CN111357827A - Novel online egg and bean curd production integrated equipment system - Google Patents
Novel online egg and bean curd production integrated equipment system Download PDFInfo
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- CN111357827A CN111357827A CN202010241223.2A CN202010241223A CN111357827A CN 111357827 A CN111357827 A CN 111357827A CN 202010241223 A CN202010241223 A CN 202010241223A CN 111357827 A CN111357827 A CN 111357827A
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- 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
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Abstract
Novel system is equipped in integration of online egg bean curd production, it relates to food production facility technical field, concretely relates to novel system is equipped in integration of online egg bean curd production. The device comprises an emulsifying head, an online defoaming emulsifying tank, a first liquid level meter, a first online defoaming cache tank, a second liquid level meter, a first rotor pump, a flowmeter, a coagulant tank, a micro metering medicine pump, a high-precision flowmeter, a static mixer, an A cache tank, a third liquid level meter, a second rotor pump, a pipeline filter, a first water-ring vacuum pump assembly, a second water-ring vacuum pump assembly, a control cabinet, a second online defoaming cache tank and a B cache tank. After the technical scheme is adopted, the invention has the beneficial effects that: it makes the stoste can stir abundant in process of production, mixes effectually, can get rid of the bubble, can incessant continuous production, and latency is shorter, and the point bittern is even, can accurate measurement, and the canning is high-efficient, and the material can not be extravagant.
Description
Technical Field
The invention relates to the technical field of food production equipment, in particular to a novel online egg and bean curd production integrated equipment system.
Background
In the production process of the existing egg bean curd production equipment, a large amount of bubbles are easily generated by liquid mixing, and the liquid mixing is not uniform enough; in the production process of the stock solution, the stirring is insufficient, the mixing effect is poor, the stock solution can not be continuously produced, and the waiting time is long; the bittern spotting is not uniform and can not be accurately measured; continuous canning is not efficient enough, and the material has the waste phenomenon.
Disclosure of Invention
The invention aims to provide a novel online egg and bean curd production integrated equipment system aiming at the defects and shortcomings of the prior art, which enables stock solution to be fully stirred in the production process, has a good mixing effect, can remove bubbles, can continuously and continuously produce, has short waiting time, is uniform in brine adding, can accurately measure, is efficient in canning, and does not waste materials.
In order to achieve the purpose, the invention adopts the following technical scheme: the on-line defoaming device comprises an emulsifying head, an on-line defoaming emulsifying tank, a first liquid level meter, a first on-line defoaming cache tank, a second liquid level meter, a first rotor pump, a flowmeter, a coagulant tank, a micro metering medicine pump, a high-precision flowmeter, a static mixer, a cache tank A, a third liquid level meter, a second rotor pump, a pipeline filter, a first water ring vacuum pump assembly, a second water ring vacuum pump assembly, a control cabinet, a second on-line defoaming cache tank and a cache tank B, wherein the emulsifying head is arranged at the upper end of the on-line defoaming emulsifying tank, the lower end of the first liquid level meter is inserted into the on-line defoaming emulsifying tank and fixed on the on-line defoaming emulsifying tank, the lower end of the second liquid level meter is vertically inserted into the first on-line defoaming cache tank and fixed on the first on-line defoaming cache tank, the lower end of the second liquid level meter is vertically inserted into the second on-line defoaming cache tank and fixed on the second on, the online defoaming emulsifying tank is connected with a first online defoaming cache tank through a pipeline, the first online defoaming cache tank is connected with a second online defoaming cache tank through a pipeline, the online defoaming emulsifying tank is connected with a second online defoaming cache tank through a pipeline, the second online defoaming cache tank is connected with a first rotor pump, the first rotor pump is connected with a flowmeter, the flowmeter is connected with a high-precision flowmeter, the high-precision flowmeter is respectively connected with a static mixer and a micro metering medicine pump, the micro metering medicine pump is connected with a coagulant tank, the static mixer is connected with an A cache tank, the lower end of a third liquid level meter is vertically inserted and fixed on the A cache tank, the A cache tank is connected with a B cache tank through a pipeline, the lower end of the second liquid level meter is vertically inserted and fixed on the B cache tank, the B cache tank is connected with a pipeline filter, the pipeline filter is connected with a second rotor pump, and a water ring vacuum pump assembly I is connected with the online defoaming cache tank, The first online defoaming cache tank and the second online defoaming cache tank are connected through pipelines, the second water-ring vacuum pump assembly is connected with the A cache tank and the B cache tank through pipelines, and the control cabinet is connected with the first water-ring vacuum pump assembly and the second water-ring vacuum pump assembly.
The vacuum feeding and vacuum emulsification defoaming system is composed of the emulsifying head, the online defoaming emulsifying tank, the first liquid level meter, the first online defoaming cache tank, the second liquid level meter, the second online defoaming cache tank and the water ring vacuum pump assembly, and the control cabinet is connected with the vacuum feeding and vacuum emulsification defoaming system.
The first online defoaming cache tank and the second online defoaming cache tank form an online continuous production system, and the control cabinet is connected with the online continuous production system.
The first rotor pump, the flowmeter, the high-precision flowmeter and the second rotor pump form an online metering system, and the control cabinet is connected with the online metering system.
The online cache tank defoaming and recycling system is composed of the cache tank A, the third liquid level meter, the second rotor pump, the pipeline type filter, the cache tank B, the water ring type vacuum pump assembly II and the valve, and the control cabinet is connected with the online cache tank defoaming and recycling system.
The type of the emulsifying head is HPR-JF11, the first rotor pump is a variable frequency rotor pump and is 40TLS12-5C, the second rotor pump is a variable frequency rotor pump and is 25TLS12-2C, the type of the first water ring type vacuum pump assembly is 2BV5131, and the type of the second water ring type vacuum pump assembly is 2BV 2070.
And a bubble pricking net is arranged in the online defoaming emulsification tank, the first online defoaming cache tank, the A cache tank, the second online defoaming cache tank and the B cache tank.
And a slow stirring system and a negative pressure system are arranged in the tank of the first online defoaming cache tank.
The structure of the first online defoaming cache tank is the same as that of the second online defoaming cache tank.
The structure of the A cache tank is the same as that of the B cache tank.
After the technical scheme is adopted, the invention has the beneficial effects that: it has formed vacuum feeding, broken bubble system of vacuum emulsification, online continuous production system, online measurement system, online buffer tank deaeration and recycle system, vacuum feeding, broken bubble system of vacuum emulsification: the use of a transport pump is reduced, the liquid in the tank can be uniformly mixed, a bubble-puncturing net is arranged in the tank, large bubbles generated in mixing can be effectively removed, and the negative pressure in the tank can timely remove micro bubbles;
an online continuous production system: slow stirring and negative pressure systems are arranged in the first online defoaming cache tank and the second online defoaming cache tank; the slow stirring system ensures that the liquid in the tank is fully stirred, and the mixing effect is ensured; the negative pressure system ensures that the mixing effect and residual bubbles can be removed in the liquid cache, and the two tanks can ensure the uninterrupted continuous production of the stock solution under the control of the system, thereby reducing the waiting time;
an online metering system: the mixed liquor is quantitatively conveyed by the cooperation of the rotor pump and the flowmeter, and the brine can be accurately metered under the control of the metering pump and the flowmeter; after the two liquids are proportioned by the Venturi pipeline, the two liquids are fully mixed by the static mixer, so that the bittern spotting uniformity of the two-phase liquids is ensured;
on-line cache tank deaeration and recycle system: the valve switches of the A cache tank and the B cache tank control the flow direction of liquid, the liquid after brine dripping is subjected to negative pressure deaeration and continuous canning again, the two tanks are alternately filled continuously more efficiently, the invalid waiting time is reduced, the recovery of the trickling materials after canning is finished through the logical relationship of the system, and the waste-free materials are realized.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic view of a first water-ring vacuum pump assembly 16 according to the present invention;
FIG. 3 is a schematic diagram of the structure of the control cabinet 18 of the present invention;
FIG. 4 is a control schematic block diagram of the present invention;
fig. 5 is a control relationship diagram of the a buffer tank 12 and the B buffer tank 20 in the present invention.
Description of reference numerals: the device comprises an emulsifying head 1, an online defoaming emulsifying tank 2, a first liquid level meter 3, a first online defoaming cache tank 4, a second liquid level meter 5, a first rotor pump 6, a flowmeter 7, a coagulant tank 8, a micro metering medicine pump 9, a high-precision flowmeter 10, a static mixer 11, an A cache tank 12, a third liquid level meter 13, a second rotor pump 14, a pipeline filter 15, a water-ring vacuum pump assembly I16, a water-ring vacuum pump assembly II 17, a control cabinet 18, a second online defoaming cache tank 19 and a B cache tank 20.
Detailed Description
Referring to fig. 1-4, the technical solution adopted by the present embodiment is that it includes an emulsification head 1, an online defoaming emulsification tank 2, a first level meter 3, a first online defoaming buffer tank 4, a second level meter 5, a first rotor pump 6, a flow meter 7, a coagulant tank 8, a micro metering medicine pump 9, a high-precision flow meter 10, a static mixer 11, an a buffer tank 12, a third level meter 13, a second rotor pump 14, a pipeline filter 15, a first water ring vacuum pump assembly 16, a second water ring vacuum pump assembly 17, a control cabinet 18, a second online defoaming buffer tank 19, and a B buffer tank 20, the emulsification head 1 is disposed at the upper end of the online defoaming emulsification tank 2, the lower end of the first level meter 3 is inserted into the online defoaming tank 2 and fixed on the online defoaming tank 2, the lower end of the second level meter 5 is vertically inserted into the first online defoaming buffer tank 4 and fixed on the first online defoaming tank 4, the lower end of a second liquid level meter 5 is vertically inserted into a second online defoaming cache tank 19 and fixed on the second online defoaming cache tank 19, an online defoaming emulsification tank 2 is connected with a first online defoaming cache tank 4 through a pipeline, the first online defoaming cache tank 4 is connected with a second online defoaming cache tank 19 through a pipeline, the online defoaming emulsification tank 2 is connected with the second online defoaming cache tank 19 through a pipeline, the second online defoaming cache tank 19 is connected with a first rotor pump 6, the first rotor pump 6 is connected with a flow meter 7, the flow meter 7 is connected with a high-precision flow meter 10, the high-precision flow meter 10 is respectively connected with a static mixer 11 and a micro metering medicine pump 9, the micro metering medicine pump 9 is connected with a coagulant tank 8, the static mixer 11 is connected with an A cache tank 12, the lower end of a third liquid level meter 13 is vertically inserted and fixed on the A cache tank 12, the A cache tank 12 is connected with a B cache tank 20 through a pipeline, the lower end of the second liquid level meter 13 is vertically inserted into and fixed on the B cache tank 20, the B cache tank 20 is connected with the pipeline type filter 15, the pipeline type filter 15 is connected with the second rotor pump 14, the first water ring type vacuum pump assembly 16 is in pipeline connection with the online defoaming emulsifying tank 2, the first online defoaming cache tank 4 and the second online defoaming cache tank 19, the second water ring type vacuum pump assembly 17 is in pipeline connection with the A cache tank 12 and the B cache tank 20, and the control cabinet 18 is connected with the first water ring type vacuum pump assembly 16 and the second water ring type vacuum pump assembly 17. The emulsifying head 1, the online defoaming emulsifying tank 2, the first liquid level meter 3, the first online defoaming cache tank 4, the second liquid level meter 5, the second online defoaming cache tank 19 and the water ring vacuum pump assembly I16 form a vacuum feeding and vacuum emulsifying defoaming system, and under the action of the vacuum feeding and vacuum emulsifying defoaming system, the mixed liquid of egg white and soybean milk is sucked into the online defoaming emulsifying tank 2 through the negative pressure of-0.07 to-0.085 in the tank, so that the use of a transport pump is reduced; the emulsifying head 1 in the on-line defoaming emulsifying tank 2 rotates at 3000r/min, and the stator and the rotor rotate at high speed at the linear speed of 25m/s to uniformly mix two-phase liquid, and the mixing effect is good.
The working principle of the invention is as follows: the mixed liquid of egg white and soybean milk is sucked into an online defoaming emulsification tank through negative pressure, the liquid is uniformly mixed through high-speed shearing collision of an emulsification head in the online defoaming emulsification tank, after the mixing is finished, the negative pressure is sucked into the online cache defoaming tank, and the defoaming process of the liquid is finished through a slow stirring system and a negative pressure system in the online cache defoaming tank; the brine liquid is added into the Venturi pipeline according to a certain proportion under the control of the micro metering chemical pump and the high-precision flow meter, so that online brine adding is realized; after the intensive mixing is accomplished through static mixer to the mixed liquid, get into A buffer tank, B buffer tank passes through the logical control of system and realizes two jar switching, both guarantee the continuous canning of liquid, the defoaming of completion liquid that again can be abundant, make liquid bubble-free when the canning, the design of canning head front end shape with be provided with the filter screen, can block, when making the canning, can ensure that the liquid bubble does not produce in a large number, the liquid of retrieving during the canning is under the transport of second rotor pump, retrieve in the A buffer tank, avoid the material extravagant.
Referring primarily to FIG. 5: the control relation of the A cache tank and the B cache tank is that when the system is initially started, the A cache tank 12 is preferentially fed, the feeding pump is started, the valve d is opened, the valve c is opened, the rest valves are closed, and the pump i is closed; when the material is filled in the A cache tank, the third liquid level meter 13 gives an alarm, after about 1.5min, the valve d is closed, the valve e is opened, the valve f is opened, the material is injected into the B cache tank 20, the valve c is closed, the valve a is opened, the A cache tank 12 is vacuumized for 2min, the valve a is closed, the valve c is opened to break the vacuum, and after 0.5min standing time, the valve g is opened to adjust and pack the material, and the flow assembly line normally starts to operate; at this time, the total time of the system for removing bubbles of one tank is 4min, and the time for boxing one tank can be kept to be 5min, so that when the A cache tank 12 is still in boxing, the B cache tank 20 has finished the vacuum breaking standing time, and after the liquid level at the bottom of the A cache tank 12 is alarmed, the valve G is closed, and the valve h can be opened to continuously ensure the assembly line boxing; when the valve h is opened, the control state of the buffer tank B20 is that the valve e is closed, the valve f is opened, and the valve B is closed; at the moment, the valve d of the buffer tank A12 is opened, the valve c is kept opened, the pump i is started, the buffer tank A12 starts to inject materials, when the high liquid level alarms, the process flow is repeated, the process flow is completed in 4min, the buffer tank B20 is replaced after waiting for about 1min, and the pump i is stopped after delaying until the liquid levels of the buffer tanks A12 and B20 are all low; and the bubble removing process control of the manual control A cache tank 12 and the manual control B cache tank 20 is added, so that the bubble removing process flow of the A cache tank 12 and the B cache tank 200 can be manually completed when the high liquid level is not reached at last.
The above description is only for the purpose of illustrating the technical solutions of the present invention and not for the purpose of limiting the same, and other modifications or equivalent substitutions made by those skilled in the art to the technical solutions of the present invention should be covered within the scope of the claims of the present invention without departing from the spirit and scope of the technical solutions of the present invention.
Claims (8)
1. Novel system is equipped in integration of online egg bean curd production, its characterized in that: the on-line defoaming device comprises an emulsifying head, an on-line defoaming emulsifying tank, a first liquid level meter, a first on-line defoaming cache tank, a second liquid level meter, a first rotor pump, a flowmeter, a coagulant tank, a micro metering medicine pump, a high-precision flowmeter, a static mixer, a cache tank A, a third liquid level meter, a second rotor pump, a pipeline filter, a first water ring vacuum pump assembly, a second water ring vacuum pump assembly, a control cabinet, a second on-line defoaming cache tank and a cache tank B, wherein the emulsifying head is arranged at the upper end of the on-line defoaming emulsifying tank, the lower end of the first liquid level meter is inserted into the on-line defoaming emulsifying tank and fixed on the on-line defoaming emulsifying tank, the lower end of the second liquid level meter is vertically inserted into the first on-line defoaming cache tank and fixed on the first on-line defoaming cache tank, the lower end of the second liquid level meter is vertically inserted into the second on-line defoaming cache tank and fixed on the second on, the online defoaming emulsifying tank is connected with a first online defoaming cache tank through a pipeline, the first online defoaming cache tank is connected with a second online defoaming cache tank through a pipeline, the online defoaming emulsifying tank is connected with a second online defoaming cache tank through a pipeline, the second online defoaming cache tank is connected with a first rotor pump, the first rotor pump is connected with a flowmeter, the flowmeter is connected with a high-precision flowmeter, the high-precision flowmeter is respectively connected with a static mixer and a micro metering medicine pump, the micro metering medicine pump is connected with a coagulant tank, the static mixer is connected with an A cache tank, the lower end of a third liquid level meter is vertically inserted and fixed on the A cache tank, the A cache tank is connected with a B cache tank through a pipeline, the lower end of the second liquid level meter is vertically inserted and fixed on the B cache tank, the B cache tank is connected with a pipeline filter, the pipeline filter is connected with a second rotor pump, and a water ring vacuum pump assembly I is connected with the online defoaming cache tank, The first online defoaming cache tank and the second online defoaming cache tank are connected through pipelines, the second water-ring vacuum pump assembly is connected with the A cache tank and the B cache tank through pipelines, and the control cabinet is connected with the first water-ring vacuum pump assembly and the second water-ring vacuum pump assembly.
2. The novel online integrated equipment system for egg bean curd production according to claim 1, wherein: the vacuum feeding and vacuum emulsification defoaming system is composed of the emulsifying head, the online defoaming emulsifying tank, the first liquid level meter, the first online defoaming cache tank, the second liquid level meter, the second online defoaming cache tank and the water ring vacuum pump assembly, and the control cabinet is connected with the vacuum feeding and vacuum emulsification defoaming system.
3. The novel online integrated equipment system for egg bean curd production according to claim 1, wherein: the first online defoaming cache tank and the second online defoaming cache tank form an online continuous production system, and the control cabinet is connected with the online continuous production system.
4. The novel online integrated equipment system for egg bean curd production according to claim 1, wherein: the first rotor pump, the flowmeter, the high-precision flowmeter and the second rotor pump form an online metering system, and the control cabinet is connected with the online metering system.
5. The novel online integrated equipment system for egg bean curd production according to claim 1, wherein: the online cache tank defoaming and recycling system is composed of the cache tank A, the third liquid level meter, the second rotor pump, the pipeline type filter, the cache tank B, the water ring type vacuum pump assembly II and the valve, and the control cabinet is connected with the online cache tank defoaming and recycling system.
6. The novel online integrated equipment system for egg bean curd production according to claim 1, wherein: the type of the emulsifying head is HPR-JF11, the first rotor pump is a variable frequency rotor pump and is 40TLS12-5C, the second rotor pump is a variable frequency rotor pump and is 25TLS12-2C, the type of the first water ring type vacuum pump assembly is 2BV5131, and the type of the second water ring type vacuum pump assembly is 2BV 2070.
7. The novel online integrated equipment system for egg bean curd production according to claim 1, wherein: and a bubble pricking net is arranged in the online defoaming emulsification tank, the first online defoaming cache tank, the A cache tank, the second online defoaming cache tank and the B cache tank.
8. The novel online integrated equipment system for egg bean curd production according to claim 1, wherein: and a slow stirring system and a negative pressure system are arranged in the tank of the first online defoaming cache tank.
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| CN202010241223.2A CN111357827B (en) | 2020-03-31 | 2020-03-31 | Novel online egg and bean curd production integrated equipment system |
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| CN202010241223.2A CN111357827B (en) | 2020-03-31 | 2020-03-31 | Novel online egg and bean curd production integrated equipment system |
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| CN111357827B CN111357827B (en) | 2022-09-16 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023203408A1 (en) * | 2022-04-19 | 2023-10-26 | Pavel Petrovich Pyvovarov | Method for obtaining an emulsion-type food product capable of being transformed into sauces |
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| CN111357827B (en) | 2022-09-16 |
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