CN204224540U - Photomagnetoelectric complementary four phase efficient cyclones - Google Patents

Photomagnetoelectric complementary four phase efficient cyclones Download PDF

Info

Publication number
CN204224540U
CN204224540U CN201420681562.2U CN201420681562U CN204224540U CN 204224540 U CN204224540 U CN 204224540U CN 201420681562 U CN201420681562 U CN 201420681562U CN 204224540 U CN204224540 U CN 204224540U
Authority
CN
China
Prior art keywords
oil
tube
water
separating tank
horizontal separating
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.)
Expired - Fee Related
Application number
CN201420681562.2U
Other languages
Chinese (zh)
Inventor
岳爱东
刘韬
王钊
王刚
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201420681562.2U priority Critical patent/CN204224540U/en
Application granted granted Critical
Publication of CN204224540U publication Critical patent/CN204224540U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model is a kind of photomagnetoelectric complementary four phase efficient cyclones, belongs to oil vapor treatment and oily water separation technique field.This separator comprises the horizontal separating tank of seat supports and the multifunctional separator of side, top setting thereof, what the gas collection is communicated with multifunctional separator pipeline that opposite side is arranged exported that tank and bottom arrange between two parties restrain by vacuum and horizontal separating tank seals the vacuum cumulative reactor of UNICOM and the three-dimensional transmitted light condensor that arranges of focus point thereof and reflected light condensor, wherein horizontal separating tank inner chamber arranges multi-functional separate chamber from left to right, first profit deversoir, current stabilization settling pocket, collection sand hopper, the drainage tube be connected with inversion eddy flow umbrella, second profit deversoir and the purification hydroecium purifying grease chamber and regulated and controled by water-oil interface variable valve.This separator has dynamic hydrocyclone, electro-dewatering, thermo-chemical demulsification, gravity settling, the multiple separation function of vortex coagulation, good separating effect, consumes energy low, is the update separating device of crude oil process.

Description

Photomagnetoelectric complementary four phase efficient cyclones
Technical field
The utility model is a kind of photomagnetoelectric complementary four phase efficient cyclones, belongs to oil vapor treatment and oily water separation technique field.
Background technology
In oil-field development, along with the prolongation of Development life, crude oil water content is more and more higher, and free gas, silt particle mix in addition, have impact on Oil extraction and subsequent purification process.Oil-water mixture is degassed, dehydration, sand fallout, treatment process is numerous and diverse, cost is high, energy consumption is large, becomes and restricts the important factor of cost for oil production.
Oil conventional both at home and abroad, gas, water, sand treatment process mainly contain gravity settling, cyclonic separation, electro-dewatering, chemical demulsification etc., and above-mentioned treatment process solves oil purification problem preferably, but also there is larger technology limitation.
Treatment effect is best in theory for the conbined usage of gravity settling and chemical demulsification, but limits by the capacity of on-the-spot container, can not have enough settling times, have impact on treatment effect; The many tank flow velocitys that enters by gas-oil mixture of cyclonic separation realize eddy flow, and separating effect is limited; Electro-dewatering oil-water separation is better, but power consumption is high, and processing cost remains high.
How to capture the limitation of the technology bottleneck of above-mentioned many profit treatment processs, become a difficult problem urgently to be resolved hurrily.
For the many contradictions of above-mentioned restriction profit process, the utility model has carried out following innovation by the advantage and defect analyzing the above-mentioned all kinds of profit treatment process of contrast:
1. being changed into mouth pressure cyclonic separation is that inlet pressure forces high-speed rotational to be separated with motor rotation, can improve centrifugal separating effect by decades of times.
2. the self power generation of innovation strong magnetic rotation stream heats and normal temperature chemical demulsification is optimized for thermo-chemical demulsification, and oil-water separation rises at double.
3. innovate strong magnetic rotation stream self power generation arc-over dewatering process, on the basis that treatment effect significantly improves, grid electricity fee cost declines at double.
4. vortex coagulation device can improve oil-water separation greatly.
5. innovation vacuum cumulative reactor and the self power generation of strong magnetic rotation stream heat coupling technique, while optimization profit treatment effect, achieve heating crude oil, simplify the heating procedure at oil vapor treatment station.
Summary of the invention
The purpose of this utility model integrates multiple oil, gas, water, sand separation technology and the superconducting heat transfer technology such as cyclonic separation, gravity settling, strong magnetic rotation stream self power generation electro-dewatering, thermo-chemical demulsification, vortex coagulation and Photospot solar, while realization oil, gas, water, sand high efficiency separation, realize mixed solution heating, for oil field a kind of high-level efficiency is provided, low consumed mixing oil four is separated treatment unit.
Working process of the present utility model and principle are:
1., when oil-water mixture flows through multifunctional separator cyclonic separation umbrella, under the combined action of hydrodynamic force and external electric motor, realize high-speed rotational one-level gas-oil separation, isolated gas enters gas collection header through a mist catching cover;
2. oil, water, sand is got rid of at a high speed sinks to cyclonic separation umbrella edge gravity, is heated, the emulsion splitter Homogeneous phase mixing added with ratio dosing pump by strong magnetic rotation stream self-generating device, realizes the oily water separation of second time thermo-chemical demulsification;
3. strong magnetic rotation stream self-generating device arc-over, realizes third time electro-dewatering oily water separation;
4. the mixed solution after degassed flows out vortex coagulation cover, realizes the 4th gas-oil separation;
5. the mixed solution after degassed flows through is inverted baffling umbrella, realize the 5th oil and gas and water from;
6. the mixed solution after degassed is turned back and is flowed through waved plate labyrinth, realize the 6th oil and gas and water from;
7. the mixed solution after multi-functional separating treatment flows through current stabilization settling pocket through the first profit deversoir, realizes the 7th oil, gas, water, sand separation;
8. after layering density the lightest gas enter gas collection header through second and third mist catching cover, a small amount of profit flows into the oil reservoir of bottom and water layer along drainage tube;
9. the self-cleaning oil that after layering, density is slightly heavy enters purification grease chamber through the second profit deversoir and concentrates outer defeated;
10. the water that after layering, density is heavier enters purification hydroecium regularly outer row through the second profit deversoir;
The silt particle that after 11. layerings, density is maximum sinks at the bottom of horizontal separating tank tank, is washed to collection sand hopper regularly outer row along slope.
Technical solution of the present utility model is:
Described photomagnetoelectric complementary four phase efficient cyclones comprise the horizontal separating tank of seat supports and the multifunctional separator 1 of side, top setting thereof, what opposite side was arranged seals the vacuum cumulative reactor 8 of UNICOM and the three-dimensional transmitted light condensor 6 that arranges of focus point thereof and reflected light condensor 7 with multifunctional separator 1 gas collection that pipeline is communicated with restraining by vacuum of exporting that tank 14 and bottom arrange between two parties and horizontal separating tank, and wherein horizontal separating tank inner chamber arranges multi-functional separate chamber from left to right first profit deversoir 5, current stabilization settling pocket collect sand hopper 9, drainage tube 10, the second profit deversoir 11 be connected with inversion eddy flow umbrella 13 and purify grease chamber with the purification hydroecium regulated and controled by water-oil interface variable valve 16
Let out slope under forming sand setting to exit end declivity 2-30 ° bottom described horizontal separating tank, two ends are sealed by manhole plate, and inner chamber arranges four weirs, Room two, and construction location and the shape on its weir, four Room two are respectively:
First multi-functional separate chamber
This room is positioned at below the multifunctional separator 1 of mixing oil import, comprise the inversion baffling umbrella 3 of lower band baffle pipe, waved plate labyrinth 4, mixing oil after degassed enters large space inversion baffling umbrella 3 through vortex coagulation cover 1-10 and continues gas-oil separation, then turn back through baffle pipe and enter waved plate labyrinth 4, realize oil, gas, water, sand separation layering by vortex coagulation.
Second current stabilization settling pocket
This room is positioned at horizontal separating tank large space stage casing, the built-in flange-cooled vacuum tube bank of pipe outer round surface playing the effect of rectification current stabilization, vacuum is restrained the vacuum cumulative reactor 8 external with horizontal separating tank and is sealed UNICOM, and wherein vacuum is restrained external radiator element and is at least one of following three types:
The horizontal sheet radiator element that the first is heat conduction of holding concurrently, rectification is separated delamination with oil, gas, water;
The waved plate thin slice radiator element that the second is double heat conduction, rectification is separated delamination with oil, gas, water;
The honeycomb shape sheet radiator element that the third is heat conduction of holding concurrently, rectification is separated delamination with oil, gas, water.
3rd purification grease chamber
It is that the longitudinal sealing laterally cut off cuts off side that this room is positioned at horizontal separating tank end with the second profit deversoir 11, and its underpart connects self-cleaning oil delivery valve.
4th purification hydroecium
It is that the longitudinal sealing laterally cut off cuts off opposite side that this room is positioned at horizontal separating tank end with the second profit deversoir 11, its underpart connects delivery valve of purifying waste water, and the water-oil interface variable valve 16 that low level treated water outlet pipe end is arranged connects the control device manually or automatically outside horizontal separating tank with leading screw.
First profit deversoir 5
This weir is positioned at waved plate labyrinth 4 afterbody, and its moisture head piece low level is concordant with horizontal separation tank bottom, and oil content head piece is a little more than water-oil interface in horizontal separating tank.
Second profit deversoir 11
After this weir is positioned at collection sand hopper, its moisture head piece low level is high-end higher than collection sand hopper 9, and oil content head piece is higher than the first profit deversoir 5 oil content head piece.
Described multifunctional separator 1 is for being placed in the oil of horizontal separating tank head end, gas, water, sand pretreatment unit, comprises the central shaft 1-7 that tank body 1-4 inner chamber is fixed by centre bearing, the permanent magnet clutch 1-3 that central shaft 1-7 is arranged from top to bottom, a mist catching cover 1-5, cyclonic separation umbrella 1-6, kicker magnet ring 1-8, sleeve type combination mouse cage 1-9, the electric motor 1-1 of the outside overhead of vortex coagulation cover 1-10, tank body 1-4, the liquid feed valve 1-11 arranged between a vapor pipe 1-2 and mist catching cover 1-5 and cyclonic separation umbrella 1-6, the chemical feed pipe 1-12 that cyclonic separation umbrella 1-6 bottom is arranged, the cyclonic separation umbrella 1-6 wherein central shaft 1-7 arranged is one or more levels, and what this cyclonic separation umbrella 1-6 and central shaft 1-7 was set with presses N, the sleeve type combination mouse cage 1-9 that the kicker magnet ring 1-8 that S polarity is stacked alternately and kicker magnet ring 1-8 periphery is arranged is that strong magnetic rotation stream self power generation four-in-one heats tripping device, the motor power that the cyclone water power provided by liquid feed valve 1-11 and electric motor 1-1 are provided by permanent magnet clutch 1-3 noncontact transmission combines driving, realizes high-speed rotational and is separated, electro-dewatering, the self power generation of strong magnetic rotation stream heats, thermo-chemical demulsification oily water separation.
Described gas collection exports tank 14 for being placed in the secondary oil gas isolation of purified tank of horizontal separating tank end, its underpart pipeline is communicated with the vapor pipe 1-2 of multifunctional separator 1, inner chamber bottom arranges the secondary mist catching cover 12 be communicated with horizontal separating tank, arrange on secondary mist catching cover 12 and be inverted eddy flow umbrella 13, be inverted eddy flow umbrella 13 top and three mist catching covers 15 are set, the tank body top on three mist catching cover 15 tops arranges the outlet pipe valve being communicated with outside gathering pipeline, wherein be inverted eddy flow umbrella 13 to fix with the centre bearing of central shaft and secondary mist catching cover 12 and three mist catching covers 15, sieve aperture opened by the drainage tube that central shaft stretches in horizontal separating tank below water-oil interface.
Described vacuum cumulative reactor 8 is for being placed in the spherical kettle of outside, horizontal separating tank stage casing, this still top arranges the vacuum tube bank sealing and stretch in horizontal separating tank, and vacuum is restrained each single tube outer round surface and arranged the radiator element that heat conduction, rectification and oil, gas, water are separated delamination; This still inner chamber fills superconduction working medium; Transmitted light condensor 6 and reflected light condensor 7 is moved with the twin shaft that this still is arranged with daylight level of synchronization circumferential motion and vertical circular motion for focus point three-dimensional.
Described kicker magnet ring 1-8 is for being sleeved on even numbered blocks rare-earth permanent magnet ring central shaft 1-7 providing strong magnetic rotation magnetic field, or the hollow rare earth permanent magnet scapus of monolithic, and its magnetizing direction is radial, and the set-up mode of even numbered blocks rare-earth permanent magnet ring is axially stacked.
Described sleeve type combination mouse cage 1-9 is high resistant non-magnet material, axially be set with in magnetic line of force range of influence, form coaxial many mouse cages electrification heat-producing unit, suit spacing 0.5-3mm, water hole is outputed in each mouse cage bottom circumferentially symmetry, and its structure formation is at least one of following Four types:
The first is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the straight slit of the closed at both ends of closed conductor or plagioclase to stitch or straight elongated hole;
The second is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the needle-like corona discharge cone point of the closed at both ends of closed conductor;
The third is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the spination arc-over cone point of the closed at both ends of closed conductor;
4th kind is co-axial shafts to the concentric tube of suit, in parallel mutually between tube and tube, and on tube wall, symmetrical open form becomes the straight slit of the closed at both ends of closed conductor or plagioclase seam or straight elongated hole or needle-like corona discharge cone point or spination arc-over cone point.
Adopt above technical scheme, the utility model has high-speed rotational separation, electro-dewatering, thermo-chemical demulsification, gravity settling, the multiple separation function of vortex coagulation, good separating effect, consumes energy low, is the update separating device of crude oil process.
Accompanying drawing explanation
Fig. 1 is photomagnetoelectric complementary four phase efficient cyclone structural representations;
Fig. 2 is the multifunctional separator structural representation of Fig. 1.
In figure:
1. multifunctional separator; 2. ratio dosing pump; 3. be inverted baffling umbrella; 4. waved plate labyrinth; 5. the first profit deversoir; 6. transmitted light condensor; 7. reflected light condensor; 8. vacuum cumulative reactor; 9. collect sand hopper; 10. drainage tube; 11. second profit deversoirs; 12. 2 mist catching covers; 13. are inverted eddy flow umbrella; 14. gas collections export tank; 15. 3 mist catching covers; 16. water-oil interface variable valve.
Wherein four Room of horizontal separating tank inner chamber are:
multi-functional separate chamber; purification grease chamber; purification hydroecium.
The each component names of multifunctional separator 1 and reference numerals are:
1-1. electric motor; 1-2. vapor pipe; 1-3. permanent magnet clutch; 1-4. tank body; 1-5. mist catching cover; 1-6. cyclonic separation umbrella; 1-7. central shaft; 1-8. kicker magnet ring; 1-9. sleeve type combination mouse cage; 1-10. vortex coagulation cover; 1-11. liquid feed valve; 1-12. chemical feed pipe.
Embodiment
As depicted in figs. 1 and 2: photomagnetoelectric complementary four phase efficient cyclones described in the utility model comprise the horizontal separating tank of seat supports and the multifunctional separator 1 of side, top setting thereof, what opposite side was arranged seals the vacuum cumulative reactor 8 of UNICOM and the three-dimensional transmitted light condensor 6 that arranges of focus point thereof and reflected light condensor 7 with multifunctional separator 1 gas collection that pipeline is communicated with restraining by vacuum of exporting that tank 14 and bottom arrange between two parties and horizontal separating tank, and wherein horizontal separating tank inner chamber arranges multi-functional separate chamber from left to right first profit deversoir 5, current stabilization settling pocket collect sand hopper 9, drainage tube 10, the second profit deversoir 11 be connected with inversion eddy flow umbrella 13 and purify grease chamber with the purification hydroecium regulated and controled by water-oil interface variable valve 16
Let out slope under forming sand setting to exit end declivity 2-30 ° bottom described horizontal separating tank, two ends are sealed by manhole plate, and inner chamber arranges four weirs, Room two, and construction location and the shape on its weir, four Room two are respectively:
First multi-functional separate chamber
This room is positioned at below the multifunctional separator 1 of mixing oil import, comprise the inversion baffling umbrella 3 of lower band baffle pipe, waved plate labyrinth 4, mixing oil after degassed enters large space inversion baffling umbrella 3 through vortex coagulation cover 1-10 and continues gas-oil separation, then turn back through baffle pipe and enter waved plate labyrinth 4, realize oil, gas, water, sand separation layering by vortex coagulation.
Second current stabilization settling pocket
This room is positioned at horizontal separating tank large space stage casing, the built-in flange-cooled vacuum tube bank of pipe outer round surface playing the effect of rectification current stabilization, vacuum is restrained the vacuum cumulative reactor 8 external with horizontal separating tank and is sealed UNICOM, and wherein vacuum is restrained external radiator element and is at least one of following three types:
The horizontal sheet radiator element that the first is heat conduction of holding concurrently, rectification is separated delamination with oil, gas, water;
The waved plate thin slice radiator element that the second is double heat conduction, rectification is separated delamination with oil, gas, water;
The honeycomb shape sheet radiator element that the third is heat conduction of holding concurrently, rectification is separated delamination with oil, gas, water.
3rd purification grease chamber
It is that the longitudinal sealing laterally cut off cuts off side that this room is positioned at horizontal separating tank end with the second profit deversoir 11, and its underpart connects self-cleaning oil delivery valve.
4th purification hydroecium
It is that the longitudinal sealing laterally cut off cuts off opposite side that this room is positioned at horizontal separating tank end with the second profit deversoir 11, its underpart connects delivery valve of purifying waste water, and the water-oil interface variable valve 16 that low level treated water outlet pipe end is arranged connects the control device manually or automatically outside horizontal separating tank with leading screw.
First profit deversoir 5
This weir is positioned at waved plate labyrinth 4 afterbody, and its moisture head piece low level is concordant with horizontal separation tank bottom, and oil content head piece is a little more than water-oil interface in horizontal separating tank.
Second profit deversoir 11
After this weir is positioned at collection sand hopper, its moisture head piece low level is high-end higher than collection sand hopper 9, and oil content head piece is higher than the first profit deversoir 5 oil content head piece.
Described multifunctional separator 1 is for being placed in the oil of horizontal separating tank head end, gas, water, sand pretreatment unit, comprises the central shaft 1-7 that tank body 1-4 inner chamber is fixed by centre bearing, the permanent magnet clutch 1-3 that central shaft 1-7 is arranged from top to bottom, a mist catching cover 1-5, cyclonic separation umbrella 1-6, kicker magnet ring 1-8, sleeve type combination mouse cage 1-9, the electric motor 1-1 of the outside overhead of vortex coagulation cover 1-10, tank body 1-4, the liquid feed valve 1-11 arranged between a vapor pipe 1-2 and mist catching cover 1-5 and cyclonic separation umbrella 1-6, the chemical feed pipe 1-12 that cyclonic separation umbrella 1-6 bottom is arranged, the cyclonic separation umbrella 1-6 wherein central shaft 1-7 arranged is one or more levels, and what this cyclonic separation umbrella 1-6 and central shaft 1-7 was set with presses N, the sleeve type combination mouse cage 1-9 that the kicker magnet ring 1-8 that S polarity is stacked alternately and kicker magnet ring 1-8 periphery is arranged is that strong magnetic rotation stream self power generation four-in-one heats tripping device, the motor power that the cyclone water power provided by liquid feed valve 1-11 and electric motor 1-1 are provided by permanent magnet clutch 1-3 noncontact transmission combines driving, realizes high-speed rotational and is separated, electro-dewatering, the self power generation of strong magnetic rotation stream heats, thermo-chemical demulsification oily water separation.
Described gas collection exports tank 14 for being placed in the secondary oil gas isolation of purified tank of horizontal separating tank end, its underpart pipeline is communicated with the vapor pipe 1-2 of multifunctional separator 1, inner chamber bottom arranges the secondary mist catching cover 12 be communicated with horizontal separating tank, arrange on secondary mist catching cover 12 and be inverted eddy flow umbrella 13, be inverted eddy flow umbrella 13 top and three mist catching covers 15 are set, the tank body top on three mist catching cover 15 tops arranges the outlet pipe valve being communicated with outside gathering pipeline, wherein be inverted eddy flow umbrella 13 to fix with the centre bearing of central shaft and secondary mist catching cover 12 and three mist catching covers 15, sieve aperture opened by the drainage tube that central shaft stretches in horizontal separating tank below water-oil interface.
Described vacuum cumulative reactor 8 is for being placed in the spherical kettle of outside, horizontal separating tank stage casing, this still top arranges the vacuum tube bank sealing and stretch in horizontal separating tank, and vacuum is restrained each single tube outer round surface and arranged the radiator element that heat conduction, rectification and oil, gas, water are separated delamination; This still inner chamber fills superconduction working medium; Transmitted light condensor 6 and reflected light condensor 7 is moved with the twin shaft that this still is arranged with daylight level of synchronization circumferential motion and vertical circular motion for focus point three-dimensional.
Described kicker magnet ring 1-8 is for being sleeved on even numbered blocks rare-earth permanent magnet ring central shaft 1-7 providing strong magnetic rotation magnetic field, or the hollow rare earth permanent magnet scapus of monolithic, and its magnetizing direction is radial, and the set-up mode of even numbered blocks rare-earth permanent magnet ring is axially stacked.
Described sleeve type combination mouse cage 1-9 is high resistant non-magnet material, axially be set with in magnetic line of force range of influence, form coaxial many mouse cages electrification heat-producing unit, suit spacing 0.5-3mm, water hole is outputed in each mouse cage bottom circumferentially symmetry, and its structure formation is at least one of following Four types:
The first is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the straight slit of the closed at both ends of closed conductor or plagioclase to stitch or straight elongated hole;
The second is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the needle-like corona discharge cone point of the closed at both ends of closed conductor;
The third is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the spination arc-over cone point of the closed at both ends of closed conductor;
4th kind is co-axial shafts to the concentric tube of suit, in parallel mutually between tube and tube, and on tube wall, symmetrical open form becomes the straight slit of the closed at both ends of closed conductor or plagioclase seam or straight elongated hole or needle-like corona discharge cone point or spination arc-over cone point.
Described photomagnetoelectric complementary four phase efficient cyclone design variables are:
Process liquid measure: 200-1000 × 10 3m 3/ d
Process tolerance: 20-100 × 10 3m 3/ d (0.6MPa)
Outlet crude oil rate: < 0.005g/M 3;
Outlet sewage with oil rate: < 200mg/L;
Overall dimensions: ∮ 3m × L20m.
Adopt above technical scheme, the utility model has dynamic hydrocyclone, electro-dewatering, thermo-chemical demulsification, gravity settling, the multiple separation function of vortex coagulation, good separating effect, consumes energy low, is the update separating device of crude oil process.

Claims (7)

1. photomagnetoelectric complementary four phase efficient cyclones, it is characterized in that: this separator comprises the horizontal separating tank of seat supports and the multifunctional separator (1) of side, top setting thereof, what opposite side was arranged seals the vacuum cumulative reactor (8) of UNICOM and the three-dimensional transmitted light condensor (6) that arranges of focus point thereof and reflected light condensor (7) with multifunctional separator (1) gas collection that pipeline is communicated with restraining by vacuum of exporting that tank (14) and bottom arrange between two parties and horizontal separating tank, wherein horizontal separating tank inner chamber arranges multi-functional separate chamber from left to right , the first profit deversoir (5), current stabilization settling pocket , collection sand hopper (9), with inversion eddy flow umbrella (13) drainage tube (10), the second profit deversoir (11) that are connected and purify grease chamber with the purification hydroecium regulated and controled by water-oil interface variable valve (16) .
2. photomagnetoelectric complementary four phase efficient cyclones according to claim 1, it is characterized in that: under forming sand setting to exit end declivity 2-30 ° bottom described horizontal separating tank, let out slope, two ends are sealed by manhole plate, inner chamber arranges four weirs, Room two, and construction location and the shape on its weir, four Room two are respectively:
First multi-functional separate chamber
This room is positioned at multifunctional separator (1) below of mixing oil import, comprise the inversion baffling umbrella (3) of lower band baffle pipe, waved plate labyrinth (4), mixing oil after degassed enters large space through vortex coagulation cover (1-10) and is inverted baffling umbrella (3) continuation gas-oil separation, then turn back through baffle pipe and enter waved plate labyrinth (4), realize oil, gas, water, sand separation layering by vortex coagulation;
Second current stabilization settling pocket
This room is positioned at horizontal separating tank large space stage casing, the built-in flange-cooled vacuum tube bank of pipe outer round surface playing the effect of rectification current stabilization, vacuum is restrained the vacuum cumulative reactor (8) external with horizontal separating tank and is sealed UNICOM, and wherein vacuum is restrained external radiator element and is at least one of following three types:
The horizontal sheet radiator element that the first is heat conduction of holding concurrently, rectification is separated delamination with oil, gas, water;
The waved plate thin slice radiator element that the second is double heat conduction, rectification is separated delamination with oil, gas, water;
The honeycomb shape sheet radiator element that the third is heat conduction of holding concurrently, rectification is separated delamination with oil, gas, water;
3rd purification grease chamber
It is that the longitudinal sealing laterally cut off cuts off side that this room is positioned at horizontal separating tank end with the second profit deversoir (11), and its underpart connects self-cleaning oil delivery valve;
4th purification hydroecium
It is that the longitudinal sealing laterally cut off cuts off opposite side that this room is positioned at horizontal separating tank end with the second profit deversoir (11), its underpart connects delivery valve of purifying waste water, and the water-oil interface variable valve (16) that low level treated water outlet pipe end is arranged connects the control device manually or automatically outside horizontal separating tank with leading screw;
First profit deversoir (5)
This weir is positioned at waved plate labyrinth (4) afterbody, and its moisture head piece low level is concordant with horizontal separation tank bottom, and oil content head piece is a little more than water-oil interface in horizontal separating tank;
Second profit deversoir (11)
After this weir is positioned at collection sand hopper, its moisture head piece low level is high-end higher than collection sand hopper (9), and oil content head piece is higher than the first profit deversoir (5) oil content head piece.
3. photomagnetoelectric complementary four phase efficient cyclones according to claim 1, it is characterized in that: described multifunctional separator (1) is for being placed in the oil of horizontal separating tank head end, gas, water, sand pretreatment unit, comprise the central shaft (1-7) that tank body (1-4) inner chamber is fixed by centre bearing, the permanent magnet clutch (1-3) that central shaft (1-7) is arranged from top to bottom, a mist catching cover (1-5), cyclonic separation umbrella (1-6), kicker magnet ring (1-8), sleeve type combination mouse cage (1-9), vortex coagulation cover (1-10), the electric motor (1-1) of tank body (1-4) outside overhead, vapor pipe (1-2) and the liquid feed valve (1-11) arranged between a mist catching cover (1-5) and cyclonic separation umbrella (1-6), the chemical feed pipe (1-12) that cyclonic separation umbrella (1-6) bottom is arranged, wherein the upper cyclonic separation umbrella (1-6) arranged of central shaft (1-7) is one or more levels, this cyclonic separation umbrella (1-6) and central shaft (1-7) be set with by N, the kicker magnet ring (1-8) that S polarity is stacked alternately and sleeve type combination mouse cage (1-9) that kicker magnet ring (1-8) periphery is arranged heat tripping device for strong magnetic rotation stream self power generation four-in-one, the motor power that the cyclone water power provided by liquid feed valve (1-11) and electric motor (1-1) are provided by permanent magnet clutch (1-3) noncontact transmission combines driving, realize high-speed rotational to be separated, electro-dewatering, the self power generation of strong magnetic rotation stream heats, thermo-chemical demulsification oily water separation.
4. photomagnetoelectric complementary four phase efficient cyclones according to claim 1, it is characterized in that: described gas collection exports tank (14) for being placed in the secondary oil gas isolation of purified tank of horizontal separating tank end, its underpart pipeline is communicated with the vapor pipe (1-2) of multifunctional separator (1), inner chamber bottom arranges the secondary mist catching cover (12) be communicated with horizontal separating tank, arrange on secondary mist catching cover (12) and be inverted eddy flow umbrella (13), be inverted eddy flow umbrella (13) top and three mist catching covers (15) are set, the tank body top on three mist catching cover (15) tops arranges the outlet pipe valve being communicated with outside gathering pipeline, wherein be inverted eddy flow umbrella (13) to fix with the centre bearing of central shaft and secondary mist catching cover (12) and three mist catching covers (15), sieve aperture opened by the drainage tube that central shaft stretches in horizontal separating tank below water-oil interface.
5. photomagnetoelectric complementary four phase efficient cyclones according to claim 1, it is characterized in that: described vacuum cumulative reactor (8) is for being placed in the spherical kettle of outside, horizontal separating tank stage casing, this still top arranges the vacuum tube bank sealing and stretch in horizontal separating tank, and vacuum is restrained each single tube outer round surface and arranged the radiator element that heat conduction, rectification and oil, gas, water are separated delamination; This still inner chamber fills superconduction working medium; Transmitted light condensor (6) and reflected light condensor (7) is moved with the twin shaft that this still is arranged with daylight level of synchronization circumferential motion and vertical circular motion for focus point three-dimensional.
6. according to claim 1 or photomagnetoelectric complementary four phase efficient cyclones according to claim 3, it is characterized in that: described kicker magnet ring (1-8) is for being sleeved on even numbered blocks rare-earth permanent magnet ring central shaft (1-7) providing strong magnetic rotation magnetic field, or the hollow rare earth permanent magnet scapus of monolithic, its magnetizing direction is radial, and the set-up mode of even numbered blocks rare-earth permanent magnet ring is axially stacked.
7. according to claim 1 or photomagnetoelectric complementary four phase efficient cyclones according to claim 3, it is characterized in that: described sleeve type combination mouse cage (1-9) is high resistant non-magnet material, axially be set with in magnetic line of force range of influence, form coaxial many mouse cages electrification heat-producing unit, suit spacing 0.5-3mm, water hole is outputed in each mouse cage bottom circumferentially symmetry, and its structure formation is at least one of following Four types:
The first is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the straight slit of the closed at both ends of closed conductor or plagioclase to stitch or straight elongated hole;
The second is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the needle-like corona discharge cone point of the closed at both ends of closed conductor;
The third is the concentric tube of co-axial shafts to suit, mutual insulating between tube and tube, and on tube wall, symmetrical open form becomes the spination arc-over cone point of the closed at both ends of closed conductor;
4th kind is co-axial shafts to the concentric tube of suit, in parallel mutually between tube and tube, and on tube wall, symmetrical open form becomes the straight slit of the closed at both ends of closed conductor or plagioclase seam or straight elongated hole or needle-like corona discharge cone point or spination arc-over cone point.
CN201420681562.2U 2014-11-15 2014-11-15 Photomagnetoelectric complementary four phase efficient cyclones Expired - Fee Related CN204224540U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420681562.2U CN204224540U (en) 2014-11-15 2014-11-15 Photomagnetoelectric complementary four phase efficient cyclones

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420681562.2U CN204224540U (en) 2014-11-15 2014-11-15 Photomagnetoelectric complementary four phase efficient cyclones

Publications (1)

Publication Number Publication Date
CN204224540U true CN204224540U (en) 2015-03-25

Family

ID=52922658

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420681562.2U Expired - Fee Related CN204224540U (en) 2014-11-15 2014-11-15 Photomagnetoelectric complementary four phase efficient cyclones

Country Status (1)

Country Link
CN (1) CN204224540U (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106152541A (en) * 2015-04-09 2016-11-23 王颖 Ten stove azeotropic de-carbons go out haze cumulative reacting furnace
CN109297951A (en) * 2018-08-29 2019-02-01 上海化工研究院有限公司 The high effect forced nebulization sampling system of Pneumatic constant pressure type for special spectrum analysis
CN109477581A (en) * 2016-12-21 2019-03-15 三井电气精机株式会社 Rotary body driving/sealing structure and including rotary body driving/sealing structure centrifugal separating device and centrifugal separation system
CN110856787A (en) * 2018-08-25 2020-03-03 江苏中远环保科技有限公司 Oil-gas separator
CN110860159A (en) * 2018-08-28 2020-03-06 江苏中远环保科技有限公司 Oil gas recovery and separation device
CN110860175A (en) * 2018-08-27 2020-03-06 江苏中远环保科技有限公司 Oil-gas separation and recovery method
CN110860160A (en) * 2018-08-28 2020-03-06 江苏中远环保科技有限公司 Centrifugal separation recovery unit
CN110860158A (en) * 2018-08-27 2020-03-06 江苏中远环保科技有限公司 Oil-gas separation method for tank body
CN112253088A (en) * 2020-10-20 2021-01-22 南宁学院 Oil-gas-water three-phase metering device

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106152541A (en) * 2015-04-09 2016-11-23 王颖 Ten stove azeotropic de-carbons go out haze cumulative reacting furnace
CN109477581A (en) * 2016-12-21 2019-03-15 三井电气精机株式会社 Rotary body driving/sealing structure and including rotary body driving/sealing structure centrifugal separating device and centrifugal separation system
CN110856787A (en) * 2018-08-25 2020-03-03 江苏中远环保科技有限公司 Oil-gas separator
CN110860175A (en) * 2018-08-27 2020-03-06 江苏中远环保科技有限公司 Oil-gas separation and recovery method
CN110860158A (en) * 2018-08-27 2020-03-06 江苏中远环保科技有限公司 Oil-gas separation method for tank body
CN110860159A (en) * 2018-08-28 2020-03-06 江苏中远环保科技有限公司 Oil gas recovery and separation device
CN110860160A (en) * 2018-08-28 2020-03-06 江苏中远环保科技有限公司 Centrifugal separation recovery unit
CN109297951A (en) * 2018-08-29 2019-02-01 上海化工研究院有限公司 The high effect forced nebulization sampling system of Pneumatic constant pressure type for special spectrum analysis
CN112253088A (en) * 2020-10-20 2021-01-22 南宁学院 Oil-gas-water three-phase metering device

Similar Documents

Publication Publication Date Title
CN204224540U (en) Photomagnetoelectric complementary four phase efficient cyclones
CN104028391B (en) Magnetic rotation flow separation method and magnetic rotation stream separator
CN202569782U (en) Centrifugal three-phase separator
CN104445681A (en) Screw type three-phase medium separator
CN202398157U (en) Double-sleeve combined solid-liquid separator
CN106746048A (en) A kind of efficient oil-contained waste water treatment device and method
CN109467208A (en) Sewage from catering business air flotation processing device
CN208726806U (en) Pipe type oil-water separator
CN203999038U (en) Cyclone-type water-and-oil separator
CN204386563U (en) Central fluid supply station many wells cluster U-shaped pipe extracting device of oil
CN204051082U (en) Bitubular screw plate oil-water separator
CN106669990B (en) Cyclone separator with inclined side cutting cyclone water inlet structure
CN105435489A (en) Whirl enhanced vertical oil water separating device with micro-channels and method
CN208414029U (en) A kind of oily waste water harmless resource processing technique equipment
CN207786141U (en) A kind of oily sludge glows steam gas-liquid separator
CN203155404U (en) Magnetic vortex separator
CN206799304U (en) A kind of sewage-treatment plant
CN206624732U (en) A kind of efficient oil-contained waste water treatment device
CN105198134B (en) Severe emulsifies oil-contaminated water processing method and its processing unit
CN109942172A (en) A kind of oil exploitation slurry filtering device
CN207903948U (en) Centering type oil-water separator
CN204107100U (en) Oily-water seperating equipment
CN102500136A (en) Combined cylindrical oil-water cyclone separating device
CN203155401U (en) Feeding distributor of horizontal screw sedimentation centrifuge
CN206069557U (en) Sewage treatment tank

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150325

Termination date: 20151115

EXPY Termination of patent right or utility model