CN104003505A - Double-chamber ozone reactor - Google Patents
Double-chamber ozone reactor Download PDFInfo
- Publication number
- CN104003505A CN104003505A CN201410264369.3A CN201410264369A CN104003505A CN 104003505 A CN104003505 A CN 104003505A CN 201410264369 A CN201410264369 A CN 201410264369A CN 104003505 A CN104003505 A CN 104003505A
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- Prior art keywords
- ozone
- chamber
- area
- casing
- reaction chamber
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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.)
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 80
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 44
- 238000006243 chemical reaction Methods 0.000 claims abstract description 39
- 238000009826 distribution Methods 0.000 claims abstract description 21
- 230000035484 reaction time Effects 0.000 abstract description 9
- 238000013461 design Methods 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract 7
- 239000007789 gas Substances 0.000 description 18
- 238000007254 oxidation reaction Methods 0.000 description 8
- 230000003647 oxidation Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 230000000630 rising effect Effects 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 230000004044 response Effects 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 210000000476 body water Anatomy 0.000 description 1
- 244000144987 brood Species 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229960001701 chloroform Drugs 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000002147 killing effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 150000002896 organic halogen compounds Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 230000000361 pesticidal effect Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000009182 swimming Effects 0.000 description 1
- 239000003053 toxin Substances 0.000 description 1
- 231100000765 toxin Toxicity 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 241001515965 unidentified phage Species 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention relates to a double-chamber ozone reactor. The double-chamber ozone reactor comprises a box body, a tail gas damage system and gas distribution devices, wherein the inside of the box body is divided by a middle separation plate into two chambers, namely a first reaction chamber and a second reaction chamber, the upper portions of the two chambers are communicated, a left separation plate is fixedly arranged between the middle separation plate and the left side of the box body, a right separation plate is fixedly arranged between the middle separation plate and the right side of the box body, the left separation plate divides the first reaction chamber into a first area and a second area, the lower portion of the first area and the lower portion of the second area are communicated, the right separation plate divides the second chamber into a third area and a fourth area, the lower portion of the third area and the lower portion of the fourth area are communicated, the first chamber gas distribution device is connected with the first area and an ozone inlet through a gas inlet pipe respectively, and the second chamber gas distribution device is connected with the third area and the ozone inlet through a gas inlet pipe respectively. The reaction time of the reactor is four times the length of the reaction time of a single-chamber singe-area reactor due to the double-chamber four-area box body design, the purpose of prolonging the reaction time is to enable raw water and ozone to be more thoroughly reacted, the use rate of the ozone is improved, and further it is guaranteed that organics in water can be thoroughly removed.
Description
Technical field
The invention belongs to water treatment field, relate to ozone reactor, especially a kind of two chambers ozone reactor.
Background technology
Ozone (O3) is strong oxidizer, disinfection sanitizer, catalyzer, discoloring agent and reodorant.Ozone technology is the gordian technique of administering environment and water pollution, is 21st century one of environmental science four large gordian techniquies, is widely used in the aspect such as sterilization and fume purifying of air, water, body surface.The core link of this technology is to realize silent discharge by specific electric field to produce a large amount of ozone gas, in this process, a series of bases occur when high-energy electron and gas molecule collision to be activated without physical reaction and by gas, produce various active free radical, thereby be there is to catalysis, oxidation and decomposition in multiple harmful substances, bacteriophage etc., and transfer nontoxic by product to, reach the object of real sterilization, cleaning.
Aspect water treatment, be mainly used in water factory, water tower, water tank, water reservoir, swimming pool and sewage disposal.Ozone application feature: oxidation capacity is strong, speed of response is fast; Bacterium, virus, brood cell, software microorganism etc. are had to extremely strong killing action; Oxidation pesticidal toxin, reduces BOD, COD in water; The raw material of ozone is taken from airborne oxygen, is reduced into again oxygen after finishing the work, and increases oxygen in water, there is no secondary pollution; Can improve the physico-chemical property of water, have good decolouring, deodorizing, the effect of eliminating the unusual smell; Can not produce poisonous trichloromethane and carcinogenic Organohalogen compounds byproduct with ozone disinfecting-sterilizing, not have any residue harmful to people and animals.
By retrieval, find following Patents document:
1, utilize the method for ozonation treatment water and relevant treatment unit (CN1190646A), this device comprises: the pneumatic plant that is located at ozone reactor bottom, compression ozone gas, and be located at ozone reactor top, the processing water receptacle of the processing water of storage; For the device of water and ozone gas supercharging, wherein, the feature of the method for pressure charged ozone water processing is to comprise the following steps: processing water is fed to ozone reactor from processing water receptacle; In compressor to ozone gas supercharging; The ozone gas of supercharging is fed to ozone reactor; Oppress ozone gas in supercharging blower time, within the regular hour, to the ozone gas pressurization of rising in ozone reactor.
2, ozone oxidation reaction device (CN201354327Y) comprises a totally enclosed reactor tank body, is arranged on the manhole plate at tank body top, is seated in the solid catalyst in tank body, the water inlet pipe, rising pipe and the ozone inlet pipe that are connected with tank body; Water inlet pipe the inner is connected with the water trap of tank internal upper part, and rising pipe the inner is connected with the water-recovering device of bottom in tank, and the outer end of rising pipe is connected with water discharge valve, and ozone inlet pipe the inner is connected with the gas pipe of bottom in tank.Described manhole plate is provided with an automatic high-pressure exhaust valve.The advantages such as this ozone oxidation reaction device adopts gas-liquid conversed stream contact mode, and operating pressure, in 0.05～0.25MPa (gauge pressure), has the reaction times short, and ozone utilization rate is high and adding less, and facility investment and working cost are low.
By comparing, above-mentioned patent and the application's structure has significant difference.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art part, a kind of two chambers ozone reactor of saving ozone usage quantity, improving ozone reaction efficiency is provided.
The technical scheme that technical solution problem of the present invention adopts is:
A kind of two chambers ozone reactor, comprise casing, tail gas destroys system and distribution device, in the exterior top surface of casing, tail gas is installed and is destroyed system, inner bottom surface at casing is fixedly mounted with distribution device, be shaped with water-in and ozone entrance at the end face of casing, sidewall at casing is shaped with water port, described box house is divided into by median septum two Room that top is communicated with, be respectively the first reaction chamber and the second reaction chamber, on median septum and a casing left side, between right two side, be fixedly mounted with respectively left clapboard and right clapboard, described left clapboard is separated into the first reaction chamber between first interval and Second Region of bottom connection, the second reaction chamber is separated into the 3rd interval and the 4th interval that bottom is communicated with by described right clapboard, be connected a Room distribution device and two Room distribution devices with ozone entrance by inlet pipe in the first interval respectively with the 3rd interval.
And, be shaped with respectively a gas port in the corresponding symmetric position of left clapboard and right clapboard.
And, be respectively connected a blow-off pipe at the bottom rear wall of the first reaction chamber and the second reaction chamber.
And, be all shaped with the manhole with rotary cap at left and right sidewall and the front side wall of casing.
And, be shaped with two visors in the front side wall bottom of casing.
Advantage of the present invention and positively effect are:
1, this reactor two Room four-range cabinet design are equivalent to four times of interval reactor reaction time of single chamber list, the object that extends the reaction times is in order to make former water and ozone reaction ground more abundant, improve the utilization ratio of ozone, and then ensured that in water, organism is removed up hill and dale.
2, this reactor is by arranging two of two Room distribution device, can regulate better the quantity discharged of ozone, when being close to completely that former water reacts at the first reaction chamber with ozone, can reduce or stop the ozone discharge of the second reaction chamber, can reduce to greatest extent like this usage quantity of ozone, avoid ozone and waste; If there is no complete reaction at the first reaction chamber, can increase the quantity discharged of ozone, more ozone is provided, can fully react, ensure that in water, organism can be by complete oxidation.
3, this reactor is arranged on distribution device the bottom of casing, ozone rise process in the former water from casing top to contacting, make its dissolving in water more abundant, and then improved the reaction efficiency of ozone.
4, this reactor is shaped with respectively a gas port in the corresponding symmetric position of left clapboard and right clapboard, and the air pressure in can balance box, prevents box deformation.
5, this reactor is compared with traditional ozone reactor, and advantage is to be convenient to observe, safeguard, adjustable controlled, reacts completely, and ozone utilization rate is high, and tail gas is well processed.
Brief description of the drawings
Fig. 1 is front view of the present invention;
Fig. 2 is the left view (broken section) of Fig. 1;
Fig. 3 is the vertical view of Fig. 1;
Fig. 4 is the internal structure schematic diagram of reactor of the present invention.
Embodiment
Below in conjunction with accompanying drawing and by specific embodiment, the invention will be further described, and following examples are descriptive, are not determinate, can not limit protection scope of the present invention with this.
A kind of two chambers ozone reactor, comprises that casing 4, tail gas destroy system 1 and distribution device, in the exterior top surface of casing, tail gas is installed and is destroyed system, is fixedly mounted with distribution device in the inner bottom surface of casing.Be shaped with water-in 7 and ozone entrance 2 at the end face of casing, be shaped with water port 3 at the sidewall of casing.
Innovative point of the present invention is:
Described box house is divided into by median septum 16 two Room that top is communicated with, be respectively the first reaction chamber and the second reaction chamber, between median septum and casing arranged on left and right sides wall, be fixedly mounted with respectively left clapboard 17 and right clapboard 10, described left clapboard is separated between first interval 18 and the Second Region that bottom is communicated with 15 by the first reaction chamber, and the second reaction chamber is separated into the the 3rd interval 12 and the 4th interval 9 that bottom is communicated with by described right clapboard.Be connected a Room distribution device 14 and two Room distribution devices 13 with ozone entrance by inlet pipe 11 in the first interval respectively with the 3rd interval.
For the air pressure in balance box, prevent box deformation, be shaped with respectively a gas port in the corresponding symmetric position of left clapboard and right clapboard.
Bottom rear wall at the first reaction chamber and the second reaction chamber is respectively connected a blow-off pipe 8, for removing the residuary water in casing.
Overhaul in order to facilitate staff to enter in casing, and before maintenance, make ozone remaining in casing discharge, be all shaped with the manhole 5 with rotary cap at left and right sidewall and the front side wall of casing.
In order to facilitate staff to observe the response situation in casing, be also shaped with two visors 6 in the front side wall bottom of casing.
Principle of work of the present invention:
The trend of former water is as shown in Fig. 4 arrow, former water is first entered the first interval of the first reaction chamber by water-in, meet with the ozone upwards disperseing from bottom at this interval Yuan Shui, ozone reacts with the organism in former water, oxidation of organic compounds is CO2 and water, because the height of casing is limited, for the reaction times that extends ozone and water is divided into the first reaction chamber between the first interval and Second Region, unreacted completely water carries ozone and enters between Second Region, by entering the second reaction chamber between Second Region, two Room ozone distribution devices are set in the bottom of the second reaction chamber, according to response situation, regulate the ozone quantity discharged of two Room distribution devices, by two reaction chambers being set and two distribution devices can be reasonable, effectively utilize ozone, avoid the use waste of ozone.Former water is discharged by water port behind the 3rd interval and the 4th interval by the second Room.Two Room four-range cabinet design are equivalent to four times of interval reactor reaction time of single chamber list, and the object that extends the reaction times is in order to make former water and ozone reaction ground more abundant, to improve the utilization ratio of ozone, and then ensured that in water, organism is removed up hill and dale.And, by two of two Room distribution device is set, can regulate better the quantity discharged of ozone, when being close to completely that former water reacts at the first reaction chamber with ozone, can reduce or stop the ozone discharge of the second reaction chamber, can reduce to greatest extent like this usage quantity of ozone, avoid ozone and waste; If there is no complete reaction at the first reaction chamber, can increase the quantity discharged of ozone, more ozone is provided, can fully react, ensure that in water, organism can be by complete oxidation.
Above-described is only the preferred embodiment of the present invention, it should be pointed out that for the person of ordinary skill of the art, not departing under the prerequisite of inventive concept, can also make some distortion and improvement, and these all belong to protection scope of the present invention.
Claims (5)
1. two chambers ozone reactor, comprise casing, tail gas destroys system and distribution device, in the exterior top surface of casing, tail gas is installed and is destroyed system, inner bottom surface at casing is fixedly mounted with distribution device, be shaped with water-in and ozone entrance at the end face of casing, sidewall at casing is shaped with water port, it is characterized in that: described box house is divided into by median septum two Room that top is communicated with, be respectively the first reaction chamber and the second reaction chamber, on median septum and a casing left side, between right two side, be fixedly mounted with respectively left clapboard and right clapboard, described left clapboard is separated into the first reaction chamber between first interval and Second Region of bottom connection, the second reaction chamber is separated into the 3rd interval and the 4th interval that bottom is communicated with by described right clapboard, be connected a Room distribution device and two Room distribution devices with ozone entrance by inlet pipe in the first interval respectively with the 3rd interval.
2. according to claim 1 pair of chamber ozone reactor, is characterized in that: the corresponding symmetric position at left clapboard and right clapboard is shaped with respectively a gas port.
3. according to claim 1 pair of chamber ozone reactor, is characterized in that: the bottom rear wall at the first reaction chamber and the second reaction chamber is respectively connected a blow-off pipe.
4. according to claim 1 pair of chamber ozone reactor, is characterized in that: left and right sidewall and front side wall at casing are all shaped with the manhole with rotary cap.
5. according to claim 1 pair of chamber ozone reactor, is characterized in that: be shaped with two visors in the front side wall bottom of casing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410264369.3A CN104003505A (en) | 2014-06-16 | 2014-06-16 | Double-chamber ozone reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410264369.3A CN104003505A (en) | 2014-06-16 | 2014-06-16 | Double-chamber ozone reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104003505A true CN104003505A (en) | 2014-08-27 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410264369.3A Pending CN104003505A (en) | 2014-06-16 | 2014-06-16 | Double-chamber ozone reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104003505A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106186279A (en) * | 2016-09-05 | 2016-12-07 | 苏州清然环保科技有限公司 | Continuous operating device for catalyzing and oxidating ozone and method |
| CN107245725A (en) * | 2017-07-18 | 2017-10-13 | 杭州尚杭科技有限公司 | A kind of intelligent environment protection toilet ozone generating-device |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003266088A (en) * | 2002-03-15 | 2003-09-24 | Toshiba Corp | Ozone accelerated oxidation water treatment system together using ultraviolet rays |
| JP2009082777A (en) * | 2007-09-28 | 2009-04-23 | Hitachi Ltd | Water treatment facility and gas generating device |
| CN203307143U (en) * | 2013-04-19 | 2013-11-27 | 北京天灏柯润环境科技有限公司 | Catalytic oxidation wastewater treatment device |
-
2014
- 2014-06-16 CN CN201410264369.3A patent/CN104003505A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003266088A (en) * | 2002-03-15 | 2003-09-24 | Toshiba Corp | Ozone accelerated oxidation water treatment system together using ultraviolet rays |
| JP2009082777A (en) * | 2007-09-28 | 2009-04-23 | Hitachi Ltd | Water treatment facility and gas generating device |
| CN203307143U (en) * | 2013-04-19 | 2013-11-27 | 北京天灏柯润环境科技有限公司 | Catalytic oxidation wastewater treatment device |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106186279A (en) * | 2016-09-05 | 2016-12-07 | 苏州清然环保科技有限公司 | Continuous operating device for catalyzing and oxidating ozone and method |
| CN106186279B (en) * | 2016-09-05 | 2023-07-21 | 苏州清然环保科技有限公司 | Continuous operation type ozone catalytic oxidation device and method |
| CN107245725A (en) * | 2017-07-18 | 2017-10-13 | 杭州尚杭科技有限公司 | A kind of intelligent environment protection toilet ozone generating-device |
| CN107245725B (en) * | 2017-07-18 | 2020-10-30 | 杭州尚杭科技有限公司 | Ozone generating device for intelligent environment-friendly toilet |
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Legal Events
| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20140827 |
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| RJ01 | Rejection of invention patent application after publication |