CN106630525A - Biological carbon ozonization reaction system - Google Patents
Biological carbon ozonization reaction system Download PDFInfo
- Publication number
- CN106630525A CN106630525A CN201710134816.7A CN201710134816A CN106630525A CN 106630525 A CN106630525 A CN 106630525A CN 201710134816 A CN201710134816 A CN 201710134816A CN 106630525 A CN106630525 A CN 106630525A
- Authority
- CN
- China
- Prior art keywords
- ozone
- charcoal
- air
- shower nozzle
- outlet
- 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.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/06—Treatment of sludge; Devices therefor by oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/78—Details relating to ozone treatment devices
- C02F2201/782—Ozone generators
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/02—Temperature
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention relates to the field of environmental protection, in particular to a biological carbon ozonization reaction system. The biological carbon ozonization reaction system comprises a reactor housing and an air pump, wherein the air pump is communicated with an ozone generator; an outlet of the ozone generator is communicated with an ozone air pipeline; a multihole metal plate is arranged in the reactor housing; the multihole metal plate divides a cavity inside the reactor housing into an oxidization reaction cavity at the top and an ozone air cavity at the bottom; the ozone air pipeline penetrates through the reactor housing and is communicated with the ozone air cavity; a sludge and biological carbon mixing feeding device penetrates through the reactor housing and is communicated with the oxidization reaction cavity; an ozonized biological carbon discharging opening is formed in the oxidization reaction cavity. The biological carbon ozonization reaction system kills germs through ozone under conditions of high moisture content of sludge and extremely high organic matter concentration, so as to prevent mass propagation which may cause pipeline blocking; the reaction success rate can be increased, and water vapors and ozone are compounded to quickly degrade pollutants in the organic matter sludge.
Description
Technical field
The present invention relates 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 on-site soil in oil field is produced out with crude oil from stratum
Come, polluted by crude oil, substantial amounts of Organic substance is contained in sludge and many suspended solids are carried, and in the oil reservoir of High Temperature High Pressure
Various salts and the gas in stratum is dissolved, has made Oilfield Soils composition more complicated, and 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
The emission request more and more higher of the materials such as oxygen amount (COD), nitrogen, phosphorus, in 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 a kind of high-efficiency appliances and technique 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：Due to sludge moisture content height,
In the case where organic concentration is too high, antibacterial amount reproduction can be caused, block pipeline, it is easy to cause reaction failure, so as to
Affect treatment effect；And, 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.
The content of the invention
In order to solve the above problems, it is an object of the invention to provide a kind of charcoal ozonization system.The system
It is high in sludge moisture content, in the case where organic concentration is too high, antibacterial is killed by ozone, prevent its amount reproduction from causing to block up
Plug 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.
For achieving the above object, the present invention is employed the following technical solutions：
A kind of charcoal ozonization system, including reactor shell and air pump, the air pump connects an ozone to be occurred
Device, the ozone generator outlet connects an ozone-air pipeline, and an expanded metal is provided with inside reactor shell, described
Reactor shell internal cavity is separated into expanded metal the oxidation reaction chamber at top and the ozone-air chamber of bottom, described smelly
Oxygen air line is connected through the reactor shell with ozone-air chamber, and a sludge organism charcoal mixed material feeding device is through reaction
Device housing is connected with oxidation reaction chamber, and oxidation reaction chamber is provided with an ozonisation charcoal floss hole, and oxidation reaction connects at the top of chamber
A logical tail gas exhaust apparatus, a flexible exhaust gas recirculation pipe is respectively communicated with tail gas exhaust apparatus and air pump, the flexible tail gas
Recirculation pipe is provided with filter near tail gas exhaust apparatus one end, and near air pump one end check valve is provided with, oxidation reaction chamber
Top is provided with the water injector with thermoinduction mechanism, and in the bottom in ozone-air chamber outlet valve is provided with, and the sludge organism charcoal is mixed
Closing charging device includes metal cylinder, and the upper end of metal cylinder is provided with feed hopper, defecator is arranged between feed hopper and metal cylinder,
Hot-air blower is provided with the inwall of feed hopper, transfer roller, transfer roller and a motor connection are installed in the inside of metal cylinder, on transfer roller
Heater is installed, metal cylinder top offers steam vent, bottom and is provided with mudhole, and the lower end of transfer roller is provided with die 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, outlet and inlet valve, the shower nozzle be connected to into
On water pipe, the outlet is located on shower nozzle, and the valve is arranged on water inlet pipe；The thermoinduction mechanism is located on shower nozzle,
It is connected and controls the keying of inlet valve with the inlet valve signal of telecommunication.
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 mouth.
Wherein, the outlet top is provided with dismountable filter screen.
The present invention has the advantages that：
1st, the present invention is high in sludge moisture content, in the case where organic concentration is too high, by ozone antibacterial is killed, and prevents its big
Amount breeding results in blockage pipeline, improves reaction success rate.
2nd, the present invention combines vapor and ozone is stronger to the removal ability containing pollutant in hardly degraded organic substance sludge.
3rd, the process tail gas that present invention flexibility exhaust gas recirculation pipe recycling tail gas exhaust apparatus is collected, energy-conserving and environment-protective,
More preferably result can be realized especially by multiple operation circulations.
4th, the shower nozzle of water injector of the invention can be around water inlet pipe in 360 ° of rotations, it is possible to which the scope of sensing is more
Greatly, sludge organism carbon mixture can uniformly be sprayed.
5th, the thermoinduction mechanism of water injector of the invention is located at the top of shower nozzle upper water-out mouth, it is to avoid damage thermoinduction machine
Structure.
6th, the outlet of water injector of the invention is additionally provided with dismountable filter screen, if the water of water inlet pipe is not clean, will
Outlet is blocked, and filter screen can be taken off into cleaning.
Description of the drawings
Fig. 1 is a kind of structural representation of charcoal ozonization system of the present invention；
Fig. 2 is the structural representation of the sludge organism charcoal mixed material feeding device of the present invention；
Fig. 3 is the structural representation of the water injector of the present invention.
Description of reference numerals：
101- air pumps, 102- ozonators, 103- ozone-airs chamber, 104- expanded metals, 105- reactor shells,
106- outlet valves, 107- oxidation reactions chamber, 108- sludge organism charcoal mixed material feeding devices, 109- ozonisation charcoal floss holes,
110- tail gas exhaust apparatus, 111- flexibility exhaust gas recirculation pipes, 112- filters, 113- check valves, 114- water injectors, 116-
Ozone-air pipeline, 201- water inlet pipes, 202- shower nozzles, 203- outlets, 204- thermoinductions mechanism, 205- inlet valves, 206-
Filter screen, 301- metal cylinders, 302- feed hoppers, 303- motors, 304- hot-air blowers, 305- defecators, 306- transfer rollers, 307- add
Hot device, 308- steam vents, 309- mudholes, 310- die heads, 311- cooling water inlet pipes, 312- cooling water outlet pipes.
Specific embodiment
The present invention 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, the air
Pump 101 connects an ozonator 102, the ozone-air pipeline 116 of 102 outlet of the ozonator one, in reactor
An expanded metal 104 is provided with inside housing 105, the expanded metal 104 is separated into the internal cavity of reactor shell 105
The oxidation reaction chamber 107 at top and the ozone-air chamber 103 of bottom, the ozone-air pipeline 116 passes through the reactor enclosure
Body 105 is connected with ozone-air chamber 103, and a sludge organism charcoal mixed material feeding device 108 is anti-with oxidation through reactor shell 105
Chamber 107 is answered to connect, oxidation reaction chamber 107 is provided with an ozonisation charcoal floss hole 109, the top connection in oxidation reaction chamber 107
One tail gas exhaust apparatus 110, a flexible exhaust gas recirculation pipe 111 is respectively communicated with tail gas exhaust apparatus 110 and air pump 101, institute
State flexible exhaust gas recirculation pipe 111 and be provided with filter 112 near the one end of tail gas exhaust apparatus 110, set near the one end of air pump 101
The top for having check valve 113, oxidation reaction chamber 107 is provided with the water injector 114 with thermoinduction mechanism 204, in ozone-air chamber
103 bottom 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 defecator 305, feed hopper are arranged between feed hopper 302 and metal cylinder 301
Hot-air blower 304 is provided with 302 inwall, transfer roller 306, the motor 303 of transfer roller 306 and are installed in the inside of metal cylinder 301
Connection, installs heater 307 on transfer roller 306, the top of metal cylinder 301 offers steam vent 308, bottom and is provided with mudhole 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 and is connected with cooling
Water outlet pipe 312.Preferably, as shown in figure 3, the water injector 114 includes water inlet pipe 201, shower nozzle 202, the and of outlet 203
Inlet valve 205, the shower nozzle 202 is connected on water inlet pipe 201, and the outlet 203 is located on shower nozzle 202, the valve
205 are arranged on water inlet pipe 201；The thermoinduction mechanism 204 is located on shower nozzle 202, is connected simultaneously with the signal of telecommunication of inlet valve 205
The keying of control inlet valve 205.
Preferably, the shower nozzle 202 can be around water inlet pipe 201 in 360 ° of rotations, due to 204, the thermoinduction mechanism
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 mouth of shower nozzle 202, it is to avoid heat is damaged during 203 leak of outlet
Induction mechanism 204.The outlet 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 the charcoal ozonization system of the present invention is as follows：
Sludge mixed biologic charcoal is put in reactor shell 105 by sludge organism charcoal mixed material feeding device 108 in proportion；It is dirty
When mud charcoal mixed material feeding device 108 works, put into by feed hopper 302 after sludge is mixed with charcoal granule, feed hopper
Hot-air blower 304 is provided with 302, drying charging can be played a part of, it is to avoid moist sludge mixed biologic charcoal granule is entered and led
Cause inefficiency, the filter sludge mixed biologic charcoal granule of defecator 305 to adsorb metal debris, it is to avoid injury device, filter
Sludge mixed biologic charcoal granule afterwards is entered inside metal cylinder 301, and transfer roller 306 drives sludge mixed biologic charcoal granule to transport forward
OK, having heaters 307 is arranged on live-roller 306 makes sludge mixed biologic charcoal granule heat up, and makes the volatilizable thing contained in sludge
Rapid evaporation, Electromagnetic Heating heats up very fast, and the top of metal cylinder 301 offers steam vent 308, bottom and offers mudhole
309, conveniently discharge the sewage stayed when the steam that is collected in metal cylinder and cleaning, transfer roller 306 is by sludge mixed biologic charcoal
Granule is sent to die head 310, and is clamp-oned in reactor shell 105 by die head 310, arranges cooling water in the top of die head 310 and enters
Water pipe 311, lower section arranges cooling water outlet pipe 312, improves the rate of cooling of die head 310, it is to avoid discharging sticks the feelings on die head 310
Condition, improve product quality；Then monitor and adjust charcoal temperature；While charcoal of the adjustment in reactor shell 105
Water content and relative humidity, according to required charcoal water content and relative humidity, the control inlet valve of thermoinduction mechanism 204
205 open, and the suitably water spray of shower nozzle 202 is to oxidation reaction chamber 107, and/or is introduced in ozone-air chamber 103 by outlet valve 106
Water vapour；The ozone that the pumping of air pump 101 is generated by ozonator 102 is in reactor shell 105；Ozone gas pass through
The expanded metal 104 of the top of ozone-air chamber 103 enters oxidation reaction chamber 107, while can be by controlling the wind of 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 gases
Component processes charcoal ozonation in reactor shell 105；At the same time it can also using flexible exhaust gas recirculation pipe 111
Recycle the process tail gas that tail gas exhaust apparatus 110 is collected；According to the temperature of charcoal in reactor shell 105 and containing ozone
Air flow set time enough make ozone and charcoal particle interaction, obtained by ozonisation charcoal floss hole 109
The soil of environmental protection and public nuisance free, by multiple operation circulations more preferably result can be realized.
The specific embodiment of the present invention is the foregoing is only, the scope of the claims of the present invention, every profit is not thereby limited
The equivalent structure transformation made with description of the invention and accompanying drawing content, or directly or indirectly it is used in other related technology necks
Domain, is included within the scope of the present invention.
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 ozonator（102）, the ozonator（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 line（116）Through the reactor shell（105）With ozone-air chamber（103）Connection, sludge organism charcoal mixing is thrown
Material device（108）Through reactor shell（105）With oxidation reaction chamber（107）Connection, oxidation reaction chamber（107）It is 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）, near 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 defecator is set（305）, feed hopper
（302）Inwall on be provided with hot-air blower（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 connects
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）, outlet（203）And inlet valve（205）, the shower nozzle（202）It is connected to water inlet pipe
（201）On, the outlet（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）The signal of telecommunication 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 mouth.
6. charcoal ozonization system as claimed in claim 5, it is characterised in that：The outlet（203）Top sets
There is dismountable filter screen（206）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710134816.7A CN106630525A (en) | 2017-03-08 | 2017-03-08 | Biological carbon ozonization reaction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710134816.7A CN106630525A (en) | 2017-03-08 | 2017-03-08 | Biological carbon ozonization reaction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106630525A true CN106630525A (en) | 2017-05-10 |
Family
ID=58848232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710134816.7A Withdrawn CN106630525A (en) | 2017-03-08 | 2017-03-08 | Biological carbon ozonization reaction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106630525A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20150144564A1 (en) * | 2013-11-25 | 2015-05-28 | University Of Idaho | Biochar water treatment |
| CN104924483A (en) * | 2015-06-26 | 2015-09-23 | 天津辉达斯高分子环保材料有限公司 | Modified plastic granulator |
| US20170036983A1 (en) * | 2015-08-06 | 2017-02-09 | James Weifu Lee | Ozonized biochar compositions and methods of making and using the same |
| CN206570182U (en) * | 2017-03-08 | 2017-10-20 | 祝凤娟 | A kind of charcoal ozonization system |
-
2017
- 2017-03-08 CN CN201710134816.7A patent/CN106630525A/en not_active Withdrawn
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20150144564A1 (en) * | 2013-11-25 | 2015-05-28 | University Of Idaho | Biochar water treatment |
| CN104924483A (en) * | 2015-06-26 | 2015-09-23 | 天津辉达斯高分子环保材料有限公司 | Modified plastic granulator |
| US20170036983A1 (en) * | 2015-08-06 | 2017-02-09 | James Weifu Lee | Ozonized biochar compositions and methods of making and using the same |
| CN206570182U (en) * | 2017-03-08 | 2017-10-20 | 祝凤娟 | A kind of charcoal ozonization system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR200468971Y1 (en) | Complex type apparatus capable of removing malodor gas of animal-excretion | |
| US7105088B2 (en) | Methods and systems for converting waste into energy | |
| KR102012631B1 (en) | System for reduction of bad smell in pigsty using the bio-curtain and the active radical produced by the plasma process | |
| KR100793115B1 (en) | Waste treatment device | |
| KR101133116B1 (en) | Compact typed apparatus capable of removing malodor gas of animal-excretion | |
| CN205550265U (en) | Take tail gas cleanup unit's adjusted temperature chemical industry reation kettle | |
| KR102067937B1 (en) | Drying treatment system of food waste or sewage and wastewater sludge | |
| CN206415416U (en) | A kind of ultraviolet light ozone combines the contaminated soil remediation system adopting recirculating of catalysis oxidation | |
| KR102024871B1 (en) | Device for removing residual ozone gas | |
| KR101387011B1 (en) | Rotary-type multi-pass dryer for waste material | |
| KR100970233B1 (en) | An organic matter disposal unit | |
| CN214781653U (en) | Continuous biomass pyrolysis equipment | |
| KR20130141852A (en) | Supplies organic waste management machine | |
| CN105366901A (en) | Sludge treatment method improving dehydration efficiency | |
| JP2005238120A (en) | Vacuum drying/carbonization device | |
| CN206570182U (en) | A kind of charcoal ozonization system | |
| CN109827215A (en) | A kind of Full-automatic tobacco Flash Gas Compression Skid System | |
| CN207031224U (en) | A kind of sludge quick drying apparatus | |
| CN106630525A (en) | Biological carbon ozonization reaction system | |
| KR20060057501A (en) | Food grabage ferment decompose extinction method and device that all processing of simultaneously processing is possible | |
| CN106493166A (en) | A kind of ultraviolet light ozone combines the contaminated soil remediation system adopting recirculating of catalysis oxidation | |
| CN109821398A (en) | A kind of environment-friendly type oil refining factory emission-control equipment | |
| CN207153463U (en) | Acid mist exhaust treatment system | |
| KR102305140B1 (en) | Organic Waste Treatment Apparatus | |
| CN205556421U (en) | Sludge heavy metal biochemical treatment jar body |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20170510 |
|
| WW01 | Invention patent application withdrawn after publication |