CN114642246A - Dried bean production unit - Google Patents
Dried bean production unit Download PDFInfo
- Publication number
- CN114642246A CN114642246A CN202210242808.5A CN202210242808A CN114642246A CN 114642246 A CN114642246 A CN 114642246A CN 202210242808 A CN202210242808 A CN 202210242808A CN 114642246 A CN114642246 A CN 114642246A
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- Prior art keywords
- carbon dioxide
- heat
- water
- production unit
- heating pipe
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Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 35
- 235000010627 Phaseolus vulgaris Nutrition 0.000 title claims abstract description 23
- 244000046052 Phaseolus vulgaris Species 0.000 title claims abstract description 23
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 96
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 48
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 48
- 239000012530 fluid Substances 0.000 claims abstract description 40
- 235000013527 bean curd Nutrition 0.000 claims abstract description 30
- 238000010438 heat treatment Methods 0.000 claims abstract description 28
- 238000009835 boiling Methods 0.000 claims abstract description 22
- 244000068988 Glycine max Species 0.000 claims abstract description 20
- 235000010469 Glycine max Nutrition 0.000 claims abstract description 20
- 238000001035 drying Methods 0.000 claims abstract description 19
- 238000004891 communication Methods 0.000 claims abstract description 16
- 235000013336 milk Nutrition 0.000 claims abstract description 12
- 239000008267 milk Substances 0.000 claims abstract description 12
- 210000004080 milk Anatomy 0.000 claims abstract description 12
- 238000002791 soaking Methods 0.000 claims abstract description 8
- 238000002360 preparation method Methods 0.000 claims abstract description 5
- 239000008399 tap water Substances 0.000 claims abstract description 5
- 235000020679 tap water Nutrition 0.000 claims abstract description 5
- 238000005338 heat storage Methods 0.000 claims description 14
- 238000000746 purification Methods 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 6
- 238000011144 upstream manufacturing Methods 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 4
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 claims description 2
- 238000004804 winding Methods 0.000 claims description 2
- 238000010411 cooking Methods 0.000 abstract description 9
- 239000007788 liquid Substances 0.000 abstract 3
- 238000007493 shaping process Methods 0.000 abstract 2
- 229910052799 carbon Inorganic materials 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 235000013322 soy milk Nutrition 0.000 description 4
- 239000003245 coal Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
- A23L3/10—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating materials in packages which are not progressively transported through the apparatus
- A23L3/12—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating materials in packages which are not progressively transported through the apparatus with packages in intercommunicating chambers through which the heating medium is circulated
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C20/00—Cheese substitutes
- A23C20/02—Cheese substitutes containing neither milk components, nor caseinate, nor lactose, as sources of fats, proteins or carbohydrates
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
- A23L3/40—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by drying or kilning; Subsequent reconstitution
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H4/00—Fluid heaters characterised by the use of heat pumps
- F24H4/02—Water heaters
- F24H4/04—Storage heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/002—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
- F25B9/008—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
-
- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J7/00—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries
- H02J7/34—Parallel operation in networks using both storage and other dc sources, e.g. providing buffering
- H02J7/35—Parallel operation in networks using both storage and other dc sources, e.g. providing buffering with light sensitive cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/90—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation
- Y02A40/924—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation using renewable energies
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Mechanical Engineering (AREA)
- Nutrition Science (AREA)
- Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Power Engineering (AREA)
- Beans For Foods Or Fodder (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention relates to the technical field of dried bean production, in particular to a dried bean production unit, which comprises: the carbon dioxide circulating system comprises a carbon dioxide water source machine, a pulp cooking tank heating pipe and a heat exchanger, wherein the carbon dioxide water source machine, the pulp cooking tank heating pipe and the heat exchanger are sequentially in fluid communication and form a loop for circulating the carbon dioxide fluid; the hot water supply system comprises a water softener and a heat supply pipe communicated with the water softener in a fluid mode, wherein the water softener is connected with tap water, the heat supply pipe can supply hot water flow and is communicated with a heat exchanger in a fluid mode, and heat exchange can supply carbon dioxide fluid to exchange heat with the hot water; the bean curd stick preparation system comprises a bean soaking tank, a crushing tower, a soybean milk boiling tank, a forming pool and a drying chamber which are sequentially arranged; wherein, carbon dioxide water source machine can heat the carbon dioxide fluid, and the boiling thick liquid jar heating pipe is arranged in boiling thick liquid jar department and can provides the heat for the boiling thick liquid jar, and the heat supply pipe loops through shaping pond and drying chamber and can provide the heat for shaping pond and drying chamber.
Description
Technical Field
The invention relates to the technical field of dried bean production, in particular to a dried bean production unit.
Background
The existing bean curd sticks production process generally adopts coal for heat supply, and the combustion of coal pollutes the environment and increases carbon emission, so that the mode is contrary to the national policy of 'double carbon'. In addition, the automation degree of the current production process is low, the manual demand is high, the quality of the produced dried beancurd sticks is unstable, and the production cost of the dried beancurd sticks is increased.
Disclosure of Invention
In order to solve the related technical problems that the bean curd stick production process of the prior burning heat supply mode pollutes the environment and increases carbon emission and the bean curd stick production process has low automation degree, the invention aims to provide a bean curd stick production unit which adopts carbon dioxide for heat supply and has high automation degree.
In order to achieve the above purpose, the invention provides the following technical scheme: a dried bean production unit comprises: the carbon dioxide circulating system comprises a carbon dioxide water source machine, a pulp cooking pot heating pipe and a heat exchanger, wherein the carbon dioxide water source machine, the pulp cooking pot heating pipe and the heat exchanger are sequentially in fluid communication and form a loop for circulating and flowing carbon dioxide fluid; the hot water supply system comprises a water softener and a heat supply pipe communicated with the water softener in a fluid mode, wherein the water softener is connected with tap water, the heat supply pipe is communicated with the heat exchanger in a fluid mode and can supply hot water to flow, and the heat exchange can supply carbon dioxide fluid to exchange heat with the hot water; the bean curd stick preparation system comprises a bean soaking tank, a crushing tower, a soybean milk boiling tank, a forming pool, a drying chamber and a humidifying chamber which are sequentially arranged; the heating pipe sequentially passes through the forming pool and the drying chamber and can provide heat for the forming pool and the drying chamber.
In the above technical solution, preferably, the carbon dioxide circulation system is further provided with a solar photovoltaic panel, and the solar photovoltaic panel is electrically and mechanically connected with the carbon dioxide water source. Still further preferably, a storage battery pack is arranged between the solar photovoltaic panel and the carbon dioxide water source machine.
In the above technical solution, preferably, the hot water supply system further includes a three-way pipe in fluid communication with the heat supply pipe, an atomizer is disposed at an upper portion of the humidification chamber, the three-way pipe is located downstream of the drying chamber and has a first water outlet pipe and a second water outlet pipe, the first water outlet pipe is in fluid communication with the atomizer, and the second water outlet pipe is in fluid communication with the water softener.
In the above preferred embodiment, it is further preferred that the atomizer is an ultrasonic atomizer.
In the above-mentioned preferred solution, it is further preferred that a purification and recovery device for purifying the hot water is arranged between the second water outlet pipe and the water softener.
In the above technical solution, preferably, the hot water supply system further includes a heat storage tank in fluid communication with the heat supply pipe, and the heat storage tank is located downstream of the heat exchanger and upstream of the forming tank. It is still further preferable that an electric heater is disposed in the heat storage tank.
In the above technical solution, preferably, the digester heating pipe is wound around the outer surface of the digester in a serpentine winding manner.
Compared with the prior art, the bean curd stick production unit provided by the invention can supply heat by recycling carbon dioxide fluid, replaces the traditional coal burning mode, reduces carbon emission and environmental pollution, and accords with the national policy of 'double carbon'. In addition, this dried bean production unit degree of automation is high, reduces the demand of manpower, improves the output stability of quality of dried bean and reduces the manufacturing cost of dried bean.
Drawings
Fig. 1 is a schematic process flow diagram of the bean curd stick production unit provided by the invention.
The labels in the figure are:
100. a bean curd stick production unit;
11. a solar photovoltaic panel; 12. a carbon dioxide water source machine; 13. a heating pipe of the pulp boiling tank; 14. a heat exchanger;
21. a water softener; 22. a heat supply pipe; 23. a heat storage tank; 24. a three-way pipe; 25. a purification and recovery device;
31. a bean soaking tank; 32. a crushing tower; 33. a pulp boiling tank; 34. a forming pool; 35. a drying chamber; 36. a humidification chamber; 37. an atomizer.
Detailed Description
To explain technical contents, structural features, achieved objects and effects of the invention in detail, the technical solutions in the embodiments of the present application will be described below with reference to the accompanying drawings in the embodiments of the present application, and it is apparent that the described embodiments are only a part of the embodiments of the present application, and not all embodiments. In the following description, for purposes of explanation, numerous specific details are set forth in order to provide a detailed description of various exemplary embodiments or implementations of the invention. However, various exemplary embodiments may be practiced without these specific details or with one or more equivalent arrangements. Moreover, the various exemplary embodiments may be different, but are not necessarily exclusive. For example, the particular shapes, configurations and characteristics of the exemplary embodiments may be used or implemented in another exemplary embodiment without departing from the inventive concept.
Fig. 1 shows a bean curd stick production unit 100 provided by the invention, and the bean curd stick production unit 100 adopts a solar power supply and carbon dioxide fluid heat supply mode to replace the traditional coal-fired heat supply mode to realize low-carbon and environment-friendly production of bean curd sticks. The bean curd stick production unit 100 comprises a carbon dioxide circulating system, a hot water supply system and a bean curd stick preparation system.
The bean curd stick preparation system comprises a bean soaking tank 31 for soaking soybeans, a crushing tower 32 for crushing the soybeans, a soybean milk cooking tank 33 for cooking the crushed beans into soybean milk, a forming tank 34 for performing a peeling forming process, a drying chamber 35 for drying bean curd sticks, and a humidifying chamber 36 for humidifying and softening the bean curd sticks. In the production process of the dried beancurd sticks, a bean soaking tank 31, a crushing tower 32, a soybean milk cooking tank 33, a forming tank 34, a drying chamber 35 and a humidifying chamber 36 are arranged from upstream to downstream in sequence. Wherein, the upper part of the humidifying chamber 36 is arranged with an atomizer 37 for atomizing hot water, the atomizer 37 is an ultrasonic atomizer.
The carbon dioxide circulation system comprises solar photovoltaic panels 1 for providing electrical energy, a carbon dioxide water source machine 12 for heating the carbon dioxide fluid, a digester heating pipe 13 and a heat exchanger 14. The solar photovoltaic panel 11 is electrically connected with the carbon dioxide water source machine 12 and transmits the electric power of the prepared high-temperature carbon dioxide fluid to the carbon dioxide water source machine. The heating pipe 13 of the soymilk boiling tank is coiled on the outer surface of the soymilk boiling tank 33 in a snake-shaped coiling way, and the arrangement way can reduce the temperature difference between the upper part and the lower part in the soymilk boiling tank 33 and improve the stability of the soybean milk in the soymilk boiling tank 33. In other embodiments, in order to further ensure the stability of power supply and avoid weather influence, a storage battery pack can be additionally arranged between the solar photovoltaic panel and the carbon dioxide water source machine to serve as a reserve power supply, or the carbon dioxide water source body is set to be in a double-line-incoming mode in which the solar photovoltaic panel and the mains supply power simultaneously.
The carbon dioxide water source machine 12, the heating pipe 13 of the pulp boiling tank and the heat exchange pipe 14 are sequentially communicated in fluid and form a loop for circulating carbon dioxide. When the unit 100 works, the high-temperature carbon dioxide fluid (the outlet temperature is controlled at 110 ℃ during the work) heated by the carbon dioxide water source machine 12 enters the heating pipe 13 of the soybean milk boiling tank to heat the soybeans in the soybean milk boiling tank 33. Thereafter, the carbon dioxide fluid exiting the digester 33 (temperature controlled at 100℃. during operation) enters the heat exchanger 14 to provide heat for the supply of hot water from the water softener 21 (see below). The carbon dioxide fluid in the heat exchanger 14 releases heat and is cooled and flows into the carbon dioxide water source machine 12 to complete a cycle.
The hot water supply system comprises a water softener 21 for receiving tap water, a heating pipe 22 for supplying hot water to flow, a heat storage tank 23 for storing the hot water, a three-way pipe 24 communicated with the heating pipe 22 and a purifying and recycling device 25 for purifying the hot water.
The water softener 21, the heat exchanger 14, the heating pipe 22 and the tee pipe 24 are in fluid communication in sequence, and the heat storage tank 23 is in fluid communication with the heating pipe 22 and is located upstream of the forming pond 34. The water softener 21 is located upstream of the heat exchanger 3 and serves to reduce calcium and magnesium ions in the water to reduce the hardness of the tap water. The hot water from the water softener 21 flows into the heat exchanger 3 and exchanges heat with the carbon dioxide fluid of the carbon dioxide circulation system, during which the temperature of the hot water rises (during operation, the outlet temperature is controlled at 95 ℃). Then, the hot water flowing out of the heat exchanger 14 flows into the heat storage tank 23, and the hot water of a stable temperature is continuously supplied to the downstream heat supply pipe 22 by the water storage and heat storage actions of the heat storage tank 23. The heating pipe 22 at the downstream of the heat storage box 23 passes through the forming tank 24 and the drying chamber 25 in sequence to provide heat for the forming tank and the drying chamber. In other embodiments, an electric heater may also be disposed within the heat storage tank 23 to further stabilize the temperature of the internal hot water supply.
The working principle of the dried bean production unit 100 is explained as follows: soybeans are soaked in the soybean soaking tank 31 and crushed in the crushing tower 32, and then are cooked in the soybean cooking tank 33 to form soybean milk, and carbon dioxide fluid in the heating pipe 13 of the soybean cooking tank provides continuous and stable heating, so that the effect of slow stewing with slow fire is achieved, and other auxiliary materials do not need to be added into the soybean milk, and the taste of the soybean milk returns to the original taste.
And then, the soybean slurry enters a forming tank 34 to be subjected to a peeling forming process to prepare the dried beancurd sticks, and the dried beancurd sticks are dried in a drying chamber 35 and humidified and softened in a humidifying chamber 36 in sequence to be finally formed. Compared with the traditional process, the bean curd stick production unit 100 has high automation degree and low labor cost, provides the quality stability of the bean curd sticks and reduces the production cost of the bean curd sticks.
The foregoing shows and describes the general principles, essential features, and advantages of the invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the foregoing description only for the purpose of illustrating the principles of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the invention as defined by the appended claims, specification, and equivalents thereof.
Claims (9)
1. A dried bean production unit is characterized by comprising:
the carbon dioxide circulating system comprises a carbon dioxide water source machine (12), a boiling tank heating pipe (13) and a heat exchanger (14), wherein the carbon dioxide water source machine (12), the boiling tank heating pipe (13) and the heat exchanger (14) are sequentially in fluid communication and form a loop for circulating and flowing carbon dioxide fluid;
the hot water supply system comprises a water softener (21) and a heating pipe (23) communicated with the water softener (21) in a fluid mode, wherein tap water is connected into the water softener (21), the heating pipe (23) is communicated with the heat exchanger (14) in a fluid mode and can supply hot water to flow, and the heat exchanger (14) can supply carbon dioxide fluid to exchange heat with the hot water;
the bean curd stick preparation system comprises a bean soaking tank (31), a crushing tower (32), a soybean milk boiling tank (33), a forming pool (34), a drying chamber (35) and a humidifying chamber (36) which are sequentially arranged;
the carbon dioxide water source machine (12) can heat carbon dioxide fluid, the boiling tank heating pipe (13) is arranged at the boiling tank (33) and can provide heat for the boiling tank (33), and the heat supply pipe (22) sequentially passes through the forming pool (34) and the drying chamber (35) and can provide heat for the forming pool (34) and the drying chamber (35).
2. A dried bean production unit according to claim 1, wherein the carbon dioxide circulating system is further provided with a solar photovoltaic panel (11), and the solar photovoltaic panel (11) is electrically connected with the carbon dioxide water source machine (12).
3. A dried bean production unit according to claim 2, wherein a storage battery pack is arranged between the solar photovoltaic panel (11) and the carbon dioxide water source machine (12).
4. A beancurd stick production unit according to claim 1, wherein the hot water supply system further comprises a tee (24) in fluid communication with the heating pipe (22), an atomizer (37) is arranged at an upper portion of the humidifying chamber (36), the tee (24) is located downstream of the drying chamber (35) and has a first water outlet conduit in fluid communication with the atomizer (37) and a second water outlet conduit in fluid communication with the water softener (21).
5. A dried bean production unit according to claim 4, characterized in that the atomizer (37) is an ultrasonic atomizer.
6. A bean curd stick production unit according to claim 4, characterized in that a purification and recovery device (25) for purifying the hot water is arranged between the second water outlet pipeline and the water softener (21).
7. A beancurd stick production unit according to claim 1, wherein the hot water supply system further comprises a heat storage tank (23) in fluid communication with the heating pipe (22), the heat storage tank (23) being located downstream of the heat exchanger (14) and upstream of the forming tank (34).
8. A dried bean production unit according to claim 7, characterized in that an electric heater is arranged in the heat storage tank (23).
9. A bean curd stick production unit according to claim 1, characterized in that the boiling pot heating pipe (13) is wound around the outer surface of the boiling pot (13) in a serpentine winding manner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202210242808.5A CN114642246B (en) | 2022-03-11 | 2022-03-11 | Dried beancurd stick production unit |
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CN202210242808.5A CN114642246B (en) | 2022-03-11 | 2022-03-11 | Dried beancurd stick production unit |
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CN114642246A true CN114642246A (en) | 2022-06-21 |
CN114642246B CN114642246B (en) | 2023-11-28 |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9025378D0 (en) * | 1990-11-22 | 1991-01-09 | Coryell Limited | A process for producing a starch jelly confectionery product |
CN204460990U (en) * | 2014-12-03 | 2015-07-08 | 许昌世纪豪嘉食品有限公司 | A kind of bean curd stick automatic baking main line |
CN106135448A (en) * | 2016-08-04 | 2016-11-23 | 济南宏金机械设备有限公司 | Full-automatic dried bean outermost layer of skin machine |
CN111449141A (en) * | 2020-05-20 | 2020-07-28 | 广西格卡环保科技有限公司 | Dried bean production forming equipment under atmospheric steam condition |
CN112902281A (en) * | 2019-12-04 | 2021-06-04 | 江苏金通灵光核能源科技有限公司 | Cold and hot combined equipment based on carbon dioxide heat pump |
CN213961659U (en) * | 2020-11-16 | 2021-08-17 | 辽宁正远食品有限公司 | Food steam energy-saving device |
-
2022
- 2022-03-11 CN CN202210242808.5A patent/CN114642246B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9025378D0 (en) * | 1990-11-22 | 1991-01-09 | Coryell Limited | A process for producing a starch jelly confectionery product |
CN204460990U (en) * | 2014-12-03 | 2015-07-08 | 许昌世纪豪嘉食品有限公司 | A kind of bean curd stick automatic baking main line |
CN106135448A (en) * | 2016-08-04 | 2016-11-23 | 济南宏金机械设备有限公司 | Full-automatic dried bean outermost layer of skin machine |
CN112902281A (en) * | 2019-12-04 | 2021-06-04 | 江苏金通灵光核能源科技有限公司 | Cold and hot combined equipment based on carbon dioxide heat pump |
CN111449141A (en) * | 2020-05-20 | 2020-07-28 | 广西格卡环保科技有限公司 | Dried bean production forming equipment under atmospheric steam condition |
CN213961659U (en) * | 2020-11-16 | 2021-08-17 | 辽宁正远食品有限公司 | Food steam energy-saving device |
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