CN-224221314-U - Yolk globulin powder extraction system

CN224221314UCN 224221314 UCN224221314 UCN 224221314UCN-224221314-U

Abstract

The utility model discloses a yolk globulin powder extraction system, which relates to the technical field of yolk globulin powder extraction and comprises a water purification device, a refrigerator body, an acidification tank body, a flocculation tank body, a filtering component and a freeze dryer body, wherein a water inlet of the water purification device is connected with a tap water source, a water outlet of the water purification device is respectively connected with a water inlet of the refrigerator body, a water inlet of the acidification tank body and a water inlet of the flocculation tank body, a liquid outlet of the acidification tank is connected with a liquid inlet of the flocculation tank, a liquid outlet of the flocculation tank is connected with a liquid inlet of the filtering component, a liquid outlet of the filtering component is connected with a liquid inlet of the freeze dryer, a flocculation tank jacket is arranged on the outer wall of the flocculation tank body, a filtering component jacket is arranged on the outer side of the filtering component, and a cooling liquid outlet of the refrigerator body is respectively communicated with the flocculation tank jacket and the filtering component jacket. The utility model can improve the extraction efficiency of the yolk globulin powder and reduce the working intensity of experimenters.

Inventors

LI ZAIXIN
FENG PAN
LI XINYANG
ZHANG ZHI

Assignees

四川轻化工大学

Dates

Publication Date: 20260512
Application Date: 20250421

Claims (10)

1. The yolk globulin powder extraction system is characterized by comprising a water purification device, a refrigerator body, an acidification tank body, a flocculation tank body, a filtering component and a freeze dryer body, wherein a water inlet of the water purification device is connected with a tap water source, a water outlet of the water purification device is respectively connected with a water inlet of the refrigerator body, a water inlet of the acidification tank body and a water inlet of the flocculation tank body, a liquid outlet of the acidification tank is connected with a liquid inlet of the flocculation tank, a liquid outlet of the flocculation tank is connected with a liquid inlet of the filtering component, a liquid outlet of the filtering component is connected with a liquid inlet of the freeze dryer, a flocculation tank jacket is arranged on the outer wall of the flocculation tank body, a filtering component jacket is arranged on the outer side of the filtering component, and a cooling liquid outlet of the refrigerator body is respectively communicated with the flocculation tank jacket and the filtering component jacket.
2. The yolk globulin powder extraction system of claim 1, wherein the water purification device is a water purifier body, a tap water pressure valve is arranged on a pipeline connected with a tap water source of the water purifier body, a water outlet pipe of the water purifier body is connected with a pure water main pipe, and a pure water main pipe valve and a pure water main pipe conveying pump are arranged on the pure water main pipe.
3. The yolk globulin powder extraction system of claim 2, wherein the end of the main water purifier tube far away from the main water purifier body is connected with a first pure water branch pipe, a second pure water branch pipe and a third pure water branch pipe; one end of the first pure water branch pipe, which is far away from the pure water main pipe, is connected with a water inlet of the refrigerator body, and a refrigerator water inlet pressure valve is arranged on the first pure water branch pipe; One end of the second pure water branch pipe, which is far away from the pure water main pipe, is connected with a water inlet of the acidification tank body, and an acidification tank water inlet pressure valve is arranged on the second pure water branch pipe; And one end, far away from the pure water main pipe, of the third pure water branch pipe is connected with the water inlet of the flocculation tank body, and a flocculation tank water inlet pressure valve is arranged on the third pure water branch pipe.
4. The yolk globulin powder extraction system of claim 1, wherein the acidification tank body is provided with an acidification tank stirring device, the acidification tank stirring device comprises an acidification tank stirring motor, an output shaft of the acidification tank stirring motor is connected with an acidification tank stirring shaft, a plurality of acidification tank stirring blades are arranged on the acidification tank stirring shaft, and the acidification tank stirring blades are positioned in the acidification tank body; the upper end of the acidification tank body is also provided with an acidification tank thermometer, and the upper end of the acidification tank body is also provided with an acidification tank opening; The lower extreme of acidizing jar body is equipped with acidizing jar sample connection and acidizing jar liquid outlet, acidizing jar sample connection department is equipped with acidizing jar sample valve, the acidizing jar liquid outlet with be equipped with the acidizing jar liquid outlet valve on the pipeline between the inlet of flocculation jar body.
5. The yolk globulin powder extraction system of claim 1, wherein the flocculation tank body is provided with a flocculation tank stirring device, the flocculation tank stirring device comprises a flocculation tank stirring motor, an output shaft of the flocculation tank stirring motor is connected with a flocculation tank stirring shaft, the flocculation tank stirring shaft is provided with a plurality of flocculation tank stirring blades, and the flocculation tank stirring blades are positioned in the flocculation tank body; The top of the flocculation tank body is provided with a flocculation tank exhaust port, and the flocculation tank exhaust port is provided with a flocculation tank exhaust valve; the top of the flocculation tank body is provided with a flocculation tank opening, and a flocculation tank inlet pressure valve is arranged at the position of the flocculation tank inlet; the lower extreme of flocculation tank body is equipped with flocculation tank sampling port and flocculation tank liquid outlet, flocculation tank sampling port department is equipped with flocculation tank sampling valve, flocculation tank liquid outlet with be equipped with flocculation tank liquid outlet valve on the pipeline between filter element's the inlet.
6. The yolk globulin powder extraction system of claim 1, wherein the filtering assembly comprises a first-stage filter, a second-stage filter and a third-stage filter which are sequentially connected, the liquid inlet of the first-stage filter is connected with the liquid outlet of the flocculation tank body, the liquid outlet of the first-stage filter is connected with the liquid inlet of the second-stage filter, the liquid outlet of the second-stage filter is connected with the liquid inlet of the third-stage filter, and the liquid outlet of the third-stage filter is connected with the liquid inlet of the freeze dryer.
7. The egg yolk globulin powder extraction system of claim 6 wherein the primary filter, the secondary filter and the tertiary filter are cross-flow filters.
8. The yolk globulin powder extraction system of claim 7, wherein the primary filter comprises a primary raw liquid tank, a first primary membrane module and two second primary membrane modules, wherein the liquid outlet of the primary raw liquid tank is connected with the liquid inlet of the first primary membrane module, the liquid outlet of the first primary membrane module is connected with the liquid inlets of the two second primary membrane modules, the filtrate outlets of the two second primary membrane modules are connected with the secondary filter, and the raw liquid outlets of the two second primary membrane modules are connected with the circulating raw liquid inlet of the primary raw liquid tank; The secondary filter comprises a secondary raw liquid tank, a first secondary membrane component and two secondary membrane components, wherein a liquid outlet of the secondary raw liquid tank is connected with a liquid inlet of the first secondary membrane component, a liquid outlet of the first secondary membrane component is connected with liquid inlets of the two secondary membrane components, a filtrate outlet of the two secondary membrane components is connected with the three-stage filter, and a raw liquid outlet of the two secondary membrane components is connected with a circulating raw liquid inlet of the secondary raw liquid tank; The three-stage filter comprises a three-stage raw liquid tank, a first three-stage membrane assembly and two second three-stage membrane assemblies, wherein a liquid outlet of the three-stage raw liquid tank is connected with a liquid inlet of the first three-stage membrane assembly, a liquid outlet of the first three-stage membrane assembly is connected with two liquid inlets of the second three-stage membrane assembly, a filtrate outlet of the second three-stage membrane assembly is connected with a filtrate collecting container, a raw liquid outlet of the second three-stage membrane assembly is connected with a circulating raw liquid inlet of the three-stage raw liquid tank, and a product solution liquid outlet of the three-stage raw liquid tank is connected with the freeze dryer.
9. The yolk globulin powder extraction system of claim 8, wherein a first-stage inlet pressure valve is arranged at a liquid inlet of the first-stage raw liquid tank, a first-stage thermometer, a first-stage filtering tank opening and a first-stage filtering exhaust opening are further arranged at the top of the first-stage raw liquid tank, a first-stage filtering exhaust valve is arranged at the first-stage filtering exhaust opening, a first-stage circulating raw liquid pressure valve is arranged at a circulating raw liquid inlet of the first-stage raw liquid tank, a first-stage filtering liquid discharge valve and a first-stage filtering liquid discharge pressure valve are arranged on a pipeline between the second-stage membrane assembly and the second-stage filter, a first-stage filtering liquid sampling pipeline is further connected to a pipeline between the second-stage membrane assembly and the second-stage filter, a first-stage filtering liquid sampling valve is arranged on the first-stage filtering liquid sampling pipeline, a first-stage raw liquid tank liquid outlet valve, a first-stage conveying pump and a first-stage pressure gauge are further arranged at the bottom of the first-stage raw liquid tank, and a first-stage raw liquid tank sampling valve is arranged at the first-stage raw liquid sampling port; The liquid inlet of the secondary raw liquid tank is provided with a secondary liquid inlet pressure valve, the top of the secondary raw liquid tank is also provided with a secondary thermometer, a secondary filtering tank opening and a secondary filtering exhaust opening, the secondary filtering exhaust opening is provided with a secondary filtering exhaust valve, the circulating raw liquid inlet of the secondary raw liquid tank is provided with a secondary circulating raw liquid pressure valve, a pipeline between the second secondary membrane component and the third-stage filter is provided with a secondary filtering liquid discharge valve and a secondary filtering liquid discharge pressure valve, a pipeline between the second secondary membrane component and the third-stage filter is also connected with a secondary filtering liquid sampling pipeline, the secondary filtering liquid sampling pipeline is provided with a secondary filtering liquid sampling valve, the pipeline between the secondary raw liquid tank and the first secondary membrane component is provided with a secondary raw liquid tank liquid outlet valve, a secondary conveying pump and a secondary pressure meter, the bottom of the secondary raw liquid tank is also provided with a secondary raw liquid sampling port, and the secondary raw liquid sampling port is provided with a secondary raw liquid sampling valve; The liquid inlet of the three-stage raw liquid tank is provided with a three-stage liquid inlet pressure valve, the top of the three-stage raw liquid tank is also provided with a three-stage thermometer, a three-stage filtering tank opening and a three-stage filtering exhaust opening, the three-stage filtering exhaust opening is provided with a three-stage filtering exhaust valve, the circulating raw liquid inlet of the three-stage raw liquid tank is provided with a three-stage circulating raw liquid pressure valve, a three-stage raw liquid tank liquid outlet valve, a three-stage delivery pump and a three-stage pressure gauge are arranged on a pipeline between the three-stage raw liquid tank and the first three-stage membrane component, the bottom of tertiary former fluid reservoir still is equipped with tertiary former fluid reservoir sample connection, tertiary former fluid reservoir sample connection department is equipped with tertiary former fluid reservoir sample valve, the second tertiary membrane module the filtrate export with be equipped with filtrate collection pressure valve on the pipeline between the filtrate collection container, the product solution liquid outlet of tertiary former fluid reservoir with be equipped with product solution delivery valve and product solution delivery pump on the pipeline that the freeze dryer is connected.
10. The yolk globulin powder extraction system of claim 6, wherein the refrigerator body is connected with a cooling liquid outflow main pipe and a cooling liquid return main pipe, a refrigerator cooling liquid outflow valve is arranged at one end of the cooling liquid outflow main pipe, which is close to the refrigerator body, and a refrigerator cooling liquid return valve is arranged at one end of the cooling liquid return main pipe, which is close to the refrigerator body; The cooling liquid outflow main pipe is connected with a liquid inlet of the flocculation tank jacket through a cooling liquid outflow first branch pipe, a cooling liquid outflow first pressure valve is arranged on the cooling liquid outflow first branch pipe, and the cooling liquid outflow main pipe is connected with a liquid inlet of a primary filtering jacket outside the primary filter through a cooling liquid outflow second branch pipe; The cooling liquid flow-back main pipe is connected with a liquid outlet of the flocculation tank jacket through a cooling liquid flow-back first branch pipe, a cooling liquid flow-back first pressure valve is arranged on the cooling liquid flow-back first branch pipe, the cooling liquid flow-back main pipe is connected with a liquid outlet of the primary filtering jacket through a cooling liquid flow-back second branch pipe, a cooling liquid flow-back second pressure valve is arranged on the cooling liquid flow-back second branch pipe, the cooling liquid flow-back main pipe is connected with a liquid outlet of the secondary filtering jacket through a cooling liquid flow-back third branch pipe, a cooling liquid flow-back third pressure valve is arranged on the cooling liquid flow-back third branch pipe, the cooling liquid flow-back main pipe is connected with a liquid outlet of the tertiary filtering jacket through a cooling liquid flow-back fourth branch pipe, and a cooling liquid flow-back fourth pressure valve is arranged on the cooling liquid flow-back fourth branch pipe.

Description

Yolk globulin powder extraction system Technical Field The utility model relates to the technical field of yolk globulin powder extraction, in particular to a yolk globulin powder extraction system. Background Egg yolk globulin (egg yolk antibodies, igY) is an immunoglobulin produced by laying hens after immunization with a specific antigen and transferred and stored in the yolk. The preparation method has the advantages of good antigen specificity recognition, safety, no residue, easy acquisition of preparation raw materials and the like, so that the preparation method is widely accepted in disease prevention and treatment. The preparation method of the yolk globulin in the laboratory comprises diluting yolk with water, adding citric acid to adjust pH, placing the solution in a refrigerator at 4 ℃ overnight, taking out the solution the next day, placing the solution on a centrifuge for centrifugation, taking supernatant, adding citric acid again to adjust pH, adding a proper amount of sodium chloride for stirring uniformly, standing in the refrigerator at 4 ℃ for six hours, centrifuging, and taking precipitate. However, the existing preparation method of egg yolk globulin has complicated process, and the equipment used in each step is different, so that the workers are required to continuously move the solution to different equipment. Thus, not only the labor intensity of the experimenters is high, but also the experimental efficiency is lower. Accordingly, there is a need in the art for an egg yolk globulin powder extraction system that addresses the above-described issues. Disclosure of utility model The utility model aims to provide an egg yolk globulin powder extraction system which solves the problems in the prior art, improves the extraction efficiency of egg yolk globulin powder and reduces the labor intensity of experimenters. In order to achieve the above object, the present utility model provides the following solutions: The utility model discloses an egg yolk globulin powder extraction system which comprises a water purification device, a refrigerator body, an acidification tank body, a flocculation tank body, a filtering component and a freeze dryer body, wherein a water inlet of the water purification device is connected with a tap water source, a water outlet of the water purification device is respectively connected with a water inlet of the refrigerator body, a water inlet of the acidification tank body and a water inlet of the flocculation tank body, a liquid outlet of the acidification tank is connected with a liquid inlet of the flocculation tank, a liquid outlet of the flocculation tank is connected with a liquid inlet of the filtering component, a liquid outlet of the filtering component is connected with a liquid inlet of the freeze dryer, a flocculation tank jacket is arranged on the outer wall of the flocculation tank body, a filtering component jacket is arranged on the outer side of the filtering component, and a cooling liquid outlet of the refrigerator body is respectively communicated with the flocculation tank jacket and the filtering component jacket. Preferably, the water purification device is a water purifier body, a tap water pressure valve is arranged on a pipeline connected with a tap water source of the water purifier body, a water outlet pipe of the water purifier body is connected with a pure water main pipe, and a pure water main pipe valve and a pure water main pipe conveying pump are arranged on the pure water main pipe. Preferably, one end of the pure water main pipe far away from the pure water machine body is connected with a first pure water branch pipe, a second pure water branch pipe and a third pure water branch pipe; one end of the first pure water branch pipe, which is far away from the pure water main pipe, is connected with a water inlet of the refrigerator body, and a refrigerator water inlet pressure valve is arranged on the first pure water branch pipe; One end of the second pure water branch pipe, which is far away from the pure water main pipe, is connected with a water inlet of the acidification tank body, and an acidification tank water inlet pressure valve is arranged on the second pure water branch pipe; And one end, far away from the pure water main pipe, of the third pure water branch pipe is connected with the water inlet of the flocculation tank body, and a flocculation tank water inlet pressure valve is arranged on the third pure water branch pipe. Preferably, an acidification tank stirring device is arranged on the acidification tank body, the acidification tank stirring device comprises an acidification tank stirring motor, an output shaft of the acidification tank stirring motor is connected with an acidification tank stirring shaft, a plurality of acidification tank stirring blades are arranged on the acidification tank stirring shaft, and the acidification tank stirring blades are positioned in the acidification tank body; the upper e