CN220818097U - Condensate water recycling system - Google Patents
Condensate water recycling system Download PDFInfo
- Publication number
- CN220818097U CN220818097U CN202322433885.1U CN202322433885U CN220818097U CN 220818097 U CN220818097 U CN 220818097U CN 202322433885 U CN202322433885 U CN 202322433885U CN 220818097 U CN220818097 U CN 220818097U
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- Prior art keywords
- heat exchange
- exchange tower
- heater
- water
- storage tank
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 96
- 238000004064 recycling Methods 0.000 title claims abstract description 18
- 244000068988 Glycine max Species 0.000 claims abstract description 37
- 235000010469 Glycine max Nutrition 0.000 claims abstract description 37
- 238000010438 heat treatment Methods 0.000 claims abstract description 32
- 238000003860 storage Methods 0.000 claims description 42
- 230000001502 supplementing effect Effects 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- 238000005086 pumping Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 235000019198 oils Nutrition 0.000 description 3
- 238000002386 leaching Methods 0.000 description 2
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 235000019764 Soybean Meal Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 150000003904 phospholipids Chemical class 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000001007 puffing effect Effects 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000004455 soybean meal Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model provides a condensate water recycling system, which relates to the technical field of condensate water utilization and comprises the following components: a heat exchange tower and a heater; the heat exchange tower is connected with the heater, the heat exchange tower is used for heating soybean through the comdenstion water, the heater is used for heating the comdenstion water that flows out through the heat exchange tower, the comdenstion water after the heater heats flows into in the heat exchange tower, has alleviated the technical problem of the heat in the extravagant comdenstion water that exists among the prior art, has reached the timely utilization of heat in the comdenstion water, avoids the extravagant technical effect of energy.
Description
Technical Field
The utility model relates to the technical field of condensate water utilization, in particular to a condensate water recycling system.
Background
The processing of soybean oil generally comprises the following process steps: 1) Primary cleaning of raw materials; 2) Quenching and tempering; 3) Crushing; 4) Rolling blanks; 5) Puffing; 6) Drying; 7) Leaching; 8) Desolventizing the soybean meal; 9) The mixed oil was evaporated. In the process steps of thermal refining, bean pulp desolventizing, mixed oil evaporating and the like, steam is converted into steam condensate water after acting, and the condensate water contains certain heat energy, and in the prior art, the condensate water is generally directly discharged or is kept stand for standby, and if the heat energy is not reasonably utilized, the energy loss is caused.
Disclosure of utility model
The utility model aims to provide a condensate water recycling system so as to solve the technical problem of wasting heat in condensate water in the prior art.
The condensate water recycling system provided by the utility model comprises: a heat exchange tower and a heater;
The heat exchange tower is connected with the heater, the heat exchange tower is used for heating soybeans through condensed water, the heater is used for heating the condensed water flowing out of the heat exchange tower, and the condensed water heated by the heater flows into the heat exchange tower.
In an alternative embodiment, an air heater is also included;
The air heater is disposed between the heat exchange tower and the heater, and is configured to heat air flowing through the air heater by condensed water.
In an alternative embodiment, the air heater includes a first heat exchanger and a second heat exchanger;
The first heat exchanger and the second heat exchanger are arranged in parallel, the first heat exchanger is respectively connected with the heat exchange tower and the heater, and the second heat exchanger is respectively connected with the heat exchange tower and the heater.
In an alternative embodiment, a preheating cavity is arranged in the heat exchange tower, the preheating cavity is respectively connected with the first heat exchanger and the second heat exchanger, the first heat exchanger and the second heat exchanger can both provide hot gas for the preheating cavity, and the preheating cavity is used for preheating soybeans.
In an alternative embodiment, a heating cavity is arranged in the heat exchanger;
The heating cavity is arranged below the preheating cavity and is communicated with the preheating cavity, the heating cavity is communicated with condensed water, and the heating cavity is used for heating soybeans through the condensed water.
In an alternative embodiment, the device further comprises a storage tank;
The storage tank is arranged between the heat exchange tower and the heater and is used for storing condensate water.
In an alternative embodiment, the method further comprises driving a pump;
The driving pump is arranged between the storage tank and the heat exchange tower, the driving pump is respectively connected with the storage tank and the heat exchange tower, and the driving pump is used for pumping the refrigerating water in the storage tank into the heat exchange tower.
In an alternative embodiment, the storage tank is provided with a water inlet and a water outlet;
the water inlet and the water outlet are respectively connected with the storage tank, the water inlet is used for supplementing condensed water in the storage tank, and the water outlet is used for discharging redundant condensed water in the storage tank.
In an alternative embodiment, a thermometer is arranged on the storage tank;
The thermometer is connected with the storage tank, and the thermometer is used for measuring the temperature of the condensed water in the storage tank.
In an alternative embodiment, the heat exchange tower is provided with a soybean inlet and a soybean outlet;
The soybean inlet is arranged at the top end of the heat exchange tower and is communicated with the interior of the heat exchange tower, so that soybean can enter the heat exchange tower through the soybean inlet;
The soybean outlet is arranged at the bottom end of the heat exchange tower and is communicated with the inside of the heat exchange tower, so that soybean can flow out of the heat exchange tower through the soybean outlet.
The condensate water recycling system provided by the utility model comprises: a heat exchange tower and a heater; the heat exchange tower is connected with the heater, the heat exchange tower is used for heating soybean through the comdenstion water, the heater is used for heating the comdenstion water that flows out through the heat exchange tower, the comdenstion water after the heater heats flows into in the heat exchange tower, has alleviated the technical problem of the heat in the extravagant comdenstion water that exists among the prior art, has reached the timely utilization of heat in the comdenstion water, avoids the extravagant technical effect of energy.
Drawings
In order to more clearly illustrate the embodiments of the present utility model or the technical solutions in the prior art, the drawings that are needed in the description of the embodiments or the prior art will be briefly described, and it is obvious that the drawings in the description below are some embodiments of the present utility model, and other drawings can be obtained according to the drawings without inventive effort for a person skilled in the art.
Fig. 1 is a schematic diagram of an embodiment of the present utility model.
Icon: 1-a heat exchange tower; 2-a heater; 3-a first heat exchanger; 4-a second heat exchanger; 5-preheating the cavity; 6-a heating cavity; 7-a storage tank; 8-driving the pump.
Detailed Description
The technical solutions of the present utility model will be clearly and completely described in connection with the embodiments, and it is apparent that the described embodiments are some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
At present, condensed water obtained after condensation of water vapor is generally directly discharged or kept stand for standby, and if the heat energy is not reasonably utilized, the energy loss is caused.
In view of this, as shown in fig. 1, the condensate recycling system provided in the embodiment of the present utility model includes: a heat exchange tower 1 and a heater 2; the heat exchange tower 1 with the heater 2 is connected, the heat exchange tower 1 is used for heating soybean through the comdenstion water, the heater 2 is used for heating the warp the comdenstion water of heat exchange tower 1 outflow, warp the comdenstion water after the heater 2 heats flows into in the heat exchange tower 1, has alleviateed the technical problem of the heat in the extravagant comdenstion water that exists among the prior art, has reached the timely utilization of heat in the comdenstion water, avoids the extravagant technical effect of energy.
Regarding the structure and shape of the heat exchange tower 1, specific are:
The soybean preheating device comprises a heat exchange tower 1, a soybean inlet, a soybean outlet, a preheating cavity 5, a heating cavity 6 and a steam heating section, wherein the soybean entering through the soybean inlet is preheated by hot gas in the preheating cavity 5, then enters the heating cavity 6, the soybean in the heating cavity 6 is subjected to heat exchange through heat in condensed water, so that the soybean is heated and tempered, then, the soybean subjected to heat exchange through the condensed water enters the steam heating section downwards, and is heated again through steam, wherein the hot gas heated by an air heater 2 can be arranged in the preheating cavity 5, the heating cavity 6 and the steam heating section, the soybean is heated by the aid of the hot gas, and the soybean subjected to heating can be discharged to the next procedure through the soybean outlet below.
Regarding the structure and shape of the air heater 2, specific ones are:
The air heater 2 comprises a first heat exchanger 3 and a second heat exchanger 4, wherein the first heat exchanger 3 and the second heat exchanger 4 are connected in parallel at the place where condensed water after heat exchange is discharged from the heat exchange tower 1, and the first heat exchanger 3 and the second heat exchanger 4 are respectively connected with an outlet of the heat exchange tower 1. The first heat exchanger 3 and the second heat exchanger 4 heat air through condensed water after condensation, and then the heated air is conveyed into the heat exchange tower 1 for heat exchange, so that heat is fully utilized.
Regarding the structure and shape of the heater 2, specific ones are:
the heater 2 can adopt the water heater, and the heater 2 can be connected with heat exchange tower 1, first heat exchanger 3 and second heat exchanger 4 respectively, and the comdenstion water that the heater 2 can heat exchange tower 1 and discharge also can heat the comdenstion water after first heat exchanger 3 and second heat exchanger 4 heat transfer, and wherein, the apopore of heater 2 can be directly connected with heat exchange tower 1 to make the comdenstion water after the heating directly utilized by heat exchange tower 1, also can be provided with a storage tank 7 between the apopore of heater 2 and the income apopore of heat exchange tower 1 for the comdenstion water after the storage heating.
Regarding the structure and shape of the tank 7, it is specific that:
One end of the storage tank 7 is connected and communicated with the heater 2, the other end of the storage tank 7 is connected and communicated with the heat exchange tower 1, a driving pump 8 is arranged between the storage tank 7 and the heat exchange tower 1, the storage tank 7 can convey heated condensed water into the heat exchange tower 1, wherein a heat preservation coating can be sprayed on the storage tank 7 to prevent the temperature loss of the condensed water in the storage tank 7, a water inlet and a water outlet can be formed in the storage tank 7, the water inlet on the storage tank 7 can be connected with condensed water in a pretreatment workshop, a leaching workshop and a phospholipid workshop of an oil mill for supplementing the condensed water, a thermometer can be arranged in the storage tank 7 and used for measuring the temperature of the condensed water in the storage tank 7, so that the temperature of the condensed water entering the heat exchange tower 1 is observed, and overhigh or overlow temperature is avoided.
Optionally, in the condensed water after heat exchange of the first heat exchanger 3 and the second heat exchanger 4, if the condensed water temperature is lower, part of the condensed water can be discharged out of the circulation system, so that the working pressure of the heater 2 is reduced, the condensation water in the circulation waterway is prevented from being excessively low, doping in the storage tank 7 is avoided, the whole temperature of the condensed water in the storage tank 7 is reduced, and meanwhile, if the condensed water temperature after heat exchange of the first heat exchanger 3 and the second heat exchanger 4 is higher, part of the condensed water can be heated through the heater 2, and the other part of the condensed water is directly discharged into the storage tank 7, so that the working cost is reduced, and the time is saved.
As for the connection mode between the devices, a pipe connection can be adopted, and the pipe comprises a stainless steel pipe, so that the reaction with condensed water is avoided.
Alternatively, the outlet and inlet locations of each device may be provided with a valve for controlling flow and a flow meter for monitoring flow, respectively.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present utility model, and not for limiting the same; although the utility model has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some or all of the technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit of the utility model.
Claims (10)
1. A condensate water recycling system, comprising: a heat exchange tower (1) and a heater (2);
The heat exchange tower (1) is connected with the heater (2), the heat exchange tower (1) is used for heating soybeans through condensed water, the heater (2) is used for heating the condensed water flowing out of the heat exchange tower (1), and the condensed water heated by the heater (2) flows into the heat exchange tower (1).
2. The condensate water recycling system of claim 1, further comprising an air heater (2);
the air heater (2) is arranged between the heat exchange tower (1) and the heater (2), and the air heater (2) is used for heating air flowing through the air heater (2) through condensed water.
3. The condensate water recycling system of claim 2, wherein the air heater (2) comprises a first heat exchanger (3) and a second heat exchanger (4);
The heat exchanger comprises a first heat exchanger (3) and a second heat exchanger (4), wherein the first heat exchanger (3) is connected with a heat exchange tower (1) and a heater (2) respectively, and the second heat exchanger (4) is connected with the heat exchange tower (1) and the heater (2) respectively.
4. A condensate water recycling system according to claim 3, wherein a preheating cavity (5) is arranged in the heat exchange tower (1), the preheating cavity (5) is respectively connected with the first heat exchanger (3) and the second heat exchanger (4), the first heat exchanger (3) and the second heat exchanger (4) can both provide hot gas for the preheating cavity (5), and the preheating cavity (5) is used for preheating soybeans.
5. The condensate water recycling system of claim 4, wherein a heating cavity (6) is arranged in the heat exchanger;
The heating cavity (6) is arranged below the preheating cavity (5) and is communicated with the preheating cavity (5), the heating cavity (6) is communicated with condensed water, and the heating cavity (6) is used for heating soybeans through the condensed water.
6. The condensate recycling system according to claim 1, further comprising a storage tank (7);
The storage tank (7) is arranged between the heat exchange tower (1) and the heater (2), and the storage tank (7) is used for storing condensed water.
7. The condensate recycling system of claim 6, further comprising a drive pump (8);
the driving pump (8) is arranged between the storage tank (7) and the heat exchange tower (1), the driving pump (8) is respectively connected with the storage tank (7) and the heat exchange tower (1), and the driving pump (8) is used for pumping the cold storage water in the storage tank (7) into the heat exchange tower (1).
8. The condensate recycling system according to claim 6, wherein the storage tank (7) is provided with a water inlet and a water outlet;
The water inlet and the water outlet are respectively connected with the storage tank (7), the water inlet is used for supplementing condensed water into the storage tank (7), and the water outlet is used for discharging redundant condensed water in the storage tank (7).
9. The condensate recycling system according to claim 6, characterized in that a thermometer is arranged on the storage tank (7);
The thermometer is connected with the storage tank (7), and the thermometer is used for measuring the temperature of condensed water in the storage tank (7).
10. Condensate recycling system according to any one of claims 1-9, characterized in that the heat exchange tower (1) is provided with a soybean inlet and a soybean outlet;
The soybean inlet is arranged at the top end of the heat exchange tower (1), and is communicated with the interior of the heat exchange tower (1) so that soybean can enter the heat exchange tower (1) through the soybean inlet;
The soybean outlet is arranged at the bottom end of the heat exchange tower (1), and the soybean outlet is communicated with the inside of the heat exchange tower (1), so that soybean can flow out of the heat exchange tower (1) through the soybean outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322433885.1U CN220818097U (en) | 2023-09-07 | 2023-09-07 | Condensate water recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322433885.1U CN220818097U (en) | 2023-09-07 | 2023-09-07 | Condensate water recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220818097U true CN220818097U (en) | 2024-04-19 |
Family
ID=90708027
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322433885.1U Active CN220818097U (en) | 2023-09-07 | 2023-09-07 | Condensate water recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220818097U (en) |
-
2023
- 2023-09-07 CN CN202322433885.1U patent/CN220818097U/en active Active
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