CN202322370U - Generator for producing chlorine dioxide by using acidified sodium chlorite - Google Patents
Generator for producing chlorine dioxide by using acidified sodium chlorite Download PDFInfo
- Publication number
- CN202322370U CN202322370U CN2011204593243U CN201120459324U CN202322370U CN 202322370 U CN202322370 U CN 202322370U CN 2011204593243 U CN2011204593243 U CN 2011204593243U CN 201120459324 U CN201120459324 U CN 201120459324U CN 202322370 U CN202322370 U CN 202322370U
- Authority
- CN
- China
- Prior art keywords
- reaction chamber
- chlorine dioxide
- water bath
- bath box
- raffinate separator
- 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.)
- Expired - Lifetime
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Abstract
The utility model discloses a generator for producing chlorine dioxide by using acidified sodium chlorite. The generator comprises a feeding system, a reaction chamber, a thermostatic water bath box (6) and a residual liquid processing device, wherein the reaction chamber is arranged in the thermostatic water bath box (6); the feeding system comprises a raw material feeding inlet (1) and an air inlet (2), and the air inlet (2) is also provided with a buffer chamber (3) in a connecting manner; the reaction chamber is divided into a first reaction chamber (4) and a second reaction chamber (5); the thermostatic water bath box (6) is internally provided with a baffle plate and is divided into a left cabin and a right cabin by the baffle plate, and the first reaction chamber (4) and the second reaction chamber (5) are respectively positioned in the left cabin and the right cabin; and the first reaction chamber (4) and the second reaction chamber (5) are communicated through a connecting pipe, and the connecting pipe is positioned above the baffle plate. The generator for producing the chlorine dioxide by using the acidified sodium chlorite, disclosed by the utility model, has the advantages of being simple in structure and convenient in operation, and being high in safety as reaction liquid can be extracted from the reaction chamber timely when the generator stops working and the reaction can be stopped.
Description
Technical field
The utility model relates to a kind of chlorine dioxide generator, is specifically related to a kind of producer with producing chlorine dioxide by acidifying chlorous sodium.
Background technology
Dioxide peroxide is owing to its good bleaching, sterilization, sterilizing function and very strong oxidisability are widely used in various occasions.Simultaneously also because the strong oxidizing property and the unstable of dioxide peroxide, decompositions of blasting easily, unsuitable hig pressure storage transports with the strange land, therefore, to be advisable in the on-the-spot now-making-now-using of use.From the preparation method of dioxide peroxide, be that raw material is aided with souring agent and produces preparation with oxymuriate or Textone mostly.Souring agent generally adopts hydrochloric acid or these strong acid type liquid acid of sulfuric acid, and not only security requirement is high, and the transportation of equipment, raw material and maintenance cost are also very high, and the complex structure of existing installation.
The utility model content
The utility model provides a kind of producer with producing chlorine dioxide by acidifying chlorous sodium, has solved the baroque problem of existing installation.
For solving above-mentioned technical problem, the utility model adopts following technical scheme:
A kind of producer with producing chlorine dioxide by acidifying chlorous sodium comprises feeder system, reaction chamber, constant water bath box and residual liquid processing apparatus, and reaction chamber places constant water bath box; Feeder system comprises that raw material adds inlet and air, also is connected to the surge chamber of control air flow on the air; Reaction chamber is divided into first reaction chamber and second reaction chamber; Be provided with dividing plate in the constant water bath box, dividing plate is divided into left and right storehouse with constant water bath box, and first reaction chamber and second reaction chamber are placed in the left and right storehouse; First reaction chamber and second reaction chamber are communicated with through pipe connecting, and pipe connecting places the dividing plate top; Residual liquid processing apparatus comprises raffinate separator, raffinate separator tube and blow-off pipe, and the raffinate separator is communicated with second reaction chamber; The top of second reaction chamber and raffinate separator is provided with the thimerosal outlet; First reaction chamber bottom is provided with blow-off pipe; The raffinate separator tube is set on the raffinate separator.
Further technical scheme is that above-mentioned raffinate separator is provided with two highly different interfaces and is communicated with second reaction chamber.
Further technical scheme is that above-mentioned first reaction chamber is provided with the air aeration pipe.
Further technical scheme is, above-mentioned thimerosal outlet is gone up ejector is installed.
Compared with prior art, the beneficial effect of the utility model is:
(1) snubber of the utility model setting can make air at the uniform velocity flow in the reaction chamber;
(2) the utility model is divided into left and right storehouse with constant water bath box, controls the temperature of reaction of first reaction chamber and second reaction chamber respectively, makes it to constitute the two warm reactive systems of differential;
(3) on the raffinate separator of the utility model two interfaces are set; Reaction solution is extracted out with reactant gases when wherein going up interface and can prevent to react; Play the liquid flooding effect, lower interface can be accelerated circulating of second reaction chamber and raffinate separator internal reaction liquid, improves operational efficiency;
(4) the utility model is simple in structure, easy to operate, and the reaction fluid power is in time extracted stopped reaction out when out of service from reaction chamber, and is safe.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Among the figure, the 1-raw material adds inlet, 2-air, 3-surge chamber, 4-first reaction chamber, 5-second reaction chamber, 6-constant water bath box, 7-blow-off pipe, 8-raffinate separator tube, 9-raffinate separator, the outlet of 10-thimerosal, 11-ejector, 12-air aeration pipe.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is further specified, but the embodiment of the utility model is not limited thereto.
A kind of producer with producing chlorine dioxide by acidifying chlorous sodium as shown in Figure 1 comprises feeder system, reaction chamber, constant water bath box 6 and residual liquid processing apparatus, and reaction chamber places constant water bath box 6; Feeder system comprises that raw material adds inlet 1 and air 2, also is connected to the surge chamber 3 of control air flow on the air 2; Reaction chamber is divided into first reaction chamber 4 and second reaction chamber 5; Be provided with dividing plate in the constant water bath box 6, dividing plate is divided into left and right storehouse with constant water bath box 6, and first reaction chamber 4 and second reaction chamber 5 are placed in the left and right storehouse, respectively temperature control; First reaction chamber 4 and second reaction chamber 5 are communicated with through pipe connecting, and pipe connecting places the dividing plate top; Residual liquid processing apparatus comprises raffinate separator 9, raffinate separator tube 8 and blow-off pipe 7, and raffinate separator 9 is communicated with second reaction chamber 5, and raffinate separator 9 is provided with two highly different interfaces; The top of second reaction chamber 5 and raffinate separator 9 is provided with thimerosal outlet 10, in the thimerosal outlet 10 ejector 11 is installed; First reaction chamber, 4 bottoms are provided with blow-off pipe 7; Raffinate separator tube 8 is set on the raffinate separator 9; Also be provided with air aeration pipe 12 on first reaction chamber 4.
Claims (4)
1. producer with producing chlorine dioxide by acidifying chlorous sodium; Comprise feeder system, reaction chamber, constant water bath box (6) and residual liquid processing apparatus; Reaction chamber places constant water bath box (6); It is characterized in that: described feeder system comprises that raw material adds inlet (1) and air (2), also is connected to the surge chamber (3) of control air flow on the said air (2); Said reaction chamber is divided into first reaction chamber (4) and second reaction chamber (5); Described constant water bath box is provided with dividing plate in (6), and dividing plate is divided into left and right storehouse with constant water bath box (6), and first reaction chamber (4) and second reaction chamber (5) are placed in the left and right storehouse; Said first reaction chamber (4) and second reaction chamber (5) are communicated with through pipe connecting, and pipe connecting places the dividing plate top; Said residual liquid processing apparatus comprises raffinate separator (9), raffinate separator tube (8) and blow-off pipe (7), and raffinate separator (9) is communicated with second reaction chamber (5); The top of said second reaction chamber (5) and raffinate separator (9) is provided with thimerosal outlet (10); Said first reaction chamber (4) bottom is provided with blow-off pipe (7); Raffinate separator tube (8) is set on the said raffinate separator (9).
2. a kind of producer with producing chlorine dioxide by acidifying chlorous sodium according to claim 1 is characterized in that: said raffinate separator (9) is provided with two highly different interfaces and is communicated with second reaction chamber (5).
3. a kind of producer with producing chlorine dioxide by acidifying chlorous sodium according to claim 1 is characterized in that: said first reaction chamber (4) is provided with air aeration pipe (12).
4. a kind of producer with producing chlorine dioxide by acidifying chlorous sodium according to claim 1 is characterized in that: described thimerosal outlet (10) is gone up ejector (11) is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204593243U CN202322370U (en) | 2011-11-17 | 2011-11-17 | Generator for producing chlorine dioxide by using acidified sodium chlorite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204593243U CN202322370U (en) | 2011-11-17 | 2011-11-17 | Generator for producing chlorine dioxide by using acidified sodium chlorite |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202322370U true CN202322370U (en) | 2012-07-11 |
Family
ID=46434360
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204593243U Expired - Lifetime CN202322370U (en) | 2011-11-17 | 2011-11-17 | Generator for producing chlorine dioxide by using acidified sodium chlorite |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202322370U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106145045A (en) * | 2016-08-02 | 2016-11-23 | 四川拓璞环保科技有限公司 | A kind of chlorine dioxide generating device |
-
2011
- 2011-11-17 CN CN2011204593243U patent/CN202322370U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106145045A (en) * | 2016-08-02 | 2016-11-23 | 四川拓璞环保科技有限公司 | A kind of chlorine dioxide generating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20151028 Address after: Dujiangyan City, Sichuan province 611830 Chengdu Sichuan City Economic Development Zone Dujiangyan Road No. 609 weir Patentee after: Sichuan Qili Lvyuan Water Treatment Technology Co., Ltd. Address before: 611843 Qingcheng Industrial Zone, Dujiangyan, Sichuan, Chengdu Patentee before: Chengdu Qili Water Treatment Science & Technology Co., Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20120711 |
|
| CX01 | Expiry of patent term |