CN218221858U

CN218221858U - Organic membrane concentration device in tea deep processing

Info

Publication number: CN218221858U
Application number: CN202222408243.1U
Authority: CN
Inventors: 王江花
Original assignee: Fujian Runbaixiang Tea Industry Co ltd
Current assignee: Fujian Runbaixiang Tea Industry Co ltd
Priority date: 2022-09-09
Filing date: 2022-09-09
Publication date: 2023-01-06
Anticipated expiration: 2032-09-09

Abstract

The utility model discloses an organic membrane enrichment facility in tealeaves deep-processing relates to the concentrated technical field of membrane, for the tealeaves that solves among the prior art at the in-process of deep-processing, uses organic membrane enrichment facility to carry out the concentration often, filters through organic membrane, then draws the trapped fluid, but will seriously block up after organic membrane uses a period, loses filterability, problem that life is short. Organic membrane enrichment facility's inside is provided with organic filtration membrane, organic filtration membrane's inside is provided with the back flush pipe, the back flush shower nozzle is installed in the outside of back flush pipe, and back flush shower nozzle and back flush pipe threaded connection, sealed dish is installed to organic filtration membrane's top, and sealed dish and organic filtration membrane pass through sealing screw fixed connection, sealed dish and organic membrane enrichment facility pass through sealing screw fixed connection, the transfer case is installed to the top of sealed dish, and the transfer case passes through fastening screw fixed connection with sealed dish.

Description

Organic membrane concentration device in tea deep processing

Technical Field

The utility model relates to a membrane concentration technical field specifically is an organic membrane enrichment facility in tealeaves deep-processing.

Background

The membrane concentration is a technology for realizing high-efficiency purification concentration by reforming the traditional process, the membrane concentration equipment realizes directional separation by utilizing the difference of the molecular weight of effective components and liquid to achieve the concentration effect, and compared with the traditional heating concentration, the membrane concentration equipment has the advantages of low energy consumption, low influence on products and the like, the basic principle of the membrane concentration is to take a selective permeable membrane as a separation medium, when pressure difference, concentration difference, potential difference, temperature difference and the like exist at two sides of the membrane, components at the raw material side selectively permeate the membrane to achieve the purposes of separation, purification and concentration, for example, a reverse osmosis membrane only allows water molecules to permeate, but retains other components in water extract to realize the enrichment concentration of the effective components, and low-grade tea leaves are processed into instant tea, so that the low-grade tea leaves are not only solved, but also the benefit is improved;

for example, the application publication number is CN215913188U, an organic film concentrating device in tea deep processing comprises a concentrating machine body, an alarm component and a buffer component, wherein the buffer component comprises a support rod, a fixed seat, a lifting plate, a sliding block, a support block a, a spring and a support block B, the support rod is installed at the bottom of the concentrating machine body, the other end of the support rod is inserted into the fixed seat, the lifting plate is installed inside the fixed seat, the sliding block is installed on the side wall of the lifting plate, a groove is formed in the bottom of the lifting plate, the support block a is installed in the groove, the spring is installed at the bottom of the support block a, the other end of the spring is installed on the support block B, and the support block B is installed at the bottom of the fixed seat;

above-mentioned application is through buffering the subassembly, cushions concentrated organism, prevents the vibrations that concentrated organism work produced, leads to empting, through the warning subassembly, is convenient for carry out timely maintenance to the user of service early warning to membrane enrichment facility, but will seriously block up after having the membrane to use a period, loses filterability, and life is short, therefore the market urgently needs to develop the organic membrane enrichment facility in the tealeaves deep-processing and helps people to solve current problem.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide an organic membrane enrichment facility in tealeaves deep-processing to solve the tealeaves that provides in the above-mentioned background art and at the in-process of deep-processing, use organic membrane enrichment facility to carry out the concentration often, filter through organic membrane, then draw and hold back liquid, but will seriously block up after organic membrane uses a period, lose filterability, problem that life is short.

In order to achieve the above purpose, the utility model provides a following technical scheme: the utility model provides an organic membrane enrichment facility in tealeaves deep-processing, includes organic membrane enrichment facility, organic membrane enrichment facility's inside is provided with organic filtration membrane, organic filtration membrane's inside is provided with the backwash pipe, the back flush shower nozzle is installed in the outside of backwash pipe, and back flush shower nozzle and backwash pipe threaded connection.

Preferably, sealed dish is installed to organic filtration membrane's top, and sealed dish and organic filtration membrane pass through sealing screw fixed connection, sealed dish and organic membrane enrichment facility pass through sealing screw fixed connection, the transfer case is installed to the top of sealed dish, and the transfer case passes through fastening screw fixed connection with sealed dish.

Preferably, a water inlet pipe is installed on one side of the transfer box and is connected with the transfer box in a welded mode, a penetrating port is formed in the outer side of the backwashing pipe, and the penetrating port and the backwashing pipe are arranged to be of an integrated structure.

Preferably, the support is installed to the top of sealed dish, and the support passes through fastening screw fixed connection with sealed dish, the motor is installed to the top of support.

Preferably, a speed reducer is installed below the motor, the speed reducer is fixedly connected with the motor through a coupling, and the speed reducer is fixedly connected with the backwashing pipe through a connecting shaft.

Preferably, a drain pipe is installed to the below of organic filtration membrane, and the drain pipe passes through sealing screw fixed connection with organic filtration membrane, the scum pipe is installed to the below of organic membrane enrichment facility, and scum pipe and organic membrane enrichment facility welded connection.

Preferably, the feed liquor pipe is installed to one side of organic membrane enrichment facility, and feed liquor pipe and organic membrane enrichment facility welded connection, the drain pipe is installed to the opposite side of organic membrane enrichment facility, and drain pipe and organic membrane enrichment facility welded connection.

Compared with the prior art, the beneficial effects of the utility model are that:

1. the utility model discloses a through the setting of backwash pipe and back flush head, tealeaves need organic filtration membrane to filter when dashing processing concentration, and the backwash pipe sets up the inside at organic filtration membrane, then at the outside installation backwash pipe of backwash pipe, and the backwash pipe has from top to bottom installed a plurality ofly, through to the inside high-pressure rivers of carrying of backwash pipe, then spray away through back flush head, by back flush to organic filtration membrane inside to outside, wash away the inside filterable impurity of organic filtration membrane, thereby make organic filtration membrane use reacquire the filterability through the back flush after a period, thereby improve organic filtration membrane's life.

2. The utility model discloses a through the setting of motor and reduction gear, order about the back flush pipe after the reduction of motor accessible reduction gear and rotate, when carrying high-pressure rivers to the recoil straw is inside, utilize motor and reduction gear to make the back flush shower nozzle can make the back flush pipe rotate equally to make the back flush shower nozzle can follow the back flush pipe rotatory, carry out omnidirectional back flush work to organic filtration membrane's inside, thereby improve the cleaning performance to organic filtration membrane.

3. The utility model discloses a through the setting of transfer case, the transfer case is connected with the backwash pipe to be in the relation of rotating the connection, the outside of backwash pipe has set up the mouth of wearing, rivers are pouring into the transfer case back, will carry to the inside of backwash pipe through wearing the mouth, thereby make the backwash pipe also can be to its inside transport rivers at rotatory in-process, thereby make things convenient for the rotation of backwash pipe and carry rivers work, improve the use convenience of backwash pipe.

Drawings

Fig. 1 is a schematic view of the internal structure of an organic membrane concentration device in tea deep processing of the present invention;

fig. 2 is an enlarged schematic view of the utility model at a;

fig. 3 is an enlarged schematic view of the point B in the drawing of the present invention.

In the figure: 1. an organic membrane concentration device; 2. an organic filtration membrane; 3. a liquid inlet pipe; 4. a liquid outlet pipe; 5. a liquid discharge pipe; 6. sealing the disc; 7. a backwash pipe; 8. a support; 9. a motor; 10. a speed reducer; 11. backwashing the spray head; 12. a transfer box; 13. a water inlet pipe; 14. perforating; 15. a slag discharge pipe.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments.

Referring to fig. 1-3, the present invention provides an embodiment: an organic membrane concentration device in tea deep processing comprises an organic membrane concentration device 1, wherein an organic filtering membrane 2 is arranged inside the organic membrane concentration device 1, a back washing pipe 7 is arranged inside the organic filtering membrane 2, a back washing nozzle 11 is installed on the outer side of the back washing pipe 7, and the back washing nozzle 11 is in threaded connection with the back washing pipe 7.

Further, sealed dish 6 is installed to organic filtration membrane 2's top, and sealed dish 6 passes through sealing screw fixed connection with organic filtration membrane 2, sealed dish 6 passes through sealing screw fixed connection with organic membrane enrichment facility 1, transfer case 12 is installed to sealed dish 6's top, and transfer case 12 passes through fastening screw fixed connection with sealed dish 6, the end cap is installed to organic filtration membrane 2's below, the end cap is connected fixedly with organic membrane enrichment facility 1, and the junction seals through sealed rubber ring.

Further, a water inlet pipe 13 is installed on one side of the transfer box 12, the water inlet pipe 13 is connected with the transfer box 12 in a welded mode, a penetrating port 14 is formed in the outer side of the backwashing pipe 7, the penetrating port 14 and the backwashing pipe 7 are arranged into an integral structure, the water inlet pipe 13 is connected with a water pump, and water flow enters the backwashing pipe 7 through the penetrating port 14.

Further, support 8 is installed to sealed top of dish 6, and support 8 and sealed dish 6 pass through fastening screw fixed connection, and motor 9 is installed to the top of support 8, and motor 9 passes through fastening screw fixed connection with support 8.

Further, a speed reducer 10 is installed below the motor 9, the speed reducer 10 is fixedly connected with the motor 9 through a coupler, the speed reducer 10 is fixedly connected with the backwashing pipe 7 through a connecting shaft, the motor 9 can drive the backwashing pipe 7 to rotate after being decelerated through the speed reducer 10, a rotating connection relation exists between the backwashing pipe 7 and the sealing disc 6, and the connection position is prevented from being provided with a sealing structure for sealing.

Further, fluid-discharge tube 5 is installed to organic filtration membrane 2's below, and fluid-discharge tube 5 passes through sealing screw fixed connection with organic filtration membrane 2, and scum pipe 15 is installed to organic membrane enrichment facility 1's below, and scum pipe 15 and organic membrane enrichment facility 1 welded connection, has installed the valve on the scum pipe 15, through the switch of valve control scum pipe 15.

Further, feed liquor pipe 3 is installed to one side of organic membrane enrichment facility 1, and feed liquor pipe 3 and 1 welded connection of organic membrane enrichment facility, and drain pipe 4 is installed to the opposite side of organic membrane enrichment facility 1, and drain pipe 4 and 1 welded connection of organic membrane enrichment facility, and feed liquor pipe 3 is located the position, and drain pipe 4 is located the high-order, and the concentrated liquid of holding back will be discharged through drain pipe 4.

The working principle is as follows: during the use, carry the tea juice of tealeaves to the inside of organic membrane enrichment facility 1 through feed liquor pipe 3, filter the tea juice through organic filtration membrane 2 inside organic membrane enrichment facility 1, permeate organic filtration membrane 2 with the hydrone and discharge from fluid-discharge tube 5, the trapped fluid still stays the inside of organic membrane enrichment facility 1, and slowly improve the height of liquid level, because of the remaining moisture of trapped fluid reduces, consequently, improve the concentration of tea juice, then concentrated tea juice discharges through drain pipe 4, when needing to wash organic filtration membrane 2, connect the water pump through inlet tube 13, high-pressure water passes through transfer case 12 and wearing port 14 and to the inside high-pressure rivers of back flush pipe 7, high-pressure rivers are sprayed away through back flush nozzle 11, carry out the washing work to organic filtration membrane 2 from inside to outside, back flush motor 9 is started simultaneously, motor 9 will drive back flush pipe 7 through reduction gear 10 after slowing down and rotate, thereby make back flush nozzle 11 also follow back flush pipe 7 and rotate, thereby carry out the washing work of all-round to organic filtration membrane 2, waste water and waste residue can discharge through fluid-discharge tube 5 and scum pipe 15.

It is obvious to a person skilled in the art that the invention is not restricted to details of the above-described exemplary embodiments, but that it can be implemented in other specific forms without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.

Claims

1. The utility model provides an organic membrane enrichment facility in tealeaves deep-processing, includes organic membrane enrichment facility (1), its characterized in that: the organic membrane concentrating device is characterized in that an organic filtering membrane (2) is arranged inside the organic membrane concentrating device (1), a back washing pipe (7) is arranged inside the organic filtering membrane (2), a back washing nozzle (11) is installed on the outer side of the back washing pipe (7), and the back washing nozzle (11) is in threaded connection with the back washing pipe (7).

2. The organic membrane concentrating device in the tea deep processing according to claim 1, wherein: sealed dish (6) is installed to the top of organic filtration membrane (2), and sealed dish (6) and organic filtration membrane (2) through sealing screw fixed connection, sealed dish (6) and organic membrane enrichment facility (1) are through sealing screw fixed connection, transfer case (12) are installed to the top of sealed dish (6), and transfer case (12) and sealed dish (6) are through fastening screw fixed connection.

3. The organic membrane concentration device in tea deep processing according to claim 2, characterized in that: a water inlet pipe (13) is installed on one side of the transfer box (12), the water inlet pipe (13) is connected with the transfer box (12) in a welded mode, a penetrating opening (14) is formed in the outer side of the backwashing pipe (7), and the penetrating opening (14) and the backwashing pipe (7) are arranged to be of an integrated structure.

4. The organic membrane concentration device in tea deep processing according to claim 2, characterized in that: support (8) are installed to the top of sealed dish (6), and support (8) pass through fastening screw fixed connection with sealed dish (6), motor (9) are installed to the top of support (8).

5. The organic membrane concentrating device in the tea deep processing according to claim 4, wherein: the motor is characterized in that a speed reducer (10) is installed below the motor (9), the speed reducer (10) is fixedly connected with the motor (9) through a coupler, and the speed reducer (10) is fixedly connected with the backwashing pipe (7) through a connecting shaft.

6. The organic membrane concentrating device in the tea deep processing according to claim 1, wherein: liquid discharge tube (5) are installed to the below of organic filtration membrane (2), and liquid discharge tube (5) pass through sealing screw fixed connection with organic filtration membrane (2), scum pipe (15) are installed to the below of organic membrane enrichment facility (1), and scum pipe (15) and organic membrane enrichment facility (1) welded connection.

7. The organic membrane concentration device in tea deep processing according to claim 1, characterized in that: feed liquor pipe (3) are installed to one side of organic membrane enrichment facility (1), and feed liquor pipe (3) and organic membrane enrichment facility (1) welded connection, drain pipe (4) are installed to the opposite side of organic membrane enrichment facility (1), and drain pipe (4) and organic membrane enrichment facility (1) welded connection.