CN206570182U - A kind of charcoal ozonization system - Google Patents

A kind of charcoal ozonization system Download PDF

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Publication number
CN206570182U
CN206570182U CN201720220898.2U CN201720220898U CN206570182U CN 206570182 U CN206570182 U CN 206570182U CN 201720220898 U CN201720220898 U CN 201720220898U CN 206570182 U CN206570182 U CN 206570182U
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China
Prior art keywords
ozone
charcoal
air
shower nozzle
reactor shell
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Expired - Fee Related
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CN201720220898.2U
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Chinese (zh)
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祝凤娟
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Individual
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Individual
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  • Treatment Of Sludge (AREA)
  • Treating Waste Gases (AREA)

Abstract

The utility model is related to field of environment protection, more particularly to a kind of charcoal ozonization system, including reactor shell and air pump, the air pump connects an ozone generator, ozone generator outlet connects an ozone-air pipeline, an expanded metal is provided with reactor enclosure body, reactor shell internal cavity is separated into the oxidation reaction chamber at top and the ozone-air chamber of bottom by expanded metal, ozone-air pipeline is connected through reactor shell with ozone-air chamber, one sludge organism charcoal mixed material feeding device is connected through reactor shell with oxidation reaction chamber, oxidation reaction chamber is provided with an ozonisation charcoal floss hole, the system is high in sludge moisture content, in the case where organic concentration is too high, bacterium is killed by ozone, prevent that its amount reproduction from resulting in blockage pipeline, reaction success rate can be improved, in combination with pollutant in vapor and the rapid degradation of organic substances sludge of ozone.

Description

A kind of charcoal ozonization system
Technical field
The utility model is related to field of environment protection, more particularly to a kind of charcoal ozonization system.
Background technology
During the entire process of crude oil collection and processing, the soil in oil field location is produced out with crude oil from stratum Come, polluted by crude oil, substantial amounts of organic matter is contained in sludge and many suspended solids are carried, and in the oil reservoir of HTHP Various salts and the gas in stratum have been dissolved, has made Oilfield Soils composition more complicated, and has been added during crude oil transmission Various chemical agents also increase soil contamination grade.It is continuous strict with mud discharging standard, chemistry in sludge is needed In the emission request more and more higher of the materials such as oxygen amount (COD), nitrogen, phosphorus, industrial sludge the removal of COD (COD) with Denitrogenation dephosphorizing faces enormous challenge.Traditional processing mode often increases the expense and energy consumption of capital expenditure, and run compared with For complexity.
Charcoal ozonization device and its sludge treatment technique are the high-efficiency appliance and technique of a kind of Treatment of Sludge.Its Few with volumetric loading, required capital expenditure, treatment effeciency is high, and operation energy consumption is low, the characteristics of operating cost is few.
But also there are problems in charcoal ozonization device of the prior art:Because sludge moisture content is high, In the case where organic concentration is too high, bacterium amount reproduction can be caused, pipeline is blocked, it is easy to cause reaction to fail, so that Influence treatment effect;Moreover, charcoal ozonization device containing pollutant in hardly degraded organic substance sludge to going decapacitation Power is limited, and the problem is the principal element for restricting the development of charcoal ozonization device technique.
Utility model content
In order to solve the above problems, the purpose of this utility model is to provide a kind of charcoal ozonization system.Should System is high in sludge moisture content, in the case where organic concentration is too high, kills bacterium by ozone, prevents its amount reproduction from making Into blocking pipeline, it is possible to increase reaction success rate, in combination with pollutant in vapor and the rapid degradation of organic substances sludge of ozone.
To achieve the above object, the utility model uses following technical scheme:
A kind of charcoal ozonization system, including reactor shell and air pump, the air pump connect an ozone Generator, the ozone generator outlet connects an ozone-air pipeline, and an expanded metal is provided with inside reactor shell, Reactor shell internal cavity is separated into the oxidation reaction chamber at top and the ozone-air chamber of bottom, institute by the expanded metal State ozone-air pipeline to connect with ozone-air chamber through the reactor shell, a sludge organism charcoal mixed material feeding device is passed through Reactor shell is connected with oxidation reaction chamber, and oxidation reaction chamber is provided with an ozonisation charcoal floss hole, the top of oxidation reaction chamber Portion connects a tail gas exhaust apparatus, and a flexible exhaust gas recirculation pipe is respectively communicated with tail gas exhaust apparatus and air pump, the flexibility Exhaust gas recirculation pipe is provided with filter close to tail gas exhaust apparatus one end, and check valve, oxidation reaction are provided with close to air pump one end The top of chamber is provided with the water injector with thermoinduction mechanism, and outlet valve, the sludge organism are provided with the bottom of ozone-air chamber Charcoal mixed material feeding device includes metal cylinder, and the upper end of metal cylinder is provided with feed hopper, and filtering is set between feed hopper and metal cylinder Air-heater is provided with device, the inwall of feed hopper, the inside of metal cylinder is installed transfer roller, transfer roller and a motor connection, passed Send and heater is installed on roller, metal cylinder top offers steam vent, bottom and is provided with mudhole, and the lower end of transfer roller is provided with mould Head, die head top is connected with cooling water inlet pipe, bottom and is connected with cooling water outlet pipe.
Wherein, the water injector also include water inlet pipe, shower nozzle, delivery port and inlet valve, the shower nozzle be connected into On water pipe, the delivery port is located on shower nozzle, and the valve is arranged on water inlet pipe;The thermoinduction mechanism is located on shower nozzle, The keying of inlet valve is connected and controlled with inlet valve electric signal.
Wherein, the shower nozzle can be around water inlet pipe in 360 ° of rotations.
Wherein, the shower nozzle is spheroid or cone.
Wherein, the thermoinduction mechanism is located at the top of shower nozzle upper water-out mouthful.
Wherein, it is provided with dismountable filter screen above the delivery port.
The utility model has the advantages that:
1st, the utility model is high in sludge moisture content, in the case where organic concentration is too high, and bacterium is killed by ozone, Prevent that its amount reproduction from resulting in blockage pipeline, improve reaction success rate.
2nd, the utility model combination vapor and ozone are to the removal ability containing pollutant in hardly degraded organic substance sludge It is stronger.
3rd, the flexible exhaust gas recirculation pipe of the utility model recycles the processing tail gas that tail gas exhaust apparatus is collected, energy-saving ring Protect, more preferably result can be realized especially by multiple operation circulations.
4th, the shower nozzle of water injector of the present utility model can be around water inlet pipe in 360 ° of rotations, it is possible to the model of sensing Enclose bigger, sludge organism carbon mixture can uniformly be sprayed.
5th, the thermoinduction mechanism of water injector of the present utility model is located at the top of shower nozzle upper water-out mouthful, it is to avoid damage thermal sensation Answer mechanism.
6th, the delivery port of water injector of the present utility model is additionally provided with dismountable filter screen, if the water of water inlet pipe is not done Only, delivery port is blocked, filter screen can be taken off to cleaning.
Brief description of the drawings
Fig. 1 is a kind of structural representation of charcoal ozonization system of the present utility model;
Fig. 2 is the structural representation of sludge organism charcoal mixed material feeding device of the present utility model;
Fig. 3 is the structural representation of water injector of the present utility model.
Description of reference numerals:
101- air pumps, 102- ozone generators, 103- ozone-airs chamber, 104- expanded metals, 105- reactor enclosures Body, 106- outlet valves, 107- oxidation reactions chamber, 108- sludge organism charcoal mixed material feedings device, 109- ozonisation charcoal discharges Mouth, the flexible exhaust gas recirculation pipe of 110- tail gas exhaust apparatus, 111-, 112- filters, 113- check valves, 114- water injectors, 116- ozone-airs pipeline, 201- water inlet pipes, 202- shower nozzles, 203- delivery ports, 204- thermoinductions mechanism, 205- inlet valves, 206- filter screens, 301- metal cylinders, 302- feed hoppers, 303- motors, 304- air-heaters, 305- filters, 306- transfer rollers, 307- heaters, 308- steam vents, 309- mudholes, 310- die heads, 311- cooling water inlet pipes, 312- cooling water outlet pipes.
Embodiment
The utility model is described in further details below in conjunction with the drawings and specific embodiments:
As shown in figure 1, a kind of charcoal ozonization system, including reactor shell 105 and air pump 101, it is described Air pump 101 connects an ozone generator 102, the ozone-air pipeline 116 of 102 outlet of ozone generator one, anti- The inside of device housing 105 is answered to be provided with an expanded metal 104, the expanded metal 104 divides the internal cavity of reactor shell 105 The oxidation reaction chamber 107 at top and the ozone-air chamber 103 of bottom are divided into, the ozone-air pipeline 116 passes through the reaction Device housing 105 is connected with ozone-air chamber 103, and a sludge organism charcoal mixed material feeding device 108 passes through reactor shell 105 and oxygen Change reaction chamber 107 to connect, oxidation reaction chamber 107 is provided with an ozonisation charcoal floss hole 109, the top of oxidation reaction chamber 107 A tail gas exhaust apparatus 110 is connected, a flexible exhaust gas recirculation pipe 111 is respectively communicated with tail gas exhaust apparatus 110 and air pump 101, the flexible exhaust gas recirculation pipe 111 is provided with filter 112 close to the one end of tail gas exhaust apparatus 110, close to air pump 101 One end is provided with check valve 113, and the top of oxidation reaction chamber 107 is provided with the water injector 114 with thermoinduction mechanism 204, in ozone The bottom of air chamber 103 is provided with outlet valve 106, as shown in Fig. 2 the sludge organism charcoal mixed material feeding device 108 includes metal Cylinder 301, the upper end of metal cylinder 301 is provided with feed hopper 302, and filter 305 is set between feed hopper 302 and metal cylinder 301, Air-heater 304 is provided with the inwall of feed hopper 302, transfer roller 306, the electricity of transfer roller 306 and one are installed in the inside of metal cylinder 301 Machine 303 is connected, and heater 307 is installed on transfer roller 306, and the top of metal cylinder 301 offers steam vent 308, bottom and is provided with blowdown Hole 309, the lower end of transfer roller 306 is provided with die head 310, and the top of die head 310 is connected with cooling water inlet pipe 311, bottom connection There is cooling water outlet pipe 312.It is preferred that, as shown in figure 3, the water injector 114 includes water inlet pipe 201, shower nozzle 202, water outlet Mouth 203 and inlet valve 205, the shower nozzle 202 are connected on water inlet pipe 201, and the delivery port 203 is located on shower nozzle 202, institute Valve 205 is stated to be arranged on water inlet pipe 201;The thermoinduction mechanism 204 is located on shower nozzle 202, with the electric signal of inlet valve 205 Connect and control the keying of inlet valve 205.
It is preferred that, the shower nozzle 202 can be around water inlet pipe 201 in 360 ° of rotations, due to 204, the thermoinduction mechanism In on shower nozzle 202, the shower nozzle 202 around water inlet pipe 201 rotate when, the scope that can be sensed is bigger.The shower nozzle 202 is spheroid Or cone.The thermoinduction mechanism 204 is located at the top of the upper water-out mouthful of shower nozzle 202, it is to avoid heat is damaged during 203 leak of delivery port Induction mechanism 204.The delivery port 203 is additionally provided with dismountable filter screen 206, if the water of water inlet pipe 201 is not clean, by water outlet Mouth 203 is blocked, and filter screen 206 can be taken off into cleaning.
The operation principle of charcoal ozonization system of the present utility model is as follows:
Sludge mixed biologic charcoal is put into reactor shell 105 by sludge organism charcoal mixed material feeding device 108 in proportion It is interior;When sludge organism charcoal mixed material feeding device 108 works, put into, entered by feed hopper 302 after sludge is mixed with charcoal particle Air-heater 304 is provided with hopper 302, drying charging can be played a part of, it is to avoid moist sludge mixed biologic charcoal particle enters Entering causes inefficiency, the filter sludge mixed biologic charcoal particle of filter 305, metal debris is adsorbed, it is to avoid injury device, Sludge mixed biologic charcoal particle after filtering enters inside metal cylinder 301, transfer roller 306 drive sludge mixed biologic charcoal particle to Set having heaters 307 sludge mixed biologic charcoal particle is heated up on preceding operation, live-roller 306, make what is contained in sludge to wave Stimulating food evaporates rapidly, Electromagnetic Heating, and heating is very fast, and the top of metal cylinder 301 offers steam vent 308, bottom and offers blowdown Hole 309, the sewage left when conveniently discharging the hot gas being collected in metal cylinder and cleaning, transfer roller 306 is by sludge mixed biologic Charcoal particle is sent to die head 310, and is squeezed into by die head 310 in reactor shell 105, and cooling water is set in the top of die head 310 Water inlet pipe 311, lower section set cooling water outlet pipe 312, improve the cooling velocity of die head 310, it is to avoid discharging is sticked on die head 310 Situation, improves product quality;Then monitor and adjust charcoal temperature;The charcoal in reactor shell 105 is adjusted simultaneously Water content and relative humidity, according to required charcoal water content and relative humidity, the control water intaking valve of thermoinduction mechanism 204 Door 205 is opened, and the suitably water spray of shower nozzle 202 arrives oxidation reaction chamber 107, and/or is drawn by outlet valve 106 in ozone-air chamber 103 Enter water vapour;The ozone that the pumping of air pump 101 is generated by ozone generator 102 is in reactor shell 105;Ozone gas leads to The expanded metal 104 for crossing the top of ozone-air chamber 103 enters oxidation reaction chamber 107, while can be by controlling air pump 101 Fan speed delivery of ozone gas;The outlet valve 106 in the bottom of ozone-air chamber 103 can also be utilized in addition, introduce other gas Body component handles charcoal ozonation to reactor shell 105 is interior;At the same time it can also utilize flexible exhaust gas recirculation pipe 111 recycle the processing tail gas that tail gas exhaust apparatus 110 is collected;According to the temperature of charcoal in reactor shell 105 and contain The air flow set time enough of ozone makes ozone and charcoal particle interaction, by ozonizing charcoal floss hole 109 The soil of environmental protection and public nuisance free is obtained, more preferably result can be realized by multiple operation circulations.
Embodiment of the present utility model is the foregoing is only, patent model of the present utility model is not thereby limited Enclose, the equivalent structure transformation that every utilization the utility model specification and accompanying drawing content are made, or be directly or indirectly used in it The technical field of his correlation, is similarly included in scope of patent protection of the present utility model.

Claims (6)

1. a kind of charcoal ozonization system, it is characterised in that:Including reactor shell(105)And air pump(101), institute State air pump(101)Connect an ozone generator(102), the ozone generator(102)The ozone-air pipeline of outlet one (116), in reactor shell(105)Inside is provided with an expanded metal(104), the expanded metal(104)By reactor Housing(105)Internal cavity is separated into the oxidation reaction chamber at top(107)With the ozone-air chamber of bottom(103), the ozone Air duct(116)Through the reactor shell(105)With ozone-air chamber(103)Connection, sludge organism charcoal mixing is thrown Expect device(108)Through reactor shell(105)With oxidation reaction chamber(107)Connection, oxidation reaction chamber(107)Provided with an ozone Change charcoal floss hole(109), oxidation reaction chamber(107)Top connect a tail gas exhaust apparatus(110), a flexible tail gas is again Circulation pipe(111)It is respectively communicated with tail gas exhaust apparatus(110)And air pump(101), the flexible exhaust gas recirculation pipe(111)Lean on Nearly tail gas exhaust apparatus(110)One end is provided with filter(112), close to air pump(101)One end is provided with check valve(113), oxygen Change reaction chamber(107)Top be provided with band thermoinduction mechanism(204)Water injector(114), in ozone-air chamber(103)Bottom Portion is provided with outlet valve(106), the sludge organism charcoal mixed material feeding device(108)Including metal cylinder(301), metal cylinder(301) Upper end be provided with feed hopper(302), feed hopper(302)With metal cylinder(301)Between filter is set(305), feed hopper (302)Inwall on be provided with air-heater(304), metal cylinder(301)Inside install transfer roller(306), transfer roller(306)With One motor(303)Connection, transfer roller(306)Upper installation heater(307), metal cylinder(301)Top offers steam vent (308), bottom be provided with mudhole(309), transfer roller(306)Lower end die head is installed(310), die head(310)Top is connected There is cooling water inlet pipe(311), bottom be connected with cooling water outlet pipe(312).
2. charcoal ozonization system as claimed in claim 1, it is characterised in that:The water injector(114)Also wrap Include water inlet pipe(201), shower nozzle(202), delivery port(203)And inlet valve(205), the shower nozzle(202)It is connected to water inlet pipe (201)On, the delivery port(203)Positioned at shower nozzle(202)On, the valve(205)It is arranged on water inlet pipe(201)On;It is described Thermoinduction mechanism(204)Positioned at shower nozzle(202)On, with inlet valve(205)Electric signal connects and controls inlet valve(205)'s Open and close.
3. charcoal ozonization system as claimed in claim 2, it is characterised in that:The shower nozzle(202)Can be around Water inlet pipe(201)In 360 ° of rotations.
4. charcoal ozonization system as claimed in claim 3, it is characterised in that:The shower nozzle(202)For spheroid or Cone.
5. charcoal ozonization system as claimed in claim 4, it is characterised in that:The thermoinduction mechanism(204)Position In shower nozzle(202)The top of upper water-out mouthful.
6. charcoal ozonization system as claimed in claim 5, it is characterised in that:The delivery port(203)Top is set There is dismountable filter screen(206).
CN201720220898.2U 2017-03-08 2017-03-08 A kind of charcoal ozonization system Expired - Fee Related CN206570182U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720220898.2U CN206570182U (en) 2017-03-08 2017-03-08 A kind of charcoal ozonization system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720220898.2U CN206570182U (en) 2017-03-08 2017-03-08 A kind of charcoal ozonization system

Publications (1)

Publication Number Publication Date
CN206570182U true CN206570182U (en) 2017-10-20

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106630525A (en) * 2017-03-08 2017-05-10 祝凤娟 Biological carbon ozonization reaction system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106630525A (en) * 2017-03-08 2017-05-10 祝凤娟 Biological carbon ozonization reaction system

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CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20171020

Termination date: 20180308