CN215873350U - Online steamed system of point of efflux - Google Patents
Online steamed system of point of efflux Download PDFInfo
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- CN215873350U CN215873350U CN202122054338.3U CN202122054338U CN215873350U CN 215873350 U CN215873350 U CN 215873350U CN 202122054338 U CN202122054338 U CN 202122054338U CN 215873350 U CN215873350 U CN 215873350U
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Abstract
The utility model relates to a jet flow online bittern spotting system, which comprises: pump, valve, jet flow mixer, accelerating jet pipe, vortex mixer, halogen-point agent charging bucket and metering pump. The inlet of the valve is connected with the outlet of the pump through a pipeline, and the outlet of the valve is connected with the inlet of the pump through a pipeline; the outlet of the pump is connected with the inlet of the jet flow mixer through a pipeline, and the inlet of the accelerating spray pipe is connected with the outlet of the jet flow mixer; the outlet of the accelerating spray pipe is connected with the inlet of the vortex mixer through a pipeline; the outlet of the halogen agent charging bucket is connected with the inlet of the metering pump through a pipeline; the outlet of the metering pump is connected with the inlet of the jet flow mixer through a pipeline. The utility model realizes continuous on-line efficient brine adding, ensures the consistency of material discharging and improves the quality of full-component bean products; the mixing efficiency is high, the time is short, the jet flow is mixed and directly and continuously discharged, and the device is suitable for some working conditions that the coagulation reaction rapidly occurs after the brine adding. The CIP online cleaning can be carried out, the automation degree is high, and the labor is saved.
Description
Technical Field
The utility model relates to the field of bean product processing, in particular to a continuous online bittern spotting system.
Background
The bean products in China have a history of more than 2000 years, and are rich in nutrition, high in protein content and high in nutritional value, and rich in vitamins, minerals, essential fatty acids, dietary fibers and the like. The traditional bean product production process basically needs the procedures of selection, soaking, grinding, deslagging, boiling and the like, wherein the soaking process needs long time, and generates a large amount of sewage to cause environmental pollution, and the deslagging process causes loss of nutrient components on one hand, and dietary fibers in bean dregs have the effects of promoting intestinal tract peristalsis, accelerating defecation speed, preventing constipation and reducing intestinal cancer risk, and can also reduce plasma cholesterol, regulate gastrointestinal functions and insulin level. In addition, the bean dregs also contain more protein and minerals such as calcium, phosphorus, iron and the like. On the other hand, the produced bean dregs also need to be specially treated, otherwise, the bean dregs are extremely easy to decay and pollute the environment. In recent years, the national requirements on environmental protection are more strict, the soybean product enterprises are greatly influenced, and the environmental protection investment and the operation cost are increased. With the increasing concern of people on environmental protection, nutrition and health, the whole-bean product technology and product development are inevitable trends in the development of bean products.
The whole bean product process requires a special bittern spotting agent and a bittern spotting process. The halogen agent adopts emulsified coagulator, and needs to be uniformly dispersed and mixed into the soybean milk to realize the coagulation forming of the whole soybean product. At present, the uniform dispersion of the emulsifying coagulant still depends on the traditional stirring type fluid material mixing technology.
However, the conventional stirring type mixing apparatus requires a bittern spotting operation in a fixed vessel. This has the following problems:
1) the process belongs to batch type treatment, and stirring type mixing needs to be continued for a certain time. However, since the soybean milk and the coagulant begin to undergo coagulation reaction in the mixed tank within a short time after mixing, the quality of the formed bean curd after being transferred to the packing box is reduced;
2) the soybean milk mixed in the tank body needs a certain time to be discharged, so that the front and back discharging is not uniform;
3) the on-line addition can not be realized, and the mixture is not uniform because the bittern accounts for the soybean milk in a low proportion and belongs to an oil-water mixing system.
SUMMERY OF THE UTILITY MODEL
In order to solve the defects in the prior art, the utility model adopts the technical scheme that:
a jet online bittern spotting system comprising: the device comprises a pump 1, a valve 2, a jet flow mixer 3, an accelerating spray pipe 4, a vortex mixer 5, a brine dripping agent charging tank, a metering pump and a pipeline;
a valve 2 is arranged between the inlet and the outlet of the pump 1, the inlet of the valve 2 is connected with the outlet of the pump 1 through a pipeline, and the outlet of the valve 2 is connected with the inlet of the pump 1 through a pipeline;
the outlet of the pump 1 is connected with the inlet of the jet flow mixer 3 through a pipeline, and the inlet of the accelerating spray pipe 4 is connected with the outlet of the jet flow mixer 3; the outlet of the accelerating jet pipe 4 is connected with the inlet of the vortex mixer 5 through a pipeline; the outlet of the halogen agent charging bucket is connected with the inlet of the metering pump through a pipeline; the outlet of the metering pump is connected to the inlet of the jet mixer 3 by a line.
The halogen adding material tank and the metering pump are respectively two, the halogen adding material tank comprises a halogen adding material tank I6 and a halogen adding material tank II7, and the metering pump comprises a metering pump I8 and a metering pump II 9; the outlet of the point halogen agent charging tank I6 is connected with the inlet of the metering pump I8 through a pipeline, and the outlet of the point halogen agent charging tank II7 is connected with the inlet of the metering pump II9 through a pipeline; the outlets of the metering pump I8 and the metering pump II9 are connected to the inlet of the jet mixer 3 through a pipeline.
The pump comprises a screw pump, a plunger pump or a centrifugal pump.
The valve comprises a ball valve, a butterfly valve or a pneumatic ball valve.
The accelerating spray pipe is a Laval spray pipe.
The valve 2 is used to regulate the delivery flow.
The materials in the halogen agent charging bucket I6 and the halogen agent charging bucket II7 are quantitatively conveyed to the jet flow mixer 3 through a metering pump I8 and a metering pump II9 respectively.
The jet flow online bittern spotting system also comprises a CIP cleaning system, and the CIP cleaning system comprises a CIPI cleaning system and a CIPII cleaning system; the CIPI cleaning system is a large-flow cleaning pipeline and is used for cleaning a liquid inlet cavity of the pump; the CIPII cleaning system comprises a pneumatic reversing valve 10, a pneumatic butterfly valve I11, a pneumatic butterfly valve II 12 and a connecting pipe, wherein the inlet of the pneumatic reversing valve 10 is connected with the outlet of the vortex mixer 5 through the connecting pipe, the outlet of the pneumatic reversing valve 10 is respectively connected with the brine dispensing material tank, the pneumatic butterfly valve I11 and the pneumatic butterfly valve II 12 through the connecting pipe, and the outlet of the pneumatic butterfly valve I11 is connected with the inlet of the jet mixer 3.
The utility model has the beneficial effects that:
continuous online efficient brine adding is realized, the consistency of material discharging is ensured, and the quality of full-component bean products is improved;
the mixing efficiency is high, the time is short, the jet flow is mixed and directly and continuously discharged, and the device is suitable for some working conditions that the coagulation reaction rapidly occurs after the brine adding.
The CIP online cleaning can be carried out, the automation degree is high, and the operation labor is saved.
Drawings
The utility model has the following drawings:
FIG. 1 is a schematic structural view of a continuous jet mixing tofu marinating system of the present invention.
FIG. 2 is a schematic diagram of the continuous jet mixing bean curd marinating system with the CIP cleaning system of the present invention.
1-screw pump, 2-pneumatic ball valve, 3-jet mixer, 4-Laval nozzle, 5-vortex mixer, 6-bittern spotting agent charging tank I, 7-bittern spotting agent charging tank II, 8-metering pump I, 9-metering pump II, 10-pneumatic reversing valve, 11-pneumatic butterfly valve I, 12-pneumatic butterfly valve II.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
Example 1: continuous jet flow mixed bean curd marinating system
As shown in FIG. 1, the jet flow online bittern spotting system of the present invention comprises: the device comprises a screw pump 1, a pneumatic ball valve 2, a jet flow mixer 3, a Laval nozzle 4, a vortex mixer 5, a brine dripping agent charging tank I6, a brine dripping agent charging tank II7, a metering pump I8, a metering pump II9 and a pipeline.
The soybean milk is conveyed to a jet flow mixer 3 through a screw pump 1, a loop is arranged at an inlet and an outlet of the screw pump, jet flow pressure is adjusted through the loop, and conveying flow is adjusted through a pneumatic ball valve 2. When the soybean milk is conveyed, the materials in the bittern spotting agent charging bucket I6 and the bittern spotting agent charging bucket II7 are quantitatively conveyed to the jet flow mixer 3 through the metering pump I8 and the metering pump II9 respectively, then 3 materials are uniformly mixed in the vortex mixer 5, and finally the materials are discharged. And discharging, feeding into a forming device, and solidifying to form the bean curd.
The capacities of the brine adding tank I and the brine adding tank II are 50L.
Example 2:
the continuous jet flow mixed bean curd bittern adding system with the CIP (Clean In Place) cleaning system has the functions of automatic control and CIP cleaning. The continuous jet mixed tofu marinating system comprises: the system comprises a screw pump 1, a pneumatic ball valve 2, a jet flow mixer 3, a Laval nozzle 4, a vortex mixer 5, a brine dripping agent charging tank I6, a brine dripping agent charging tank II7, a metering pump I8, a metering pump II9, a pipeline and a CIP cleaning system.
The soybean milk is conveyed to a jet flow mixer 3 through a screw pump 1, a loop is arranged at an inlet and an outlet of the screw pump, and the conveying flow is adjusted by a pneumatic ball valve 2. When the soybean milk is conveyed, the materials in the bittern spotting agent charging bucket I6 and the bittern spotting agent charging bucket II7 are quantitatively conveyed to the jet flow mixer 3 through the metering pump I8 and the metering pump II9 respectively, then 3 materials are uniformly mixed in the vortex mixer 5, and finally the materials are discharged through the pneumatic reversing valve 10. And discharging, feeding into a forming device, and solidifying to form the bean curd.
CIPI is a large-flow cleaning pipeline and is used for cleaning a liquid inlet cavity of a screw pump. The cleaning liquid is added from the soybean milk inlet on the screw pump, and is directly discharged after cleaning the liquid inlet cavity.
The CIPII circulation is that cleaning liquid is added from a soybean milk inlet on a screw pump on a mixing line, and finally the direction of the cleaning liquid is adjusted by a pneumatic reversing valve, most of the cleaning liquid (for example, alkaline solution prepared according to a certain proportion) returns to the screw pump through a pneumatic butterfly valve I11 (at the moment, a pneumatic butterfly valve II 12 is closed), the rest part of the cleaning liquid enters a halogen agent material tank I6 and a halogen agent material tank II7, and is respectively conveyed to a jet mixer 3 through a metering pump I and a metering pump II, and then enters a vortex mixer 5, the circulation is carried out, after a certain time, the pneumatic butterfly valve I11 is closed, the pneumatic butterfly valve II 12 is opened, the cleaning liquid is discharged from the pipeline, and cleaning is completed.
The above embodiments are merely illustrative, and not restrictive, and those skilled in the relevant art can make various changes and modifications without departing from the spirit and scope of the utility model, and therefore all equivalent technical solutions also belong to the scope of the utility model.
Those not described in detail in this specification are within the skill of the art.
Claims (8)
1. A jet online bittern spotting system, comprising: the device comprises a pump (1), a valve (2), a jet flow mixer (3), an accelerating spray pipe (4), a vortex mixer (5), a brine dripping agent material tank, a metering pump and a pipeline;
a valve (2) is arranged between an inlet and an outlet of the pump (1), the inlet of the valve (2) is connected with the outlet of the pump (1) through a pipeline, and the outlet of the valve (2) is connected with the inlet of the pump (1) through a pipeline;
the outlet of the pump (1) is connected with the inlet of the jet flow mixer (3) through a pipeline, and the inlet of the accelerating spray pipe (4) is connected with the outlet of the jet flow mixer (3); the outlet of the accelerating spray pipe (4) is connected with the inlet of the vortex mixer (5) through a pipeline; the outlet of the halogen agent charging bucket is connected with the inlet of the metering pump through a pipeline, and the outlet of the metering pump is connected with the inlet of the jet flow mixer (3) through a pipeline.
2. The jet on-line bittern spotting system of claim 1 wherein: the device comprises a halogen dispensing material tank and a metering pump, wherein the halogen dispensing material tank comprises a halogen dispensing material tank I (6) and a halogen dispensing material tank II (7), and the metering pump comprises a metering pump I (8) and a metering pump II (9); the outlet of the brine adding tank I (6) is connected with the inlet of the metering pump I (8) through a pipeline, and the outlet of the brine adding tank II (7) is connected with the inlet of the metering pump II (9) through a pipeline; the outlets of the metering pump I (8) and the metering pump II (9) are connected with the inlet of the jet flow mixer (3) through a pipeline.
3. The jet on-line bittern spotting system of claim 1 wherein: the pump comprises a screw pump, a plunger pump or a centrifugal pump.
4. The jet on-line bittern spotting system of claim 1 wherein: the valve comprises a ball valve, a butterfly valve or a pneumatic ball valve.
5. The jet on-line bittern spotting system of claim 1 wherein: the accelerating spray pipe is a Laval spray pipe.
6. The jet on-line bittern spotting system of claim 1 wherein: the valve (2) is used for regulating the delivery flow.
7. The jet on-line bittern spotting system of claim 2 wherein: the materials in the halogen agent charging bucket I (6) and the halogen agent charging bucket II (7) are quantitatively conveyed to the jet flow mixer (3) through a metering pump I (8) and a metering pump II (9) respectively.
8. The jet on-line bittern spotting system of any of claims 1-7 wherein: the jet flow online bittern spotting system also comprises a CIP cleaning system, and the CIP cleaning system comprises a CIPI cleaning system and a CIPII cleaning system; the CIPI cleaning system is a large-flow cleaning pipeline and is used for cleaning a liquid inlet cavity of the pump; CIPII cleaning system includes pneumatic switching-over valve (10), pneumatic butterfly valve I (11), pneumatic butterfly valve II (12) and connecting pipe, the entry of pneumatic switching-over valve (10) passes through the connecting pipe with the export of vortex mixer (5) and is connected, the export of pneumatic switching-over valve (10) passes through the connecting pipe and the steamed material jar of some bittern, pneumatic butterfly valve I (11), pneumatic butterfly valve II (12) are connected respectively, the export of pneumatic butterfly valve I (11) and the access connection of efflux blender (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122054338.3U CN215873350U (en) | 2021-08-27 | 2021-08-27 | Online steamed system of point of efflux |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122054338.3U CN215873350U (en) | 2021-08-27 | 2021-08-27 | Online steamed system of point of efflux |
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| CN215873350U true CN215873350U (en) | 2022-02-22 |
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| CN202122054338.3U Active CN215873350U (en) | 2021-08-27 | 2021-08-27 | Online steamed system of point of efflux |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115028677A (en) * | 2022-06-28 | 2022-09-09 | 山东国宏生物科技有限公司 | Production process for improving salt tolerance of soybean protein isolate |
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2021
- 2021-08-27 CN CN202122054338.3U patent/CN215873350U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115028677A (en) * | 2022-06-28 | 2022-09-09 | 山东国宏生物科技有限公司 | Production process for improving salt tolerance of soybean protein isolate |
| CN115028677B (en) * | 2022-06-28 | 2023-08-15 | 山东国宏生物科技有限公司 | Production process for improving salt tolerance of isolated soy protein |
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