CN102847345A - Oil-water automatic control separation device - Google Patents
Oil-water automatic control separation device Download PDFInfo
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- CN102847345A CN102847345A CN2012103587780A CN201210358778A CN102847345A CN 102847345 A CN102847345 A CN 102847345A CN 2012103587780 A CN2012103587780 A CN 2012103587780A CN 201210358778 A CN201210358778 A CN 201210358778A CN 102847345 A CN102847345 A CN 102847345A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 238000000926 separation method Methods 0.000 title claims abstract description 30
- 239000003814 drug Substances 0.000 claims abstract description 68
- 238000002156 mixing Methods 0.000 claims abstract description 38
- 238000010438 heat treatment Methods 0.000 claims abstract description 32
- 238000007689 inspection Methods 0.000 claims abstract description 14
- 239000002351 wastewater Substances 0.000 claims abstract description 8
- 235000019198 oils Nutrition 0.000 claims description 117
- 230000006698 induction Effects 0.000 claims description 23
- 230000002146 bilateral effect Effects 0.000 claims description 18
- 239000007788 liquid Substances 0.000 claims description 13
- 235000015927 pasta Nutrition 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 6
- 235000019476 oil-water mixture Nutrition 0.000 claims description 4
- 238000001802 infusion Methods 0.000 claims description 3
- 229910000831 Steel Inorganic materials 0.000 claims description 2
- 239000010959 steel Substances 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims 1
- 229940079593 drug Drugs 0.000 abstract description 2
- 238000007789 sealing Methods 0.000 abstract 2
- 239000003921 oil Substances 0.000 description 128
- 239000007789 gas Substances 0.000 description 21
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 16
- 230000000694 effects Effects 0.000 description 7
- 239000003345 natural gas Substances 0.000 description 7
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 238000010348 incorporation Methods 0.000 description 2
- 239000003129 oil well Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000406668 Loxodonta cyclotis Species 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000002343 natural gas well Substances 0.000 description 1
- 238000001935 peptisation Methods 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 238000012876 topography Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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Abstract
The invention discloses an oil-water automatic control separation device which comprises a cylinder and a device base, wherein an oil-water separation chamber and an oil storage tank are arranged inside the cylinder, and an oil-medicine secondary mixing tank is arranged inside the cylinder; a right protruding circular plate inverted triangular weir is arranged between the oil-medicine secondary mixing tank and the oil-water separation chamber; a left protruding circular plate inverted triangular weir is arranged between the oil storage tank and the oil-water separation chamber; a top cover of the cylinder is a horizontal circular sealing head; the middle of the circular sealing head is an inspection hole; the left side of the inspection hole is an exhaust pipe; and right side of the inspection hole is a medication adding room; semi-closed separation plates are evenly arranged in the oil-medicine secondary mixing tank; gas distribution pipes are evenly paved at the bottom of the oil-water separation chamber; a waste water discharge pipe and a manual control water discharge pipe are arranged at the bottom of the oil-water separation chamber simultaneously; a gas supply pipe of a heater is located in the device base, gas supply is provided by a gas collection tank; and then the gas is provided for a middle heating disc and a high-position heating disc through a heating disc gas supply branch pipe. The oil-water automatic control separation device is simple in structure, complex in distribution, high in space using ratio and simple to operate, and is capable of saving energy and reducing emission.
Description
Technical field
The present invention relates to the oily water separating equipment of field of petroleum exploitation, be specifically related to a kind of profit and automatically control separation equipment, this equipment integrates the functions such as separation, air supporting, automatically control, dosing, mixing, energy dissipating, is a kind of novel oil equipment for purifying.
Background technology
In recent years, because the energetically exploitation of China's oil, the water content in the oil grows with each passing day, and oil content is fewer and feweri.So that being faced with oil, each elephant company draws up that cost improves greatly in the oil water separation process that comes the later stage.Below be that example is further analyzed from the Oil Fields in North Shaanxi of China:
A, natural gas: North Shaanxi also is the important petroleum gas producing region of China except being the important oildom of China.But less because of the relative oil of its amount of natural gas, and oil well disperses, the factor such as with a varied topography causes and collects difficulty, thereby most natural gas just directly burns or emptying at well head.
B, water-oil separating technique and effect analysis
One, water-oil separating technique
Shown in accompanying drawing 1, the oil development enterprise of North Shaanxi mainly comprises brick wall bearing 01, the groove 02 of heating to the equipment of water-oil separating employing at present, oil storage tank 03, passage 04, oil guide pipe 05 and valve 06 etc. mainly contain two aspects for the separation of oil and the processing method of waste water:
(1) will draw up the oil-water direct that comes from oil well and connect into oil storage tank 03, because the density of oil is less than the density of water, oil floats on the surface, and by artificial Open valve 06, the water of oil storage tank 03 lower floor of draining is until see till the oil when getting rid of.In the winter time, because the winter temperature of northern Shensi at subzero about 20 ℃, therefore must adopt the groove 02 of heating to heat to oil storage tank 03 in winter, to guarantee that oil storage tank 03 turns round normally.The used energy of heating at present is coal, and its consumption is about 20 tons of every well points of per season.
(2) by pipeline each well point oil-water mixture is delivered directly to master station, carries out water-oil separating in master station.Because the complexity of northern Shensi landform adopts the enterprise of this tubing oil transportation still to occupy the minority.
Two, oil-water separation analysis
Through applicant's investigation, there is following problem mostly in the oil development enterprise of North Shaanxi at present:
(1) water-oil separating is not thorough;
(2) the petroleum resources waste is large.
Required coal amount was large when (3) heated winter.
(4) water-oil separating precision is not high, and the probability that contingency occurs is large.
(5) natural gas that produces in the oil exploitation is mostly directly got rid of, thereby does not realize economic effect, has also wasted valuable resource.
(6) contaminated environment.
Summary of the invention
Defective or deficiency for existing water-oil separating the object of the invention is to, and provide a kind of novel profit automatically to control separation equipment, and this equipment can carry out water-oil separating efficiently, and oil is purified.
In order to realize above-mentioned task, the present invention takes following technical solution:
A kind of profit is controlled separation equipment automatically, it is characterized in that, this equipment comprises a cylinder and plant bottom case, is provided with water-oil separating chamber and oil storage tank in cylinder interior, and is provided with oily medicine secondary mixing channel, and this oil medicine secondary mixing channel is rectangular channel; Be provided with right convex circular slab inverted triangle weir between oil medicine secondary mixing channel and the water-oil separating chamber; Be provided with left convex circular slab inverted triangle weir between oil storage tank and the water-oil separating chamber;
The top cover of cylinder is horizontal circular head, is provided with inspection opening in the middle of the circular head, and there is blast pipe in the inspection opening left side, and in cylinder interior, being positioned at the inspection opening right side has between dosing, and the top connects oil inlet pipe between dosing;
Be divided into one-level energy dissipating chamber between described dosing, horn mouth adds cartridge case, splashguard area and the elementary mixing pit of oily medicine; Wherein, one-level energy dissipating chamber and horn mouth add cartridge case and are positioned at top between dosing, and upper end, one-level energy dissipating chamber connects oil inlet pipe, and horn mouth adds cartridge case and is connected with the bilateral rotary blade, and a spoonful type dosing blade is installed on the bilateral rotary blade; The one-level energy dissipating is indoor one-sided rotary blade, on the one-sided rotary blade backward bent vane is installed; One-sided rotary blade is connected by driving belt with the bilateral rotary blade; There is liquid medicine down-pipe at the elementary mixing pit of oil medicine center, is used for profit and infusion of medicine are arrived oily medicine secondary mixing channel;
Described splashguard area is positioned at directly over the elementary mixing pit of oily medicine, is used for preventing polluting when the profit that oil guide pipe enters passes through one-sided rotary blade the bilateral rotary blade; Be injected in the secondary oil medicine mixing channel through liquid medicine down-pipe through the oil water mixture between dosing;
In the oil medicine secondary mixing channel semiclosed dividing plate is set evenly, has the impartial spout hole of size on the liquid medicine down-pipe;
Water level control ball and water level float induction end are housed in the water-oil separating chamber; Water-oil separating chamber bottom even is equipped with a plurality of gas distribution pipes, and the used gas of gas distribution pipe connects air collector by the air supporting pipe through plant bottom case and supplies with;
Be provided with simultaneously wastewater discharge pipe in bottom, water-oil separating chamber and manually control drainpipe; Wherein, be connected with altitude valve on the wastewater discharge pipe;
Oil storage tank is positioned at left side, water-oil separating chamber, at the oil storage tank sidewall oil level control ball float and ball float induction end is housed, and oil storage tank connects oil exit pipe and manual control oil exit pipe, and wherein, oil exit pipe is equipped with oil level control valve;
The heater air supply pipe is arranged in plant bottom case, and its air feed is provided by air collector, then supplies with respectively central heating plate and high-level heating dish via the heating plate gas manifold.
Profit of the present invention is automatically controlled separation equipment and is had following advantage:
1, a small amount of natural gas is collected through air collector, it is indoor to pass into water-oil separating, forms air-float technology to improve separating effect.
2, the use of oil-water interfaces ball float:
Utilize the oil-water interfaces ball float to be in all the time on the oil-water separation interface, drive the lifting of ball float according to the lifting at interface, when raising or be reduced to certain position, ball float will trigger induction end, induction end passes to fluid level control valve with signal, make the instruction of unlatching or valve-off, reach the purpose of automatic control.
3, the use of fluid level control valve:
Drive the lifting of ball float according to the lifting at pasta and interface, then touch the ball float induction end, signal is passed to fluid level control valve, liquid level valve is made and being opened or the instruction of valve-off, reaches the purpose of automatic control.
4, the utilization of natural gas:
Because the northern Shensi temperature is lower winter, so must consume a large amount of coals, this equipment takes full advantage of natural gas, makes in the oil water separation process and heats, and reaches the effect of energy-saving, emission-reducing, environment friendly.
5, the main component of medicine mainly comprises surfactant, dispersant etc.Utilize its dispersion, emulsification, peptization and many bulb junctions to close air supporting and reach better separating effect, thus the suspending power of raising oil.
6, medicine adds and utilizes the intermittent energy that has of oiling to transfer to the one-sided rotary blade of one-level energy dissipating chamber, drives the bilateral rotary blade by one-sided rotary blade and rotates the purpose that realizes dosing, has also avoided the waste of medicine.
Description of drawings
Fig. 1 is existing oily water separating equipment schematic diagram;
Fig. 2 is the structural representation that profit of the present invention is controlled separation equipment automatically;
Fig. 3 is the top view of Fig. 2;
Fig. 4 is the cross section view of Fig. 2;
Fig. 5 is the left and right convex circular slab inverted triangle weir schematic diagram of Fig. 2;
Fig. 6 is structural representation between dosing, wherein, (a) is front view, (b) is the top view of (a);
Fig. 7 is air supporting pipe schematic diagram;
Fig. 8 is the location drawing that the heating plate gas manifold is supplied with respectively central heating plate and high-level heating dish.
Label among the figure represents respectively: 1, oil inlet pipe, 2, between dosing, 3, one-level energy dissipating chamber, 4, one-sided rotary blade, 5, the bilateral rotary blade, 6, horn mouth adds cartridge case, 7, backward bent vane, 8, the impeller fixed axis, 9, driving belt, 10, spoon type dosing blade, 11, liquid medicine down-pipe, 12, splashguard area, 13, the elementary mixing pit of oil medicine, 14, oil medicine secondary mixing channel, 15, semiclosed dividing plate, 16, spout hole, 17, right convex circular slab inverted triangle weir, 18, the water-oil separating chamber, 19, gas distribution pipe, 20, the air supporting hole, 21, the air supporting pipe, 22, the gas distribution pipe support column, 23, level controling floating ball, 24, the water level float induction end, 25, wastewater drainage pipe, 26, altitude valve, 27, manually control drainpipe, 28, left convex circular slab inverted triangle weir, 29, oil storage tank, 30, oil level control ball float, 31, oil level ball float induction end, 32, oil exit pipe, 33, oil level control valve, 34, manually control oil exit pipe, 35, the heater air supply pipe, 36, the heating plate gas manifold, 37, the high-level heating dish, 38, central authorities' heating plate, 39, plant bottom case, 40, blast pipe, 41, inspection opening, 42, opening board, 43, air collector, 44, horizontal circular head, 45, cylinder.
The invention will be further described below in conjunction with drawings and Examples.
The specific embodiment
The main design idea of profit automatic control equipment of the present invention is, water-oil separating is theoretical, evenly gas distribution is theoretical, Theory of Automatic Control, the combinations such as mixing and energy dissipating theory are with the natural gas of oil mining process generation, it is fully utilized, the simultaneously effect with medicine mutually combines, and carries out efficient water-oil separating, finally reaches the purpose of energy-saving and emission-reduction.
Objectionable intermingling is theoretical under certain conditions according to profit, adds the base attribute of medicine by pneumatically supported characteristic and institute, makes profit reach efficient separation, then according to automatic control system, and with the profit device for transferring that separates, thus the cycle operation of realization equipment.This device structure simple-arranged is compact, and space availability ratio is high, and is simple to operate.
Referring to Fig. 2, Fig. 3 and Fig. 4, present embodiment provides a kind of profit and automatically controls separation equipment, this equipment comprises a cylinder 45 and plant bottom case 39, be provided with successively from right to left water-oil separating chamber 18, oil storage tank 29 and oily medicine secondary mixing channel 14 in cylinder 45 inside, this oil medicine secondary mixing channel 14 is rectangular channels; Be provided with right convex circular slab inverted triangle weir 17 between oil medicine secondary mixing channel 14 and the water-oil separating chamber 18; Be provided with left convex circular slab inverted triangle weir 28 between oil storage tank 29 and the water-oil separating chamber 18.
The top cover of cylinder 45 is horizontal circular head 44, is inspection opening 41(manhole in the middle of the circular head 44), opening board 42 is arranged on the inspection opening 41, there is blast pipe 40 in inspection opening 41 left sides, and inspection opening 41 right sides are between dosing 2.2 tops connect oil inlet pipe 1 between dosing.
Be injected in the oily medicine secondary mixing channel 14 through liquid medicine down-pipe 11 through 2 oil water mixture between dosing, oily medicine secondary mixing channel 14 is interior evenly to arrange semiclosed dividing plate 15, to increase oily medicine incorporation time.Liquid medicine down-pipe 11 has the impartial spout hole 16 of size, prevents that profit is for entering the elementary mixed zone 13 of oily medicine.Enter in the water-oil separating chamber 18 through right convex circular slab inverted triangle weir 17 through well-mixed profit and the medicine that adds.Water-oil separating chamber 18 bottom evens are laid gas distribution pipe 19, and gas distribution pipe 19 is gases used to be connected to air collector 43 by air supporting pipe 21 through plant bottom cases 39 and to supply with.
There is simultaneously wastewater discharge pipe 25 18 bottoms, water-oil separating chamber and manually controls drainpipe 27.On the left convex circular slab inverted triangle weir 28 in 18 interior left sides, water-oil separating chamber level controling floating ball 23 and water level float induction end 24 are housed.18 left sides, water-oil separating chamber are oil storage tank 29, oil level control ball float 30, oil level ball float induction end 31, oil exit pipe 32 is housed on the oil storage tank 29 left side outer walls and manually controls oil exit pipe 34.Oil exit pipe 32 is equipped with oil level control valve 33.
Heater air supply pipe 35 is arranged in plant bottom case 39, and then its air feed supplies with respectively central heating plate 38 and high-level heating dish 37 by heating plate gas manifold 36 by heater air supply pipe 35 air feed.
Referring to Fig. 6,2 be divided into one-level energy dissipating chamber 3 between dosing, horn mouth adds the elementary mixing pit 13 of cartridge case 6, splashguard area 12 and oily medicine; Wherein: one-level energy dissipating chamber 3 and horn mouth add cartridge case 6 and are positioned between dosing 2 top, and 3 upper ends, one-level energy dissipating chamber connect oil inlet pipe 1, and horn mouth adds cartridge case 6 and is connected with bilateral rotary blade 5, and a spoonful type dosing blade 10 is installed on the bilateral rotary blade 5; One-sided rotary blade 4 is arranged in the one-level energy dissipating chamber 3, on the one-sided rotary blade 4 backward bent vane 7 is installed; One-sided rotary blade 4 and bilateral rotary blade 5 are fixing by impeller fixed axis 8, and one-sided rotary blade 4 is connected by driving belt 9 with bilateral rotary blade 5; There is liquid medicine down-pipe 11 at the elementary mixing pit of oil medicine 13 centers, are used for profit and infusion of medicine are arrived oily medicine secondary mixing channel 14.
Oil inlet pipe 1 intermittence oils and drives one-sided rotary blade 4(dosing driving wheel) rotation, drive bilateral rotary blade 5(dosing wheel through driving belt 9 in the time of one-sided rotary blade 4 rotation) rotation, spoon type dosing blade 10 on the bilateral rotary blade 5 adds the cartridge case 6 from horn mouth takes medicine out of, has realized oiling with to add medicine synchronous.The profit of process one-level energy dissipating chamber 3 adds cartridge case 6 added medicines with horn mouth and carries out elementary the mixing at the elementary mixing pit 13 of oily medicine, be splashguard area 12 directly over the elementary mixing pit 13 of oil medicine, be used for preventing when the profit that oil guide pipe 1 enters passes through one-sided rotary blade 4, polluting bilateral rotary blade 5.
Referring to Fig. 2, be injected in the oily medicine secondary mixing channel 14 through liquid medicine down-pipe 11, oily medicine secondary mixing channel 14 is interior evenly to arrange semiclosed dividing plate 15, increases oily medicine incorporation time.Liquid medicine down-pipe 11 has the impartial spout hole 16 of size, prevents that oil-water direct from tapping into into the elementary mixed zone 13 of oily medicine, adds the medicine that cartridge case 6 adds through well-mixed profit and horn mouth and enters in the water-oil separating chamber 18 through right convex circular slab inverted triangle weir 17.
Referring to Fig. 7,18 bottoms, water-oil separating chamber arrange gas distribution pipe 19.Gas distribution pipe 19 is comprised of the pipe that is uneven in length, the bilateral symmetry setting, and shorten gradually to both sides from the centre, and be 5 degree angles with ground.Gas distribution pipe 19 is fixed on the bottom surface of water-oil separating chamber 18 by gas distribution pipe support column 22.Evenly have air supporting hole 20 on the gas distribution pipe 19, there is air supporting pipe 21 at gas distribution pipe 19 centers, on the air supporting pipe 21 control valve are installed, and regulate gas consumption.
Referring to Fig. 2, when enter into through well-mixed profit and medicine water-oil separating chamber 18 interior after, the dehydration property through medicine makes the preliminary separation of profit.Then a large amount of bubbles that produced by medicine are under the drive of the bubble that air supporting pipe 21 produces, and bubble all moves upward, and oil residual in the water is taken on the pasta.The water level of water-oil separating chamber 18 control ball 23 is between the oil water surface always during this period, through the regular hour, water level control ball 23 arrives ball float induction end 24 peaks that set, after ball float induction end 23 is sensed signal, signal is passed to the altitude valve 26 that is positioned on the drainpipe 25, after altitude valve 26 receives signal, just open draining valve 26, carry out draining.When the water level control ball 23 that is in oil water surface drops to lowermost end and touches water level float induction end 24, send the signal of valve-off, this process is carried out repeatedly.Because the enriching quantity of oil increases, final oil enters in the oil storage tank 29 through crude oil overcurrent plate 28, be provided with oil level control ball float 30 in the oil storage tank 29, oil level control ball float 30 is on the pasta all the time, to touch oil level induction end 31 according to the lifting oil level of pasta control ball float 30, and be positioned at oil level control valve 33 on the oil storage tank 29 bottom oil exit pipes 32 and make and open and close operation thereby send signal of telecommunication control.For Accident prevention, the lowermost end of water-oil separating chamber 18 and oil storage tank 29 is respectively equipped with Manual draining valve 27 and manual draining valve 34.
Participate in Fig. 8, heater air supply pipe 35 is arranged in plant bottom case 39, heater air supply pipe 35 is connected to air collector 43, then distributes to heating plate by heating plate gas manifold 36, and heating plate is divided into two kinds of specifications, be central heating plate 38 and high-level heating dish 37, heater air supply pipe 35 is fixed by steel pipe frame, and in the present embodiment, central heating plate 38 uses 1, high-level heating dish 37 uses 4, and 37 on high-level heating dish is evenly distributed in the plant bottom case 39 centered by central heater 38.
The profit of present embodiment preparation is controlled the operation principle of separation equipment automatically: the principle different according to profit density, oil floats on the surface.Then according to adding medicine dehydration property profit is carried out preliminary dehydration, then under pneumatically supported effect, the oil bloom that remain in the water are taken on the pasta by the bubble that air supporting produces.Meanwhile according to the variation of water level and oil level, water level induction end 24 and oil level induction end 31 in water-oil separating chamber 18 and oil storage tank 29 are made induction, altitude valve 26 and oil level control valve 33 on control drainpipe 25 and the oil exit pipe 32 are realized the automatic control of oil-water discharge.
Claims (5)
1. a profit is controlled separation equipment automatically, it is characterized in that, this equipment comprises a cylinder (45) and plant bottom case (39), be provided with water-oil separating chamber (18) and oil storage tank (29) in cylinder (45) inside, and being provided with oily medicine secondary mixing channel (14), this oil medicine secondary mixing channel (14) is rectangular channel; Be provided with right convex circular slab inverted triangle weir (17) between oil medicine secondary mixing channel (14) and water-oil separating chamber (18); Be provided with left convex circular slab inverted triangle weir (28) between oil storage tank (29) and water-oil separating chamber (18);
The top cover of cylinder (45) is horizontal circular head (44), be provided with inspection opening (41) in the middle of the circular head (44), there is blast pipe (40) in inspection opening (41) left side, in cylinder (45) inside, being positioned at inspection opening (41) right side has (2) between dosing, and (2) top connects oil inlet pipe (1) between dosing;
(2) are divided into one-level energy dissipating chamber (3) between described dosing, horn mouth adds cartridge case (6), splashguard area (12) and the elementary mixing pit of oily medicine (13); Wherein, one-level energy dissipating chamber (3) and horn mouth add the top that cartridge case (6) is positioned at (2) between dosing, upper end, one-level energy dissipating chamber (3) connects oil inlet pipe (1), horn mouth adds cartridge case (6) and is connected with bilateral rotary blade (5), and a spoonful type dosing blade (10) is installed on the bilateral rotary blade (5); One-sided rotary blade (4) is arranged in the one-level energy dissipating chamber (3), backward bent vane (7) is installed on the one-sided rotary blade (4); One-sided rotary blade (4) is connected by driving belt (9) with bilateral rotary blade (5); There is liquid medicine down-pipe (11) at the oil elementary mixing pit of medicine (13) center, is used for profit and infusion of medicine are arrived oily medicine secondary mixing channel (14);
Described splashguard area (12) is positioned at directly over the elementary mixing pit of oily medicine (13), is used for preventing polluting when the profit that oil guide pipe (1) enters passes through one-sided rotary blade (4) bilateral rotary blade (5); Oil water mixture through (2) between dosing is injected in the oily medicine secondary mixing channel (14) through liquid medicine down-pipe (11);
In the oil medicine secondary mixing channel (14) semiclosed dividing plate (15) is set evenly, has the impartial spout hole (16) of size on the liquid medicine down-pipe (11);
In water-oil separating chamber (18) water level control ball (23) and water level float induction end (24) are housed; Water-oil separating chamber (18) bottom even is equipped with a plurality of gas distribution pipes (19), and the used gas of gas distribution pipe (19) connects air collector (43) by air supporting pipe (21) through plant bottom case (39) and supplies with;
Be provided with simultaneously wastewater discharge pipe (25) in water-oil separating chamber (18) bottom and manually control drainpipe (27); Wherein, be connected with altitude valve (26) on the wastewater discharge pipe (25);
Oil storage tank (29) is positioned at left side, water-oil separating chamber (18), at oil storage tank (29) sidewall oil level control ball float (30) and ball float induction end (31) are housed, oil storage tank (29) connects oil exit pipe (32) and manually controls oil exit pipe (34), wherein, oil exit pipe (32) is equipped with oil level control valve (33);
Heater air supply pipe (35) is arranged in plant bottom case (39), and its air feed is provided by air collector (43), then supplies with respectively central heating plate (38) and high-level heating dish (37) via heating plate gas manifold (36).
2. profit as claimed in claim 1 is controlled separation equipment automatically, it is characterized in that, described gas distribution pipe (19) is comprised of multitube, and being uneven in length of each pipe is symmetrical arranged, and the length of each pipe shortens to both sides gradually from the centre, and is 5 degree angles with ground; Gas distribution pipe (19) is fixed on the bottom surface of water-oil separating chamber (18) by gas distribution pipe support column (22); Have air supporting hole (20) on the gas distribution pipe (19), there is air supporting pipe (21) at gas distribution pipe (19) center, and air supporting pipe (21) both sides connect gas distribution pipe support column (22), the upper valve that is used for regulating gas consumption of installing of air supporting pipe (21).
3. profit as claimed in claim 1 is controlled separation equipment automatically, it is characterized in that, described water-oil separating chamber (18) also arranges water level control ball (23), arrive ball float induction end (24) peak that has set when water level control ball (23), after ball float induction end (23) is sensed signal, signal is passed to the altitude valve (26) that is positioned on the drainpipe (25), after altitude valve (26) receives signal, just open draining valve (26), carry out draining; When the lowermost end that drops to induction end (24) when water level control ball (23) touches the ball float induction end, send the signal of valve-off, this process is carried out repeatedly.
4. profit as claimed in claim 1 is controlled separation equipment automatically, it is characterized in that, described oil level control ball float (30) is on the pasta all the time, lifting according to pasta, oil level control ball float (30) and oil level induction end (31) contact, and are positioned at oil level control valve (33) on oil storage tank (29) the bottom oil exit pipe (32) and make opening and closing and operate thereby send signal of telecommunication control.
5. automatically control separation equipment such as claim 1 profit, it is characterized in that, described heater air supply pipe (35) is fixed in the plant bottom case (39) by steel pipe frame, described central heating plate (38) is 1, high-level heating dish (37) is 4, and high-level heating dish (37) is evenly distributed centered by central heater (38).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210358778.0A CN102847345B (en) | 2012-09-24 | 2012-09-24 | Oil-water automatic control separation device |
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|---|---|---|---|
| CN201210358778.0A CN102847345B (en) | 2012-09-24 | 2012-09-24 | Oil-water automatic control separation device |
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| CN102847345B CN102847345B (en) | 2014-07-16 |
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| CN104628084A (en) * | 2015-02-12 | 2015-05-20 | 苏州美生环保科技有限公司 | Special oil-water separator |
| CN105413240A (en) * | 2015-12-29 | 2016-03-23 | 天津理工大学 | Marine oil-water separator simulation device for crew training |
| CN106390527A (en) * | 2016-12-02 | 2017-02-15 | 沈阳航天新光集团有限公司 | Anti-explosion fuel oil dehydration and deoxidizing device |
| CN107080978A (en) * | 2017-05-26 | 2017-08-22 | 中国海洋石油总公司 | Spraying type inlet distributor under gas distribution on submersible |
| CN107352485A (en) * | 2017-07-19 | 2017-11-17 | 天奇自动化工程股份有限公司 | A kind of lift for possessing belt fracture warning function |
| CN108341456A (en) * | 2018-04-18 | 2018-07-31 | 深圳市玖品空气净化科技有限公司 | A kind of energy-saving organic waste oily-water seperating equipment with regulatory function |
| CN110422816A (en) * | 2019-07-24 | 2019-11-08 | 山东裕泰石油装备有限公司 | A kind of water-oil separating skid-mounted gas station |
| CN112415140A (en) * | 2020-11-09 | 2021-02-26 | 内蒙古电力（集团）有限责任公司薛家湾供电局 | Real-time on-line monitoring device for vacuum on-load tap-changer acetylene of transformer |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2401249Y (en) * | 1999-12-12 | 2000-10-18 | 张洪俊 | Oil-sludge separation treatment device |
| CN2710719Y (en) * | 2004-07-19 | 2005-07-20 | 抚顺市明尧石油机械有限公司 | Floating circulation oil recovery appts. |
| JP2007330951A (en) * | 2006-06-13 | 2007-12-27 | Fukuhara Co Ltd | Method and apparatus for separating foreign matter mainly comprising oil from oil-containing sewage |
| CN201049220Y (en) * | 2007-06-08 | 2008-04-23 | 北京东方海联科技发展有限公司 | Oil-water separating oil-separation device for dining waste water |
| CN202297295U (en) * | 2011-10-10 | 2012-07-04 | 张炳俊 | Automatic grease separating equipment |
-
2012
- 2012-09-24 CN CN201210358778.0A patent/CN102847345B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2401249Y (en) * | 1999-12-12 | 2000-10-18 | 张洪俊 | Oil-sludge separation treatment device |
| CN2710719Y (en) * | 2004-07-19 | 2005-07-20 | 抚顺市明尧石油机械有限公司 | Floating circulation oil recovery appts. |
| JP2007330951A (en) * | 2006-06-13 | 2007-12-27 | Fukuhara Co Ltd | Method and apparatus for separating foreign matter mainly comprising oil from oil-containing sewage |
| CN201049220Y (en) * | 2007-06-08 | 2008-04-23 | 北京东方海联科技发展有限公司 | Oil-water separating oil-separation device for dining waste water |
| CN202297295U (en) * | 2011-10-10 | 2012-07-04 | 张炳俊 | Automatic grease separating equipment |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104628084A (en) * | 2015-02-12 | 2015-05-20 | 苏州美生环保科技有限公司 | Special oil-water separator |
| CN105413240A (en) * | 2015-12-29 | 2016-03-23 | 天津理工大学 | Marine oil-water separator simulation device for crew training |
| CN106390527A (en) * | 2016-12-02 | 2017-02-15 | 沈阳航天新光集团有限公司 | Anti-explosion fuel oil dehydration and deoxidizing device |
| CN106390527B (en) * | 2016-12-02 | 2018-11-30 | 沈阳航天新光集团有限公司 | Explosion-proof type fuel oil dehydration and deoxidation device |
| CN107080978A (en) * | 2017-05-26 | 2017-08-22 | 中国海洋石油总公司 | Spraying type inlet distributor under gas distribution on submersible |
| CN107352485A (en) * | 2017-07-19 | 2017-11-17 | 天奇自动化工程股份有限公司 | A kind of lift for possessing belt fracture warning function |
| CN107352485B (en) * | 2017-07-19 | 2023-01-06 | 天奇自动化工程股份有限公司 | Elevator with belt breakage early warning function |
| CN108341456A (en) * | 2018-04-18 | 2018-07-31 | 深圳市玖品空气净化科技有限公司 | A kind of energy-saving organic waste oily-water seperating equipment with regulatory function |
| CN110422816A (en) * | 2019-07-24 | 2019-11-08 | 山东裕泰石油装备有限公司 | A kind of water-oil separating skid-mounted gas station |
| CN112415140A (en) * | 2020-11-09 | 2021-02-26 | 内蒙古电力（集团）有限责任公司薛家湾供电局 | Real-time on-line monitoring device for vacuum on-load tap-changer acetylene of transformer |
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