CN115736160A - Continuous steam processing system and method - Google Patents
Continuous steam processing system and method Download PDFInfo
- Publication number
- CN115736160A CN115736160A CN202211344964.9A CN202211344964A CN115736160A CN 115736160 A CN115736160 A CN 115736160A CN 202211344964 A CN202211344964 A CN 202211344964A CN 115736160 A CN115736160 A CN 115736160A
- Authority
- CN
- China
- Prior art keywords
- bin
- pressure
- transition bin
- cooking
- storehouse
- 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.)
- Pending
Links
- 238000012545 processing Methods 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 22
- 230000007704 transition Effects 0.000 claims abstract description 153
- 239000000463 material Substances 0.000 claims abstract description 61
- 238000010411 cooking Methods 0.000 claims abstract description 60
- 239000000498 cooling water Substances 0.000 claims abstract description 24
- 238000007789 sealing Methods 0.000 claims abstract description 18
- 238000005507 spraying Methods 0.000 claims abstract description 16
- 230000008569 process Effects 0.000 abstract description 5
- 238000001816 cooling Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 241000209094 Oryza Species 0.000 description 8
- 235000007164 Oryza sativa Nutrition 0.000 description 8
- 238000003672 processing method Methods 0.000 description 8
- 235000009566 rice Nutrition 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 230000001954 sterilising effect Effects 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 239000013590 bulk material Substances 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 235000021395 porridge Nutrition 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Images
Landscapes
- Commercial Cooking Devices (AREA)
Abstract
A continuous steam processing system and a method thereof, wherein a steam system comprises a cooking bin, a front transition bin connected with the inlet end of the cooking bin, and a rear transition bin connected with the outlet end of the cooking bin, a first and/or a second series pipeline and a first and/or a second series pipeline valve are arranged between the front transition bin and/or the rear transition bin and the cooking bin, a cooling water spraying device is arranged in the rear transition bin, and the system further comprises a controller used for controlling the first and/or the second series pipeline valve and the cooling water spraying device. The air pressure inside the sealing box for bearing the processed material is balanced with the air pressure in the bin, which is lifted by heating, through control, so that the sealing box is prevented from being damaged. Moreover, through cooling water sprinkler, the temperature is lower when the material is taken out of the warehouse, need not to wait for the cooling and can transfer it to next process, has saved material transfer latency, has also reduced simultaneously because of the easy injured risk of material high temperature messenger operating personnel.
Description
Technical Field
The present invention relates to steam systems, and more particularly to a continuous steam processing system and method.
Background
An existing steam processing system such as a sterilization kettle is composed of a pot body, a pot cover, an opening device, a locking wedge block, a sterilization basket, a steam spray pipe and the like, but intermittent production can only be achieved, equipment needs to be pressurized again during production every time, and materials need to be conveyed manually in and out of a bin. The utility model patent No. 202023248760.4 of "totally closed steam processing system of continuous type" that figure 8 shows adopts the sectional type design in preceding transition storehouse, steam chamber, back transition storehouse, connects through pipeline, valve, gate between each storehouse and can realize continuous type production, and the while greatly reduces steam and leaks. However, in the steam processing system, when a product such as a lunch box is processed, the plastic box may be damaged. This occurs primarily when material enters the front transition bin and is ready to be taken out of the rear transition bin. When the material got into preceding transition storehouse, need open the connecting valve between preceding transition storehouse and the steam chamber, balanced two atmospheric pressure between the storehouse, the gate between two storehouses could be opened, lets the material get into the storehouse of cooking in the past transition storehouse. At this moment, the atmospheric pressure in the preceding transition storehouse promotes at the excessive speed, and the sealed plastic envelope box of shriveling can be pressed to the high atmospheric pressure in the storehouse to make the sealing opening damaged. And when the materials are ready to be taken out from the rear transition bin, the rear transition bin can open the gate only by reducing the pressure and keeping the pressure equal to the external air pressure. At the moment, the material still has higher temperature for also have higher atmospheric pressure in the seal box, then the step-down of transition bin has also increased the inside and external pressure differential of seal box, will lead to the bulging of plastic packaging box and the damage of sealing opening eventually.
Disclosure of Invention
The present invention is directed to overcoming the disadvantages of the prior art and providing a continuous steam processing system and method that solves the above-mentioned problems of the prior art.
According to one aspect of the invention, a continuous steam processing system is provided, comprising a cooking chamber, a front transition chamber connected to an inlet end of the cooking chamber, and a rear transition chamber connected to an outlet end of the cooking chamber, wherein a first and/or a second serial pipeline and a first and/or a second serial pipeline valve are arranged between the front transition chamber and/or the rear transition chamber and the cooking chamber, a cooling water spraying device is arranged in the rear transition chamber, and the system further comprises a controller for controlling the first and/or the second serial pipeline valve and the cooling water spraying device.
The controller controls the opening and closing of the first and/or second series pipe valves according to a predetermined pressure-increasing curve and/or pressure-decreasing curve.
The system also comprises an outer discharge device arranged on the front transition bin and/or the rear transition bin, wherein the outer discharge device comprises a water discharge and/or evacuation pipeline and a water discharge and/or evacuation valve.
The rear transition bin is also provided with a gas pipeline and a gas pipeline valve for inputting high-pressure air.
The controller controls the opening and closing of the gas pipeline valve according to a preset gas pressure range.
The controller is a PLC.
According to another aspect of the present invention there is provided a method of processing a material in a continuous steam processing system, the material being carried by a sealed box, the method comprising the steps of:
a. feeding the sealed box bearing the material into a front transition bin;
b. opening a first serial pipeline valve between the front transition bin and the cooking bin to enable steam in the cooking bin to flow into the front transition bin;
c. controlling the steam amount flowing into the front transition bin according to a set pressure-increasing curve;
d. detecting the pressure and/or temperature in the front transition bin;
e. judging whether the pressure raised in the front transition bin conforms to the boosting curve or not;
f. when the air pressure in the sealing box and the pressure raised in the front transition bin are kept balanced and the pressure difference between the front transition bin and the cooking bin is also balanced, the first serial pipeline valve is closed, and the sealing box is conveyed into the cooking bin.
According to another aspect of the invention, the method further comprises the steps of:
g. feeding the processed sealed box into a post-transition bin from the cooking bin;
h. opening a cooling water spraying device in the rear transition bin;
i. introducing high-pressure air into the rear transition bin;
j. judging whether the air pressure in the rear transition bin is maintained within a preset first air pressure range or not;
k. continuously opening the cooling water spraying device and introducing high-pressure air until the air pressure in the rear transition bin is maintained within a preset second air pressure range;
when the pressure difference between the post-transition bin and the cooking bin is balanced, and closing the cooling water spraying device and the introduction of high-pressure air, and sending the seal box out of the rear transition bin.
The first air pressure range is 1.3-1.35Bar, and the second air pressure range is 1.15-1.20Bar.
The method further comprises the step of opening a drain/evacuation valve of the front transition bin prior to step a.
According to the continuous steam processing system and the continuous steam processing method, the air pressure in the front transition bin is controlled to slowly rise, so that the air pressure in the sealing box for bearing the processed material, which is increased by heating, is balanced with the air pressure in the bin, and the sealing box is prevented from being damaged. Moreover, because the inside cooling water sprinkler that is provided with of back transition bin, the temperature is lower when the material is taken out of the warehouse, need not to wait for the cooling and can circulate it to next process, has saved material circulation latency, has also reduced simultaneously and has made the easy injured risk of operating personnel because of material high temperature.
Drawings
Other objects, advantages and effects of the present invention will become more apparent from the following description of the embodiments of the present invention taken in conjunction with the accompanying drawings. In the drawings:
FIG. 1 is an overall schematic diagram illustrating a continuous steam processing system according to one embodiment of the present invention.
FIG. 2 is a schematic diagram showing the pressure rise profile of a front transition bin in the continuous steam processing system of FIG. 1.
FIG. 3 is a partial schematic view illustrating an aft transition bin in the continuous steam processing system of FIG. 1.
FIG. 4 is a graph showing the pressure drop curve for the aft transition bin of FIG. 3.
Fig. 5 is a schematic flow diagram illustrating a continuous steam processing method according to an embodiment of the present invention.
Fig. 6 is a schematic flow chart showing a continuous steam processing method according to another embodiment of the present invention.
Fig. 7 is a schematic flow chart showing a continuous steam processing method according to another embodiment of the present invention.
FIG. 8 is a schematic diagram illustrating a prior art steam processing system.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the technical solutions of the present invention will be described in detail below with reference to specific embodiments of the present invention and accompanying drawings. It is to be understood that the described embodiments are merely a few embodiments of the invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The continuous steam processing system and the method can be used for processing foods such as rice cooking, porridge cooking and cooked wheaten food, and can also be used for sterilizing other objects at high temperature, killing enzyme at high pressure, drying and the like. The method has the characteristics of fast temperature rise of the whole system, no loss of steam, high production line and automation degree and the like. Thus, it will be understood by those skilled in the art that the "material" is not limited to rice, but may be carried by a carrier such as a "plastic box" (also referred to as a "sealed box"), for example, when the "material" is a bulk material such as rice.
Fig. 1 is an overall schematic view showing a continuous steam processing system according to an embodiment of the present invention. Referring to fig. 1, the continuous steam processing system according to the present invention includes a cooking compartment 1, a front transition compartment 2 connected to an inlet end of the cooking compartment 1, and a rear transition compartment 3 connected to an outlet end of the cooking compartment 1. In a preferred embodiment, the front end of the front transition bin 2 is further provided with a loading area 6, the rear end of the rear transition bin 3 is further provided with a unloading area 7, and a rotary conveyor line 8 is arranged between the unloading area and the loading area, for example, so that a material tray from which processed material has been unloaded in the unloading area can be reloaded with material to be processed and sent to the loading area. In another preferred embodiment, for example, a vibrating mechanism is provided on the conveyor belt in the loading zone, which is automatically activated for about 5 to 10 seconds when the material is ready to be fed into the front transition bin, for example, to allow a uniform distribution of the material in the sealed box.
The front transition bin 2 is provided with an inner gate 21 at a port interfacing with the cooking bin 1, for example, and an outer gate 22 at a port receiving the material (not shown). A conveyor belt is arranged between the outer gate 22 and the inner gate 21 for conveying the material fed from the outer gate 22 to the side of the inner gate 21 and to the inside of the cooking chamber 1 through the inner gate 21. In a preferred embodiment, the inner gate 21 and the outer gate 22 can be automatically lifted and lowered by the driving of the air cylinder. For example, when the material is fed into the front transition bin 2, the outer gate 22 is opened through the driving of the air cylinder, and after the material enters the front transition bin 2, the outer gate 22 is closed.
An external discharge device is arranged in the front transition bin 2, and can discharge air or condensed water in the bin out of the bin. This is due to the fact that the front transition bin, the cooking bin and/or the rear transition bin, for example, need to be preheated during the process, even if the steam pressure inside the front transition bin 2 would reach around 4kg, in which case the outer lock 22 cannot be opened for feeding the material into the front transition bin 2. Therefore, the front transition bin 2 needs to be firstly decompressed by the outer discharge device. Preferably, the discharge device of the front transition bin 2 includes a drainage/evacuation pipeline and a drainage/evacuation valve, for example, so that the front transition bin 2 can be depressurized before the material is fed into the discharge device to facilitate the opening of the outer gate 22, and the frequent opening and closing of the outer gate 22 increases the amount of air and condensed water inside the front transition bin 2, so that the drainage/evacuation valve needs to be opened for a certain time and then closed when the steam is introduced, so as to be discharged through the drainage/evacuation pipeline in due time. And when the pressure in the front transition bin and the atmospheric pressure difference are less than 0.2bar, the materials can be fed into the front transition bin 2.
According to one embodiment of the invention, a first communication pipe 25 and a first communication pipe valve 26 are arranged between the front transition bin 2 and the cooking bin 1, and can be used for guiding steam inside the cooking bin 1 to the front transition bin 2. That is, after the material is fed into the front transition bin 2, the pressure difference between the front transition bin 2 and the cooking bin 1 is large due to the pressure relief measures taken previously, and in this case, the inner gate 21 cannot be opened to feed the material into the cooking bin 1. Set up first serial pipeline and just can close the back at the outer gate in preceding transition storehouse 2, will cook the inside steam of storehouse 1 and introduce in preceding transition storehouse 2 inside, make preceding transition storehouse 2 and the steam pressure of cooking both insides in storehouse 1 equal to gate 21 in opening. In another embodiment, the first through-flow duct may also connect the front transition bin 2 directly to an external steam generator (not shown), for example, from which steam may also be introduced directly into the interior of the front transition bin 2 after the material is fed into the front transition bin 2 and the outer shutter 22 is closed.
FIG. 2 is a schematic graph showing the pressure rise profile of a front transition bin in the continuous steam processing system of FIG. 1. Referring to fig. 1 and 2, when a material to be processed, such as rice, is carried by a sealed box, such as a plastic box, the air pressure in the good chamber must be controlled to increase speed, so that the pressure inside and outside the sealed box is balanced. If the air pressure rises too fast, the high pressure in the bin will collapse the sealing box and cause the sealing opening to be broken. According to another embodiment of the present invention, the first through-line valve is controlled in opening degree by a controller (e.g., PLC) according to a set pressure and time. That is, the controller detects the pressure and/or temperature in the bin, for example, by a pressure sensor and/or a temperature sensor, and controls the steam amount flowing into the front transition bin from the cooking bin through the first through pipe valve, so that the air pressure in the front transition bin is boosted according to a set boosting curve, and the air pressure raised by the steam heating in the sealed box loaded with the materials is balanced with the pressure raised in the front transition bin, so that the sealed box is not damaged, for example, is deflated, due to too large difference between the inner pressure and the outer pressure. It will be understood by those skilled in the art that the pressure-increasing curve shown in fig. 2 is tested and set according to parameters such as processing properties of rice, and when the material carried in the sealed box is of other varieties, for example, the pressure-increasing curve can be adjusted according to specific situations.
FIG. 3 is a schematic illustration of a portion of an aft transition bin of the continuous steam processing system of FIG. 1, and FIG. 4 is a schematic illustration of a pressure reduction curve of the aft transition bin of FIG. 3. With combined reference to fig. 1 to 4, as with the arrangement of the front transition bin 2, the rear transition bin 3 is provided with an inner gate 31, for example at the port where it is docked with the cooking bin 1, and an outer gate 32 at the port where the material (not shown) is delivered. A conveyor belt is also arranged between the inner gate 31 and the outer gate 32 for conveying the material output from the cooking chamber 1 to the outer gate 32 and outputting outwards through the outer gate 32. Preferably, an external discharge device is also arranged on the rear transition bin 3, and the external discharge device comprises a drainage/evacuation pipeline and a drainage/evacuation valve. A second communicating pipeline 35 and a second communicating pipeline valve 36 are arranged between the rear transition bin 3 and the cooking bin 1. In another embodiment, the second series-pass duct may also connect the rear transition bin 3 directly to an external steam generator (not shown), for example. The rear transition bin 3 is provided with a cooling water spraying device 35 inside, which is located above the conveyor belt, for example, and comprises a plurality of atomizing nozzles 351 arranged along the length direction of the rear transition bin, and the latter is mounted on a cooling water pipeline through a flange, for example, so as to be convenient for later maintenance. After the material is processed in the cooking bin 1, the system controller controls to open a second serial pipeline valve between the cooking bin and the rear transition bin, and the steam in the cooking bin is introduced into the rear transition bin. When the air pressure in the rear transition bin is increased to be less than 0.2bar of the air pressure difference with the cooking bin, the system opens the inner gate 31 between the rear transition bin 3 and the cooking bin 1, and the sealing box for loading materials is conveyed into the rear transition bin 3 by the conveyor belt. Then, the system closes the inner gate 31 and the second serial pipeline valve, opens the outer discharge device in the rear transition bin, slightly reduces the air pressure in the rear transition bin, seals the inner gate 31 due to the adsorption of the air pressure difference between the two bins, and forms a closed space again in the rear transition bin. At this time, the system opens the cooling water spraying device 35, and the cooling water is sprayed on the surface of the seal box through the atomizing nozzle 351, so that the temperature of the material in the seal box is reduced, thereby reducing the air pressure inside the seal box and preventing the seal box from being broken by expansion or the seal opening from being damaged due to overhigh air pressure in the seal box.
Meanwhile, the system inputs high-pressure air into the rear transition bin 3 through a pipeline 38, and the opening degree of a valve of the gas pipeline is controlled by the controller, so that the air pressure in the rear transition bin is kept at 1.3-1.35bar (which can be adjusted according to different materials), and the steam in the rear transition bin is prevented from being condensed due to the spraying of cooling water, and the air pressure in the rear transition bin is prevented from being sharply reduced. After a period of time, the pressure in the chamber is maintained between 1.15 and 1.20bar. After the temperature is reduced for a plurality of times (the specific time is determined according to the types and the quantity of the processed materials), the system closes the cooling water spraying device 35, opens the outer discharging device in the rear transition bin again, reduces the pressure in the rear transition bin, and meanwhile recovers the cooling water to a reservoir (not shown) through a pipeline for reutilization. When the pressure difference between the air pressure in the rear transition bin and the atmospheric pressure is less than 0.2bar, the system opens the outer gate 32 of the rear transition bin, and the sealed box for loading materials is conveyed out of the bin to a discharging area. It will be understood by those skilled in the art that the pressure-reducing curve shown in fig. 4 is tested and set according to parameters such as processing properties of rice, and when the material carried in the sealed box is of other varieties, for example, the pressure-reducing curve can be adjusted according to specific situations.
The interior of the cooking chamber 1 is provided with a conveyor belt for conveying materials entering the inlet end 11 of the cooking chamber 1 from the front transition chamber 2 to the interior thereof, and the materials in the sealing box, such as rice grains, are cooked by the steam in the cooking chamber and then conveyed to the rear transition chamber 3 by the conveyor belt through the outlet end 12 thereof. According to one embodiment of the invention, the cooking bin 1, the front transition bin 2 and the rear transition bin 3 are respectively provided with a material conveying belt, the latter comprises a conveying chain and a net rack, each section of the conveying belt can be controlled by an independent motor to operate, operation and control of each bin can be simpler and more convenient, and the net rack adopts a grid structure to increase friction force between the net rack and a material sealing box, so that the material is conveyed more stably. Preferably, a pressure sensor 41 and a temperature sensor 42 are arranged in the front transition bin, the cooking bin and the rear transition bin, and are matched with a system controller to monitor and control the air pressure and the temperature in each bin in real time.
Fig. 5 is a schematic flow diagram illustrating a continuous steam processing method according to an embodiment of the present invention. Referring to fig. 1 and 5 in combination, the continuous steam processing method according to the present invention includes the steps of: s1, preheating a front transition bin, a cooking bin and a rear transition bin by a system; s2, controlling the front transition bin to exhaust by the system; and S3, judging whether the pressure of the front transition bin and the atmospheric pressure difference are less than 0.2Bar by the system. If not, the system sends out an alarm prompt, if yes, in step S4, the system sends the sealing box loaded with the processed material into the front transition bin and slowly inflates the front transition bin; and S5, judging whether the pressure difference between the front transition bin and the cooking bin is less than 0.2Bar by the system. If not, the system sends out an alarm prompt, if yes, in step S6, the system sends the sealing box into the cooking bin and processes the materials; s7, controlling the rear transition bin to inflate by the system; s8, the system judges whether the pressure difference between the post-transition bin and the cooking bin is less than 0.2Bar. If not, the system sends out an alarm prompt, if so, in step S9, the system sends the seal box into a rear transition bin; and S10, the system continuously judges whether the air pressure of the rear transition bin and the atmospheric pressure difference are less than 0.2Bar. If not, the system sends out an alarm prompt, and if so, the system sends the seal box out of the rear transition bin for blanking.
Fig. 6 is a schematic flow chart showing a continuous steam processing method according to another embodiment of the present invention. Referring to fig. 1, 5 and 6, in step S40, the system determines whether the sealed box loaded with the processed material has been fed into the front transition bin. If yes, in step S41, the system opens a first serial pipeline valve between the front transition bin and the cooking bin to enable steam in the cooking bin to flow into the front transition bin; s42, controlling the steam amount flowing into the front transition bin by the system according to a set pressure-increasing curve; s43, detecting the pressure and/or temperature in the front transition bin by the system; in step S44, the system determines whether the pressure in the front transition bin is consistent with the boost curve (i.e. the consistency indicates that the pressure in the seal box is substantially balanced with the pressure in the front transition bin). If not, the system returns to the step S42, if so, the system enters the step S45, and whether the pressure difference between the front transition bin and the cooking bin is balanced or not is judged. If so, the system closes the first series line valve and feeds the capsule into the cooking chamber in step S46.
Fig. 7 is a schematic flow chart showing a continuous steam processing method according to another embodiment of the present invention. Referring to fig. 1, 5 and 7 in combination, in step S90, the system determines whether the sealed box with the processed material has been fed into the rear transition bin. If yes, in step S91, the system turns on the cooling water spray device; step S92, introducing high-pressure air into the rear transition bin by the system; and step S93, judging whether the air pressure in the rear transition bin is maintained within the range of 1.3-1.35Bar by the system. If yes, the system continues to determine whether the spraying of the cooling water and the introduction of the high pressure air have been for a prescribed time in step S94. If yes, the system proceeds to step S95 to determine whether the air pressure maintained in the post-transition bin has dropped to 1.15-1.20Bar. If yes, the system shuts down the cooling water spray and the introduction of high pressure air in step S96. Those skilled in the art will appreciate that some steps in the flow shown in fig. 7 may be adjusted according to the type of the material to be processed, the processing conditions, and other parameters, including the adjustment of the sequence of the front and back processing, the adjustment of the pressurization amount of the high-pressure air, and the adjustment of the processing time. For reference, table 1 lists the operating node schedule for a sealed box of material to be processed, such as rice, in the post-transition bin cooling process.
TABLE 1
| Time (S) | |
| 0 | Material is prepared to enter the rear transition bin |
| 80-100 | First pressurization: 1.34-1.35Bar |
| 85 | The materials enter the bin and start to spray water |
| 100-430 | And (3) second pressurization: 1.25-1.3Bar |
| 450 | Beginning to drain |
| 550 | Stop spraying water |
| 599 | Stopping the drainage |
According to another embodiment of the invention, a system is configured, for example, with a computer device including a processor and a memory, which when executed by the processor, performs the method flows illustrated in fig. 5-7.
Various changes and modifications may be suggested to one skilled in the art based on the teachings herein, but are within the scope of the appended claims.
Claims (10)
1. The utility model provides a continuous steam processing system, includes the storehouse of cooking, connects the preceding transition storehouse of the storehouse entrance point of cooking, and connects the back transition storehouse of the storehouse exit end of cooking, preceding transition storehouse and/or back transition storehouse with be provided with first and/or second intercommunication pipeline and first and/or second intercommunication pipeline valve between the storehouse of cooking, be provided with cooling water sprinkler in the back transition storehouse, the system still includes and is used for controlling first and/or second intercommunication pipeline valve with cooling water sprinkler's controller.
2. The system of claim 1, wherein the controller controls opening and closing of the first and/or second series-connected piping valves according to a predetermined pressure-up profile and/or pressure-down profile.
3. The system according to claim 1, further comprising an external discharge device disposed at the front transition bin and/or the rear transition bin, wherein the external discharge device comprises a drain and/or an evacuation pipe and a drain and/or an evacuation valve.
4. The system of any one of claims 1 to 3, wherein the rear transition bin is further provided with a gas pipeline for inputting high pressure air and a gas pipeline valve.
5. The system of claim 4, wherein the controller controls the opening and closing of the gas line valve according to a predetermined gas pressure range.
6. The system of claim 1 or 5, wherein the controller is a PLC.
7. A method of processing a material carried by a sealed box using the continuous steam processing system of claim 1, the method comprising the steps of:
a. feeding the sealed box bearing the material into a front transition bin;
b. opening a first serial pipeline valve between the front transition bin and the cooking bin to enable steam in the cooking bin to flow into the front transition bin;
c. controlling the steam amount flowing into the front transition bin according to a set pressure-rising curve;
d. detecting the pressure and/or temperature in the front transition bin;
e. judging whether the pressure raised in the front transition bin conforms to the boosting curve or not;
f. when the air pressure in the sealing box and the pressure raised in the front transition bin are kept balanced and the pressure difference between the front transition bin and the cooking bin is also balanced, the first serial pipeline valve is closed, and the sealing box is conveyed into the cooking bin.
8. The method of claim 7, further comprising the steps of:
g. feeding the processed sealed box into a rear transition bin from the cooking bin;
h. opening a cooling water spraying device in the rear transition bin;
i. introducing high-pressure air into the rear transition bin;
j. judging whether the air pressure in the rear transition bin is maintained within a preset first air pressure range or not;
k. continuously opening the cooling water spraying device and introducing high-pressure air until the air pressure in the rear transition bin is maintained within a preset second air pressure range;
and l, when the pressure difference between the rear transition bin and the cooking bin is balanced, closing the cooling water spraying device and the high-pressure air, and sending the sealing box out of the rear transition bin.
9. The method of claim 8, wherein said first gas pressure is in the range of 1.3-1.35Bar and said second gas pressure is in the range of 1.15-1.20Bar.
10. A computer device comprising a processor and a memory, characterized in that when said memory is run by said processor, the method according to claim 7 or 8 is performed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211344964.9A CN115736160A (en) | 2022-10-31 | 2022-10-31 | Continuous steam processing system and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211344964.9A CN115736160A (en) | 2022-10-31 | 2022-10-31 | Continuous steam processing system and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN115736160A true CN115736160A (en) | 2023-03-07 |
Family
ID=85354421
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202211344964.9A Pending CN115736160A (en) | 2022-10-31 | 2022-10-31 | Continuous steam processing system and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN115736160A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN208510003U (en) * | 2017-12-22 | 2019-02-19 | 大姚华盛饮料食品有限责任公司 | A kind of integrated sterilized device of storehouse formula of beverage bottle tank |
| CN111374261A (en) * | 2018-12-27 | 2020-07-07 | 广东东软学院 | Cooking equipment with rapid cooling function |
| CN112773182A (en) * | 2020-12-29 | 2021-05-11 | 浙江同景新能源集团有限公司 | Continuous totally-enclosed steam processing system and method |
| CN213153836U (en) * | 2020-07-14 | 2021-05-11 | 浙江五芳斋实业股份有限公司 | Horizontal high-pressure water bath of zongzi cooling all-in-one that disinfects of cooking |
| CN214371295U (en) * | 2021-02-25 | 2021-10-08 | 佛山市潜信达酿酒包装设备有限公司 | Cooling device of rice steaming machine |
| CN114009655A (en) * | 2021-11-24 | 2022-02-08 | 广东巧能机电科技有限公司 | Full-automatic efficient energy-saving cooking production line |
-
2022
- 2022-10-31 CN CN202211344964.9A patent/CN115736160A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN208510003U (en) * | 2017-12-22 | 2019-02-19 | 大姚华盛饮料食品有限责任公司 | A kind of integrated sterilized device of storehouse formula of beverage bottle tank |
| CN111374261A (en) * | 2018-12-27 | 2020-07-07 | 广东东软学院 | Cooking equipment with rapid cooling function |
| CN213153836U (en) * | 2020-07-14 | 2021-05-11 | 浙江五芳斋实业股份有限公司 | Horizontal high-pressure water bath of zongzi cooling all-in-one that disinfects of cooking |
| CN112773182A (en) * | 2020-12-29 | 2021-05-11 | 浙江同景新能源集团有限公司 | Continuous totally-enclosed steam processing system and method |
| CN214371295U (en) * | 2021-02-25 | 2021-10-08 | 佛山市潜信达酿酒包装设备有限公司 | Cooling device of rice steaming machine |
| CN114009655A (en) * | 2021-11-24 | 2022-02-08 | 广东巧能机电科技有限公司 | Full-automatic efficient energy-saving cooking production line |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6442866B2 (en) | Method and apparatus for drying or heat-treating products | |
| US4830278A (en) | Steam sterilizing apparatus | |
| EP0302586B1 (en) | Method and apparatus for the continuous preservation of products in lump form | |
| US4547383A (en) | Continuous food sterilization system with hydrostatic sealed treatment chamber | |
| US5361683A (en) | Apparatus for batch cooking and packing fruit and vegetable pieces | |
| US8919080B2 (en) | Machine and method for packaging and high-pressure treatment of products | |
| JP2011226774A (en) | Apparatus for cooling or heating discrete materials | |
| US4604948A (en) | Continuous food sterilization system with hydrostatic sealed treatment chamber | |
| US5427810A (en) | Method for hydrothermal treatment of starch products, particularly rice | |
| CN115736160A (en) | Continuous steam processing system and method | |
| CA2585919A1 (en) | Treatment device and method for treating food products with conditioned air | |
| US6557319B1 (en) | Temperature coordinated through-line food packaging system | |
| KR100242633B1 (en) | Microwave sterillizer | |
| US3780446A (en) | Automatic hopper loader | |
| US5447550A (en) | Method and apparatus for the pneumatic transport of iron-bearing particles | |
| US5084243A (en) | Turret sterilizer | |
| CN112773182A (en) | Continuous totally-enclosed steam processing system and method | |
| CN210250633U (en) | High-temperature continuous sterilizer | |
| JPH0224514B2 (en) | ||
| CN101444321A (en) | Fully automatic high temperature high pressure sterilizing method | |
| US6637982B2 (en) | Gas transportation method for grain | |
| CN214712025U (en) | Continuous totally-enclosed steam processing system | |
| EP0222965A1 (en) | Method and apparatus for pre-cooking rice and other cereals | |
| JPH0420587B2 (en) | ||
| AU783404B2 (en) | Gas transportation method for grain |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |