CN111620283A - Heavy oxygen water purification packaging process - Google Patents
Heavy oxygen water purification packaging process Download PDFInfo
- Publication number
- CN111620283A CN111620283A CN202010491772.5A CN202010491772A CN111620283A CN 111620283 A CN111620283 A CN 111620283A CN 202010491772 A CN202010491772 A CN 202010491772A CN 111620283 A CN111620283 A CN 111620283A
- Authority
- CN
- China
- Prior art keywords
- oxygen water
- heavy oxygen
- room
- machine
- packaging process
- Prior art date
- Legal status (The legal status 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 status listed.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67B—APPLYING CLOSURE MEMBERS TO BOTTLES JARS, OR SIMILAR CONTAINERS; OPENING CLOSED CONTAINERS
- B67B3/00—Closing bottles, jars or similar containers by applying caps
- B67B3/003—Pretreatment of caps, e.g. cleaning, steaming, heating or sterilizing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B21/00—Packaging or unpacking of bottles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67B—APPLYING CLOSURE MEMBERS TO BOTTLES JARS, OR SIMILAR CONTAINERS; OPENING CLOSED CONTAINERS
- B67B3/00—Closing bottles, jars or similar containers by applying caps
- B67B3/02—Closing bottles, jars or similar containers by applying caps by applying flanged caps, e.g. crown caps, and securing by deformation of flanges
- B67B3/10—Capping heads for securing caps
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
- B67C7/00—Concurrent cleaning, filling, and closing of bottles; Processes or devices for at least two of these operations
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/05—Conductivity or salinity
Abstract
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.
Description
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.
Claims (5)
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).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010491772.5A CN111620283A (en) | 2020-06-02 | 2020-06-02 | Heavy oxygen water purification packaging process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010491772.5A CN111620283A (en) | 2020-06-02 | 2020-06-02 | Heavy oxygen water purification packaging process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111620283A true CN111620283A (en) | 2020-09-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010491772.5A Pending CN111620283A (en) | 2020-06-02 | 2020-06-02 | Heavy oxygen water purification packaging process |
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| Country | Link |
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| CN (1) | CN111620283A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030141177A1 (en) * | 2002-01-30 | 2003-07-31 | Countz John W. | Process for re-purfying highly enriched [H2180] |
| CN1631768A (en) * | 2003-12-24 | 2005-06-29 | 上海化工研究院 | H218O production method and apparatus for rectifying 18O isotope enriched water |
| CN1923715A (en) * | 2005-09-01 | 2007-03-07 | 上海化工研究院 | Purifying method of removing bacteria and organic compound in heavy oxygen water |
| CN101619285A (en) * | 2009-07-15 | 2010-01-06 | 闫铭杰 | Production platform system of human body fluid and tissue cells |
| CN202538406U (en) * | 2012-05-07 | 2012-11-21 | 西安汉术化学工程股份有限公司 | Rectification device for enriching heavy-oxygen water |
| EP3329982A1 (en) * | 2016-12-02 | 2018-06-06 | HWP Production OÜ | Method and apparatus for producing heavy oxygen water |
| CN208711446U (en) * | 2018-03-30 | 2019-04-09 | 陆松 | Symmetrical expression electrolysis pure water prepares heavy water and heavy oxygen water installations simultaneously |
-
2020
- 2020-06-02 CN CN202010491772.5A patent/CN111620283A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030141177A1 (en) * | 2002-01-30 | 2003-07-31 | Countz John W. | Process for re-purfying highly enriched [H2180] |
| CN1631768A (en) * | 2003-12-24 | 2005-06-29 | 上海化工研究院 | H218O production method and apparatus for rectifying 18O isotope enriched water |
| CN1923715A (en) * | 2005-09-01 | 2007-03-07 | 上海化工研究院 | Purifying method of removing bacteria and organic compound in heavy oxygen water |
| CN101619285A (en) * | 2009-07-15 | 2010-01-06 | 闫铭杰 | Production platform system of human body fluid and tissue cells |
| CN202538406U (en) * | 2012-05-07 | 2012-11-21 | 西安汉术化学工程股份有限公司 | Rectification device for enriching heavy-oxygen water |
| EP3329982A1 (en) * | 2016-12-02 | 2018-06-06 | HWP Production OÜ | Method and apparatus for producing heavy oxygen water |
| CN208711446U (en) * | 2018-03-30 | 2019-04-09 | 陆松 | Symmetrical expression electrolysis pure water prepares heavy water and heavy oxygen water installations simultaneously |
Non-Patent Citations (1)
| Title |
|---|
| 滕文锋: "《检验仪器分析技术》", 31 March 2012, 人民军医出版社 * |
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Application publication date: 20200904 |