阅读说明：本技术 一种重氧水净化封装工艺 (Heavy oxygen water purification packaging process ) 是由 不公告发明人 于 2020-06-02 设计创作，主要内容包括：本发明公开了一种重氧水净化封装工艺,主要包括多个空间和设备,且自动化程度高,能够效率的进行重氧水的净化和封装工作。本发明的工艺可以非常洁净的对重氧水进行封装,效率高,自动化程度高,无污染问题。本发明改进了普通包装重氧水的系统设备,其结构简单、操作方便,可以做到定量、洁净的封装。(The invention discloses a heavy oxygen water purification and packaging process which mainly comprises a plurality of spaces and equipment, has high automation degree and can efficiently purify and package heavy oxygen water. The process can be used for packaging the oxygenated water very cleanly, and has the advantages of high efficiency, high automation degree and no pollution problem. The invention improves the common system equipment for packaging the heavy oxygen water, has simple structure and convenient operation, and can realize quantitative and clean packaging.)

1. A heavy oxygen water purification packaging process is characterized in that: the method comprises the following steps:

A. when the personnel enter into the work, the personnel firstly enter into the shoe changing room to change shoes, then enter into the changing room to change clothes, and enter into the working room from the buffer room after all the shoes are prepared;

B. after entering a working room, a worker firstly controls the indoor temperature and humidity through an air conditioner, a series of preparation works are carried out, a bottle cap is prepared, the bottle cap is cleaned by an ultrasonic cleaning machine and is placed into a dryer for drying;

C. after the preparation is finished, inputting the stock solution into a sub-boiling distiller, adjusting the flow of a flow meter, opening a metering pump, enabling heavy oxygen water to pass through a purification column, and observing the numerical value of a conductivity detector;

D. after the heavy oxygen water is filled, putting the dried bottle cap into a capping machine for capping;

E. finished products after the cover pressing enter a box filling machine through a conveying belt, the box filling machine can automatically fill the finished products into boxes according to certain arrangement and quantity, and finally the finished products are conveyed into a transmission window.

2. The heavy oxygen water purification packaging process according to claim 1, wherein: in the step A, a primary changing room (2) is arranged at one side of the shoe changing room (1), and a secondary changing room (3) is arranged at one side of the primary changing room (2); one side of the secondary dressing room (3) is provided with a buffer room (4), one side of the buffer room (4) is provided with a working area (5), and one side of the working area (5) is provided with a transfer window (6).

3. The heavy oxygen water purification packaging process according to claim 1, wherein: step B, the air conditioner (7) is arranged in a working area (5), a transfer window (6), an ultrasonic cleaning machine (8), a dryer (9) and an inlet (10) are arranged in the working area (5), the transfer window (6) is connected with a box filling machine (12) through a conveyor belt (11), the box filling machine (12) is connected with a capping machine (13), the capping machine (13) is connected with a workbench (14), and a purifying device (15) and a quantitative racking machine (16) are arranged on the workbench (14).

4. The heavy oxygen water purification packaging process according to claim 3, wherein: the conveying belt (11) is used for conveying a non-gland product (17), the conveying belt (11) is arranged below the capping machine (13), and a finished product (18) is arranged below the capping machine (13).

5. The heavy oxygen water purification packaging process according to claim 1, wherein: step C in the boiling distiller of inferior (19) upper end set up stoste entry (20), purification post (21) is passed through the pipe connection to boiling distiller of inferior (19) lower extreme, set up measuring pump (22) and flow valve (23) on the pipeline, be equipped with cock board (24) on purification post (21), splendid attire resin (25) in purification post (21), conductivity detector (26) is connected to purification post (21) lower extreme, motor (27) are connected in measuring pump (22), flowmeter (28) is connected in flow valve (23).

Technical Field

The invention relates to the technical field of purification, in particular to a heavy oxygen water purification packaging process.

Background

At present, heavy oxygen water is mainly prepared by oxidation-reduction reaction under the action of a metal catalyst. The conductivity of the heavy oxygen water on the market is generally less than 3.0%, and the conductivity of the heavy oxygen water purified by the process through a sub-boiling distiller and a purification column is less than 0.88%.

The net content difference of the common packaged heavy oxygen water is generally between 5% and 10%, and the balance is difficult to achieve. Therefore, equivalent net content packaging can be realized through a quantitative subpackaging instrument, and the difference is controlled within 1 percent.

Most heavy oxygen water packing spaces in the market are difficult to achieve certain cleanliness, and partial cleaning problems of heavy oxygen water are caused. And in the packaging of the heavy oxygen water, the cleaning of the bottle cap does not reach the standard. The full-automatic purification and encapsulation of the heavy oxygen water are difficult to achieve, and the partial encapsulation and purification are carried out by manpower, so that partial pollution is caused.

Disclosure of Invention

The invention aims to provide a heavy oxygen water purification packaging process to solve the problems in the background technology.

In order to achieve the purpose, the invention provides the following technical scheme: a heavy oxygen water purification packaging process comprises the following steps:

A. when the personnel enter into the work, the personnel firstly enter into the shoe changing room to change shoes, then enter into the changing room to change clothes, and enter into the working room from the buffer room after all the shoes are prepared;

B. after entering a working room, a worker firstly controls the indoor temperature and humidity through an air conditioner, a series of preparation works are carried out, a bottle cap is prepared, the bottle cap is cleaned by an ultrasonic cleaning machine and is placed into a dryer for drying;

C. after the preparation is finished, inputting the stock solution into a sub-boiling distiller, adjusting the flow of a flow meter, opening a metering pump, enabling heavy oxygen water to pass through a purification column, and observing the numerical value of a conductivity detector;

D. after the heavy oxygen water is filled, putting the dried bottle cap into a capping machine for capping;

E. finished products after the cover pressing enter a box filling machine through a conveying belt, the box filling machine can automatically fill the finished products into boxes according to certain arrangement and quantity, and finally the finished products are conveyed into a transmission window.

Preferably, a primary changing room is arranged at one side of the shoe changing room in the step A, and a secondary changing room is arranged at one side of the primary changing room; one side of the secondary dressing room is provided with a buffer room, one side of the buffer room is provided with a working area, and one side of the working area is provided with a transfer window.

Preferably, the air conditioner in the step B is arranged in a working area, a transfer window, an ultrasonic cleaner, a dryer and an inlet are arranged in the working area, the transfer window is connected with a box filling machine through a conveyor belt, the box filling machine is connected with a capping machine, the capping machine is connected with a working table, and a purifying device and a quantitative racking machine are arranged on the working table.

Preferably, one side of the conveying belt conveys the non-capping products, the conveying belt is arranged below the capping machine, and finished products are arranged below the capping machine.

Preferably, step C middle boiling distiller upper end sets up the stoste entry, the purification post is passed through the pipe connection to boiling distiller lower extreme, set up measuring pump and flow valve on the pipeline, be equipped with the cock board on the purification post, splendid attire resin in the purification post, the conductivity detector is connected to the purification post lower extreme, the motor is connected to the measuring pump, flow valve connects the flowmeter.

Compared with the prior art, the invention has the beneficial effects that: compared with the purification process on the market, the heavy oxygen water purified by the technology has very low conductivity. The normal production of heavy oxygen water through the purification column reduces the conductivity, which reduces the conductivity, but the resin loss degree is high, the resin cost is high, and the cost is high, so we use the sub-boiling distiller to reduce the conductivity before passing through the purification column, which can prolong the service time of the resin. The national standard requires that the conductivity range G is less than 3%, and the technology can reach G = 0.88%.

Drawings

FIG. 1 is a schematic view of the present invention in space;

FIG. 2 is a schematic view of a workshop arrangement according to the present invention;

FIG. 3 is a schematic view of the capping process of the present invention;

FIG. 4 is a schematic view of the purification apparatus and the quantitative dispensing process of the present invention.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

Referring to fig. 1-4, the present invention provides a technical solution: a heavy oxygen water purification packaging process comprises the following steps:

A. when the personnel enter into the work, the personnel firstly enter into the shoe changing room to change shoes, then enter into the changing room to change clothes, and enter into the working room from the buffer room after all the shoes are prepared;

B. after entering a working room, a worker firstly controls the indoor temperature and humidity through an air conditioner, a series of preparation works are carried out, a bottle cap is prepared, the bottle cap is cleaned by an ultrasonic cleaning machine and is placed into a dryer for drying;

C. after the preparation is finished, inputting the stock solution into a sub-boiling distiller, adjusting the flow of a flow meter, opening a metering pump, enabling heavy oxygen water to pass through a purification column, and observing the numerical value of a conductivity detector;

D. after the heavy oxygen water is filled, putting the dried bottle cap into a capping machine for capping;

E. finished products after the cover pressing enter a box filling machine through a conveying belt, the box filling machine can automatically fill the finished products into boxes according to certain arrangement and quantity, and finally the finished products are conveyed into a transmission window.

In the invention, in the step A, a primary changing room 2 is arranged at one side of a shoe changing room 1, and a secondary changing room 3 is arranged at one side of the primary changing room 2; a buffer room 4 is arranged on one side of the secondary dressing room 3, a working area 5 is arranged on one side of the buffer room 4, and a transfer window 6 is arranged on one side of the working area 5.

In the invention, the air conditioner 7 in the step B is arranged in a working area 5, a transfer window 6, an ultrasonic cleaning machine 8, a dryer 9 and an inlet 10 are arranged in the working area 5, the transfer window 6 is connected with a box filling machine 12 through a conveyor belt 11, the box filling machine 12 is connected with a capping machine 13, the capping machine 13 is connected with a workbench 14, and the workbench 14 is provided with a purifying device 15 and a quantitative racking machine 16; one side of the conveyor belt 11 conveys the uncapped products 17, the conveyor belt 11 is arranged below the capping machine 13, and finished products 18 are arranged below the capping machine 13.

In the invention, in the step C, the upper end of a sub-boiling distiller 19 is provided with a stock solution inlet 20, the lower end of the sub-boiling distiller 19 is connected with a purification column 21 through a pipeline, the pipeline is provided with a metering pump 22 and a flow valve 23, the purification column 21 is provided with a plug plate 24, the purification column 21 is filled with resin 25, the lower end of the purification column 21 is connected with a conductivity detector 26, the metering pump 22 is connected with a motor 27, and the flow valve 23 is connected with a flow meter 28. The raw liquid is firstly subjected to conductivity reduction through a sub-boiling distiller, then is subjected to quantitative treatment through a metering pump and a flow control valve, and finally is subjected to conductivity reduction again through a purification column containing resin; meanwhile, a conductivity detector is arranged at the lower outlet, so that the conductivity of the heavy oxygen water can be displayed, and an alarm can be given once the heavy oxygen water exceeds the standard.

In conclusion, compared with the purification process on the market, the heavy oxygen water purified by the technology has very low conductivity. The normal production of heavy oxygen water through the purification column reduces the conductivity, which reduces the conductivity, but the resin loss degree is high, the resin cost is high, and the cost is high, so we use the sub-boiling distiller to reduce the conductivity before passing through the purification column, which can prolong the service time of the resin. The national standard requires that the conductivity range G is less than 3%, and the technology can reach G = 0.88%.

Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.