CN105126718A - Blending device and blending method of H2O2 - Google Patents
Blending device and blending method of H2O2 Download PDFInfo
- Publication number
- CN105126718A CN105126718A CN201510439530.0A CN201510439530A CN105126718A CN 105126718 A CN105126718 A CN 105126718A CN 201510439530 A CN201510439530 A CN 201510439530A CN 105126718 A CN105126718 A CN 105126718A
- Authority
- CN
- China
- Prior art keywords
- hydrogen peroxide
- valve
- pipeline
- pump
- stoste
- 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.)
- Granted
Links
Landscapes
- Accessories For Mixers (AREA)
- Measuring Volume Flow (AREA)
Abstract
The invention relates to a blending device and a blending method of H2O2, wherein the H2O2 blending device comprises a raw liquid pre-treatment pot, a H2O2 blending main pot, and a first pump arranged therebetween. A first pipeline connects the first pump to the H2O2 blending main pot. A first on/off valve is arranged on the first pipeline. A second pipeline connects the raw liquid pre-treatment pot to the first pump. A third pipeline, which is connected to the raw liquid pre-treatment pot, is arranged on the pipeline connected between the first on/off valve and the first pump. A second on/off valve is arranged on the third pipeline. A first exhaust hole is formed on the upper end of the raw liquid pre-treatment pot. According to the blending device and the blending method of H2O2, the H2O2 raw liquid pumped into the H2O2 blending main pot is firstly subjected to initial exhaust circulation, thereby effectively exhausting the gas generated due to instability of the H2O2 raw liquid and avoiding the influence on metering of the H2O2 raw liquid during blending process so as to prepare a H2O2 liquid in stable concentration.
Description
Technical field
The present invention relates to hydrogen peroxide configuring technical, particularly a kind of hydrogen peroxide deployment device and method.
Background technology
Can the sterilization of packaging material virus killing and space environment be the important step of sterile filling, by packaging material and the thorough sterilization of sterile filling space environment, reach commercial sterilization have very important significance to the product produced.Can the thimerosal that hydrogen peroxide is commonly used as a kind of sterile filling, obtain a kind of hydrogen peroxide of steady concentration in process of production, most important in whole disinfection process.The hydrogen peroxide liquid being conventionally used to sterile filling normally utilizes pump to throw hydrogen peroxide stoste into blend tank, then adds a certain amount of water and allocate, and the hydrogen peroxide concentration which mixes is inaccurate.
Summary of the invention
Based on this, be necessary the defect for prior art, a kind of hydrogen peroxide deployment device and method are provided, the hydrogen peroxide liquid of steady concentration can be configured.
Its technical scheme is as follows:
A kind of hydrogen peroxide deployment device, comprise stoste pretreatment tank, main tank allocated by hydrogen peroxide, and be arranged on stoste pretreatment tank and hydrogen peroxide and allocate the first pump between main tank, described first pump and hydrogen peroxide are allocated between main tank by the first pipeline connection, described first pipeline is provided with the first on-off valve, by the second pipeline connection between described stoste pretreatment tank and the first pump, described first on-off valve and the connecting pipeline of the first pump are provided with the 3rd pipeline be communicated with stoste pretreatment tank, described 3rd pipeline is provided with the second on-off valve, the upper end of described stoste pretreatment tank is provided with first row pore.
Its further technical scheme is as follows:
Described hydrogen peroxide deployment device also comprises the second pump, described hydrogen peroxide is allocated between main tank and the second pump by the 4th pipeline connection, by the 5th pipeline connection between described second pump and filling main frame, described 5th pipeline is provided with the 3rd on-off valve, described 3rd on-off valve and the connecting pipeline of the second pump are provided with the 6th pipeline allocated main tank with hydrogen peroxide and be communicated with, described 6th pipeline is provided with the 4th on-off valve, and the described upper end allocating main tank with hydrogen peroxide is provided with second row pore.
Described hydrogen peroxide deployment device also comprises the filler pipe allocated main tank with hydrogen peroxide and be communicated with, described first pipeline is communicated with described filler pipe, the connecting pipeline of described first on-off valve and filler pipe is provided with check valve, and this check valve is communicated with to filler pipe direction by the first pipeline.
Described first pump is measuring pump, and described filler pipe is provided with flowmeter.
Described second pipeline is provided with the first control valve, and described filler pipe is provided with the second control valve, and described first control valve, the second control valve are manual adjustments butterfly valve and/or pneumatic regulating butterfly valve.
Described filler pipe is also provided with the 5th on-off valve, described 5th on-off valve is arranged on main tank allocated by flowmeter one end away from hydrogen peroxide.
Described first on-off valve, the second on-off valve, the 3rd on-off valve, the 4th on-off valve and the 5th on-off valve are Pneumatic butterfly valve.
Described stoste pretreatment tank is communicated with hydrogen peroxide original liquid box by the 7th pipeline, and described 7th pipeline is provided with the 3rd pump.
A kind of hydrogen peroxide concocting method, comprises the steps:
First row pore is offered in stoste pretreatment tank upper end;
Hydrogen peroxide stoste in stoste pretreatment tank is carried out preliminary exhaust cycle, and gas is discharged by first row pore;
Allocate in main tank by the hydrogen peroxide stoste suction hydrogen peroxide after preliminary exhaust cycle, allocate in main tank by water suction hydrogen peroxide, hydrogen peroxide stoste mixes in specific proportions with water simultaneously.
Further, described hydrogen peroxide concocting method also comprises the steps:
Allocate main tank upper end at hydrogen peroxide and offer second row pore;
Mixed liquor hydrogen peroxide being allocated hydrogen peroxide stoste in main tank and water carries out exhaust cycle again, and gas is discharged by second row pore;
Obtain the hydrogen peroxide seasoning liquid of concentration stabilize.
Below the advantage of preceding solution or principle are described:
Because hydrogen peroxide stoste character has strong oxidizing property and unstability, extract in stoste process at pump and easily produce a large amount of gas, the accuracy of impact metering, thus affect the accuracy of final redeployed hydrogen peroxide concentration, above-mentioned hydrogen peroxide deployment device, during use, extract hydrogen peroxide stoste to stoste pretreatment tank, close the first on-off valve, open the second on-off valve, start the first pump, hydrogen peroxide stoste is at stoste pretreatment tank, 3rd pipeline, the passage Inner eycle that first pump and the second pipeline are formed, in cyclic process, gas is discharged by the first row pore of pretreatment tank upper end, after circulation certain hour, obtain metastable hydrogen peroxide stoste, then the second on-off valve is closed, open the first on-off valve, hydrogen peroxide stoste is drawn into hydrogen peroxide and allocates in main tank and allocate, the impact that effective elimination gas measures hydrogen peroxide stoste, thus the hydrogen peroxide liquid of steady concentration can be configured.
Above-mentioned hydrogen peroxide concocting method, the hydrogen peroxide stoste of being allocated by suction hydrogen peroxide in main tank first carries out preliminary exhaust cycle, the gas that effective discharge hydrogen peroxide stoste unstable characteristic produces, again the hydrogen peroxide stoste after exhaust is allocated main tank with water suction hydrogen peroxide to mix in specific proportions, avoid the metering of hydrogen peroxide stoste in gases affect allocation process, thus configure the hydrogen peroxide liquid of steady concentration.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the hydrogen peroxide deployment device described in the embodiment of the present invention.
Description of reference numerals:
10, stoste pretreatment tank, 11, first row pore, 12, first Level meter, 20, main tank allocated by hydrogen peroxide, 21, second row pore, 22, 3rd Level meter, 23, thermometer, 30, first pump, 40, second pump, 50, hydrogen peroxide original liquid box, 51, second Level meter, 60, 3rd pump, 100, first pipeline, 110, first on-off valve, 120, check valve, 200, second pipeline, 210, first control valve, 300, 3rd pipeline, 310, second on-off valve, 400, filler pipe, 410, flowmeter, 420, 5th on-off valve, 430, second control valve, 500, 4th pipeline, 600, 5th pipeline, 610, 3rd on-off valve, 700, 6th pipeline, 710, 4th on-off valve, 800, 7th pipeline, 900, first emptying passage, 910, first emptying valve, 1000, second emptying passage, 1010, second emptying valve.
Detailed description of the invention
As shown in Figure 1, a kind of hydrogen peroxide deployment device, comprise stoste pretreatment tank 10, main tank 20 allocated by hydrogen peroxide, and be arranged on stoste pretreatment tank 10 and hydrogen peroxide and allocate the first pump 30 between main tank 20, described first pump 30 and hydrogen peroxide are allocated between main tank 20 and are communicated with by the first pipeline 100, described first pipeline 100 is provided with the first on-off valve 110, described stoste pretreatment tank 10 is communicated with by the second pipeline 200 with between the first pump 30, described first on-off valve 110 and the connecting pipeline of the first pump 30 are provided with the 3rd pipeline 300 be communicated with stoste pretreatment tank 10, described 3rd pipeline 300 is provided with the second on-off valve 310, the upper end of described stoste pretreatment tank 10 is provided with first row pore 11.
Because hydrogen peroxide stoste character has strong oxidizing property and unstability, extract in stoste process at pump and easily produce a large amount of gas, the accuracy of impact metering, thus affect the accuracy of final redeployed hydrogen peroxide concentration, above-mentioned hydrogen peroxide deployment device, during use, extract hydrogen peroxide stoste to stoste pretreatment tank 10, close the first on-off valve 110, open the second on-off valve 310, start the first pump 30, hydrogen peroxide stoste is at stoste pretreatment tank 10, 3rd pipeline 300, the passage Inner eycle that first pump 30 and the second pipeline 200 are formed, in cyclic process, gas is discharged by the first row pore 11 of pretreatment tank upper end, after circulation certain hour, obtain metastable hydrogen peroxide stoste, then the second on-off valve 310 is closed, open the first on-off valve 110, hydrogen peroxide stoste is drawn into hydrogen peroxide and allocates in main tank 20 and allocate, the impact that effective elimination gas measures hydrogen peroxide stoste, thus the hydrogen peroxide liquid of steady concentration can be configured.Described in the present embodiment, the first pump 30 is measuring pump, the capacity that the hydrogen peroxide stoste in main tank 20 allocated by suction hydrogen peroxide can be measured simultaneously, be convenient to allotment, first pump 30 also can be common water pump, only for extracting hydrogen peroxide stoste, first pipeline 100 arranging a quantifier in addition, allocating the capacity of the hydrogen peroxide stoste in main tank 20 for measuring suction hydrogen peroxide.
As shown in Figure 1, hydrogen peroxide deployment device described in the present embodiment also comprises the filler pipe 400 allocated main tank 20 with hydrogen peroxide and be communicated with, described first pipeline 100 is communicated with described filler pipe 400, described first on-off valve 110 is provided with check valve 120 with the connecting pipeline of filler pipe 400, and this check valve 120 is communicated with to filler pipe 400 direction by the first pipeline 100.Hydrogen peroxide stoste in first pipeline 100 enters hydrogen peroxide again after first mixing with the water in filler pipe 400 and allocates main tank 20, the check valve 120 be communicated with to filler pipe 400 direction by the first pipeline 100 is set, water or hydrogen peroxide mixed liquor is avoided to flow backwards, impact allotment accuracy, according to demand, also filler pipe 400, first pipeline 100 can be allocated main tank 20 respectively with hydrogen peroxide to be communicated with, mix again after directly water and hydrogen peroxide stoste suction hydrogen peroxide being allocated main tank 20.Described filler pipe 400 is provided with flowmeter 410 and the 5th on-off valve 420, the capacity of the water in main tank 20 allocated by flowmeter 410 for being metered into hydrogen peroxide, described 5th on-off valve 420 is arranged on main tank 20 allocated by flowmeter 410 one end away from hydrogen peroxide, for controlling the break-make of water, 5th on-off valve 420 is arranged on main tank 20 allocated by flowmeter 410 one end away from hydrogen peroxide, can guarantee that flowing into hydrogen peroxide allocates water in main tank 20 by accurate-metering.Described first on-off valve 110, second on-off valve 310, the 3rd on-off valve 610, the 4th on-off valve 710 and the 5th on-off valve 420 are Pneumatic butterfly valve, adopt pneumatic control, convenient and swift.
Described second pipeline 200 is provided with the first control valve 210, described filler pipe 400 is provided with the second control valve 430, described first control valve 210, second control valve 430 is manual adjustments butterfly valve and/or pneumatic regulating butterfly valve, first control valve 210 enters into hydrogen peroxide stoste the size that main tank 20 allocated by hydrogen peroxide for regulating, second control valve 430 is for regulate water to enter the size that main tank 20 allocated by hydrogen peroxide, pneumatic adjustment and manual adjustments two kinds of modes can be adopted, flexible control feed liquor speed, guarantees the accuracy of allocating further.
As shown in Figure 1, described hydrogen peroxide deployment device also comprises the second pump 40, described hydrogen peroxide is allocated between main tank 20 with the second pump 40 and is communicated with by the 4th pipeline 500, described second pump 40 is communicated with by the 5th pipeline 600 with between filling main frame, described 5th pipeline 600 is provided with the 3rd on-off valve 610, described 3rd on-off valve 610 and the connecting pipeline of the second pump 40 are provided with the 6th pipeline 700 allocated main tank 20 with hydrogen peroxide and be communicated with, described 6th pipeline 700 is provided with the 4th on-off valve 710, and the described upper end allocating main tank 20 with hydrogen peroxide is provided with second row pore 21.Before the filling main frame of hydrogen peroxide mixed liquor suction, close the 3rd on-off valve 610, open the 4th on-off valve 710, start the second pump 40, hydrogen peroxide mixed liquor allocates main tank 20 at hydrogen peroxide, 6th pipeline 700, the passage Inner eycle that second pump 40 and the 4th pipeline 500 are formed, again be vented in cyclic process, gas is allocated main tank 20 upper end by hydrogen peroxide and is provided with second row pore 21 and discharges, after circulation certain hour, obtain the hydrogen peroxide liquid of concentration stabilize, after the concentration mixing hydrogen peroxide liquid is up to standard, close the 4th on-off valve 710, open the 3rd on-off valve 610, qualified hydrogen peroxide liquid is drawn in filling main frame, for carrying out thorough disinfection and sterilization to packaging material and sterile filling space environment.
As shown in Figure 1, described stoste pretreatment tank 10 is communicated with hydrogen peroxide original liquid box 50 by the 7th pipeline 800, and described 7th pipeline 800 is provided with the 3rd pump 60.3rd pump 60 starts, hydrogen peroxide in extraction hydrogen peroxide original liquid box 50 is to stoste pretreatment tank 10, when the first Level meter 12 in described stoste pretreatment tank 10 shows a high position, 3rd pump 60 stops, described 3rd pump 60 is pneumatic diaphragm pump, pneumatic diaphragm pump has function of measuring, stoste pretreatment tank 10 bottom is provided with the first emptying passage 900, described first emptying passage 900 is provided with first emptying valve 910, for the residual liquid in stoste pretreatment tank 10 is discharged, be convenient to cleaning, the second Level meter 51 is provided with in described hydrogen peroxide original liquid box 50, for detecting the capacity of liquid in hydrogen peroxide original liquid box 50, described hydrogen peroxide is allocated in main tank 20 and is provided with the 3rd Level meter 22 and thermometer 23, capacity and the temperature of liquid in main tank 20 is allocated for detecting hydrogen peroxide, and hydrogen peroxide is allocated main tank 20 bottom and is provided with the second emptying path 10 00, described second emptying path 10 00 is provided with second emptying valve 1010, discharge for residual liquid hydrogen peroxide allocated in main tank 20, be convenient to cleaning, described first emptying valve 910, second emptying valve 1010 is manual adjustments butterfly valve, convenient adjustment fluid speed.
With reference to Fig. 1, a kind of hydrogen peroxide concocting method, comprises the steps:
First row pore 11 is offered in stoste pretreatment tank 10 upper end;
Hydrogen peroxide stoste in stoste pretreatment tank 10 is carried out preliminary exhaust cycle, and gas is discharged by first row pore 11, allocate between main tank 20 at stoste pretreatment tank 10 and hydrogen peroxide and the first pump 30 is set, described first pump 30 and hydrogen peroxide are allocated between main tank 20 and are communicated with by the first pipeline 100, described first pipeline 100 arranges the first on-off valve 110, described stoste pretreatment tank 10 is communicated with by the second pipeline 200 with between the first pump 30, described first on-off valve 110 arranges with on the connecting pipeline of the first pump 30 the 3rd pipeline 300 be communicated with stoste pretreatment tank 10, described 3rd pipeline 300 arranges the second on-off valve 310, preliminary exhaust cycle passage is stoste pretreatment tank 10, 3rd pipeline 300, the passage formed between first pump 30 and the second pipeline 200, close the first on-off valve 110, open the second on-off valve 310, start the first pump 30, hydrogen peroxide stoste flows in preliminary exhaust cycle passage, realize exhaust,
Allocate in main tank 20 by the hydrogen peroxide stoste suction hydrogen peroxide after preliminary exhaust cycle, allocated in main tank 20 by water suction hydrogen peroxide, hydrogen peroxide stoste mixes in specific proportions with water simultaneously.Filler pipe 40 and hydrogen peroxide are allocated main tank 20 and are communicated with, described first pipeline 100 is communicated with described filler pipe 400, described first on-off valve 110 is provided with check valve 120 with the connecting pipeline of filler pipe 400, and this check valve 120 is communicated with to filler pipe 400 direction by the first pipeline 100.Hydrogen peroxide stoste in first pipeline 100 enters hydrogen peroxide again after first mixing with the water in filler pipe 400 and allocates main tank 20, also filler pipe 400, first pipeline 100 can be allocated main tank 20 respectively with hydrogen peroxide to be communicated with, mix again after directly water and hydrogen peroxide stoste suction hydrogen peroxide being allocated main tank 20, the check valve 120 be communicated with to filler pipe 400 direction by the first pipeline 100 is set, water or hydrogen peroxide mixed liquor is avoided to flow backwards, impact allotment accuracy.
Further, described hydrogen peroxide concocting method also comprises the steps:
Allocate main tank 20 upper end at hydrogen peroxide and offer second row pore 21;
Mixed liquor hydrogen peroxide being allocated hydrogen peroxide stoste in main tank 20 and water carries out exhaust cycle again, and gas is discharged by second row pore 21, allocate between main tank 20 and filling main frame at hydrogen peroxide and the second pump 40 is set, described hydrogen peroxide is allocated between main tank 20 with the second pump 40 and is communicated with by the 4th pipeline 500, described second pump 40 is communicated with by the 5th pipeline 600 with between filling main frame, described 5th pipeline 600 is provided with the 3rd on-off valve 610, described 3rd on-off valve 610 and the connecting pipeline of the second pump 40 are provided with the 6th pipeline 700 allocated main tank 20 with hydrogen peroxide and be communicated with, described 6th pipeline 700 is provided with the 4th on-off valve 710, exhaust cycle passage is that main tank 20 allocated by hydrogen peroxide again, 6th pipeline 700, the passage that second pump 40 and the 4th pipeline 500 are formed, close the 3rd on-off valve 610, open the 4th on-off valve 710, start the second pump 40, hydrogen peroxide mixed liquor flows in exhaust cycle passage again, realize again being vented,
Obtain the hydrogen peroxide seasoning liquid of concentration stabilize.
This hydrogen peroxide concocting method, by suction hydrogen peroxide, the hydrogen peroxide stoste of allocating in main tank 20 first carries out preliminary exhaust cycle, the gas that effective discharge hydrogen peroxide stoste unstable characteristic produces, again the hydrogen peroxide stoste after exhaust is allocated main tank 20 with water suction hydrogen peroxide to mix in specific proportions, avoid the metering of hydrogen peroxide stoste in gases affect allocation process, and before the filling main frame of suction, mixed liquor hydrogen peroxide being allocated hydrogen peroxide stoste in main tank 20 and water carries out exhaust cycle again, thus configure the hydrogen peroxide liquid of steady concentration, for sterilization and sterilization.
Each technical characteristic of the above embodiment can combine arbitrarily, for making description succinct, the all possible combination of each technical characteristic in above-described embodiment is not all described, but, as long as the combination of these technical characteristics does not exist contradiction, be all considered to be the scope that this description is recorded.
The above embodiment only have expressed several embodiment of the present invention, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to the scope of the claims of the present invention.It should be pointed out that for the person of ordinary skill of the art, without departing from the inventive concept of the premise, can also make some distortion and improvement, these all belong to protection scope of the present invention.Therefore, the protection domain of patent of the present invention should be as the criterion with claims.
Claims (10)
1. a hydrogen peroxide deployment device, it is characterized in that, comprise stoste pretreatment tank, main tank allocated by hydrogen peroxide, and be arranged on stoste pretreatment tank and hydrogen peroxide and allocate the first pump between main tank, described first pump and hydrogen peroxide are allocated between main tank by the first pipeline connection, described first pipeline is provided with the first on-off valve, by the second pipeline connection between described stoste pretreatment tank and the first pump, described first on-off valve and the connecting pipeline of the first pump are provided with the 3rd pipeline be communicated with stoste pretreatment tank, described 3rd pipeline is provided with the second on-off valve, the upper end of described stoste pretreatment tank is provided with first row pore.
2. hydrogen peroxide deployment device as claimed in claim 1, it is characterized in that, it also comprises the second pump, described hydrogen peroxide is allocated between main tank and the second pump by the 4th pipeline connection, by the 5th pipeline connection between described second pump and filling main frame, described 5th pipeline is provided with the 3rd on-off valve, described 3rd on-off valve and the connecting pipeline of the second pump are provided with the 6th pipeline allocated main tank with hydrogen peroxide and be communicated with, described 6th pipeline is provided with the 4th on-off valve, and the described upper end allocating main tank with hydrogen peroxide is provided with second row pore.
3. hydrogen peroxide deployment device as claimed in claim 2, it is characterized in that, it also comprises the filler pipe allocated main tank with hydrogen peroxide and be communicated with, described first pipeline is communicated with described filler pipe, the connecting pipeline of described first on-off valve and filler pipe is provided with check valve, and this check valve is communicated with to filler pipe direction by the first pipeline.
4. hydrogen peroxide deployment device as claimed in claim 3, it is characterized in that, described first pump is measuring pump, and described filler pipe is provided with flowmeter.
5. hydrogen peroxide deployment device as claimed in claim 4, it is characterized in that, described second pipeline is provided with the first control valve, and described filler pipe is provided with the second control valve, and described first control valve, the second control valve are manual adjustments butterfly valve and/or pneumatic regulating butterfly valve.
6. hydrogen peroxide deployment device as claimed in claim 5, it is characterized in that, described filler pipe is also provided with the 5th on-off valve, described 5th on-off valve is arranged on main tank allocated by flowmeter one end away from hydrogen peroxide.
7. hydrogen peroxide deployment device as claimed in claim 6, it is characterized in that, described first on-off valve, the second on-off valve, the 3rd on-off valve, the 4th on-off valve and the 5th on-off valve are Pneumatic butterfly valve.
8. the hydrogen peroxide deployment device as described in any one of claim 1 to 7, is characterized in that, described stoste pretreatment tank is communicated with hydrogen peroxide original liquid box by the 7th pipeline, and described 7th pipeline is provided with the 3rd pump.
9. a hydrogen peroxide concocting method, is characterized in that, comprises the steps:
First row pore is offered in stoste pretreatment tank upper end;
Hydrogen peroxide stoste in stoste pretreatment tank is carried out preliminary exhaust cycle, and gas is discharged by first row pore;
Allocate in main tank by the hydrogen peroxide stoste suction hydrogen peroxide after preliminary exhaust cycle, allocate in main tank by water suction hydrogen peroxide, hydrogen peroxide stoste mixes in specific proportions with water simultaneously.
10. hydrogen peroxide concocting method as claimed in claim 9, is characterized in that, also comprise the steps:
Allocate main tank upper end at hydrogen peroxide and offer second row pore;
Mixed liquor hydrogen peroxide being allocated hydrogen peroxide stoste in main tank and water carries out exhaust cycle again, and gas is discharged by second row pore;
Obtain the hydrogen peroxide seasoning liquid of concentration stabilize.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510439530.0A CN105126718B (en) | 2015-07-23 | 2015-07-23 | Hydrogen peroxide deployment device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510439530.0A CN105126718B (en) | 2015-07-23 | 2015-07-23 | Hydrogen peroxide deployment device and method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105126718A true CN105126718A (en) | 2015-12-09 |
| CN105126718B CN105126718B (en) | 2017-09-01 |
Family
ID=54712493
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510439530.0A Active CN105126718B (en) | 2015-07-23 | 2015-07-23 | Hydrogen peroxide deployment device and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105126718B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107930356A (en) * | 2017-11-16 | 2018-04-20 | 襄阳先天下环保设备有限公司 | A kind of recycling device of coloured industry flue gas desulfurization Sulphuric acid |
| CN110559896A (en) * | 2019-10-12 | 2019-12-13 | 广州达意隆包装机械股份有限公司 | Blending device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202682853U (en) * | 2012-05-24 | 2013-01-23 | 上海旭熠电子技术有限公司 | Chemical liquid debubbling device |
| CN103430116A (en) * | 2011-02-01 | 2013-12-04 | 比尔克特韦尔克有限公司 | Metering unit |
| JP2014087752A (en) * | 2012-10-30 | 2014-05-15 | Toray Eng Co Ltd | Microreactor system, method of producing compound using the same, and method of producing alkenyl phosphorus compound |
| CN104226187A (en) * | 2014-09-03 | 2014-12-24 | 江苏新美星包装机械股份有限公司 | Multi-liquid proportioned mixing device |
| CN204159307U (en) * | 2014-09-30 | 2015-02-18 | 华北电力大学（保定） | A kind of mixed gas preparation device |
| CN204911402U (en) * | 2015-07-23 | 2015-12-30 | 广州达意隆包装机械股份有限公司 | Hydrogen peroxide solution allotment device |
-
2015
- 2015-07-23 CN CN201510439530.0A patent/CN105126718B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103430116A (en) * | 2011-02-01 | 2013-12-04 | 比尔克特韦尔克有限公司 | Metering unit |
| CN202682853U (en) * | 2012-05-24 | 2013-01-23 | 上海旭熠电子技术有限公司 | Chemical liquid debubbling device |
| JP2014087752A (en) * | 2012-10-30 | 2014-05-15 | Toray Eng Co Ltd | Microreactor system, method of producing compound using the same, and method of producing alkenyl phosphorus compound |
| CN104226187A (en) * | 2014-09-03 | 2014-12-24 | 江苏新美星包装机械股份有限公司 | Multi-liquid proportioned mixing device |
| CN204159307U (en) * | 2014-09-30 | 2015-02-18 | 华北电力大学（保定） | A kind of mixed gas preparation device |
| CN204911402U (en) * | 2015-07-23 | 2015-12-30 | 广州达意隆包装机械股份有限公司 | Hydrogen peroxide solution allotment device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107930356A (en) * | 2017-11-16 | 2018-04-20 | 襄阳先天下环保设备有限公司 | A kind of recycling device of coloured industry flue gas desulfurization Sulphuric acid |
| CN110559896A (en) * | 2019-10-12 | 2019-12-13 | 广州达意隆包装机械股份有限公司 | Blending device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105126718B (en) | 2017-09-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US9970149B2 (en) | Detergent dosing controller | |
| CN105521527B (en) | Dialysate concentrate Preparation equipment | |
| CN201173881Y (en) | Transformer standard oil sample concoction device | |
| CN105126718A (en) | Blending device and blending method of H2O2 | |
| RU2013107707A (en) | MIXING DEVICE FOR PREPARING READY FOR USE OF MEDICAL WASHING SOLUTIONS, BEFORE ALL HEMODIALYSIS CONCENTRATES | |
| CN203043862U (en) | Oilfield flooding profile control agent mixing device | |
| CN203725342U (en) | Precise liquid flow control device | |
| RU2009136681A (en) | METHOD FOR MIXING LIQUID AT LEAST WITH ONE OTHER SUBSTANCE, MIXING DEGASATION AND DISPLACING THE MIXTURE | |
| CN102369054A (en) | Fluid mixing device, medical fluid testing device, and endoscope processing device | |
| CN205550207U (en) | Rare salt solution proportioning device | |
| CN204911402U (en) | Hydrogen peroxide solution allotment device | |
| CN104084067A (en) | Fully-automatic ozone water mixing device | |
| CN204911266U (en) | Normal atmospheric temperature is in liquid gaseous reference material down and takes place system | |
| CN204017775U (en) | A kind of liquid deployment device and there is the cleaning equipment of this device | |
| CN204073880U (en) | A kind of full-automatic ozone water admixing device | |
| CN204307587U (en) | A kind of chemical liquids mixing arrangement | |
| CN104062169B (en) | A kind of automatic on-line micro-example dilution mixing device and mixed method | |
| CN203400682U (en) | Multifunctional mixer | |
| CN207496973U (en) | A kind of racking machine | |
| TWI513504B (en) | Chemical liquid mixing apparatus and chemical liquid mixing method | |
| CN109464928A (en) | The box unpowered ratio supply device of static state | |
| CN209060922U (en) | A kind of weak brine automatic matching device | |
| CN203002230U (en) | Chemical liquid mixing device | |
| CN203777954U (en) | Ozone water generator | |
| CN204740337U (en) | Prepare device of online electric conductance counting rate meter standard calibration solution |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |