CN204162562U - The oil-field flooding of electromagnetism catalyzed oxidation and waste disposal plant - Google Patents
The oil-field flooding of electromagnetism catalyzed oxidation and waste disposal plant Download PDFInfo
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- CN204162562U CN204162562U CN201420641535.2U CN201420641535U CN204162562U CN 204162562 U CN204162562 U CN 204162562U CN 201420641535 U CN201420641535 U CN 201420641535U CN 204162562 U CN204162562 U CN 204162562U
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- 230000003647 oxidation Effects 0.000 title claims abstract description 14
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 14
- 239000002699 waste material Substances 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 74
- 239000010865 sewage Substances 0.000 claims abstract description 37
- 239000003381 stabilizer Substances 0.000 claims abstract description 33
- 230000005672 electromagnetic field Effects 0.000 claims abstract description 32
- 230000001954 sterilising effect Effects 0.000 claims abstract description 29
- 239000011941 photocatalyst Substances 0.000 claims abstract description 27
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 24
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 18
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 abstract description 10
- 239000000126 substance Substances 0.000 abstract description 8
- 239000010815 organic waste Substances 0.000 abstract description 3
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- FRXSZNDVFUDTIR-UHFFFAOYSA-N 6-methoxy-1,2,3,4-tetrahydroquinoline Chemical compound N1CCCC2=CC(OC)=CC=C21 FRXSZNDVFUDTIR-UHFFFAOYSA-N 0.000 description 3
- 241000195493 Cryptophyta Species 0.000 description 3
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- 238000005516 engineering process Methods 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 238000005842 biochemical reaction Methods 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000001727 in vivo Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 230000004060 metabolic process Effects 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 235000019600 saltiness Nutrition 0.000 description 2
- 238000005728 strengthening Methods 0.000 description 2
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- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
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- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
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- 230000000813 microbial effect Effects 0.000 description 1
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- 239000000243 solution Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Physical Water Treatments (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The oil-field flooding of electromagnetism catalyzed oxidation and waste disposal plant, comprise base, base is installed into water pipe, water inlet pipe is communicated with pulse electromagnetic field Sterilizers, the tube wall periphery of water inlet pipe arranges magnetic sleeve pipe, and pulse electromagnetic field Sterilizers is communicated with Photocatalyst sterilization device, installs ultraviolet lamp tube and photochemical catalysis rod in Photocatalyst sterilization device, Photocatalyst sterilization device is communicated with electrolysis current stabilizer, and electrolysis current stabilizer sets out water pipe.Mass disposal organic waste water is achieved by the technique means of pure physics, thoroughly solve chemical treatment means inevitably to produce secondary pollution, repeat the problem of corroding and to the healthy threat caused of operator, simultaneously the utility model also has the advantages such as working cost is low, volume is little, can dispose of sewage continuously.
Description
Technical field
The utility model relates to a kind of water treating equipment, specifically the oil-field flooding of a kind of electromagnetism catalyzed oxidation and waste disposal plant.
Background technology
Oil-field flooding is the waste water that oil-extracting and water-injecting oil-extraction method carries out oil producing in recovery process, the fluctuation of its complicated component, water quality and quantity is large, Pollutant levels are high and difficult degradation, pollutent mostly is poisonous and hazardous organism, and single treatment process is difficult to reach water quality re-injection requirement.The treatment technology that research is efficient, economic, energy-conservation, the efficient combination of exploitation different process is main contents and the developing direction of petrochemical wastewater Processing Technology Research.The heavily contaminated sewage such as existing oil-field flooding can only process by chemical means, but this process means need longer chemical time, the continuous process of sewage cannot be realized, and large-scale conversion unit need be equipped with, what also can be difficult to avoid causes the secondary pollution of chemical reaction reagent, the repetition etching problem of equipment simultaneously, also can constitute a threat to the healthy of operator in addition.
Utility model content
The purpose of this utility model is to provide the oil-field flooding of a kind of electromagnetism catalyzed oxidation and waste disposal plant, and it can carry out the process such as effective sterilizing, algae removal, purification, scale removal by pure physical means to oil-field flooding and the large sewage of other multiple intractability.
The utility model for achieving the above object, be achieved through the following technical solutions: comprise base, base is installed into water pipe, water inlet pipe is communicated with pulse electromagnetic field Sterilizers, the tube wall periphery of water inlet pipe arranges magnetic sleeve pipe, and pulse electromagnetic field Sterilizers is communicated with Photocatalyst sterilization device, installs ultraviolet lamp tube and photochemical catalysis rod in Photocatalyst sterilization device, Photocatalyst sterilization device is communicated with electrolysis current stabilizer, and electrolysis current stabilizer sets out water pipe.Described pulse electromagnetic field Sterilizers comprises feed-water end housing and water side housing, between feed-water end housing and water side housing, dividing plate is set, cathode sleeve installed by dividing plate, cathode sleeve two ends lay respectively in feed-water end housing and water side housing, cathode sleeve in feed-water end housing arranges flow inlet, cathode sleeve in the housing of water side arranges water export, and the shaft core position in cathode sleeve installs conductive anode rod, and the external diameter of conductive anode rod is less than the internal diameter of cathode sleeve.Described electrolysis current stabilizer comprises current stabilizer housing, current stabilizer housing sidewall bottom arranges water-in and sewage draining exit, and current stabilizer housing sidewall top sets out water pipe, and current stabilizer case top arranges top cover, installing electrodes post on top cover, electrode column end is positioned at current stabilizer lower housing portion.The housing of described Photocatalyst sterilization device is Horizontal tubular housing, ultraviolet lamp tube and photochemical catalysis rod all horizontal positioned in the housing of Photocatalyst sterilization device.Feed-water end housing and the water side housing of described pulse electromagnetic field Sterilizers are Horizontal tubular housing, cathode sleeve and the equal horizontal positioned of conductive anode rod.Magnetic sleeve pipe periphery wall arranges magnetic shield cover.
The utility model has the advantage of: achieve mass disposal organic waste water by the technique means of pure physics, thoroughly solve chemical treatment means inevitably to produce secondary pollution, repeat the problem of corroding and to the healthy threat caused of operator, simultaneously the utility model also has the advantages such as working cost is low, volume is little, can dispose of sewage continuously.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
Fig. 2 is that the A-A of Fig. 1 analyses and observe structure for amplifying schematic diagram;
Fig. 3 is that the B-B of Fig. 1 analyses and observe structure for amplifying schematic diagram;
Fig. 4 is that the C-C of Fig. 1 analyses and observe structure for amplifying schematic diagram;
Fig. 5 is the left TV structure schematic diagram of Fig. 4.
Embodiment
Electromagnetism catalyzed oxidation described in the utility model oil-field flooding and waste disposal plant comprise base 1, base 1 is installed into water pipe 2, water inlet pipe 2 is communicated with pulse electromagnetic field Sterilizers 3, the tube wall periphery of water inlet pipe 2 arranges magnetic sleeve pipe 4, pulse electromagnetic field Sterilizers 3 is communicated with Photocatalyst sterilization device 5, install ultraviolet lamp tube 15 and photochemical catalysis rod 16 in Photocatalyst sterilization device 5, Photocatalyst sterilization device 5 is communicated with electrolysis current stabilizer 6, electrolysis current stabilizer 6 sets out water pipe 7.Sewage flows through water inlet pipe 2 successively, pulse electromagnetic field Sterilizers 3, Photocatalyst sterilization device 5 and electrolysis current stabilizer 6, finally flow out from rising pipe 7, effluent stream is when water inlet pipe 2, electromotive force can be produced, make lattice refinement, the particle diameter of the brilliant particle of the dirt namely in sewage significantly reduces (to find in experiment that effluent stream is after water inlet pipe 2, wherein particle diameter can be down to 0.22 micron at the particle diameter of the brilliant particle of the dirt of 39 microns, and it is faster to have flow velocity, the electromotive force produced is larger, the feature that dirty brilliant thinning effect is better), thus reach antiscale, scale removal object, guarantee inner non flouling behaviour in the utility model operational process, ensure system stable operation, good running environment is provided for follow-up system runs, during the magnetic field that effluent stream produces through magnetic sleeve pipe 4, in sewage, microbial cell osmotic pressure changes, microorganism cells is broken, cell stops breeding, reach sterilization, the effect of algae removal, ordered arrangement is formed under the action of a magnetic field that water molecules in sewage can also produce at magnetic sleeve pipe 4, produce magnetization, be conducive to strengthening electric conductivity, and then strengthen the sterilising effect of next step pulse electromagnetic field Sterilizers 3, after sewage enters pulse electromagnetic field Sterilizers 3, the Electric and magnetic fields alternating action of pulses generation, microorganism cells membrane permeability in sewage is increased, film toughness weakens, material outflow in film, the outer material of film infiltrates, cause organism thalline dead, electromagnetic field produces ionizing event, normal bio chemical reaction and the metabolism of organism cytolemma are blocked, organism bacterium substance in vivo is changed, ring-type, many rings, backbone is broken as short chain and even unit molecule structure, for the Photocatalyst sterilization device 5 of next stage provides excellent running environment, the effect of the photochemical catalytic oxidation of photocatalyst can be made more remarkable, after sewage enters Photocatalyst sterilization device 5, because the ring-type of residual organic substances thalline in water, many rings, backbone have been broken to as short chain or unit molecule structure, therefore the photochemical catalytic oxidation efficiency of photocatalyst system can be promoted at double compared with existing independently photocatalyst system, realizes existing photocatalyst sterilizing that sewage disposal device is beyond one's reach, algae removal efficiency, after sewage enters electrolysis current stabilizer 6, current are steady gradually in electrolysis current stabilizer 6, and the organism in sewage electrochemical reaction occurs in electrolysis current stabilizer 6 and is degraded, and realizes dirty water purification.The utility model achieves mass disposal petrochemical industry organic waste water by the technique means of pure physics, thoroughly solve chemical treatment means inevitably to produce secondary pollution, repeat the problem of corroding and to the healthy threat caused of operator, simultaneously the utility model also has the advantages such as working cost is low, volume is little, can dispose of sewage continuously.For improving sewage treatment capacity further, multistage water inlet pipe 2, pulse electromagnetic field Sterilizers 3, Photocatalyst sterilization device 5 and electrolysis current stabilizer 6 also can be combined by the mode of serial or parallel connection by the utility model, thus reach the object strengthening wastewater treatment efficiency further, improve sewage treating efficiency.
Pulse electromagnetic field Sterilizers 3 described in the utility model can adopt various structures, wherein preferred structure is: described pulse electromagnetic field Sterilizers 3 comprises feed-water end housing 8 and water side housing 9, dividing plate 10 is set between feed-water end housing 8 and water side housing 9, dividing plate 10 is installed cathode sleeve 11, cathode sleeve 11 two ends lay respectively in feed-water end housing 8 and water side housing 9, cathode sleeve 11 in feed-water end housing 8 arranges flow inlet 12, cathode sleeve 11 in water side housing 9 arranges water export 13, shaft core position in cathode sleeve 11 installs conductive anode rod 14, the external diameter of conductive anode rod 14 is less than the internal diameter of cathode sleeve 11.During use, pulse electromagnetic field is produced by electric current between cathode sleeve 11 and conductive anode rod 14, after sewage enters pulse electromagnetic field Sterilizers 3 from feed-water end housing 8, the water export 13 on cathode sleeve 11 is flowed to from the flow inlet 12 cathode sleeve 11, finally flow out pulse electromagnetic field Sterilizers 3 from water side housing 9, sewage is when flowing through cathode sleeve 11 and being inner, the Electric and magnetic fields alternating action of pulses generation, microorganism cells membrane permeability in sewage is increased, film toughness weakens, material outflow in film, the outer material of film infiltrates, cause organism thalline dead, electromagnetic field produces ionizing event, normal bio chemical reaction and the metabolism of organism cytolemma are blocked, organism bacterium substance in vivo is changed, ring-type, many rings, backbone is broken as short chain and even unit molecule structure, for the Photocatalyst sterilization device 5 of next stage provides excellent running environment, dividing plate 10 is formed and intercepts between feed-water end housing 8 and water side housing 9, prevent sewage when directly flowing out pulse electromagnetic field Sterilizers 3 without when pulse electromagnetic field process.This structure can force whole sewage all to pass through between pulse electromagnetic field, and this structure is convenient to arrange multiple water stream channel in pulse electromagnetic field Sterilizers 3, namely many group cathode sleeves 11 and conductive anode rod 14 are installed in pulse electromagnetic field Sterilizers 3, can realize the dispersion treatment of sewage like this, sterilising effect is better.In addition, described pulse electromagnetic field Sterilizers 3 described in the utility model also can adopt other various structures, such as cathode sleeve can be set in inner walls, in cathode sleeve, conductive anode rod etc. is installed, but these structures are all difficult to when processing sewage guarantee that whole sewage is all subject to electromagnetic field effect, also cannot realize the dispersion treatment of sewage, be difficult to the sterilising effect reaching preferred version.
The preferred structure of electrolysis current stabilizer 6 described in the utility model is: described electrolysis current stabilizer 6 comprises current stabilizer housing 17, current stabilizer housing 17 lower sidewall arranges water-in 18 and sewage draining exit 19, current stabilizer housing 17 side wall upper part sets out water pipe 7, current stabilizer housing 17 top arranges top cover 20, installing electrodes post 21 on top cover 20, electrode column 21 end is positioned at current stabilizer housing 17 bottom.This structure adopts overflow type water outlet, and organism residual after can making electrolytic sewage forms precipitation, again can rise by electrode column 21 electrolysis on current stabilizer housing 17 top with current after organism precipitation, ensures that wastewater purifying efficiency is excellent, stable.
The housing of Photocatalyst sterilization device 5 described in the utility model and the feed-water end housing 8 of pulse electromagnetic field Sterilizers 3 and water side housing 9 all preferably adopt horizontal type shell, ultraviolet lamp tube 15, photochemical catalysis rod 16, cathode sleeve 11 and conductive anode rod 14 be horizontal positioned all, this structure drainage flow resistance is minimum, and equipment cost is minimum.But when the utility model is used for the sewage disposal that saltiness is high, because sewage vertical direction concentration difference is larger, the situation that the treatment facility of horizontal type shell and horizontal positioned easily causes levels sewage disposal uneven, the phenomenon that electrode burns partially also can be caused when vertical direction concentration difference is excessive, therefore when the sewage disposal high to saltiness, the housing of Photocatalyst sterilization device 5 and the feed-water end housing 8 of pulse electromagnetic field Sterilizers 3 and water side housing 9 need adopt upright shell, simultaneously by ultraviolet lamp tube 15, photochemical catalysis rod 16, cathode sleeve 11 is arranged with conductive anode rod 14 is all vertical, to overcome the negative impact that sewage vertical direction concentration difference is brought, but the resistance to flow of equipment cost and sewage can rise thereupon.
The utility model is prevent the magnetic field of magnetic sleeve pipe 4 outside diffusion from causing electromagnetic pollution to automatically controlled part of the present utility model and periphery miscellaneous equipment, can arrange magnetic shield cover 22 at magnetic sleeve pipe 4 periphery wall.
Claims (6)
1. the oil-field flooding of electromagnetism catalyzed oxidation and waste disposal plant, it is characterized in that: comprise base (1), base (1) is installed into water pipe (2), water inlet pipe (2) is communicated with pulse electromagnetic field Sterilizers (3), the tube wall periphery of water inlet pipe (2) arranges magnetic sleeve pipe (4), pulse electromagnetic field Sterilizers (3) is communicated with Photocatalyst sterilization device (5), in Photocatalyst sterilization device (5), ultraviolet lamp tube (15) and photochemical catalysis rod (16) are installed, Photocatalyst sterilization device (5) is communicated with electrolysis current stabilizer (6), electrolysis current stabilizer (6) sets out water pipe (7).
2. electromagnetism catalyzed oxidation according to claim 1 oil-field flooding and waste disposal plant, it is characterized in that: described pulse electromagnetic field Sterilizers (3) comprises feed-water end housing (8) and water side housing (9), dividing plate (10) is set between feed-water end housing (8) and water side housing (9), dividing plate (10) is installed cathode sleeve (11), cathode sleeve (11) two ends lay respectively in feed-water end housing (8) and water side housing (9), cathode sleeve (11) in feed-water end housing (8) arranges flow inlet (12), cathode sleeve (11) in water side housing (9) arranges water export (13), shaft core position in cathode sleeve (11) installs conductive anode rod (14), the external diameter of conductive anode rod (14) is less than the internal diameter of cathode sleeve (11).
3. electromagnetism catalyzed oxidation according to claim 1 oil-field flooding and waste disposal plant, it is characterized in that: described electrolysis current stabilizer (6) comprises current stabilizer housing (17), current stabilizer housing (17) lower sidewall arranges water-in (18) and sewage draining exit (19), current stabilizer housing (17) side wall upper part sets out water pipe (7), current stabilizer housing (17) top arranges top cover (20), the upper installing electrodes post (21) of top cover (20), electrode column (21) end is positioned at current stabilizer housing (17) bottom.
4. electromagnetism catalyzed oxidation according to claim 1 oil-field flooding and waste disposal plant, it is characterized in that: the housing of described Photocatalyst sterilization device (5) is Horizontal tubular housing, ultraviolet lamp tube (15) and photochemical catalysis rod (16) all horizontal positioned in the housing of Photocatalyst sterilization device (5).
5. electromagnetism catalyzed oxidation according to claim 2 oil-field flooding and waste disposal plant, it is characterized in that: feed-water end housing (8) and the water side housing (9) of described pulse electromagnetic field Sterilizers (3) are Horizontal tubular housing, cathode sleeve (11) and conductive anode rod (14) all horizontal positioned.
6. electromagnetism catalyzed oxidation according to claim 1 oil-field flooding and waste disposal plant, is characterized in that: magnetic sleeve pipe (4) periphery wall arranges magnetic shield cover (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420641535.2U CN204162562U (en) | 2014-10-31 | 2014-10-31 | The oil-field flooding of electromagnetism catalyzed oxidation and waste disposal plant |
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| CN201420641535.2U CN204162562U (en) | 2014-10-31 | 2014-10-31 | The oil-field flooding of electromagnetism catalyzed oxidation and waste disposal plant |
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| CN204162562U true CN204162562U (en) | 2015-02-18 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104291512A (en) * | 2014-10-31 | 2015-01-21 | 李伟东 | Device for treating oilfield reinjection water and sewage through electromagnetic catalytic oxidation |
-
2014
- 2014-10-31 CN CN201420641535.2U patent/CN204162562U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104291512A (en) * | 2014-10-31 | 2015-01-21 | 李伟东 | Device for treating oilfield reinjection water and sewage through electromagnetic catalytic oxidation |
| CN104291512B (en) * | 2014-10-31 | 2016-08-24 | 李伟东 | Electromagnetism catalysis oxidation oil-field flooding and sewage-treatment plant |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20191011 Address after: 250022 No. 8, West Street, Ying Ying, Ji'nan, Shandong Patentee after: Ji'nan Tai Reed Environmental Technology Co., Ltd. Address before: Ying Shi Xi Jie, Huaiyin District of Ji'nan city of Shandong Province, No. 8 250022 Patentee before: Li Wei Dong |
|
| TR01 | Transfer of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Device for treating oilfield reinjection water and sewage through electromagnetic catalytic oxidation Effective date of registration: 20200424 Granted publication date: 20150218 Pledgee: Branches of Jinan Rural Commercial Bank Co., Ltd. Pledgor: Ji'nan Tai Reed Environmental Technology Co., Ltd. Registration number: Y2020980001748 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |