CN221237849U - Water circulation system for aerobic fermentation - Google Patents
Water circulation system for aerobic fermentation Download PDFInfo
- Publication number
- CN221237849U CN221237849U CN202322368640.5U CN202322368640U CN221237849U CN 221237849 U CN221237849 U CN 221237849U CN 202322368640 U CN202322368640 U CN 202322368640U CN 221237849 U CN221237849 U CN 221237849U
- Authority
- CN
- China
- Prior art keywords
- water
- boiler
- pipeline
- communicated
- waste liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 113
- 238000010564 aerobic fermentation Methods 0.000 title claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 239000002699 waste material Substances 0.000 claims abstract description 23
- 238000011084 recovery Methods 0.000 claims abstract description 17
- 238000000855 fermentation Methods 0.000 claims abstract description 13
- 230000004151 fermentation Effects 0.000 claims abstract description 12
- 239000002918 waste heat Substances 0.000 claims abstract description 11
- 238000005338 heat storage Methods 0.000 claims description 12
- 238000000746 purification Methods 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 239000003337 fertilizer Substances 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract 2
- 239000008213 purified water Substances 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a water circulation system for aerobic fermentation, which is suitable for the organic chemical fertilizer manufacturing industry and belongs to the field of organic chemical industry, and comprises a boiler, a waste liquid recovery mechanism and a waste heat recovery mechanism, wherein the waste liquid recovery mechanism comprises a water purifying and storing device and a water purifying device, a waste liquid collecting pipeline communicated with the lower part of a fermentation tank is arranged at the upper end of the water purifying device and used for collecting waste liquid generated in the fermentation process, the water purifying device is provided with a pipeline and is communicated with the water purifying and storing device, a fourth water pipeline is communicated between the boiler and the water purifying and storing device, and an electromagnetic valve IV is arranged on the fourth water pipeline. The waste liquid recycling mechanism is adopted, various waste liquids generated in the production process can be effectively recycled and purified through the water purifying equipment, and the waste heat recycling mechanism is adopted, so that the waste heat generated during or after the use of the boiler can be recycled.
Description
Technical Field
The utility model relates to a water circulation system for aerobic fermentation, which is suitable for the manufacturing industry of organic fertilizers and belongs to the field of organic chemical industry.
Background
In the field of organic chemical industry, equipment is sterilized according to the specified requirement, a large amount of heat and a large amount of water are remained after the equipment is sterilized by steam through a boiler, the heat and the water are not recycled, the cost of enterprises is increased intangibly, especially, in the fermentation process, the supply of hot water and the discharge of residual hot water are frequently caused, and the full utilization of resources is very important.
Disclosure of utility model
In order to solve the problems, the utility model provides a water circulation system for aerobic fermentation, which is characterized by comprising a boiler, a waste liquid recovery mechanism and a waste heat recovery mechanism, wherein the waste liquid recovery mechanism comprises a water purifying and storing device and a water purifying device, the upper end of the water purifying device is provided with a waste liquid collecting pipeline communicated with the lower part of a fermentation tank for collecting waste liquid generated in the fermentation process, the water purifying device is provided with a pipeline and is communicated with the water purifying and storing device, a fourth water pipeline is communicated between the boiler and the water purifying and storing device, and an electromagnetic valve IV is arranged on the fourth water pipeline;
the waste heat recovery mechanism comprises a heat storage tank and a heat exchanger, a fifth water pipeline is communicated between the heat storage tank and the boiler, the heat storage tank is communicated with the heat exchanger through a pipeline and is used for conveying and storing heat, a first water inlet pipeline and a first water outlet pipeline which are communicated with the boiler water storage device are arranged on the heat exchanger and are used for exchanging heat, and an electromagnetic valve V, an electromagnetic valve VI and an electromagnetic valve VII are correspondingly arranged on the fifth water pipeline, the first water inlet pipeline and the first water outlet pipeline respectively.
The utility model provides a water circulation system for aerobic fermentation, which has the following beneficial effects:
1. the utility model adopts the waste liquid recovery mechanism, can effectively recover various waste liquids generated in the production process and recover and purify the waste liquids through the water purification equipment, and the recovered and purified water can be put into a boiler for use, thereby greatly improving the utilization rate of resources;
2. The utility model adopts the waste heat recovery mechanism, and can recycle the surplus heat generated during or after the use of the boiler, thereby greatly improving the utilization rate of resources.
In conclusion, the utility model has the characteristics of simple structure, scientific and reasonable design, convenient use, high resource utilization rate and environmental protection.
Drawings
FIG.1 is a schematic diagram of the structure of the present utility model;
In the figure: 1-boiler, 2-second water pipe, 3-boiler water reservoir, 4-solenoid valve III, 5-third water pipe, 6-solenoid valve I, 7-first water pipe, 8-manometer, 9-inlet channel, 10-solenoid valve II, 11-fourth water pipe, 12-solenoid valve IV, 13-solenoid valve V, 14-fifth water pipe, 15-thermometer I, 16-thermometer II, 17-heat storage tank, 18-heat exchanger, 19-purified water reservoir, 20-water purifying equipment, 21-waste liquid collecting pipe, 22-fermentation tank, 23-first inlet pipe, 24-outlet pipe, 25-second inlet pipe, 26-solenoid valve VI, 27-solenoid valve VII.
Detailed Description
The following description of the embodiments of the present application will be made clearly and fully with reference to the accompanying drawings, in which it is evident that the embodiments described are only some, but not all embodiments of the application.
In the description of the embodiments, it should be noted that the positional or positional relationship indicated by the terms "upper", "lower", "ascending", "descending", "etc. are based on the positional or positional relationship shown in the drawings, are merely for convenience of describing the present application and simplifying the description, and do not indicate or imply that the apparatus or element referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present application. In the description of the present application, unless explicitly stated and limited otherwise, the terms "mounted," "configured to," "connected," and the like are to be construed broadly as, for example, "connected" as either a fixed connection, a removable connection, or an integral connection, as either a mechanical connection or an electrical connection, as either a direct connection or an indirect connection via an intermediary, as well as a communication between two elements. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance. It will be understood by those of ordinary skill in the art that the terms described above are in the specific sense of the present application.
As shown in fig. 1, the utility model comprises a boiler 1, a waste liquid recovery mechanism and a waste heat recovery mechanism, wherein the waste liquid recovery mechanism comprises a water purifying and storing device 19 and a water purifying device 20, a waste liquid collecting pipeline 21 communicated with the lower part of a fermentation tank 22 is arranged at the upper end of the water purifying device 20 and used for collecting waste liquid generated in the fermentation process, the water purifying device 20 is provided with a pipeline and is communicated with the water purifying and storing device 19, a fourth water conveying pipeline 11 is communicated between the boiler 1 and the water purifying and storing device 19, and an electromagnetic valve IV 12 is arranged on the fourth water conveying pipeline 11.
The waste heat recovery mechanism comprises a heat storage tank 17 and a heat exchanger 18, a fifth water conveying pipeline 14 is communicated between the heat storage tank 17 and the boiler 1, the heat storage tank 17 is communicated with the heat exchanger 18 through a pipeline and is used for conveying and storing heat, the heat exchanger 18 is provided with a first water inlet pipeline 23 and a first water outlet pipeline 24 which are communicated with the boiler water reservoir 3 and are used for exchanging heat, and an electromagnetic valve V13, an electromagnetic valve VI 26 and an electromagnetic valve VII 27 are correspondingly arranged on the fifth water conveying pipeline 14, the first water inlet pipeline 23 and the first water outlet pipeline 24 respectively.
The utility model discloses a boiler, including boiler 1, boiler water reservoir 3, first water conduit 7 and inlet channel 9 are provided with respectively, correspond respectively on first water conduit 7 and the inlet channel 9 and install solenoid valve I6 and solenoid valve II 10, manometer 8 is still installed to boiler 1 upper end and thermometer I15 is installed to the lower extreme, boiler 1 is provided with the second water conduit 2 with boiler water reservoir 3 intercommunication, thermometer II 16 is installed to boiler water reservoir 3 lower extreme, boiler water reservoir 3 upper end is provided with third water conduit 5 and second inlet channel 25, install solenoid valve III 4 on the third water conduit 5.
The first water conveying pipeline 7 and the third water conveying pipeline 5 are connected in parallel and then communicated with the fermentation tank 22.
The electromagnetic valve is characterized by further comprising a control console, and the electromagnetic valve I6, the electromagnetic valve II 10, the electromagnetic valve III 4, the electromagnetic valve IV 12, the electromagnetic valve V13, the electromagnetic valve VI 26 and the electromagnetic valve VII 27 are respectively and electrically connected with the control console.
The working principle and the working process of the utility model are as follows:
As shown in fig. 1, before disinfection, the boiler 1 is started to generate high-temperature steam, the electromagnetic valve i 6 is opened to be discharged from the first water conveying pipeline 7 to disinfect the fermentation tank 22, after disinfection, excessive water enters the water purifying device 20 through the waste liquid collecting pipeline 21, after the water purification is finished, the water is discharged into the water purifying water storage device 19 for the boiler at any time, the electromagnetic valve iii 4 can be opened at any time when the water is needed to be obtained from the boiler water storage device 3, after the boiler is used, the boiler is not cooled completely, at the moment, the electromagnetic valve v 13 is opened to enable the steam to be introduced into the heat storage tank 17 for heat storage, and then the stored heat is conveyed into the heat exchanger 18 through the pipeline to heat the water stored in the boiler water storage device 3 so as to realize waste heat utilization until the boiler is cooled completely.
The embodiments of the present utility model are all preferred embodiments of the present utility model, and are not intended to limit the scope of the present utility model in this way, therefore: all equivalent changes in structure, shape and principle of the utility model should be covered in the scope of protection of the utility model.
Claims (4)
1. The utility model provides a water circulation system of aerobic fermentation, its characterized in that includes boiler (1), waste liquid recovery mechanism, waste heat recovery mechanism, waste liquid recovery mechanism includes water purification water receiver (19), water purification unit (20) upper end be equipped with fermentation tank (22) lower part intercommunication waste liquid collection pipeline (21) be used for collecting the waste liquid that produces in the fermentation process, water purification unit (20) are provided with the pipeline and with water purification water receiver (19) intercommunication, the intercommunication has fourth conduit (11) between boiler (1) and water purification water receiver (19), install solenoid valve IV (12) on fourth conduit (11);
The waste heat recovery mechanism comprises a heat storage tank (17) and a heat exchanger (18), a fifth water conveying pipeline (14) is communicated between the heat storage tank (17) and the boiler (1), the heat storage tank (17) is communicated with the heat exchanger (18) through a pipeline and conveys heat for storage, a first water inlet pipeline (23) and a water outlet pipeline (24) which are communicated with the boiler water receiver (3) are arranged on the heat exchanger (18) and are used for exchanging heat, and an electromagnetic valve V (13), an electromagnetic valve VI (26) and an electromagnetic valve VII (27) are correspondingly arranged on the fifth water conveying pipeline (14), the first water inlet pipeline (23) and the water outlet pipeline (24) respectively.
2. The water circulation system for aerobic fermentation according to claim 1, wherein a first water conveying pipeline (7) and a water inlet pipeline (9) are respectively arranged at the upper end of the boiler (1), an electromagnetic valve I (6) and an electromagnetic valve II (10) are respectively correspondingly arranged on the first water conveying pipeline (7) and the water inlet pipeline (9), a pressure gauge (8) is further arranged at the upper end of the boiler (1), a thermometer I (15) is arranged at the lower end of the boiler, a second water conveying pipeline (2) communicated with the boiler water receiver (3) is arranged at the lower end of the boiler water receiver (3), a thermometer II (16) is arranged at the lower end of the boiler water receiver (3), a third water conveying pipeline (5) and a second water inlet pipeline (25) are arranged at the upper end of the boiler water receiver (3), and an electromagnetic valve III (4) is arranged on the third water conveying pipeline (5).
3. The water circulation system for aerobic fermentation according to claim 2, wherein the first water pipe (7) and the third water pipe (5) are connected in parallel and then communicated with the fermentation tank (22).
4. The aerobic fermentation water circulation system according to claim 2, further comprising a console, wherein the solenoid valve I (6), the solenoid valve II (10), the solenoid valve III (4), the solenoid valve IV (12), the solenoid valve V (13), the solenoid valve VI (26) and the solenoid valve VII (27) are electrically connected with the console, respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322368640.5U CN221237849U (en) | 2023-09-01 | 2023-09-01 | Water circulation system for aerobic fermentation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322368640.5U CN221237849U (en) | 2023-09-01 | 2023-09-01 | Water circulation system for aerobic fermentation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221237849U true CN221237849U (en) | 2024-06-28 |
Family
ID=91594431
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322368640.5U Active CN221237849U (en) | 2023-09-01 | 2023-09-01 | Water circulation system for aerobic fermentation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221237849U (en) |
-
2023
- 2023-09-01 CN CN202322368640.5U patent/CN221237849U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203244811U (en) | Device for resourceful treatment of steel hydrochloric acid pickle liquor | |
| CN203203020U (en) | Steam waste heat water recycling device for machining paper | |
| CN221237849U (en) | Water circulation system for aerobic fermentation | |
| CN201598246U (en) | Melamine and urea co-production heat energy recycling device | |
| CN203648348U (en) | Tail gas absorbing device of formic acid acidifying workshop section | |
| CN212805234U (en) | Ethylene gasification system | |
| CN202371700U (en) | Recycling device for steam condensate | |
| CN208032252U (en) | A kind of system of recycling low-temperature methanol washing tail-gas cold | |
| CN203068485U (en) | Closed type condensate water recovering equipment | |
| CN218001869U (en) | Heat pump unit device for waste heat recovery and energy storage | |
| CN217714893U (en) | Self-checking and waste heat utilization system of steam generator sewage system | |
| CN214307682U (en) | Printing and dyeing wastewater waste heat recovery device with solar energy direct absorption type heat supply | |
| CN201424388Y (en) | Urea process wastewater recovering device | |
| CN205953886U (en) | Take dimethyl ether production system of cogeneration | |
| CN220919218U (en) | Urea hydrolysis reactor utilizing water drainage | |
| CN221207104U (en) | Device for improving water quality of 5-degree water | |
| CN218202483U (en) | Solar constant-temperature sludge anaerobic digestion hydrogen filling station | |
| CN217909030U (en) | Low-energy-consumption difluorochloroethane production equipment | |
| CN217844854U (en) | Device for cooling and recovering steam exhaust steam in coking chemical industry | |
| CN204829858U (en) | Boiler blow -off waste water enthalpy difference compensation dilatation purifies recovery unit | |
| CN219453989U (en) | Heat recycling structure of boiler waste gas | |
| CN215311359U (en) | Flue gas waste heat comprehensive utilization system of coke oven flue gas semi-dry process technology | |
| CN221036882U (en) | System for recycling and recovering condensate water of ammonia steam prepared by hydrolysis of denitration urea | |
| CN203517754U (en) | Condensation water recycling device of generator set | |
| CN214121230U (en) | Synthetic ammonia production instrument companion heat system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant |