WO2023040177A1 - Dispositif d'extraction segmenté pour solution nutritive utilisée dans la production de protéine de salamandre géante - Google Patents

Dispositif d'extraction segmenté pour solution nutritive utilisée dans la production de protéine de salamandre géante Download PDF

Info

Publication number
WO2023040177A1
WO2023040177A1 PCT/CN2022/076553 CN2022076553W WO2023040177A1 WO 2023040177 A1 WO2023040177 A1 WO 2023040177A1 CN 2022076553 W CN2022076553 W CN 2022076553W WO 2023040177 A1 WO2023040177 A1 WO 2023040177A1
Authority
WO
WIPO (PCT)
Prior art keywords
liquid
sliding
protein
giant salamander
housing
Prior art date
Application number
PCT/CN2022/076553
Other languages
English (en)
Chinese (zh)
Inventor
裴金金
金文刚
陈德经
耿敬章
王金泽
黄一刚
刘哲
Original Assignee
陕西理工大学
陕西墨博信息科技有限公司
浙江鲲鹄科技股份有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 陕西理工大学, 陕西墨博信息科技有限公司, 浙江鲲鹄科技股份有限公司 filed Critical 陕西理工大学
Priority to GB2300602.6A priority Critical patent/GB2615650A/en
Publication of WO2023040177A1 publication Critical patent/WO2023040177A1/fr

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14—Extraction; Separation; Purification
    • C07K1/34—Extraction; Separation; Purification by filtration, ultrafiltration or reverse osmosis
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/435—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • C07K14/46—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans from vertebrates
    • C07K14/463—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans from vertebrates from amphibians
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14—Extraction; Separation; Purification
    • C07K1/145—Extraction; Separation; Purification by extraction or solubilisation

Definitions

  • the invention belongs to the technical field of biological extraction, and in particular relates to a segmental extraction device for nutrient solution used for production of giant salamander protein.
  • Giant salamander is a kind of amphibian.
  • the skin of giant salamander is thick and viscous, and the content of colloidal components is high. It is rich in high-quality protein, amino acid, natural active substances and abundant collagen, which can improve cell microcirculation, promote protein synthesis, collagen Protein is rich in glycine, proline and hydroxyproline, and its hydrolyzate is also rich in physiologically active peptides. It is one of the most popular beauty and health care products in recent years. Therefore, giant salamander is used as raw material to process water-soluble protein And its series of products have very good prospects and value.
  • collagen extraction methods can be divided into acid method, alkali method, enzymatic method, salt method and hot water extraction method, etc.
  • the basic principle is to change the external environment of the protein according to the characteristics of collagen.
  • different methods are often combined with each other.
  • the existing extraction technology requires multiple mixing, filtration, washing and centrifugation, which not only has complicated steps but also makes the extraction efficiency of multi-stage nutrient solution lower.
  • the purpose of the embodiments of the present invention is to provide a segmented extraction device for nutrient solution for the production of giant salamander protein, so as to solve the above-mentioned problems in the background technology.
  • the present invention provides the following technical solutions:
  • a segmental extraction device for nutrient solution for giant salamander protein production comprising a housing assembly, the housing assembly includes a main housing, a sump and an opening and closing groove, and the sump is circumferentially arranged on the inner wall of the main housing On the top, it is used to extract the giant salamander protein nutrient solution in sections, and the opening and closing groove is arranged on one side of the main shell, and is used to input the raw material of the giant salamander protein to be extracted into the main shell;
  • the liquid supply tube set includes a fixed shaft frame and a catheter
  • the fixed shaft frame is fixedly arranged on one side of the main casing
  • one end of the catheter tube is fixedly assembled in the fixed shaft frame
  • the other end is arranged on the main casing
  • the catheter tube is connected to a number of liquid inlet pipes on the side close to the outside of the main casing, and the side of the catheter pipe near the interior of the main casing is provided with a number of liquid outlets, and the liquid inlet pipe and the liquid outlet connected in sequence, for outputting protein extracts of different components into the main shell;
  • a liquid storage mechanism the liquid storage mechanism includes a fixed-rotation housing and an abutting piece, one end of the fixed-rotation housing is rotatably sleeved on the fixed shaft frame, and the other end of the fixed-rotation housing is covered outside the catheter for use
  • the protein extraction liquid output in the catheter is contained, and a number of drain nozzles are arranged on the fixed-rotor housing, and the drain nozzles are matched with the liquid collection tank to discharge the protein extract in the fixed-rotor housing.
  • the extraction liquid is output to the side of the liquid collection tank, and the side of the fixed-rotation housing is also equipped with abutting parts, which are connected to the catheter in rotation, and a filter membrane is arranged on it to separate the giant salamander raw material and protein extract;
  • the sliding sleeve is set on the fixed-rotation shell, and one end is in sliding contact with the abutment piece, which is used to cooperate with the abutment piece to filter the mixture of giant salamander raw material and protein extract, and there are several communication channels on it.
  • the nozzle, the connecting nozzle is arranged between the liquid collection tank and the liquid discharge nozzle, and the connecting nozzle is matched with the liquid collection tank and the liquid discharge nozzle, and is used to slide and control the protein extract on one side of the discharge nozzle.
  • the liquid discharge member is fixedly assembled in the fixed-rotation housing, and the liquid discharge member includes several covering shells.
  • the protein extract in the drain port is output to the fixed-rotor housing, and the other end of the coating shell is movably inserted into the drain nozzle, and is set in linkage with the drain port to control the protein extract of different components from the corresponding Discharge from the drain pipe;
  • a plugging component arranged in the outlet of the discharge pipe, used for actively blocking the discharge pipe outlet, and set in linkage with the discharge member, used to control the opening and closing of the discharge pipe outlet;
  • the driving member is assembled on one side of the sliding shell mechanism, and one end is connected with a driver, which is used to drive the rotation of the sliding shell mechanism, so that the sliding shell mechanism drives the liquid storage mechanism to rotate, thereby centrifuging the mixture of giant salamander raw material and protein extract, and During the rotation, the sliding shell mechanism is driven to slide on the liquid storage mechanism, so that the liquid collection tank, the discharge nozzle and the communication nozzle are connected, so that the protein extracts of different components are discharged into different liquid collection tanks.
  • the present invention has the following beneficial effects:
  • the liquid discharge member arranged on the liquid supply pipe group by rotating the liquid discharge member arranged on the liquid supply pipe group, protein extracts of different components can be sequentially input into the liquid storage mechanism, and the giant salamander raw material can be mixed, stirred and centrifuged in conjunction with the rotation of the sliding shell mechanism. operation, and the passage between the liquid storage mechanism and the sliding shell mechanism can be connected through the liquid discharge member, so that the protein extracts of different components are discharged correspondingly through different passages, and the segmental extraction of the giant salamander protein nutrient solution is realized, and the extraction steps All are implemented in the same container, which not only facilitates operation but also improves efficiency.
  • Fig. 1 is a structural schematic diagram of a segmented extraction device for nutrient solution for production of giant salamander protein provided in an embodiment of the present invention.
  • Fig. 2 is a schematic diagram of the structure marked A in the staged extraction device for nutrient solution for production of giant salamander protein provided in an embodiment of the present invention.
  • Fig. 3 is a schematic side view of the liquid drainage member in the staged extraction device for nutrient solution for production of giant salamander protein provided in an embodiment of the present invention.
  • Fig. 4 is a schematic diagram of the structure marked B in the staged extraction device for nutrient solution for production of giant salamander protein provided in an embodiment of the present invention.
  • Fig. 5 is a three-dimensional cutaway view of the liquid storage mechanism in the staged extraction device for the nutrient solution used in the production of giant salamander protein provided in an embodiment of the present invention.
  • Fig. 6 is a perspective cross-sectional view of the back of the liquid storage mechanism in the staged extraction device for nutrient solution for production of giant salamander protein provided in an embodiment of the present invention.
  • the segmental extraction device for the nutrient solution used in the production of giant salamander protein in one embodiment of the present invention comprises housing assembly 1, and housing assembly 1 comprises main housing 101, liquid sump 102 and start The closed tank 103 and the liquid collecting tank 102 are arranged circumferentially on the inner wall of the main housing 101 for segmentally extracting the nutrient solution of giant salamander protein.
  • the opening and closing tank 103 is arranged on one side of the main housing 101 for feeding Input the raw material of giant salamander protein to be extracted;
  • the liquid supply tube group 2 includes a fixed shaft frame 201 and a catheter 202, the fixed shaft frame 201 is fixedly arranged on one side of the main housing 101, and one end of the catheter tube 202 It is fixedly assembled in the fixed shaft frame 201, and the other end is arranged inside the main housing 101.
  • the catheter tube 202 is connected with a number of liquid inlet tubes 203 on the side close to the outside of the main housing 101.
  • the catheter tube 202 is close to the inside of the main housing 101.
  • the liquid storage mechanism 3 includes The fixed-rotation housing 301 and the abutting piece 303, one end of the fixed-rotation housing 301 is rotatably sleeved on the fixed shaft frame 201, and the other end of the fixed-rotation housing 301 is covered outside the catheter 202 for containing the catheter 202
  • the protein extract output in the fixed-rotor housing 301 is provided with a number of drain nozzles 305, the drain nozzle 305 is matched with the liquid collection tank 102, and is used to remove the protein extract in the fixed-rotor housing 301.
  • abutment 303 which is connected to the catheter 202 in rotation, and a filter membrane 304 is arranged on it to separate giant salamanders.
  • Raw materials and protein extract; sliding shell mechanism 4, the sliding sleeve is set on the fixed-rotor housing 301, and one end is in sliding contact with the abutment piece 303, which is used to cooperate with the abutment piece 303 to carry out the mixed solution of the giant salamander raw material and the protein extract solution.
  • the liquid discharge member 5 includes a number of coating housings 501.
  • the coating housing 501 is rotatably sleeved on the catheter 202 and communicated with the discharge port 205.
  • the other end of the coating housing 501 is movably inserted into the discharge nozzle 305, and is set in linkage with the discharge port 205 for controlling
  • the protein extracts of different components are discharged from the corresponding discharge nozzles 305;
  • the blocking component 6 is arranged in the discharge nozzles 305, and is used to actively block the discharge nozzles 305, and is linked with the discharge member 5 Set, for controlling the opening and closing of the drain nozzle 305;
  • One side and one end of the shell mechanism 4 are connected with a driver 8, which is used to drive the rotation of the sliding shell mechanism 4, so that the sliding shell mechanism 4 drives the liquid storage mechanism 3 to rotate, thereby centrifuging the mixture of the giant salamander raw material and the protein extract solution, and rotating
  • the sliding shell mechanism 4 is driven to slide on the liquid storage mechanism 3, so that the liquid collection tank 102, the discharge nozzle 305 and the communication nozzle 405
  • the giant salamander raw material is transported to the liquid storage mechanism 3 and the sliding shell mechanism 4 through the opening and closing tank 103, it is first output through the liquid inlet pipe 203 to the liquid discharge port 205 on the side of the liquid guide pipe 202.
  • the pure water when the pure water output from the liquid discharge port 205 side is output to the fixed-rotation housing 301 through the coating housing 501, the pure water passes through the filter membrane 304 on the abutting member 303 and contacts with the giant salamander raw material, and cooperates with the drive
  • the driving effect of the component 7 and the driver 8 drives the liquid storage mechanism 3 and the sliding shell mechanism 4 to rotate at a low speed, so that the pure water and the giant salamander raw material are mixed and stirred to obtain the mixed slurry and slurry, and the driver 8 is driven to rotate at a high speed after mixing to drive
  • the slider mechanism 4 and the liquid storage mechanism 3 rotate at the same speed, and at this time, the driving member 7 can drive the slider mechanism 4 to slide directionally on the surface of the liquid storage mechanism 3 under the condition of high speed, so that the abutment 303 and the slider mechanism 4 The distance between them is reduced, and the pressurized slurry enters the fixed-rotation housing 301 after passing through the filter membrane 304.
  • the discharge nozzle 305 on the fixed-rotation housing 301 and the communication nozzle 405 on the sliding shell mechanism 4 are both It is connected with the liquid collection tank 102 after matching and docking, and because the liquid discharge port 205 through which pure water flows is driven by the liquid discharge member 5 on this side to move the blocking assembly 6 on this side before entering the fixed-rotation housing 301, so that it is connected with the pure water
  • the corresponding discharge nozzle 305 is connected, and the slurry can be discharged from the discharge nozzle 305 on this side through the communication nozzle 405 to the sump 102 when the set high-speed rotation condition is reached, and the slurry can be discharged through the collection tank 102.
  • the liquid tank 102 is discharged to the outside of the device to achieve the extraction of the giant salamander raw material slurry in the first stage, and leave the slurry to be treated for the second time.
  • the slide housing mechanism 4 is reset on the side of the liquid storage mechanism 3 through the deceleration driver 8, and at the same time, the passage between the communication nozzle 405 and the liquid collection tank 102 and the liquid discharge nozzle 305 is blocked.
  • the acid solution extraction liquid is output to the guide pipe 202 side through the liquid inlet pipe 203, and the acid solution is contacted with the giant salamander raw material after passing through the filter membrane 304.
  • the The raw material and the acid solution extract are centrifuged to obtain acid-soluble collagen and filter residue.
  • the sliding shell mechanism 4 can be driven to slide toward the side of the liquid storage mechanism 3 again. And control the opening of the discharge nozzle 305 corresponding to the acid solution extraction liquid, so that the acid-soluble collagen liquid is discharged from the discharge nozzle 305 on this side through the communication nozzle 405 to the corresponding liquid collection tank 102, and the process is completed.
  • the alkali solution extract, the salt solution extract and the enzyme solution extract are sequentially output to the fixed-rotation housing 301 through the liquid inlet pipe 203, and the alkali-soluble collagen,
  • the salt-soluble collagen and the enzyme-promoted soluble collagen are discharged from the corresponding drain nozzle 305 into the corresponding sump 102 to achieve segmental extraction of the giant salamander protein nutrient solution.
  • the liquid inlet pipe 203 includes a pure water pipeline, an acid solution extraction solution pipeline, an alkali solution extraction solution pipeline, a salt solution extraction solution pipeline and an enzyme solution extraction solution pipeline. All the solutions are pressurized into the catheter 202 by the booster pump 204 to ensure sufficient pressure when discharged at the side of the discharge port 205.
  • the giant salamander raw material to be processed is chopped and sterilized before collagen extraction, which will not be described in detail here.
  • the housing assembly 1 also includes: a liquid discharge nozzle 104, which communicates with the sump 102, and is used to extract the protein of different components in the sump 102 The liquid is discharged in stages; the slag discharge port 105 is arranged on the bottom side of the main housing 101 for recycling the cleaned waste residue; and the isolation chamber 106 is arranged on the side of the slide mechanism 4 and between the slide mechanism 4 It is sealed and isolated by the partition member 107 .
  • the liquid collecting tank 102 is surrounded and arranged outside the communicating nozzle 405, and is connected with the sliding shell mechanism 4 in a sliding seal, so that the sliding shell mechanism 4 rotates inside the main casing 101,
  • the protein extraction solution discharged through the connecting nozzle 405 is discharged into the sump 102 under the action of rotation and centrifugation, and flows to the drain nozzle 104 in the sump 102 to be discharged by gravity.
  • the liquid collection tank 102 is in clearance fit with the sliding shell mechanism 4, and the influence of the clearance distance on the leakage of the solution is negligible.
  • a slide groove group 10 is arranged between the liquid storage mechanism 3 and the sliding shell mechanism 4, and the sliding groove set 10 is used to limit the position of the sliding shell mechanism 4 in the liquid storage mechanism. 3 on the slide direction.
  • the sliding case mechanism 4 is slidably assembled on the liquid storage mechanism 3 through the sliding groove group 10, the sliding direction of the sliding case mechanism 4 can be limited, and the rotation of the liquid storage mechanism 3 can be driven by the sliding case mechanism 4 , so that the liquid storage mechanism 3 and the slider mechanism 4 move synchronously.
  • the sliding groove group 10 is in sealing contact with the liquid storage mechanism 3 and the sliding shell mechanism 4, so as to prevent the leakage of the protein extract.
  • the sliding case mechanism 4 further includes: a sliding housing 401 , which is slidably sleeved on the fixed rotating housing 301 so that the fixed rotating housing 301 and the fixed rotating housing 301
  • the sliding housing 401 rotates synchronously on the side of the fixed shaft frame 201;
  • the pressing member 402 is arranged towards the side of the abutting member 303, and a raw material chamber 9 is arranged between the pressing member 402 and the abutting member 303, and the raw material chamber 9 is used and the movable valve port 403, which is movably assembled on one side of the sliding housing 401 and matched with the opening and closing groove 103, is used for inputting the raw material of giant salamander to be processed into the raw material chamber 9.
  • the sliding housing 401 is connected with a sliding cylinder 404, and the sliding cylinder 404 is slidably arranged on the fixed rotating housing 301 through the sliding groove group 10, and when the pressing member 402 and the contacting member 303 When abutting, the giant salamander raw material and protein extract located in the raw material chamber 9 can quickly output the protein extract through the filter membrane 304 to the fixed-rotor housing 301 in the squeezed state, and cooperate with the rotation of the liquid storage mechanism 3 to transfer the protein extract The extraction liquid is discharged into the corresponding sump 102 through the corresponding drain nozzle 305 .
  • the movable valve port 403 is movably assembled on the sliding housing 401, and is set to match the position of the opening and closing groove 103. After opening the opening and closing groove 103, the movable valve port 403 can move toward the The giant salamander raw material is placed in the raw material chamber 9. During the cleaning process of the device, the movable valve port 403 can be opened and the opening and closing groove 103 can be closed. , clean the waste slag contained in the raw material chamber 9 during the rotation process, and discharge it from the movable valve port 403 and finally discharge it from the slag discharge port 105 to the outside of the device.
  • the liquid drainage member 5 further includes: a liquid storage chamber 502, arranged between the covering shell 501 and the catheter 202, for containing the drainage The protein extraction solution output in the liquid port 205; the narrow mouth end 503 is arranged on one side of the coating shell 501, and a sliding plug 504 is elastically mounted on one side thereof, and the sliding plug 504 is matched with the liquid discharge port 205 to make the liquid discharge
  • the liquid pressure generated in the port 205 pushes the sliding plug 504 to move; one end of the trigger 505 is assembled with the sliding plug 504, and the other end is slidably arranged on the side of the discharge pipe port 305, and is matched with the discharge pipe port 305 to trigger
  • One side of the piece 505 is provided with a card slot 507; the elastic card block 506 is elastically assembled on one side of the card slot 507, and is used for sliding the elastic limit trigger member 505 through the card slot 507, and through the card slot 507 and the
  • the sliding buckle drives the rest of the sliding plugs 504 to reset, so that only one group of sliding plugs 504 is in the buckling state among the plurality of sliding plugs 504;
  • the protein extraction liquid in the chamber 502 is unidirectionally output into the fixed-rotor casing 301 .
  • the solution when the solution is output from the side of the discharge port 205, the solution first fills the liquid storage chamber 502, and after the narrow end 503 rotates to the side of the liquid discharge port 205, the liquid in the narrow end 503
  • the instantaneous pressure increases, and pushes the sliding plug 504 to overcome the elastic force to slide on the side of the casing 501, and when the slot 507 on the side of the trigger 505 slides against the elastic block 506, the elastic block can be pushed 506 overcomes the elastic action force and moves.
  • the trigger 505 can abut against one side of the blocking assembly 6, so that the drain nozzle 305 on this side is connected, and the protein extraction liquid can be discharged through the drain nozzle 305 on this side.
  • the one-way valve 508 restricts the one-way flow of the protein extract in the liquid storage chamber 502 to the fixed-rotor housing 301 to prevent the extracts of different components from reacting with each other, and on this side
  • the liquid discharge port 205 is in a non-liquid supply state, which can prevent the liquid from flowing backward and causing contamination of the extraction liquid.
  • the blocking assembly 6 further includes: a blocking port 601, which is fixedly arranged in the discharge pipe port 305, and is set close to the inner wall of the fixed-rotation housing 301; the base 602, assembled in the discharge pipe port 305, and arranged on the side of the plugging port 601; and the movable plug head 603, elastically assembled on the side of the base 602, and movably abutting against the plugging port 601, for elastic plugging Drain pipe port 305 .
  • a blocking port 601 which is fixedly arranged in the discharge pipe port 305, and is set close to the inner wall of the fixed-rotation housing 301
  • the base 602 assembled in the discharge pipe port 305, and arranged on the side of the plugging port 601
  • the movable plug head 603 elastically assembled on the side of the base 602, and movably abutting against the plugging port 601, for elastic plugging Drain pipe port 305 .
  • the movable plug head 603 when the trigger member 505 abuts against the movable plug head 603, the movable plug head 603 can be pressed to slide on the base 602 along the discharge nozzle 305, and the extraction liquid can pass through the seal at this time. After the gap between the blocking port 601 and the movable plug 603 , it flows to the side of the connecting nozzle 405 through the base 602 , and enters the liquid collection tank 102 through the connecting nozzle 405 after the connecting nozzle 405 is connected to the drain nozzle 305 .
  • the driving member 7 also includes: a connecting shaft 701, which is slidably inserted in the partition member 107 and one end is fixedly connected with the sliding housing 401; the first connecting seat 702, assembled on the other side of the connecting shaft 701, one end of which is movably inserted with the second connecting seat 703, and the first connecting seat 702 and the second connecting seat 703 are elastically connected; the connecting arm 704 is movably connected to the first connecting seat between the seat 702 and the second connecting seat 703 and are respectively connected to the first connecting seat 702 and the second connecting seat 703 in rotation; the magnetic block 705 is assembled at the joint of the connecting arm 704; and the electrically controlled magnetic pole 706 is arranged on the magnetic block 705 and is electrically connected to the driver 8 .
  • the driver 8 drives the second connecting seat 703 to rotate, the second connecting seat 703 and the first connecting seat 702 are in a retracted state under the elastic force, and at this time, they are located on the side of the magnetic block 705.
  • the electronically controlled magnetic pole 706 on the side generates a magnetic field under the action of current, and repels the magnetic pole of the magnetic block 705, driving the magnetic block 705 to pull the connecting arm 704 to move, so that the first connecting seat 702 is close to the second connecting seat 703, when the driver 8
  • the magnetic block 705 drives the connecting arm 704 to overcome the elastic force and the magnetic force of the electronically controlled magnetic pole 706, and push the connecting shaft 701 toward the slider mechanism 4- side movement, thereby driving the sliding shell mechanism 4 to slide on the liquid storage mechanism 3.
  • the driving member 7 can also be replaced with a telescopic structure to drive the expansion and contraction of the driver 8, thereby controlling the sliding of the sliding housing mechanism 4, which is not specifically limited here.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Biochemistry (AREA)
  • Biophysics (AREA)
  • Genetics & Genomics (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Analytical Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Toxicology (AREA)
  • Zoology (AREA)
  • Gastroenterology & Hepatology (AREA)
  • Peptides Or Proteins (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

L'invention concerne un dispositif d'extraction segmenté pour une solution nutritive utilisée dans la production de protéine de salamandre géante, se rapportant au domaine technique de l'extraction biologique, qui comprend un ensemble boîtier (1), et qui comprend en outre un groupe de tubes (2) d'alimentation en liquide pour délivrer en sortie des extraits protéiques de différents composants à l'ensemble boîtier (1) ; un mécanisme de stockage de liquide (3) emmanché en rotation sur le groupe de tubes d'alimentation en liquide (2), est utilisé pour contenir les extraits protéiques ; un mécanisme de boîtier coulissant (4), emmanché à coulissement sur un boîtier de rotation fixe (301) et est utilisé pour commander de manière coulissante l'ouverture et la fermeture de buses d'évacuation de liquide (305) ; et un élément d'évacuation de liquide (5), qui est utilisé pour commander l'évacuation d'extraits protéiques de différents composants à partir des buses d'évacuation de liquide correspondantes (305). La rotation de l'élément d'évacuation de liquide (5) qui est placé sur le groupe de tubes d'alimentation en liquide (2), permet d'introduire séquentiellement des extraits protéiques de différents composants dans le mécanisme de stockage de liquide (3), et la coopération avec le mécanisme de boîtier coulissant (4), permet de mélanger, mettre sous agitation et centrifuger des matières premières de salamandre géante. L'utilisation de l'élément d'évacuation de liquide (5), permet d'évacuer les extraits protéiques de différents composants par passage à travers différents canaux, de façon à obtenir une extraction segmentée de la solution nutritive protéique de salamandre géante. De plus, les étapes d'extraction sont toutes effectuées dans le même récipient, et donc non seulement le mode opératoire est pratique et rapide mais l'efficacité est également améliorée.
PCT/CN2022/076553 2021-09-17 2022-02-17 Dispositif d'extraction segmenté pour solution nutritive utilisée dans la production de protéine de salamandre géante WO2023040177A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2300602.6A GB2615650A (en) 2021-09-17 2022-02-17 Segmented extraction device for nutrient solution used in giant salamander protein production

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202111093235.6 2021-09-17
CN202111093235.6A CN113773363A (zh) 2021-09-17 2021-09-17 一种大鲵蛋白生产用养分液分段提取装置

Publications (1)

Publication Number Publication Date
WO2023040177A1 true WO2023040177A1 (fr) 2023-03-23

Family

ID=78852138

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2022/076553 WO2023040177A1 (fr) 2021-09-17 2022-02-17 Dispositif d'extraction segmenté pour solution nutritive utilisée dans la production de protéine de salamandre géante

Country Status (3)

Country Link
CN (1) CN113773363A (fr)
LU (1) LU502026B1 (fr)
WO (1) WO2023040177A1 (fr)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2615650A (en) * 2021-09-17 2023-08-16 Univ Shaanxi Technology Segmented extraction device for nutrient solution used in giant salamander protein production
CN113773363A (zh) * 2021-09-17 2021-12-10 陕西理工大学 一种大鲵蛋白生产用养分液分段提取装置

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000210502A (ja) * 1999-01-25 2000-08-02 Niigata Eng Co Ltd 抽出装置
EP2561913A1 (fr) * 2011-08-26 2013-02-27 MAHLE International GmbH Dispositif de filtration
CN107136438A (zh) * 2017-05-25 2017-09-08 巫溪县海丰水产养殖有限公司 高效的大鲵皮肤黏液提取装置
CN207596764U (zh) * 2017-11-28 2018-07-10 李子扬 超声波鱼蛋白提取设备
CN211078995U (zh) * 2019-11-26 2020-07-24 李向阳 一种大鲵胶原皮肤及分泌物蛋白肽提取装置
CN113117359A (zh) * 2021-03-05 2021-07-16 张再艳 一种用于胶原蛋白提取用的无菌式蒸馏瓶
CN113773363A (zh) * 2021-09-17 2021-12-10 陕西理工大学 一种大鲵蛋白生产用养分液分段提取装置

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000210502A (ja) * 1999-01-25 2000-08-02 Niigata Eng Co Ltd 抽出装置
EP2561913A1 (fr) * 2011-08-26 2013-02-27 MAHLE International GmbH Dispositif de filtration
CN107136438A (zh) * 2017-05-25 2017-09-08 巫溪县海丰水产养殖有限公司 高效的大鲵皮肤黏液提取装置
CN207596764U (zh) * 2017-11-28 2018-07-10 李子扬 超声波鱼蛋白提取设备
CN211078995U (zh) * 2019-11-26 2020-07-24 李向阳 一种大鲵胶原皮肤及分泌物蛋白肽提取装置
CN113117359A (zh) * 2021-03-05 2021-07-16 张再艳 一种用于胶原蛋白提取用的无菌式蒸馏瓶
CN113773363A (zh) * 2021-09-17 2021-12-10 陕西理工大学 一种大鲵蛋白生产用养分液分段提取装置

Also Published As

Publication number Publication date
CN113773363A (zh) 2021-12-10
LU502026B1 (en) 2023-03-24

Similar Documents

Publication Publication Date Title
WO2023040177A1 (fr) Dispositif d'extraction segmenté pour solution nutritive utilisée dans la production de protéine de salamandre géante
CN205687904U (zh) 一种用于核酸提取的微流控装置及控制系统
CN104297501B (zh) 用于微流控检测的果蔬农药残留提取与进样装置及方法
CN207119498U (zh) 自清洁出水装置和摆动水出水装置
CN109530354A (zh) 一种妇产科专用奶瓶内外壁清洗消毒装置
CN113337395A (zh) 一种干细胞智能离心快速提取装置及其提取方法
CN114085769A (zh) 一种干细胞提取用离心智能抽取系统
CN205796119U (zh) 深部吸痰用吸痰器
CN205710700U (zh) 一种核酸提取纯化一体化装置
GB2615650A (en) Segmented extraction device for nutrient solution used in giant salamander protein production
CN208574262U (zh) 一种用于黄芩提取工艺的提取设备
CN209405367U (zh) 一种腹膜透析机
CN108030563B (zh) 一种多方位易操作高效口腔清理装置
CN103012622B (zh) 用于肝素钠提取过程中的完全搅拌罐
CN109231558A (zh) 一种城镇生活污水低能耗处理装置及其使用方法
CN215137084U (zh) 一种花青素提取的浓缩装置
CN114653434A (zh) 一种多肽配合物制备用混合方法和应用
CN210645214U (zh) 一种植物液体分离装置
CN208250044U (zh) 一种化学化工废液分类回收处理装置
CN208756634U (zh) 一种肝胆外科用智能引流瓶
CN215962231U (zh) 一种蓝莓花青素提取装置
CN215353073U (zh) 一种透明质酸的纯化装置
CN208660458U (zh) 一种用于凉茶的中草药醇沉处理装置
CN207371357U (zh) 一种高效同位素分离装置
CN220056771U (zh) 一种高效型线粒体提取装置

Legal Events

Date Code Title Description
ENP Entry into the national phase

Ref document number: 202300602

Country of ref document: GB

Kind code of ref document: A

Free format text: PCT FILING DATE = 20220217

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 22868557

Country of ref document: EP

Kind code of ref document: A1