CN219272163U - Drying device is used in pricklyash peel peptide production - Google Patents

Abstract

The utility model provides a drying device is used in prickly ash peptide production, includes annular desicator, one side middle part position sets up the power fan in the desicator, the opposite side upper portion of desicator sets up the atomizing orifice plate, the atomizing orifice plate passes through pipeline and prickly ash peptide liquid memory in the intercommunication, set up the high-pressure liquid pump on the connecting line between atomizing orifice plate and the prickly ash peptide liquid memory, the opposite side lower part and the high-pressure high temperature air pipe intercommunication of desicator, desicator bottom and prickly ash peptide exit tube intercommunication, set up the solenoid valve on the prickly ash peptide exit tube. According to the utility model, the drying of the Zanthoxylum peptide can be conveniently realized by adopting the dryer, and the size of the Zanthoxylum peptide dryer is smaller, but the drying of the Zanthoxylum peptide can be efficiently finished, so that the drying efficiency is ensured, and meanwhile, the production cost is saved.

Description

Drying device is used in pricklyash peel peptide production

Technical Field

The utility model belongs to the field of production of Zanthoxylum peptide, and particularly relates to a drying device for production of Zanthoxylum peptide.

Background

The pepper is a common seasoning in daily life, but the pepper is mainly pepper skin, the application of the pepper seeds is gradually developed, the seed oil can be extracted from the pepper seeds, nutrients such as polypeptide and the like can be extracted from the oil residues, the final step of extracting the pepper peptide is generally that the solution containing the pepper peptide is directly dried to obtain the pepper peptide powder, the direct evaporation solvent efficiency is lower, and the spray drying equipment is generally adopted to improve the drying efficiency, but the spray drying equipment is larger in whole and larger in energy consumption, and the pepper seed seasoning is suitable for mass production, but the yield of the pepper seeds is not high, and meanwhile, the quality of the pepper peptide is higher, but the protein content in the pepper seeds is lower, so the cost of the spray drying equipment is higher.

Disclosure of Invention

The utility model provides a drying device for producing Zanthoxylum peptide, which is used for solving the defects in the prior art.

The utility model is realized by the following technical scheme:

the utility model provides a drying device is used in prickly ash peptide production, includes annular desicator, one side middle part position sets up the power fan in the desicator, the opposite side upper portion of desicator sets up the atomizing orifice plate, the atomizing orifice plate passes through pipeline and prickly ash peptide liquid memory in the intercommunication, set up the high-pressure liquid pump on the connecting line between atomizing orifice plate and the prickly ash peptide liquid memory, the opposite side lower part and the high-pressure high temperature air pipe intercommunication of desicator, desicator bottom and prickly ash peptide exit tube intercommunication, set up the solenoid valve on the prickly ash peptide exit tube.

The drying device for producing the Zanthoxylum peptide is characterized in that a baffle cavity is arranged at the position between the power fan at one side of the dryer and the Zanthoxylum peptide outlet pipe, one end of the baffle cavity is communicated with the dryer, a baffle is arranged in the baffle cavity, the longitudinal section of the baffle cavity is also identical in length and width, one end of the baffle cavity, which is far away from the dryer, is fixedly connected with one end of a multi-stage electric push rod, the other end of the multi-stage electric push rod is fixedly connected with the central position of one end, which is far away from the dryer, of the baffle, a slot is formed in the inner side inner wall of the dryer, corresponding to the baffle, and the baffle can be inserted into the slot.

According to the drying device for producing the Zanthoxylum bungeanum peptide, the heating cavity is formed in the wall of the Zanthoxylum bungeanum peptide liquid storage device, the top of the dryer is communicated with the bottom of the heating cavity through the pipeline, the connecting end of the dryer and the heating cavity connecting pipeline and the dryer is provided with the high polymer breathable film, and the top of the heating cavity is communicated with the steam discharge pipe.

According to the drying device for producing the Zanthoxylum peptide, the check valve is arranged on the connecting pipeline between the high-pressure high-temperature air pipe and the atomizing orifice plate and the Zanthoxylum peptide liquid storage.

The utility model has the advantages that: according to the utility model, the drying of the Zanthoxylum peptide can be conveniently realized by adopting the dryer, and the size of the Zanthoxylum peptide dryer is smaller, but the drying of the Zanthoxylum peptide can be efficiently finished, so that the drying efficiency is ensured, and meanwhile, the production cost is saved.

Drawings

In order to more clearly illustrate the embodiments of the present utility model or the technical solutions of the prior art, the drawings that are needed in the embodiments or the description of the prior art will be briefly described below, it will be obvious that the drawings in the following description are some embodiments of the present utility model, and that other drawings can be obtained according to these drawings without inventive effort to a person skilled in the art.

FIG. 1 is a schematic diagram of the structure of the present utility model;

fig. 2 is a partial enlarged view of the section I of fig. 1.

Reference numerals: 1. a dryer; 2. a power fan; 3. an atomization orifice plate; 4. a pepper peptide liquid storage; 5. a high pressure liquid pump; 6. a pepper peptide outlet pipe; 7. an electromagnetic valve; 8. a baffle cavity; 9. a baffle; 10. a multi-stage electric push rod; 11. a slot; 12. a heating chamber; 13. a polymeric breathable film; 14. a steam discharge pipe; 15. a one-way valve; 16. high pressure and high temperature air pipes.

Detailed Description

For the purpose of making the objects, technical solutions and advantages of the embodiments of the present utility model more apparent, the technical solutions of the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model, and it is apparent that the described embodiments are some embodiments of the present utility model, but not all embodiments of the present utility model. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.

The utility model provides a drying device is used in prickly ash peptide production, includes annular desicator 1, one side middle part position sets up power fan 2 in the desicator 1, the opposite side upper portion of desicator 1 sets up atomizing orifice plate 3, atomizing orifice plate 3 communicates in through pipeline and prickly ash peptide liquid memory 4, set up high-pressure liquid pump 5 on the connecting pipe way between atomizing orifice plate 3 and the prickly ash peptide liquid memory 4, the opposite side lower part and the high-pressure high-temperature air pipe 16 intercommunication of desicator 1, desicator 1 bottom and prickly ash peptide exit tube 6 intercommunication, set up solenoid valve 7 on the prickly ash peptide exit tube 6. When the utility model is used, the high-pressure liquid pump 5 is started to pump the Zanthoxylum bungeanum peptide liquid in the Zanthoxylum bungeanum peptide liquid storage 4 and spray out through the high-pressure atomization of the atomization orifice plate 3, meanwhile, the high-pressure high-temperature air pipe 16 continuously pumps high-temperature air into the dryer 1, meanwhile, the power fan 2 is started to drive the atomized liquid and the high-temperature air in the dryer 1 to circularly rotate in the dryer 1 in the anticlockwise direction, so that the atomized liquid and the high-temperature air are in full contact, after a certain amount of powdery Zanthoxylum bungeanum peptide is accumulated after drying for a period of time, the feeding of Zanthoxylum bungeanum peptide liquid is stopped, the high-temperature air is stopped after the appointed time is continuously fed, the drying operation is ensured to be thoroughly carried out, the steam obtained after heat exchange is discharged through the top of the dryer 1, then the electromagnetic valve 7 is opened, the powdery Zanthoxylum bungeanum peptide is driven to be discharged through the Zanthoxylum bungeanum peptide outlet pipe 6 under the driving of the power fan 2, and then the electromagnetic valve 7 is closed to repeat the operation, so that the drying operation is conveniently and efficiently completed, and the production cost is effectively reduced.

Specifically, because the power fan 2 drives the powdered pricklyash Peel peptide and still has some pricklyash Peel peptide to follow and continue the cyclic motion and can influence follow-up dry operation when passing through pricklyash Peel peptide exit tube 6 and discharge, in order to overcome above-mentioned problem, the setting baffle chamber 8 of the position between 1 side power fan 2 of desicator and the pricklyash Peel peptide exit tube 6, baffle chamber 8 one end and desicator 1 intercommunication, set up baffle 9 in the baffle chamber 8, the longitudinal section length and width of baffle 9 are the same in the longitudinal section of baffle chamber 8 still, the one end of multistage electric putter 10 of one end fixed connection of keeping away from desicator 1 in the baffle chamber 8, the other end of multistage electric putter 10 and the one end central position fixed connection of keeping away from desicator 1 with baffle 9, slot 11 is seted up with the corresponding position of baffle 9 on the inboard inner wall of desicator 1, in the slot 11 can be inserted to baffle 9. In the drying process, the baffle plate 9 is always positioned in the baffle plate cavity 8, meanwhile, the baffle plate 9 can be just correspondingly inserted and matched with the baffle plate cavity 8, so that the drying process cannot be influenced, when the powdery pricklyash Peel peptide is to be removed, the multi-stage electric push rod 10 drives the baffle plate 9 to be removed from the baffle plate cavity 8 until the baffle plate 9 is inserted and matched with the slot 11, at the moment, the baffle plate 9 isolates a loop in the dryer 1, and the air flow is blocked to form a circulation loop, so that the air flow drives the powdery pricklyash Peel peptide to be discharged through the pricklyash Peel peptide outlet pipe 6, and the dried powdery pricklyash Peel peptide is conveniently discharged, and is convenient for subsequent drying operation.

Specifically, because the steam still has higher heat and does not recycle and can lead to the wasting of resources after the heat transfer, simultaneously pricklyash peel peptide liquid and high temperature air are all continuous high pressure and throw into, also easily lead to the interior pressure of desicator 1 to increase continuously and can cause the machine damage even the incident to take place even in the drying process, in order to overcome above-mentioned problem, pricklyash peel peptide liquid memory 4 wall in this embodiment set up heating chamber 12, the bottom intercommunication of heating chamber 12 is passed through to desicator 1 top, the desicator 1 is connected pipeline with heating chamber 12 and is set up polymer ventilated membrane 13 with the link department of desicator 1, heating chamber 12 top and steam discharge pipe 14 intercommunication. The steam after heat exchange can be pressed into the heating cavity 12 through the pipeline to continuously exchange heat with the pepper peptide liquid continuously entering the pepper peptide liquid storage 4 due to the large pressure in the dryer 1, so that the direct recovery of heat is realized, the problem that the heat loss is large in the transportation process caused by the transportation and recovery of heat through multiple pipelines is avoided, if more residual heat is used for indoor heating in winter or for heat exchange with water to produce warm water is solved, the full utilization of resources is realized, meanwhile, the normal operation of drying operation is not influenced due to the fact that the powdery pepper peptide of the high-molecular breathable film 13 cannot pass through, the resources are fully utilized while the normal operation of drying operation is ensured, and the potential safety hazard is solved.

Further, since the powder peppertree peptide is driven by the power fan 2 to be discharged through the peppertree peptide outlet pipe 6, the powder peppertree peptide may be lost along with the connecting pipeline between the high-pressure high-temperature air pipe 16 and the atomizing orifice plate 3 and the peppertree peptide liquid storage 4, thereby affecting the drying efficiency, and in order to overcome the above-mentioned problems, the connecting pipeline between the high-pressure high-temperature air pipe 16 and the atomizing orifice plate 3 and the peppertree peptide liquid storage 4 is provided with the one-way valve 15. The powder Zanthoxylum peptide can be effectively prevented from losing along with the connecting pipeline between the high-pressure high-temperature air pipe 16 and the atomizing orifice plate 3 and the Zanthoxylum peptide liquid storage 4 through the one-way valve 15, so that the drying efficiency is ensured.

Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present utility model, and are not limiting; although the utility model has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit and scope of the technical solutions of the embodiments of the present utility model.

Claims (4)

1. Drying device is used in production of pricklyash peel peptide, its characterized in that: including annular desicator (1), one side middle part position sets up power fan (2) in desicator (1), the opposite side upper portion of desicator (1) sets up atomizing orifice plate (3), atomizing orifice plate (3) are through pipeline and interior intercommunication of prickly ash peptide liquid memory (4), set up high-pressure liquid pump (5) on the connecting pipe between atomizing orifice plate (3) and prickly ash peptide liquid memory (4), the opposite side lower part and the high-pressure high-temperature air pipe (16) of desicator (1) communicate, desicator (1) bottom and prickly ash peptide exit tube (6) intercommunication, set up solenoid valve (7) on prickly ash peptide exit tube (6).

2. The drying device for producing the Zanthoxylum peptide according to claim 1, which is characterized in that: the utility model provides a dryer, including setting up baffle chamber (8) of the position between power fan (2) and prickly ash peptide exit tube (6) on one side of dryer (1), baffle chamber (8) one end and dryer (1) intercommunication, set up baffle (9) in baffle chamber (8), the longitudinal section of baffle chamber (8) is the same in length and width of the longitudinal section of baffle (9) in addition, the one end of multistage electric putter (10) of one end fixed connection of keeping away from dryer (1) in baffle chamber (8), the one end central point fixed connection of keeping away from dryer (1) of the other end of multistage electric putter (10) and baffle (9), slot (11) are seted up with the corresponding position of baffle (9) on the inboard inner wall of dryer (1), in slot (11) can be inserted to baffle (9).

3. The drying device for producing the Zanthoxylum peptide according to claim 1, which is characterized in that: the wall of the pepper peptide liquid storage (4) is internally provided with a heating cavity (12), the top of the dryer (1) is communicated with the bottom of the heating cavity (12) through a pipeline, a high polymer breathable film (13) is arranged at the connection end of the connecting pipeline of the dryer (1) and the heating cavity (12) and the dryer (1), and the top of the heating cavity (12) is communicated with a steam discharge pipe (14).

4. The drying device for producing the Zanthoxylum peptide according to claim 1, which is characterized in that: a one-way valve (15) is arranged on a connecting pipeline between the high-pressure high-temperature air pipe (16) and the atomizing orifice plate (3) and the pricklyash peel peptide liquid storage (4).

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