CN106145044A - A kind of chlorine dioxide generator - Google Patents
A kind of chlorine dioxide generator Download PDFInfo
- Publication number
- CN106145044A CN106145044A CN201510190235.6A CN201510190235A CN106145044A CN 106145044 A CN106145044 A CN 106145044A CN 201510190235 A CN201510190235 A CN 201510190235A CN 106145044 A CN106145044 A CN 106145044A
- Authority
- CN
- China
- Prior art keywords
- chlorine dioxide
- multistage reactor
- water tank
- cooling water
- air compressor
- 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.)
- Pending
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses a kind of chlorine dioxide generator, this equipment includes multistage reactor, cooling water tank, air compressor and temperature measurement instrument, described temperature measurement instrument is located in multistage reactor, described multistage reactor be respectively provided on two sides with material inlet, chlorine dioxide outlet it is additionally provided with on described multistage reactor, described air compressor is located at below cooling water tank, and described cooling water tank is connected with outlet pipe by water inlet pipe with multistage reactor.The invention has the beneficial effects as follows: by multistage reactor by high-concentration sulfuric acid and raw material reaction, reaction quickly cools down chlorine dioxide method of purification by cooling water tank and air compressor simultaneously, extract high concentration chlorine dioxide with high purity, for disinfection of tap water, sewage disposal needs the occasion of Chlorine Dioxide Oxidation agent, reduces low concentration and reacts insufficient negative interaction to water source.
Description
Technical field
The present invention relates to a kind of chlorine dioxide production equipment, specifically a kind of chlorine dioxide generator, belong to chlorine dioxide raw
Produce apparatus field.
Background technology
Existing chlorine dioxide generator uses low concentration raw material as reaction raw materials, causes conversion ratio low, and low-concentration sulfuric acid
Reaction will not produce heat, purifies difficulty big.
Summary of the invention
For drawbacks described above present in prior art, the invention provides one and can regulate temperature, and feed stock conversion is high,
The chlorine dioxide generator that after conversion, purity is high.
The present invention is achieved by the following technical solution:
A kind of chlorine dioxide generator, it is characterised in that this equipment include multistage reactor, cooling water tank, air compressor and
Temperature measurement instrument, described temperature measurement instrument is located in multistage reactor, described multistage reactor be respectively provided on two sides with material inlet,
Being additionally provided with chlorine dioxide outlet on described multistage reactor, described air compressor is located at below cooling water tank, described cooling water tank
It is connected with outlet pipe by water inlet pipe with multistage reactor.
Concrete, in the present embodiment, described raw material is high-concentration sulfuric acid, hydrogen peroxide and potassium chlorate.
The invention has the beneficial effects as follows: by multistage reactor, supercooled water is led in high-concentration sulfuric acid and raw material reaction, reaction simultaneously
Case and air compressor quickly cool down chlorine dioxide method of purification, extract high concentration chlorine dioxide with high purity, for disinfection of tap water,
Sewage disposal needs the occasion of Chlorine Dioxide Oxidation agent, reduces low concentration and reacts insufficient negative interaction to water source.
Accompanying drawing explanation
Fig. 1 is the structural representation in the present invention；
In figure, 1-multistage reactor, 2-cooling water tank, 3-air compressor, 4-temperature measurement instrument, 5-material inlet,
6-chlorine dioxide exports, 7-water inlet pipe, 8-outlet pipe.
Detailed description of the invention
Make present disclosure more clear understandable, below in conjunction with Figure of description, present disclosure is described further.
Certainly the invention is not limited in this specific embodiment, the general replacement known to those skilled in the art is also covered by this
In bright protection domain.Secondly, the present invention utilizes schematic diagram to carry out detailed statement, when describing present example in detail, in order to
Being easy to explanation, schematic diagram, should be in this, as the restriction to type of the present invention not according to general ratio partial enlargement.
It should be noted that in following embodiment, utilize the structural representation of Fig. 1 to occur by one chlorine dioxide of the present invention
Device has carried out detailed statement.When describing embodiments of the present invention in detail, for convenience of description, each schematic diagram not according to typically than
Partial enlargement is drawn and carried out to example and omission processes, and therefore, should avoid in this, as limitation of the invention.
As it is shown in figure 1, the invention provides a kind of chlorine dioxide generator, this equipment include multistage reactor 1, cooling water tank 2,
Air compressor 3 and temperature measurement instrument 4, temperature measurement instrument 4 is located in multistage reactor 1, and the both sides of multistage reactor 1 are divided
Not being provided with material inlet 5, multistage reactor 1 is additionally provided with chlorine dioxide outlet 6, air compressor 3 is located at cooling water tank 2 times
Side, cooling water tank 2 is connected with outlet pipe 8 by water inlet pipe 7 with multistage reactor 1.
Concrete, in the present embodiment, raw material is high-concentration sulfuric acid, hydrogen peroxide and potassium chlorate.
The invention has the beneficial effects as follows: by multistage reactor, supercooled water is led in high-concentration sulfuric acid and raw material reaction, reaction simultaneously
Case and air compressor quickly cool down chlorine dioxide method of purification, extract high concentration chlorine dioxide with high purity, for disinfection of tap water,
Sewage disposal needs the occasion of Chlorine Dioxide Oxidation agent, reduces low concentration and reacts insufficient negative interaction to water source.
Claims (2)
1. a chlorine dioxide generator, it is characterised in that this equipment includes multistage reactor, cooling water tank, air compressor
With temperature measurement instrument, described temperature measurement instrument is located in multistage reactor, and the raw material that is respectively provided on two sides with of described multistage reactor enters
Mouthful, described multistage reactor is additionally provided with chlorine dioxide outlet, described air compressor is located at below cooling water tank, described cooling
Water tank is connected with outlet pipe by water inlet pipe with multistage reactor.
2. chlorine dioxide generator as claimed in claim 1, it is characterised in that described raw material is high-concentration sulfuric acid, hydrogen peroxide
And potassium chlorate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510190235.6A CN106145044A (en) | 2015-04-16 | 2015-04-16 | A kind of chlorine dioxide generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510190235.6A CN106145044A (en) | 2015-04-16 | 2015-04-16 | A kind of chlorine dioxide generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106145044A true CN106145044A (en) | 2016-11-23 |
Family
ID=58058413
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510190235.6A Pending CN106145044A (en) | 2015-04-16 | 2015-04-16 | A kind of chlorine dioxide generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106145044A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1347841A (en) * | 2000-11-13 | 2002-05-08 | 山东大学 | Large high-purity chlorine dioxide generator and its production process |
| CN101650134A (en) * | 2009-08-10 | 2010-02-17 | 江苏华机环保设备有限责任公司 | Flat plate type indirect condenser for chlorine dioxide preparation system |
| CN201737692U (en) * | 2010-05-28 | 2011-02-09 | 雷宁 | Dual-tank multi-stage chlorine dioxide generator |
| CN102275878A (en) * | 2010-06-11 | 2011-12-14 | 广西博世科环保科技股份有限公司 | Low-acidity energy-saving production process for high-purity chlorine dioxide |
| CN102502507A (en) * | 2011-11-04 | 2012-06-20 | 成都齐力水处理科技有限公司 | Preparation device and technology for chlorine dioxide |
| CN203486897U (en) * | 2013-09-30 | 2014-03-19 | 青岛金海晟环保设备有限公司 | Chlorine dioxide generator with quenching water tank |
-
2015
- 2015-04-16 CN CN201510190235.6A patent/CN106145044A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1347841A (en) * | 2000-11-13 | 2002-05-08 | 山东大学 | Large high-purity chlorine dioxide generator and its production process |
| CN101650134A (en) * | 2009-08-10 | 2010-02-17 | 江苏华机环保设备有限责任公司 | Flat plate type indirect condenser for chlorine dioxide preparation system |
| CN201737692U (en) * | 2010-05-28 | 2011-02-09 | 雷宁 | Dual-tank multi-stage chlorine dioxide generator |
| CN102275878A (en) * | 2010-06-11 | 2011-12-14 | 广西博世科环保科技股份有限公司 | Low-acidity energy-saving production process for high-purity chlorine dioxide |
| CN102502507A (en) * | 2011-11-04 | 2012-06-20 | 成都齐力水处理科技有限公司 | Preparation device and technology for chlorine dioxide |
| CN203486897U (en) * | 2013-09-30 | 2014-03-19 | 青岛金海晟环保设备有限公司 | Chlorine dioxide generator with quenching water tank |
Non-Patent Citations (2)
| Title |
|---|
| 唐珲军等: "二氧化氯制备技术及装备应用介绍", 《设备自动化》 * |
| 美国杜邦公司: "二氧化氯制备、使用和安全性评述", 《2011 二氧化氯与水处理技术研讨会论文集》 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104445573A (en) | Novel supercritical water oxidation comprehensive treatment system and method | |
| CN111330412B (en) | System and process for absorbing and purifying byproduct hydrogen chloride gas in chlorination section into acid | |
| CN103980246A (en) | Production method for preparing propylene (ethylene) carbonate from carbon dioxide and propylene oxide (ethylene oxide) through tubular reaction | |
| CN204251405U (en) | A kind of Novel supercritical Water oxidize total system | |
| CN104032128A (en) | Method for producing electrolytic nickel by leaching and purifying manganese-containing nickel hydroxide | |
| CN203959838U (en) | A kind of reaction unit of removing chlorine impurity in boron trichloride | |
| CN103910342A (en) | Nitrogen purification device | |
| CN106145044A (en) | A kind of chlorine dioxide generator | |
| CN107758964B (en) | System for treating waste alkali liquid and treatment method thereof | |
| CN103372362B (en) | Method and apparatus for purifying mixed gas | |
| CN205740560U (en) | Hypergravity ammonia nitrogen waste water processing system | |
| CN203448097U (en) | Nitration reaction kettle | |
| CN201567228U (en) | Ammonia decomposition pressure swing adsorption hydrogen production tail gas recovery device | |
| CN102745793A (en) | Method for removing free chlorine from solution after cobalt electrolysis | |
| CN101891153A (en) | Chlorine dioxide compound disinfectant generator and use method thereof | |
| CN112295390A (en) | Industrial tail gas treatment method and system | |
| CN202139042U (en) | Chemical industry byproduct hydrogen deoxygenization system | |
| CN203187406U (en) | Energy-saving nitric acid purifying device | |
| CN202226656U (en) | Deoxidization device for hydrogen | |
| JP2007106656A (en) | Hydrogen production apparatus and hydrogen production method | |
| CN2892837Y (en) | High-concentration industrial waste water processing system | |
| CN104477911A (en) | Method and device for simplifying thermo-chemical ZnSI cyclic decomposition of carbon dioxide and water | |
| CN204607669U (en) | A kind of sewage disposal Ozone recycling system | |
| CN204672116U (en) | A kind of SO 3cooler acid mist treatment device | |
| CN210085207U (en) | Sewage treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20161123 |
|
| WD01 | Invention patent application deemed withdrawn after publication |