CN203040612U - Continuous-type material soaking-cooking device - Google Patents
Continuous-type material soaking-cooking device Download PDFInfo
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- CN203040612U CN203040612U CN 201320014776 CN201320014776U CN203040612U CN 203040612 U CN203040612 U CN 203040612U CN 201320014776 CN201320014776 CN 201320014776 CN 201320014776 U CN201320014776 U CN 201320014776U CN 203040612 U CN203040612 U CN 203040612U
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Abstract
The utility model discloses a continuous-type material soaking-cooking device. The continuous-type material soaking-cooking device comprises a basket for holding materials, and a tunnel-type soaking-cooking device for enabling the basket to run continuously, wherein a material preheating section, a material soaking-cooking section, a material pre-cooling section and a material cooling section are arranged in the soaking-cooking device; after the basket enters the inlet end of the soaking-cooking device, the basket sequentially passes through the material preheating section, the material soaking-cooking section, the material pre-cooling section and the material cooling section under the driving of a chain drive mechanism, and then runs to the outlet end of the soaking-cooking device; the material preheating section, the material soaking-cooking section, the material pre-cooling section and the material cooling section are provided with circulating water storage grooves respectively; the material preheating section is provided with a preheating water spray tube, the material soaking-cooking section is provided with a soaking-cooking hot water spray tube, and the material pre-cooling section is provided with a pre-cooling water spray tube; and the basket is of a periphery-closed structure, a plurality of rows of water outlets are formed in the bottom of the basket, and the water level of the basket is always kept at the height needed by material soaking-cooking. The sterilized materials are always soaked and cooked in hot water during a running process; and the continuous-type material soaking-cooking device is remarkable in heat transfer effect, uniform in heating, and good in sterilization effect.
Description
Technical field
The utility model relates to a kind of material sterilizing unit, relates in particular to a kind of continuous material digestion device.
Background technology
At present, the sterilization of material such as flexible packaging food, tinned food mainly contains full ability of swimming sterilizing unit, goes up sterilizing units such as fountain sterilizing unit, side fountain sterilizing unit.
Full ability of swimming sterilizing unit is exactly that product is fully immersed in the sterilization form of carrying out in the hot water.The advantage of this sterilizing unit is to treat that sterilization material (product) contacts fully with hot water, and heat-transfer effect is remarkable.But owing to treat that the sterilization material layering is placed in the cage basket (or sterilization dish), recirculated water mobile property in centre is bad, heat inhomogeneous, for the product that is placed in the centre is fully heated, heat time heating time must be prolonged, this the material that reaches peripheral tier up and down will occur being placed in and produce the sterilization phenomenon, makes same batch material can not reach same bactericidal effect.
Last fountain sterilizing unit is to heat the mode of carrying out sterilization from last towards treating that sterilization material (product) sprays, and the advantage of this sterilizing unit is that the material that each level is put is heated evenly, but heat-transfer effect does not have full ability of swimming sterilization remarkable.
Side fountain sterilizing unit be with hot water by all directions are to treating sterilization material hot-water spraying simultaneously from the side in the nozzle, the material homogeneous heating of each position, but need the shower water passage takies bigger space.
Summary of the invention
The utility model is intended to the advantage of comprehensive above-mentioned sterilizing unit, overcome its shortcoming, a kind of continuous material digestion device is provided, and this device can be continuously carry out automation sterilization (digestion) to same batch of material to be handled, and heat-transfer effect is good, homogeneous heating, heat energy utilization rate height.
The technical scheme that the utility model adopts is: a kind of continuous material digestion device, comprise and hold the cage basket for the treatment of the digestion material and provide the cage basket to make the tunnel type digestion device of operation continuously, be provided with material preheating section, material digestion section, material precooling zone in the described digestion device, the material cooling section, after the cage basket enters the arrival end of digestion device, pass through material preheating section, material digestion section, material precooling zone under the driving of chain drive mechanism successively, the port of export to the digestion device behind the material cooling section moves; The lower position of cage basket operation is respectively equipped with and described material preheating section, material digestion section, material precooling zone, corresponding material preheating water circulation aqua storage tank, material digestion hot water circuit aqua storage tank, material pre-cold water circulation aqua storage tank and the material cooling water circulation aqua storage tank that arranges in material cooling section position; Described material preheating section is provided with the preheating water jet pipe, described material digestion section is provided with digestion hot water jet pipe, described material precooling zone is provided with the precooling water spray pipe, described material cooling section is provided with cooling water nozzle, and above-mentioned each jet pipe places the top position of cage basket operation respectively and is connected the realization periodical feeding by water circulating pump with separately aqua storage tank; Described material digestion water circulation aqua storage tank is connected with digestion device vapour source outward by steam valve and jet chimney; The outer cold water source of digestion device is connected with cooling water nozzle with described material cooling water circulation aqua storage tank respectively by cooling water replenishment valve and cooling water pipeline; Described preheating water jet pipe is provided with draining valve and drainpipe; In material digestion section, the flow direction of the recirculated water of material digestion aqua storage tank and the traffic direction of cage basket are reverse, and its temperature is by the temperature of the steam flow in the automatic steam regulation pipe of water temperature control device with the required hot water of realization digestion; Described cage basket is the border seal structure, its bottom is provided with the water holes of discharging more, the water yield three's of the injection flow rate of the digestion hot water jet pipe of the flow of water circulating pump, material digestion section and cage basket bottom aperture relation with keep height of water level certain in the cage basket to adapt and flow by the control water circulating pump maintains the required height of digestion material all the time with the water level that guarantees the cage basket.
The beneficial effects of the utility model: 1, this device holds the cage basket of material in running in material sterilization processing process, by the sterilization material all the time digestion in hot water, contact fully with hot water, heat-transfer effect is remarkable; And sterilization hot water is constantly replenished by the top jet pipe, and the water level in the cage basket is that recirculated water keeps under flow regime, and cage basket temperature everywhere is consistent, and it is temperature required to make the material by sterilization that enters material digestion section remain sterilization, homogeneous heating.2, the antikinesis of cage basket (material) and recirculated water can also greatly improve the cleanliness factor of material, has improved the quality of product, and the entrained heat of recirculated water has also passed to material simultaneously, has saved the consumption of recirculated water and steam.3, the water in the cage basket be under the news that constantly flows more by transmission continuously, so just realized serialization production.
In sum, this device has full ability of swimming sterilizing unit heat and transmits the advantage that (exchange) abundant and last fountain sterilizing unit, side fountain sterilizing unit material are heated evenly, compact overall structure, heat-transfer effect are good, homogeneous heating, heat energy utilization rate height, can carry out the automation continuous sterilizing to same batch of material and handle.
The utility model is described in further detail below in conjunction with accompanying drawing and the specific embodiment.
Description of drawings
Fig. 1 is overall structure and the process flow diagram of an embodiment of the utility model.
Fig. 2 is the front view of cage basket.
Fig. 3 is the vertical view of Fig. 1.
Fig. 4 is the side view of Fig. 1.
Drawing major part explanation: 1. cage basket, 2. material preheating section, 3. preposition vacant section, 4. material digestion section, 5. rearmounted vacant section, 6. material precooling zone, 7. material cooling section, 8. chain drive mechanism, 9. water circulating pump, 10. steam valve, 11. jet chimneys, 12. cooling water replenishment valve, 13. cooling water pipeline, 14. drainpipes, 15. draining valves, 16. the digestion device, 17. lifting carts, 18. excessive supports.
The specific embodiment
As shown in Figure 1, a kind of continuous material digestion of present embodiment device, comprise and hold the cage basket for the treatment of the digestion material and provide the cage basket to make the tunnel type digestion device 16 of operation continuously, be provided with material preheating section 2, material digestion section 4, material precooling zone 6 in the described digestion device 16, material cooling section 7, after cage basket 1 enters the arrival end of digestion device, pass through material preheating section 2, material digestion section 4, material precooling zone 6 under the driving of chain drive mechanism 8 successively, material cooling section 7 backs are to the port of export operation of digestion device; The lower position of cage basket operation is respectively equipped with and described material preheating section 2, material digestion section 4, material precooling zone 6, corresponding material preheating water circulation aqua storage tank 2.1, material digestion hot water circuit aqua storage tank 4.1, the pre-cold water circulation of material aqua storage tank 6.1 and the material cooling water circulation aqua storage tank 7.1 that arranges in material cooling section 7 positions; Described material preheating section 2 is provided with preheating water jet pipe 2.2, described material digestion section 4 is provided with digestion hot water jet pipe 4.2, described material precooling zone 6 is provided with precooling water spray pipe 6.2, described material cooling section 7 is provided with cooling water nozzle 7.2, and above-mentioned each jet pipe places the top position of cage basket operation respectively and is connected the realization periodical feeding by water circulating pump 9 with separately aqua storage tank; Described material digestion water circulation aqua storage tank 4.1 is connected with digestion device 16 vapour source outward by steam valve 10 and jet chimney 11; Digestion device 16 outer cold water sources are connected with cooling water nozzle 7.2 with described material cooling water circulation aqua storage tank 7.1 respectively by cooling water replenishment valve 12 and cooling water pipeline 13; Described preheating water jet pipe 2.2 is provided with draining valve 15 and drainpipe 14; In material digestion section 4, the flow direction of the recirculated water of material digestion aqua storage tank and the traffic direction of cage basket are reverse, and its temperature is by the temperature of the steam flow in the automatic steam regulation pipe of water temperature control device with the required hot water of realization digestion; Described cage basket 1 is the border seal structure, its bottom is provided with the water holes 1.1 of discharging more, the water yield three's of the injection flow rate of the digestion hot water jet pipe 4.2 of the flow of water circulating pump 9, material digestion section 4 and cage basket bottom aperture relation adapts with maintenance cage basket 1 interior certain height of water level and maintains the required height of digestion material by the flow of controlling water circulating pump 9 all the time with the water level that guarantees the cage basket, constitute the nozzle of top setting continuously to sterilization cage basket spray recirculated water, sterilization cage basket is by the cyclic process of bottom apopore water outlet, digestion bottom of device continuous effluent.
At each process section, as long as water level descends, all can replenish automatically, thereby reach the constant of the interior recirculated water water level of each process section aqua storage tank.
In the present embodiment, for the more abundant heat that how to reclaim, at this material preheating section 2 is designed to two sections, namely described material preheating section 2 is divided into initial intensification section 2a and secondary temperature elevation section 2b.For preventing that granular material in the cage basket is in the digestion process, because the phenomenon that foams and overflow may appear in recirculated water in the cage basket, be provided with a circle spout hole 1.2 at h place, the upper edge of described cage basket 1, the foam that foaming is produced overflows the cage basket, and prevents that recirculated water and material from coming out with the current that overflow from cage basket upper edge.Influence flowing of cage basket recirculated water for preventing that under any circumstance granular material can not blocked slotted hole, the width of the apopore of cage basket 1 bottom be less than the solid material that holds minimum dimension (diameter) 1/2, length be greater than the solid material that holds full-size (diameter) 4-6 doubly.The upper outside of cage basket 1 is provided with boss 1.3, can conveniently the cage basket be installed in to move also on the chain drive to prevent that the material in the cage basket from being polluted by external environment condition.
For the water in the cage basket has been flowed fully, the recirculated water that makes heating does not mix with water in the secondary temperature elevation section.Be provided with preposition vacant section 3 between described material preheating section 2 and the material digestion section 4, its top does not have sparge pipe.For the water in the cage basket has been flowed fully, the recirculated water that makes heating does not mix with cold water in the cooling section, is provided with rearmounted vacant section 5 between described material digestion section 4 and the material precooling zone 6, does not have sparge pipe above it.
Be energy savings, described material preheating water circulation aqua storage tank 2.1, material digestion water circulation aqua storage tank 4.1, the pre-cold water circulation of material aqua storage tank 6.1 and material cooling water circulation aqua storage tank 7.1 are communicated with successively.Material preheating water circulation aqua storage tank 2.1 hot water are transmitted by material digestion water circulation aqua storage tank.The recirculated water of the pre-cold water circulation of material aqua storage tank is transmitted by material cooling water circulation aqua storage tank, through circulation, material temperature can be reduced.The temperature of recirculated water improves, and reaches the heat recovery purpose.
What deserves to be explained is: under identical environmental condition, only relevant with the liquid level of water by the flow velocity of cage basket bottom many platoon leaders Kong Shui.Because the flow of the water that gets off from the top spray of cage basket is certain, so the water yield that the cage basket obtained in the unit interval also is certain.Simultaneously, because the perforated area of cage basket bottom also is certain, then enter the flow Q of the water of cage basket
Advance=Q
Go out=SV (S is the gross area of cage basket bottom slotted hole, and V is water flow velocity).Work as Q
AdvanceQ
Go outThe time, will cause the liquid level of the water in the cage basket to raise, and the rising of the liquid level of the water in the cage basket cause the increase of the water flow velocity that spills, Q again conversely from the slotted hole of cage basket bottom
AdvanceBe constant, then when the liquid level of the water in the cage basket is elevated to a certain degree, will make Q
Advance=Q
Go out, the water yield that namely keeps during the liquid level of the water in new cage basket entering in the unit interval in the cage basket equates with the water yield in the outflow cage basket.Therefore in the full-automatic continous way sterilizing unit with spray and hot water circulating device, hold treat the sterilization material the cage basket in running, by the sterilization material all the time digestion in hot water, contact fully with hot water, heat-transfer effect is remarkable; And sterilization hot water is constantly replenished by upper spray pipe, water level in the cage basket in the transmission remains at desired location, cage basket temperature everywhere is consistent, and it is temperature required to make the material by sterilization that enters material digestion section remain sterilization, homogeneous heating.
The continuous operation under the control of system control device of this continous way digestion device, treat that the sterilization material dosing is contained in the cage frame, the cage frame is under the driving of chain, material in the cage frame continuously from the material inlet end successively along material preheating section 2, preposition vacant section 3, material digestion section 4, rearmounted vacant section 5, material precooling zone 6, material cooling section 7 travels at the uniform speed towards the material outlet end, and the shower water on cage basket top is successive, unrestrained in the cage basket uniformly, spray the material in the water process cage basket in the cage basket, flow out from the apopore of cage basket bottom, finish the digestion continuous sterilizing process of material.Used time when the steaming stage is exactly the needed digestion time of material material.
Advance the material preheating section at the cage frame, material is sprayed and is formed soaking state and pre-the intensification by warm water.These shower waters are transmitted by material digestion section, but the hot water that material digestion section is come no longer is heated herein, only are the heat transferred materials that hot water carries oneself, so material temperature is raise, and the temperature of recirculated water reduces gradually.
At the material preheating section, operating personnel can judge the dense degree of recirculated water according to the observation, with the amount of this this section recirculated water of determining to drain.
In material digestion section, the temperature of recirculated water will be automatically controlled on the boiling temperature numerical value that requires.Material used time during through material digestion section is exactly the needed digestion time of material.Can realize needed treatment effect by the length of regulating the speed of service and material digestion section.The flow direction of the recirculated water that digestion is used and be contrary by the traffic direction of digestion material, such Design Mode, can so that the transfer of heat that material can be absorbed in the digestion process at cooling section in digestion water, both reduced by the digestion material temperature, also improved the temperature of recirculated water.And in material digestion section, the material in the cage basket in the new access to plant of heat transferred that can recirculated water is entrained reaches the purpose of energy savings.
At the material cooling section, control the inlet of new water simultaneously by the water level of the temperature of recirculated water and recirculated water, in the hope of reaching the requirement that drop temperature meets digestion technology.
According to output and the time requirement of material digestion, can design the material digestion section of different length, other each active sections are constant.This device is implemented omnidistance control by automatic control system.
Claims (10)
1. continuous material digestion device, comprise and hold the cage basket for the treatment of the digestion material and provide the cage basket to make the tunnel type digestion device (16) of operation continuously, it is characterized in that: be provided with material preheating section (2) in the described digestion device (16), material digestion section (4), material precooling zone (6), material cooling section (7), after cage basket (1) enters the arrival end of digestion device, under the driving of chain drive mechanism (8), pass through material preheating section (2) successively, material digestion section (4), material precooling zone (6), material cooling section (7) back is to the port of export operation of digestion device; The lower position of cage basket operation is respectively equipped with and described material preheating section (2), material digestion section (4), material precooling zone (6), corresponding material preheating water circulation aqua storage tank (2.1), material digestion hot water circuit aqua storage tank (4.1), the pre-cold water circulation of material aqua storage tank (6.1) and the material cooling water circulation aqua storage tank (7.1) that arranges in material cooling section (7) position; Described material preheating section (2) is provided with preheating water jet pipe (2.2), described material digestion section (4) is provided with digestion hot water jet pipe (4.2), described material precooling zone (6) is provided with precooling water spray pipe (6.2), described material cooling section (7) is provided with cooling water nozzle (7.2), and above-mentioned each jet pipe places the top position of cage basket operation respectively and is connected the realization periodical feeding by water circulating pump (9) with separately aqua storage tank; Described material digestion water circulation aqua storage tank (4.1) is connected with digestion device (16) vapour source outward by steam valve (10) and jet chimney (11); The outer cold water source of digestion device (16) is connected with cooling water nozzle (7.2) with described material cooling water circulation aqua storage tank (7.1) respectively by cooling water replenishment valve (12) and cooling water pipeline (13); Described preheating water jet pipe (2.2) is provided with draining valve (15) and drainpipe (14); In material digestion section (4), the flow direction of the recirculated water of material digestion aqua storage tank and the traffic direction of cage basket are reverse, and its temperature is by the temperature of the steam flow in the automatic steam regulation pipe of water temperature control device with the required hot water of realization digestion; Described cage basket (1) is the border seal structure, its bottom is provided with the water holes (1.1) of discharging more, the water yield three's of the injection flow rate of the digestion hot water jet pipe (4.2) of the flow of water circulating pump (9), material digestion section (4) and cage basket bottom aperture relation with keep height of water level certain in the cage basket (1) to adapt and flow by control water circulating pump (9) maintains the required height of digestion material all the time with the water level of assurance cage basket.
2. continuous material digestion device according to claim 1 is characterized in that: a circle spout hole (1.2) is located to be provided with in the upper edge (h) of described cage basket (1).
3. continuous material digestion device according to claim 1 and 2, it is characterized in that: also be provided with between described material preheating section (2) and the material digestion section (4) preposition vacant section (3), also be provided with rearmounted vacant section (5) between material digestion section (4) and the material precooling zone (6), the top of described preposition vacant section (3) and rearmounted vacant section (5) does not have sparge pipe.
4. continuous material digestion device according to claim 1 and 2, it is characterized in that: described material preheating water circulation aqua storage tank (2.1), material digestion water circulation aqua storage tank (4.1), the pre-cold water circulation of material aqua storage tank (6.1) and material cooling water circulation aqua storage tank (7.1) are communicated with successively.
5. continuous material digestion device according to claim 3, it is characterized in that: described material preheating water circulation aqua storage tank (2.1), material digestion water circulation aqua storage tank (4.1), the pre-cold water circulation of material aqua storage tank (6.1) and material cooling water circulation aqua storage tank (7.1) are communicated with successively.
6. continuous material digestion device according to claim 1 and 2 is characterized in that: described material preheating section (2) is divided into initial intensification section (2a) and secondary temperature elevation section (2b).
7. continuous material digestion device according to claim 3 is characterized in that: described material preheating section (2) is divided into initial intensification section (2a) and secondary temperature elevation section (2b).
8. continuous material digestion device according to claim 4 is characterized in that: described material preheating section (2) is divided into initial intensification section (2a) and secondary temperature elevation section (2b).
9. continuous material digestion device according to claim 5 is characterized in that: described material preheating section (2) is divided into initial intensification section (2a) and secondary temperature elevation section (2b).
10. continuous material digestion device according to claim 6 is characterized in that: described material preheating section (2) is divided into initial intensification section (2a) and secondary temperature elevation section (2b).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320014776 CN203040612U (en) | 2013-01-11 | 2013-01-11 | Continuous-type material soaking-cooking device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320014776 CN203040612U (en) | 2013-01-11 | 2013-01-11 | Continuous-type material soaking-cooking device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203040612U true CN203040612U (en) | 2013-07-10 |
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ID=48723631
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320014776 Expired - Fee Related CN203040612U (en) | 2013-01-11 | 2013-01-11 | Continuous-type material soaking-cooking device |
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| Country | Link |
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| CN (1) | CN203040612U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103040070A (en) * | 2013-01-11 | 2013-04-17 | 中天昊宇科技股份有限公司 | Continuous material digesting device |
| CN104161278A (en) * | 2014-08-25 | 2014-11-26 | 厦门银鹭食品集团有限公司 | Walnut membrane separation production line and production process thereof |
| CN105533391A (en) * | 2015-12-30 | 2016-05-04 | 解慧芳 | Food steaming and sterilizing tray, food steaming and sterilizing device as well as steaming and sterilizing method |
-
2013
- 2013-01-11 CN CN 201320014776 patent/CN203040612U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103040070A (en) * | 2013-01-11 | 2013-04-17 | 中天昊宇科技股份有限公司 | Continuous material digesting device |
| CN104161278A (en) * | 2014-08-25 | 2014-11-26 | 厦门银鹭食品集团有限公司 | Walnut membrane separation production line and production process thereof |
| CN105533391A (en) * | 2015-12-30 | 2016-05-04 | 解慧芳 | Food steaming and sterilizing tray, food steaming and sterilizing device as well as steaming and sterilizing method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130710 Termination date: 20160111 |