CN205222685U - System takes place for chlorine dioxide - Google Patents
System takes place for chlorine dioxide Download PDFInfo
- Publication number
- CN205222685U CN205222685U CN201520966996.1U CN201520966996U CN205222685U CN 205222685 U CN205222685 U CN 205222685U CN 201520966996 U CN201520966996 U CN 201520966996U CN 205222685 U CN205222685 U CN 205222685U
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- CN
- China
- Prior art keywords
- hydrochloric acid
- sodium chlorate
- import
- pipe
- chlorine dioxide
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- 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.)
- Withdrawn - After Issue
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Abstract
System takes place for chlorine dioxide, including the sodium chlorate batch meter, the hydrochloric acid batch meter, reation kettle and microcomputer control ware, the hydrochloric acid liquid outlet passes through the hydrochloric acid drain pipe and connects mixed import, be provided with the measuring pump on the hydrochloric acid drain pipe, the sodium chlorate liquid outlet passes through the sodium chlorate drain pipe and connects mixed import, be provided with the measuring pump on the sodium chlorate drain pipe, it is equipped with the aeration intake pipe in addition to mix the import, the import of entrance pressure power water piping connection pressure water, advance the flow pipe and establish a branch connection areator in addition, advance the flow pipe and establish the 2nd branch connection the 2nd areator in addition, an areator sets up chlorine dioxide pipe connection chlorine dioxide discharge port, the 2nd areator sets up the vacuum tube way and connects the evacuation mouth. Chlorine dioxide reaction efficiency is high, the full automation operation.
Description
Technical field
The utility model relates to field of environment protection equipment, particularly relates to chlorine dioxide generator generation systems.
Background technology
Chlorine dioxide generator is a kind of simple to operate, medium and small dioxide peroxide multi-stage generator of high conversion, high purity, multi-usage, environmental-protecting chemical method.Be made up of by acidproof conduit and water-jetting type vacuum pump set tank reactor.What tank reactor adopted is two-stage or staged reactor, and be provided with air-distributor in main reaction still, secondary reacting kettle is provided with equilibration tube, and make reaction more thorough, reacted raffinate can qualified discharge.The dioxide peroxide generated obtains the aqueous solution, also can obtain stabilized chlorine chlorine solution.
Disinfection by chlorine dioxide equipment meets the relevant water hygiene of country and sewage drainage standard.
Disinfection by chlorine dioxide equipment performance is reliable, has the matured product of external or domestic modern technique.Dioxide peroxide in five minutes in the tap water of airport various have determine bacterium average kill ratio 95%, and do not produce trichloromethane (carcinogenic substance), chlorophenol etc., after Chlorine Dioxide Oxidation sterilization, meet relevant health and emission standard.
The chlorine dioxide generator luminous efficiency of prior art is not high, and at the bottom of level of automation, haves much room for improvement.
Summary of the invention
The utility model, for the deficiencies in the prior art, provides a kind of dioxide peroxide luminous efficiency high, the chlorine dioxide generating system of whole-course automation operation.
For realizing the utility model object, provide following technical scheme: chlorine dioxide generating system, it is characterized in that comprising sodium chlorate batch meter, hydrochloric acid batch meter, reactor and microcomputer controller, described sodium chlorate batch meter comprises the whipping appts in casing, the sodium chlorate import on casing top, the pressure water import of wall box, the sodium chlorate drain of the nearly bottom of casing, sodium chlorate liquid outlet, be provided with fluid level controller in sodium chlorate batch meter casing, described reactor comprises tank body, electric heater is provided with in tank body, tank base is provided with mixing import, and the nearly top of tank body is provided with dioxide peroxide discharge outlet, and described hydrochloric acid batch meter comprises hydrochloric acid drain, the hydrochloric acid liquid outlet of top hydrochloric acid import, vacuum orifice, nearly bottom, hydrochloric acid liquid outlet connects mixing import by hydrochloric acid drain pipe, hydrochloric acid drain pipe is provided with volume pump, sodium chlorate liquid outlet connects mixing import by sodium chlorate drain pipe, sodium chlorate drain pipe is provided with volume pump, mixing import is separately provided with aeration inlet pipe, enter pressure water pipe Bonding pressure water inlet, entering pressure water pipe separately establishes the first arm to connect the first gas-water mixer, entering pressure water pipe separately establishes the second arm to connect the second gas-water mixer, first gas-water mixer arranges dioxide peroxide pipeline and connects dioxide peroxide discharge outlet, second gas-water mixer arranges vacuum lead and connects vacuum orifice.
As preferably, described in enter on pressure water pipe to arrange tensimeter, described tensimeter, fluid level controller, volume pump, electric heater are all electrically connected microcomputer controller.
The utility model beneficial effect: the utility model, by the optimization of system and improvement, substantially increase the luminous efficiency of dioxide peroxide, and level of automation is high, simple to operation.
Accompanying drawing explanation
Fig. 1 is system schematic of the present utility model.
Embodiment
Embodiment 1: chlorine dioxide generating system, comprise sodium chlorate batch meter 1, hydrochloric acid batch meter 2, reactor 3 and microcomputer controller 4, described sodium chlorate batch meter 1 comprises the whipping appts 1.1 in casing, the sodium chlorate import 1.2 on casing top, the pressure water import 1.3 of wall box, the sodium chlorate drain 1.4 of the nearly bottom of casing, sodium chlorate liquid outlet 1.5, be provided with fluid level controller 1.6 in sodium chlorate batch meter 1 casing, described reactor 3 comprises tank body, electric heater 3.1 is provided with in tank body, tank base is provided with mixing import 3.2, the nearly top of tank body is provided with dioxide peroxide discharge outlet 3.3, and described hydrochloric acid batch meter 2 comprises hydrochloric acid drain 2.3, the hydrochloric acid liquid outlet 2.4 of top hydrochloric acid import 2.1, vacuum orifice 2.2, nearly bottom, hydrochloric acid liquid outlet 2.4 connects mixing import 3.2 by hydrochloric acid drain pipe 4, hydrochloric acid drain pipe 4 is provided with volume pump 5, sodium chlorate liquid outlet 1.5 connects mixing import 3.2 by sodium chlorate drain pipe 6, sodium chlorate drain pipe 6 is provided with volume pump 5, mixing import 3.2 is separately provided with aeration inlet pipe 7, enter pressure water pipe 8 Bonding pressure water inlet 1.3, entering pressure water pipe 8 separately establishes the first arm 8.1 to connect the first gas-water mixer 9, entering pressure water pipe 8 separately establishes the second arm 8.2 to connect the second gas-water mixer 10, first gas-water mixer 9 arranges dioxide peroxide pipeline 11 and connects dioxide peroxide discharge outlet 3.3, second gas-water mixer 10 arranges vacuum lead 12 and connects vacuum orifice 2.2.Describedly enter pressure water pipe 8 arrange tensimeter 13, described tensimeter 13, fluid level controller 1.6, volume pump 5, electric heater 3.1 are all electrically connected microcomputer controller 4.
Chlorine dioxide generating system Technique performance parameter
:
Model: BH-300,
Exert oneself: 300g/h,
Material concentration: HCI:31%; NaCI03:25%,
Refined solution ClO2 content: >=95%,
Mixed solution ClO2 content: 40-70%,
Raw material dosage compares: (HCI:NaCI03): 1:1,
Producer operating temperature: 71 DEG C,
Voltage/power: voltage 220V/ power 1.5KW,
Quantity: 2 covers (1 is standby with 1),
Singly overlap configuration:
(1) material-compound tank:
Quantity: 2,
Volume: 200L,
Physical dimension: φ 500 × 1200mm,
Material: PVC.
(2) hydrochloric acid volume pump:
Flow passage part structure material: PVC,
Barrier film material: PTFE,
Check ball (valve) material: pottery,
Pattern: diaphragm type,
Flow: 8L/H,
Top hole pressure: 1.5kg/cm2,
Pump speed: 0-360 beat/min,
Hand adjustment flow range/precision: 0-100%,
Quantity: 1,
Manufacturer: general sieve name is special.
(3) sodium chlorate volume pump:
Flow passage part structure material: PVC,
Barrier film material: PTFE,
Check ball (valve) material: pottery,
Pattern: diaphragm type,
Flow: 8L/H,
Top hole pressure: 1.5kg/cm2,
Pump speed: 0-360 beat/min,
Hand adjustment flow range/precision: 0-100%,
Quantity: 1,
Manufacturer: general sieve name is special.
(4) water sprayer:
Specification: DN25,
Flow: 0.5L/S,
Material: PVC,
(5) residual chlorine monitoring instrument: 1.
Claims (2)
1. chlorine dioxide generating system, it is characterized in that comprising sodium chlorate batch meter, hydrochloric acid batch meter, reactor and microcomputer controller, described sodium chlorate batch meter comprises the whipping appts in casing, the sodium chlorate import on casing top, the pressure water import of wall box, the sodium chlorate drain of the nearly bottom of casing, sodium chlorate liquid outlet, be provided with fluid level controller in sodium chlorate batch meter casing, described reactor comprises tank body, electric heater is provided with in tank body, tank base is provided with mixing import, and the nearly top of tank body is provided with dioxide peroxide discharge outlet, and described hydrochloric acid batch meter comprises hydrochloric acid drain, the hydrochloric acid liquid outlet of top hydrochloric acid import, vacuum orifice, nearly bottom, hydrochloric acid liquid outlet connects mixing import by hydrochloric acid drain pipe, hydrochloric acid drain pipe is provided with volume pump, sodium chlorate liquid outlet connects mixing import by sodium chlorate drain pipe, sodium chlorate drain pipe is provided with volume pump, mixing import is separately provided with aeration inlet pipe, enter pressure water pipe Bonding pressure water inlet, entering pressure water pipe separately establishes the first arm to connect the first gas-water mixer, entering pressure water pipe separately establishes the second arm to connect the second gas-water mixer, first gas-water mixer arranges dioxide peroxide pipeline and connects dioxide peroxide discharge outlet, second gas-water mixer arranges vacuum lead and connects vacuum orifice.
2. chlorine dioxide generating system according to claim 1, enters described in it is characterized in that on pressure water pipe and arranges tensimeter, and described tensimeter, fluid level controller, volume pump, electric heater are all electrically connected microcomputer controller.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520966996.1U CN205222685U (en) | 2015-11-30 | 2015-11-30 | System takes place for chlorine dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520966996.1U CN205222685U (en) | 2015-11-30 | 2015-11-30 | System takes place for chlorine dioxide |
Publications (1)
Publication Number | Publication Date |
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CN205222685U true CN205222685U (en) | 2016-05-11 |
Family
ID=55897762
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201520966996.1U Withdrawn - After Issue CN205222685U (en) | 2015-11-30 | 2015-11-30 | System takes place for chlorine dioxide |
Country Status (1)
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105399054A (en) * | 2015-11-30 | 2016-03-16 | 江苏海祥环保工程有限公司 | Chlorine dioxide generation system |
-
2015
- 2015-11-30 CN CN201520966996.1U patent/CN205222685U/en not_active Withdrawn - After Issue
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105399054A (en) * | 2015-11-30 | 2016-03-16 | 江苏海祥环保工程有限公司 | Chlorine dioxide generation system |
CN105399054B (en) * | 2015-11-30 | 2017-09-29 | 江苏海祥环保工程有限公司 | Chlorine dioxide generating system |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20160511 Effective date of abandoning: 20170929 |