CN209768840U - Steam jet device for peptide process - Google Patents
Steam jet device for peptide process Download PDFInfo
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- CN209768840U CN209768840U CN201920218221.4U CN201920218221U CN209768840U CN 209768840 U CN209768840 U CN 209768840U CN 201920218221 U CN201920218221 U CN 201920218221U CN 209768840 U CN209768840 U CN 209768840U
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Abstract
the utility model relates to the field of food processing equipment, in particular to a steam injection device for peptide technology, which comprises a steam injector and is characterized in that a steam inlet port of the steam injector is sequentially connected with a steam regulating valve, a flow sensor and a steam room through a steam pipeline, a feed port of the steam injector is sequentially connected with a feed valve, a booster pump, a filter screen and a storage box through a feed pipeline, and an injection port of the steam injector is sequentially connected with a discharge valve, a temperature sensor and a mixing chamber through a discharge pipeline; the steam regulating valve is connected with the output end of the controller, and the flow sensor and the temperature sensor are connected with the input end of the controller.
Description
Technical Field
The utility model relates to a food processing equipment field, especially a steam jet equipment for peptide technology.
background
Proteins, as nutrients, exist in the form of peptides and partially free amino acids in the human body and are absorbed by the human body to exert various physiological functions. The rice peptide is further extracted from rice protein, has higher nutritive value, and has double effects of regulating the physiological function of an organism and providing nutrition for the organism, so the rice peptide has good prospect in the field of current nutritional food.
The traditional method for producing rice peptide is mainly a compound protease enzymolysis method, firstly, rice starch and rice protein in rice are separated by the enzymolysis method, then, a series of steps of centrifuging, drying and the like are carried out on the rice protein, and finally, a rice peptide finished product is obtained. However, the currently used apparatuses for separating rice starch and rice protein do not separate them well.
SUMMERY OF THE UTILITY MODEL
Not enough to the above-mentioned technique, the utility model provides a steam jet system that separation rice starch and rice protein in-process were used, the device not only with low costs, simple structure, separation are effectual, difficult jam, have still guaranteed the stability of rice peptide production quality.
The utility model discloses a realize through following technical scheme:
A steam jet device for a peptide process comprises a steam jet, and is characterized in that a steam inlet port of the steam jet is sequentially connected with a steam regulating valve, a flow sensor and a steam room through a steam pipeline, a feed port of the steam jet is sequentially connected with a feed valve, a booster pump, a filter screen and a storage box through a feed pipeline, and a jet port of the steam jet is sequentially connected with a discharge valve, a temperature sensor and a mixing chamber through a discharge pipeline; the steam regulating valve is connected with the output end of the controller, and the flow sensor and the temperature sensor are connected with the input end of the controller.
Preferably, a backwashing water inlet pipeline for preventing the steam ejector from being blocked is further arranged on the discharge pipeline between the injection port and the outlet valve of the steam ejector, and a backwashing water inlet valve is arranged on the backwashing water inlet pipeline.
As a preferred scheme, the feeding pipeline is also provided with a blow-down pipeline for blow-down and blow-down, and the blow-down pipeline is provided with a blow-down valve.
Preferably, the controller is a programmable logic controller.
Compared with the prior art, the beneficial effects of the utility model are that:
1. The utility model adopts the mode of carrying the material with steam to spray, the steam pressure is stable, the steam and the liquid are mixed evenly, the dispersion effect of the large protein in the sprayed material liquid is good, the filtering speed is fast when the sprayed material liquid enters the next procedure for filtering, and the finally generated rice peptide has high quality; in addition, a temperature sensor is arranged on the discharging pipeline, feedback automatic adjustment is formed between the temperature sensor and the steam adjusting valve, namely, the opening size of the steam adjusting valve is automatically adjusted according to temperature change, so that the phenomenon of overhigh local temperature and discoloration caused by nonuniform heating of the feed liquid is eliminated, the next procedure is prevented from being influenced, and the product quality is guaranteed.
2. The utility model discloses a backwash pipeline and backwash water intaking valve have the effect that prevents the inside jam of feed liquid pipeline and steam jet, do not need often to dismantle and wash feed pipeline and steam jet, have practiced thrift the cost, have improved work efficiency.
Drawings
Fig. 1 is a schematic structural view of the present invention;
1 steam room, 2 flow sensor, 3 steam control valve, 4 steam jet wares, 5 storage tanks, 6 booster pumps, 7 filter screens, 8 feed valves, 9 bleeder valves, 10 temperature sensor, 11 mixing chambers, 12 blowoff valves, 13 backwash valves, 14 steam conduit, 15 feed conduit, 16 discharge conduit.
Detailed Description
The present invention will be further specifically described below with reference to examples.
As shown in figure 1, a steam jet device for peptide technology comprises a steam ejector 4, a steam inlet port of the steam ejector 4 is connected with a steam room 1 through a steam pipeline 14, the steam pipeline is provided with a flow sensor 2 and a steam regulating valve 3, in order to avoid the influence of the opening and closing of the steam regulating valve 3 on the measuring accuracy of the flow sensor 2, the flow sensor 2 is installed at the initial end of the steam pipeline 14, the steam regulating valve 3 is installed behind the flow sensor 2, a feed port of the steam ejector 4 is connected with a feed valve 8, a booster pump 6, a filter screen 7 and a storage tank 5 in sequence through a feed pipeline 15, the filter screen 7 is installed at the outlet of the storage tank 5, feed liquid is pressurized and conveyed to the feed port of the steam ejector 4 through the booster pump 6 after being filtered by the filter screen 7, the feed valve 8 for controlling whether to feed is arranged on the feed, a sewage draining pipeline for backwashing sewage draining is also arranged on the feeding pipeline 15, and a sewage draining valve 12 is arranged on the sewage draining pipeline.
The injection port of the steam injector 4 is sequentially connected with a discharge valve 9, a temperature sensor 10 and a mixing chamber 11 through a discharge pipeline 16, a filter screen steam regulating valve 3 is arranged in the mixing chamber 11 and is connected with the output end of a controller, the temperature sensor 10 is connected with the input end of the controller, the temperature sensor 10 is used for monitoring the temperature of the discharge pipeline in real time and feeding back a temperature signal to the controller, an algorithm module is arranged in the controller and can calculate the opening size of the steam regulating valve to be regulated according to a temperature value, so that the temperature of the discharged material is always kept at a constant temperature; a backwashing water inlet pipeline for preventing the steam ejector from being blocked is arranged on a discharge pipeline 16 between the injection port of the steam ejector 4 and the discharge valve 9, a backwashing water inlet valve 13 is arranged on the backwashing water inlet pipeline, the backwashing water inlet valve 13 is opened, one end of the backwashing water inlet pipeline is connected with a water tap or a device capable of discharging water by using a section of water pipe, and the other end of the backwashing water inlet pipeline is connected with the backwashing water inlet pipeline, so that the washing and cleaning can be carried out.
Further, the controller adopts a programmable logic controller.
The working process is as follows: steam generated by the steam room is conveyed to the steam inlet port of the steam ejector through the steam pipeline, feed liquid of the storage box is conveyed to the steam inlet port of the pressure ejector through the feed pipeline through the booster pump, the feed liquid is driven by the steam, the feed liquid is sprayed out from the injection port of the steam ejector to the mixing chamber, and then the feed liquid enters the next production process. When the temperature detected by the temperature sensor is too high, the opening degree of the steam regulating valve is automatically reduced; when the temperature detected by the temperature sensor is too low, the opening degree of the steam regulating valve can be automatically increased, and the constant temperature state of the whole injection device is realized.
The utility model discloses technical characteristics that have not described can be through or adopt prior art to realize, no longer describe here, and of course, above-mentioned embodiment is not right the utility model discloses a restriction, the utility model discloses also not only be limited to above-mentioned embodiment, ordinary skilled person in this technical field is in the utility model discloses a change, modification, interpolation or replacement made in the essential scope also should fall into the utility model discloses a protection scope.
Claims (4)
1. A steam jet device for a peptide process comprises a steam jet device (4) and is characterized in that a steam inlet port of the steam jet device (4) is sequentially connected with a steam regulating valve (3), a flow sensor (2) and a steam room (1) through a steam pipeline (14), a feed port of the steam jet device (4) is sequentially connected with a feed valve (8), a booster pump (6), a filter screen (7) and a storage box (5) through a feed pipeline (15), and a jet port of the steam jet device (4) is sequentially connected with a discharge valve (9), a temperature sensor (10) and a mixing chamber (11) through a discharge pipeline (16); the steam regulating valve (3) is connected with the output end of the controller, and the flow sensor (2) and the temperature sensor (10) are connected with the input end of the controller.
2. The steam injection device for the peptide process according to claim 1, wherein a backwash water inlet pipe for preventing the steam injector from being blocked is further arranged on the discharge pipe (16) between the injection port of the steam injector (4) and the discharge valve (9), and a backwash water inlet valve (13) is arranged on the backwash water inlet pipe.
3. A steam injection apparatus for peptide processing according to claim 1, wherein the feed line is further equipped with a blowdown line for backwash blowdown, the blowdown line being provided with a blowdown valve (12).
4. The steam injection apparatus for peptide process as claimed in claim 1, wherein said controller employs a programmable logic controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920218221.4U CN209768840U (en) | 2019-02-21 | 2019-02-21 | Steam jet device for peptide process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920218221.4U CN209768840U (en) | 2019-02-21 | 2019-02-21 | Steam jet device for peptide process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209768840U true CN209768840U (en) | 2019-12-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920218221.4U Active CN209768840U (en) | 2019-02-21 | 2019-02-21 | Steam jet device for peptide process |
Country Status (1)
| Country | Link |
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| CN (1) | CN209768840U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115074409A (en) * | 2022-08-18 | 2022-09-20 | 意润健康产业（广州）有限公司 | Micromolecule active peptide separation and purification system based on organic animal and plant raw materials |
-
2019
- 2019-02-21 CN CN201920218221.4U patent/CN209768840U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115074409A (en) * | 2022-08-18 | 2022-09-20 | 意润健康产业（广州）有限公司 | Micromolecule active peptide separation and purification system based on organic animal and plant raw materials |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210609 Address after: 274000 east section of Hedong Road, Luling Town, hi tech Zone, Heze City, Shandong Province Patentee after: Shandong Dashu Eurasia natural seasoning Co., Ltd Address before: 274000 east section of Hedong Road, Luling Town, hi tech Zone, Heze City, Shandong Province Patentee before: SHANDONG DASHU DAFU SPECIAL MEAL FOOD Co.,Ltd. |
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| TR01 | Transfer of patent right |