852U (en) | 2023-06-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223493491.7U Active CN219157852U (en) | 2022-12-27 | 2022-12-27 | Bitter water direct drinking and heat supply dual-supply integrated system |
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| Country | Link |
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| CN (1) | CN219157852U (en) |
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2022
- 2022-12-27 CN CN202223493491.7U patent/CN219157852U/en active Active
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