CN101607146B - Oil and water separation system - Google Patents
Oil and water separation system Download PDFInfo
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- CN101607146B CN101607146B CN2009101042782A CN200910104278A CN101607146B CN 101607146 B CN101607146 B CN 101607146B CN 2009101042782 A CN2009101042782 A CN 2009101042782A CN 200910104278 A CN200910104278 A CN 200910104278A CN 101607146 B CN101607146 B CN 101607146B
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Abstract
The invention discloses an oil and water separation device. The system comprises a pipeline (19), a filter and a storage tank, and is characterized in that the pipeline (19) is sequentially connected with a front-mounted crushing pump (1), a first filter (2), a pushing pump (3), a first storage tank (4), a homogenizing pump (5), a second filter (6), a second storage tank (7) and an output booster pump (8) in series. The device is used for performing pre-dispersion treatment on easily agglomerate and difficultly separated dope and polymer before separation, mainly uses various different treatment devices for sequential treatment, changes the original single treatment mode, and causes the agglomerate dope or polymer to be subject to a series of treatment such as crushing, homogenizing, filtering and the like in the conveying process, thus achieving very good dispersion effect.
Description
Technical field
The invention belongs to a kind of separation equipment, specifically, is a kind of oil and water separation equipment.
Background technology
Dope such as fluid and polymer, the material that two compare dissolves each other owing to be polarity all, perhaps all is nonpolar, the very easy gathering that attracts each other is agglomerating, is not easy to disperse to come out, and more talks and separates.At present, the way that all also has nothing good commonly used is all just utilized traditional centrifugal separation, and centrifugal two kinds of liquid that the difference of sinking speed is different with weight separately, but centrifugation runs under the also suitable situation of density, wants two-phase is disperseed out to be not easy very much.
Some mixed liquors are just poorer as the effect that, crude oil etc. separate.Now also taking earlier in this case, the material that polymerization is agglomerating spreads out, the operation that could separate once more, disperse to adopt often and be divided into ultrasonic dispersion and mechanical dispersion, ultrasonic dispersion mainly is a kind of higher-order of oscillation equipment, the void effect of utilizing the higher-order of oscillation to produce forms impact grinding to poly-agglomerating material, make that the polymer beads of reuniting disperses, homogeneous, this higher-order of oscillation equipment, though effect is preferably arranged, but cost an arm and a leg, cause and disperse cost higher, be unfavorable for promoting; Mechanical dispersion equipment, as cut out, equipment such as homogeneous, this equipment gathers the certain effect that is dispersed with in the liquid phase of rolling into a ball, but acting on all more singlely, comprise that all there is such problem in ultrasonic dispersion etc., all is homogeneous, shearing etc., the shortcoming that all has function singleness, the neither one complete device is gathered again after the dispersion easily, and the later stage is separated situations such as difficult.
Summary of the invention
Technical problem to be solved by this invention is to provide that a kind of preliminary treatment is beneficial to the oil and water separation equipment of separation to material.
Technical scheme of the present invention is as follows: a kind of oil and water separation equipment, comprise pipeline, filter and storage tank, its key is: be in series with preposition breakage pump, first filter, pusher pump, first storage tank, Homogenizing pump, second filter, second storage tank, supercharging rear pump on the described pipeline successively.In the described device, the outlet of previous device links to each other with the import of a back device, and all devices all are communicated with.Material is imported from pipe head, and through preposition breakage pump, preposition breakage pump be that general the conveying used pump, at the front end of the pump housing breaker is housed, and in the breaker is and the blade of rotor unitary rotation, and material is carried out the fragmentation stirring.Pump carries out fragmentation to polymer when carrying, the material that polymerization is agglomerating is smashed and separated, and this preliminary treatment allows its elimination of trying one's best assemble agglomerating material.Utilize filter to filter out oarse-grained dregs, aggregate or the like material then.Pump into first storage tank by the pusher pump again by the material after filtering, the material of first storage tank carries out the extruding of material again by Homogenizing pump, makes the material refinement under the triple role of thump and decompression expansion, thereby makes the material can be more even.Carefully filter by second filter once more, enter the storage of second storage tank, just material is pushed output at last by booster pump through the material after filtering.The processing successively of a set of equipment is effectively opened viscous fluid or polymer dispersed, sends into to be convenient to client's its separate demand in client's hand.Also be connected with simultaneously the reservation feed pipe of another band gate valve on pipeline, this tie point of reserving feed pipe and pipeline is between the 14 gate valve and the 3rd arm.
The pipeline of above-mentioned preposition breakage pump entrance point is provided with first gate valve, pipeline between the described preposition breakage pump and first filter is provided with second gate valve, pipeline between described first filter and the pusher pump is provided with the 3rd gate valve, pipeline between the described pusher pump and first storage tank is provided with the 4th gate valve, pipeline between described first storage tank and the Homogenizing pump is provided with the 5th gate valve, pipeline between the described Homogenizing pump and second filter is provided with the 6th gate valve, be disposed with the 7th gate valve and the 8th gate valve on the pipeline between described second filter and second storage tank, pipeline between described second storage tank and the supercharging rear pump is provided with the 17 gate valve, and the pipeline of described supercharging rear pump output is provided with the 9th gate valve.The opening and closing of above-mentioned gate valve can to whole process flow carry out open close, regulate and control, wherein the gate valve between two treatment facilities can also be set to motor-driven valve, utilizes the circuit control appliance that it is controlled.
Be connected with first return duct between above-mentioned first storage tank and second storage tank, the charging aperture of described first storage tank and second storage tank all is positioned at storage tank top separately, the discharging opening of this first storage tank and second storage tank all is positioned at storage tank bottom separately, and the junction of described first return duct and first storage tank and second storage tank all is higher than the charging aperture of storage tank separately.The charging aperture of first storage tank and second storage tank all is positioned at storage tank top separately, and discharging opening is positioned at storage tank bottom separately, charging aperture is higher than discharging opening, material enters storage tank from the position that is higher than discharging opening, because gravity effect, open the gate valve on the storage tank discharging opening pipeline, will get rid of automatically.
The charging aperture height can be stored more material simultaneously, and the material that is unlikely to store is higher than charging aperture and causes refluence.Close when the 17 gate valve owing to be connected with first return duct between first storage tank and second storage tank, material will flow back into first storage tank from second storage tank, filters once more and flows back to second storage tank through the processing of Homogenizing pump homogeneous, second filter once more; The junction of described first return duct and first storage tank and second storage tank all is higher than the charging aperture of storage tank separately.
By controlling the turnover flow of the second storage tank material, when material influent stream amount need not be closed the 8th gate valve during greater than outflow, when material liquid surface was higher than the junction of first return duct and second storage tank in second storage tank, material also was back in first storage tank through first return duct in second storage tank.
Be connected with second return duct on above-mentioned first return duct, this second return duct, one end is connected first return duct middle part, and the described second return duct other end is connected on the pipeline between first gate valve and the preposition breakage pump.Described second return duct is provided with the 16 gate valve.Needs and standard according to discharging, close the 5th gate valve and the 17 gate valve, material can enter in the pipeline between first gate valve and the preposition breakage pump through second return duct in first storage tank and second storage tank, pass through preposition breakage pump, first filter, pusher pump, first storage tank, Homogenizing pump, second filter process once more, also can repeatedly handle the standard of reaching.
Also can take to control the flow of the turnover material of first storage tank and second storage tank, enter first storage tank and the second storage tank inventory greater than discharging inventory, do not close the 5th gate valve and the 17 gate valve, under the situation that does not stop supercharging rear pump discharge material, material also can enter in the pipeline between first gate valve and the preposition breakage pump through second return duct, pass through preposition breakage pump, first filter, pusher pump, first storage tank, Homogenizing pump, second filter process once more, or the standard that reaches is repeatedly handled in recirculation.
Be parallel with first arm on the pipeline between above-mentioned preposition breakage pump and the pusher pump, this first arm, this first arm is provided with the tenth gate valve, the 11 gate valve and the 3rd filter, and described the 3rd filter bits is between the tenth gate valve and the 11 gate valve.When first filter is blocked when need cleaning or need keep in repair, close second gate valve and the 3rd gate valve, open the tenth gate valve and the 11 gate valve and switch to the 3rd filter and filter, can not influence whole material and disperse flow process.
Be parallel with second arm on the pipeline between above-mentioned Homogenizing pump and the 8th gate valve, this second arm is provided with the 12 gate valve, the 13 gate valve and the 4th filter, and described the 4th filter bits is between the 12 gate valve and the 13 gate valve.Equally needed to clean or need keep in repair the time, close the 6th gate valve and the 7th gate valve, open the 12 gate valve and the 13 gate valve and switch to the 4th filter and filter, can not influence whole material dispersion flow process when second filter blocks.
Be connected with the probe tube of strap brake valve on the pipeline between above-mentioned supercharging rear pump and the 9th gate valve.Open the 9th gate valve and can take a sample at any time and detect, detect the standard that whether reaches discharge.
The pipeline of the above-mentioned first gate valve entrance point is provided with the 14 gate valve, be connected with grug feeding jar through the 3rd arm on the pipeline between described first gate valve and the 14 gate valve, the 3rd arm is provided with the 14 gate valve, water pump and the 15 gate valve, and wherein water pump is between the 14 gate valve and the 15 gate valve.Being provided with grug feeding jar is at needing to add the processing that chemicals is beneficial to disperse in some material dispersion processes, can open the 14 gate valve and the 15 gate valve in the material fill process, utilizing water pump that chemicals is imported in the material.
The most conventional processing that is in operation of this equipment is to open the 14 gate valve, first gate valve, second gate valve, the 3rd gate valve, the pusher pump, the 4th gate valve, the 5th gate valve, the 6th gate valve, the 7th gate valve, the 8th gate valve, the 17 gate valve, the 9th gate valve, close the 15 gate valve simultaneously, the 16 gate valve, the tenth gate valve, the 11 gate valve, the 12 gate valve, the 13 gate valve, material enters by the 14 gate valve from conduit entrance, first gate valve, enter preposition breakage pump conveying and broken, entering first filter by second gate valve then filters, be pumped into first storage tank through the 3rd gate valve by pusher again, the material that stores in first storage tank enters the Homogenizing pump homogeneous through the 5th gate valve again and handles, material after the processing enters second filter by the 6th gate valve and filters once more, material after the filtration enters second storage tank by the 7th gate valve and the 8th gate valve again and stores, and is exported by the supercharging of supercharging rear pump by the 17 gate valve again.Material on pipeline between supercharging rear pump and the 9th gate valve can take out a part by probe tube, and this part material of taking-up detects the standard that whether reaches of seeing.
The sampling material detects and does not reach standard, can all handle again as required or all processing of part, if all handle again, on processed conventionally basis, does not open earlier the 9th gate valve.Taking out a part of material by probe tube on the pipeline between supercharging rear pump and the 9th gate valve, this part material of taking-up detects the standard that whether reaches of seeing.If the standard of not reaching, circulate and handle again, no longer open the 9th gate valve this moment, also open the 16 gate valve simultaneously, described first storage tank, the material of second storage tank accumulation increases gradually, and material liquid surface exceeds first return duct and first storage tank and the second storage tank junction, then in first return duct and two return ducts are back to pipeline between first gate valve and the preposition breakage pump.Also can close the 5th gate valve, allow first storage tank be back in the pipeline between first gate valve and the preposition breakage pump by first return duct and two return ducts, circulation is handled one time again once more.In running, also can take to reduce the second storage tank output quantity, increase the second storage tank input quantity simultaneously, when input quantity greater than output quantity the time, the partial material of second storage tank also can be in first return duct and two return ducts be back to pipeline between first gate valve and the preposition breakage pump.Circulation is handled one time again once more.
Part is handled again if desired, does not open earlier the 9th gate valve.Taking out a part of material by probe tube on the pipeline between supercharging rear pump and the 9th gate valve, this part material of taking-up detects the standard that whether reaches of seeing.If the standard of not reaching, carrying out the cyclic part homogeneous handles, no longer open the 9th gate valve this moment, the material of second storage tank accumulation increases gradually, material liquid surface exceeds first return duct and the second storage tank junction, be back to first storage tank through return duct then, handle again one time by Homogenizing pump, filter cyclic part once more.Equally also can open the 9th gate valve, reduce the second storage tank output quantity by control, increase the second storage tank input quantity simultaneously, when input quantity greater than output quantity the time, the partial material of second storage tank also can be handled one time by Homogenizing pump, filter cyclic part in first return duct enters first storage tank once more again.
Above-mentioned three kinds of situations when needs add chemicals, are added medicine in the grug feeding jar in advance, just open the 14 gate valve, the 15 gate valve, utilize water pump to send into medicine in the pipeline and the material before handling is mixed together and enters processing.
Above-mentioned various situation is all controlled by the gate valve that is provided with in the opening and closing equipment, gate valve in the equipment is a motor-driven valve as required, be connected with the circuit kit control appliance it is controlled, each gate valve of opening and closing is all very convenient, and various situations are switched easily and be convenient.
Beneficial effect: present device is used for dope or the easily poly-group of polymer, not easily separated, dispersion treatment in advance before separating, mainly utilize various treating apparatus to handle successively, single processing mode before changing, the dope of feasible poly-group or polymer carry out a series of processing such as fragmentation, homogeneous, filtration and reach extraordinary dispersion effect in the process that is transferred; Special in processing procedure for the different needs of handling the back material, can be for material not up to standard with material circular treatment one time once more before discharging, circular treatment also can be according to circumstances, part is handled again and is all handled again, only need just can realize whole adjusting and switching easily by ON/OFF part gate valve.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The specific embodiment
The invention will be further described below in conjunction with drawings and Examples:
As shown in Figure 1, a kind of oil and water separation equipment of the present invention, form by pipeline 19, grug feeding jar 33, preposition breakage pump 1, filter, storage tank, Homogenizing pump 5, first storage tank 4, second storage tank 7, supercharging rear pump 8 and gate valve etc., be in series with preposition breakage pump 1, first filter 2, pusher pump 3, first storage tank 4, Homogenizing pump 5, second filter 6, second storage tank 7, supercharging rear pump 8 on the described pipeline 19 successively.Whole flow process is from left to right moved.
Control for the ease of whole flow process, the pipeline 19 of preposition breakage pump 1 entrance point is provided with first gate valve 9, pipeline 19 between the described preposition breakage pump 1 and first filter 2 is provided with second gate valve 10, pipeline 19 between described first filter 2 and the pusher pump 3 is provided with the 3rd gate valve 11, pipeline 19 between the described pusher pump 3 and first storage tank 4 is provided with the 4th gate valve 12, pipeline 19 between described first storage tank 4 and the Homogenizing pump 5 is provided with the 5th gate valve 13, pipeline 19 between the described Homogenizing pump 5 and second filter 6 is provided with the 6th gate valve 14, be disposed with the 7th gate valve 15 and the 8th gate valve 16 on the pipeline 19 between described second filter 6 and second storage tank 7, pipeline 19 between described second storage tank 7 and the supercharging rear pump 8 is provided with the 17 gate valve 17, and the pipeline 19 of described supercharging rear pump 8 outputs is provided with the 9th gate valve 18.
The bottom of first storage tank 4 and second storage tank 7 all is connected with blow-off pipe, makes things convenient for blowdown to tilt, and is provided with gate valve equally at blow-off pipe.The charging aperture of first storage tank 4 and second storage tank 7 all is positioned at storage tank top separately, the discharging opening of this first storage tank 4 and second storage tank 7 all is positioned at storage tank bottom separately, circular treatment also can be according to circumstances, realize material not up to standard before discharging once more cyclic part handle one time, be connected with first return duct 20 between first storage tank 4 and second storage tank 7, the junction of described first return duct 20 and first storage tank 4 and second storage tank 7 all is higher than the charging aperture of storage tank separately.
Circular treatment also can be according to circumstances, realize material not up to standard before discharging once more circulation all handle again one time, be connected with second return duct 21 on first return duct 20, these second return duct, 21 1 ends are connected first return duct, 20 middle parts, described second return duct, 21 other ends are connected on the pipeline 19 between first gate valve 9 and the preposition breakage pump 1, and described second return duct 21 is provided with the 16 gate valve 37.
For the ease of not shutting down cleaning and maintenance to filter; be parallel with first arm 22 on the pipeline 19 between preposition breakage pump 1 and the pusher pump 3; this first arm 22; this first arm 22 is provided with the tenth gate valve the 23, the 11 gate valve 24 and the 3rd filter 25, and described the 3rd filter 25 is between the tenth gate valve 23 and the 11 gate valve 24.Be parallel with second arm 26 on the pipeline 19 between described Homogenizing pump 5 and the 8th gate valve 16, this second arm 26 is provided with the 12 gate valve the 27, the 13 gate valve 28 and the 4th filter 29, and described the 4th filter 29 is between the 12 gate valve 27 and the 13 gate valve 28.
It is convenient to be used for sampling, detects at any time, is connected with the probe tube 30 of strap brake valve on the pipeline 19 between above-mentioned supercharging rear pump 8 and the 9th gate valve 18.
In the process that material is handled, at some materials, for the better effects if of handling, need in material, add chemicals before the charging, the pipeline 19 of described first gate valve, 9 entrance points is provided with the 14 gate valve 31, be connected with grug feeding jar 33 through the 3rd arm 32 on the pipeline 19 between described first gate valve 9 and the 14 gate valve 31, the 3rd arm 32 is provided with the 14 gate valve 34, water pump 35 and the 15 gate valve 36, and wherein water pump 35 is between the 14 gate valve 34 and the 15 gate valve 36.
Operation principle: situation 1, open the 14 gate valve 31, first gate valve 9, second gate valve 10, the 3rd gate valve 11, pusher pump 3, the 4th gate valve 12, the 5th gate valve 13, the 6th gate valve 14, the 7th gate valve 15, the 8th gate valve 16, the 17 gate valve 17, the 9th gate valve 18, close the 15 gate valve 36 simultaneously, the 16 gate valve 37, the tenth gate valve 23, the 11 gate valve 24, the 12 gate valve 27, the 13 gate valve 28, material enters by the 14 gate valve 31 from pipeline 19 imports, first gate valve 9, entering preposition breakage pump 1 carries and fragmentation, entering first filter 2 by second gate valve 10 then filters, send into first storage tank 4 through the 3rd gate valve 11 by pusher pump 3 again, the material that stores in first storage tank 4 enters Homogenizing pump 5 homogeneous through the 5th gate valve 13 again and handles, material after the processing enters second filter 6 by the 6th gate valve 14 and filters once more, material after the filtration enters second storage tank 7 by the 7th gate valve 15 and the 8th gate valve 16 again and stores, and is exported by 8 superchargings of supercharging rear pump by the 17 gate valve 17 again.Material on pipeline 19 between supercharging rear pump 8 and the 9th gate valve 18 can take out a part by probe tube 30, and this part material of taking-up detects the standard that whether reaches of seeing.
Situation 2, open the 14 gate valve 31, first gate valve 9, second gate valve 10, the 3rd gate valve 11, pusher pump 3, the 4th gate valve 12, the 5th gate valve 13, the 6th gate valve 14, the 7th gate valve 15, the 8th gate valve 16, the 17 gate valve 17, close the 15 gate valve 36 simultaneously, the 16 gate valve 37, the tenth gate valve 23, the 11 gate valve 24, the 12 gate valve 27, the 13 gate valve 28, material enters by the 14 gate valve 31 from pipeline 19 imports, first gate valve 9, entering preposition breakage pump 1 carries and fragmentation, entering first filter 2 by second gate valve 10 then filters, send into first storage tank 4 through the 3rd gate valve 11 by pusher pump 3 again, the material that stores in first storage tank 4 enters Homogenizing pump 5 homogeneous through the 5th gate valve 13 again and handles, material after the processing enters second filter 6 by the 6th gate valve 14 and filters once more, material after the filtration enters second storage tank 7 by the 7th gate valve 15 and the 8th gate valve 16 again and stores, by before the supercharging rear pump 8 superchargings output, do not open earlier the 9th gate valve 18 by the 17 gate valve 17.Take out a part of material by probe tube 30 on pipeline 19 between supercharging rear pump 8 and the 9th gate valve 18, this part material of taking-up detects the standard that whether reaches of seeing.If the standard of not reaching, circulate and handle again, no longer open the 9th gate valve 18 this moment, also open the 16 gate valve 37 simultaneously, described first storage tank 4, the material of second storage tank 7 accumulation increases gradually, and material liquid surface exceeds first return duct 20 and first storage tank 4 and second storage tank, 7 junctions, then in return duct 20 and two return ducts 21 are back to pipeline 19 between first gate valve 9 and the preposition breakage pump 1.Also can close the 5th gate valve 13, allow first storage tank 4 be back in the pipeline 19 between first gate valve 9 and the preposition breakage pump 1 by first return duct 20 and two return ducts 21, circulation is handled one time again once more.In running, also can take to reduce second storage tank, 7 output quantities, increase second storage tank, 7 input quantities simultaneously, when input quantity greater than output quantity the time, the accumulation of the partial material of second storage tank 7 too much also can be in first return duct 20 and two return ducts 21 be back to pipeline 19 between first gate valve 9 and the preposition breakage pump 1.Circulation is handled one time again once more.
Situation 3, open the 14 gate valve 31, first gate valve 9, second gate valve 10, the 3rd gate valve 11, pusher pump 3, the 4th gate valve 12, the 5th gate valve 13, the 6th gate valve 14, the 7th gate valve 15, the 8th gate valve 16, the 17 gate valve 17, close the 15 gate valve 36 simultaneously, the 16 gate valve 37, the tenth gate valve 23, the 11 gate valve 24, the 12 gate valve 27, the 13 gate valve 28, material enters by the 14 gate valve 31 from pipeline 19 imports, first gate valve 9, entering preposition breakage pump 1 carries and fragmentation, entering first filter 2 by second gate valve 10 then filters, send into first storage tank 4 through the 3rd gate valve 11 by pusher pump 3 again, the material that stores in first storage tank 4 enters Homogenizing pump 5 homogeneous through the 5th gate valve 13 again and handles, material after the processing enters second filter 6 by the 6th gate valve 14 and filters once more, material after the filtration enters second storage tank 7 by the 7th gate valve 15 and the 8th gate valve 16 again and stores, by before the supercharging rear pump 8 superchargings output, do not open earlier the 9th gate valve 18 by the 17 gate valve 17.Take out a part of material by probe tube 30 on pipeline 19 between supercharging rear pump 8 and the 9th gate valve 18, this part material of taking-up detects the standard that whether reaches of seeing.If the standard of not reaching, carrying out the cyclic part homogeneous handles, no longer open the 9th gate valve 18 this moment, the material of second storage tank, 7 accumulation increases gradually, material liquid surface exceeds first return duct 20 and second storage tank, 7 junctions, be back to first storage tank 4 through return duct 20 then, handle again one time by Homogenizing pump 5, filter cyclic part once more.Equally also can open the 9th gate valve 18, reduce second storage tank, 7 output quantities by control, increase second storage tank, 7 input quantities simultaneously, when input quantity the time greater than output quantity, the accumulation of second storage tank, 7 materials is too much, and wherein partial material also can be handled one time by Homogenizing pump 5, filter cyclic part in first return duct 20 enters first storage tank 4 once more again.
Above-mentioned three kinds of situations when needs add chemicals, are added medicine in the grug feeding jar 33 in advance, just open the 14 gate valve the 34, the 15 gate valve 36, utilize water pump 35 that medicine is sent into pipeline 19 interior being mixed together with the preceding materials of processing and enter processing.
Claims (7)
1. oil and water separation equipment, comprise pipeline (19), filter and storage tank, it is characterized in that: be in series with preposition breakage pump (1), first filter (2), pusher pump (3), first storage tank (4), Homogenizing pump (5), second filter (6), second storage tank (7), supercharging rear pump (8) on the described pipeline (19) successively, in above-mentioned each device, the outlet of previous device links to each other with the import of a back device, and all devices all are communicated with; The pipeline (19) of described preposition breakage pump (1) entrance point is provided with first gate valve (9), pipeline (19) between described preposition breakage pump (1) and first filter (2) is provided with second gate valve (10), pipeline (19) between described first filter (2) and the pusher pump (3) is provided with the 3rd gate valve (11), pipeline (19) between described pusher pump (3) and first storage tank (4) is provided with the 4th gate valve (12), pipeline (19) between described first storage tank (4) and the Homogenizing pump (5) is provided with the 5th gate valve (13), pipeline (19) between described Homogenizing pump (5) and second filter (6) is provided with the 6th gate valve (14), be disposed with the 7th gate valve (15) and the 8th gate valve (16) on the pipeline (19) between described second filter (6) and second storage tank (7), pipeline (19) between described second storage tank (7) and the supercharging rear pump (8) is provided with the 17 gate valve (17), and the pipeline (19) of described supercharging rear pump (8) output is provided with the 9th gate valve (18); The charging aperture of described first storage tank (4) and second storage tank (7) all is positioned at storage tank top separately, and the discharging opening of this first storage tank (4) and second storage tank (7) all is positioned at storage tank bottom separately.
2. according to the described oil and water separation equipment of claim 1, it is characterized in that: be connected with first return duct (20) between described first storage tank (4) and second storage tank (7), described first return duct (20) all is higher than the charging aperture of storage tank separately with the junction of first storage tank (4) and second storage tank (7).
3. according to the described oil and water separation equipment of claim 2, it is characterized in that: be connected with second return duct (21) on described first return duct (20), these second return duct (21) one ends are connected first return duct (20) middle part, described second return duct (21) other end is connected on the pipeline (19) between first gate valve (9) and the preposition breakage pump (1), and described second return duct (21) is provided with the 16 gate valve (37).
4. according to the described oil and water separation equipment of claim 2, it is characterized in that: be parallel with first arm (22) on the pipeline (19) between described preposition breakage pump (1) and the pusher pump (3), this first arm (22) is provided with the tenth gate valve (23), the 11 gate valve (24) and the 3rd filter (25), and described the 3rd filter (25) is positioned between the tenth gate valve (23) and the 11 gate valve (24).
5. according to the described oil and water separation equipment of claim 2, it is characterized in that: be parallel with second arm (26) on the pipeline (19) between described Homogenizing pump (5) and the 8th gate valve (16), this second arm (26) is provided with the 12 gate valve (27), the 13 gate valve (28) and the 4th filter (29), and described the 4th filter (29) is positioned between the 12 gate valve (27) and the 13 gate valve (28).
6. according to the described oil and water separation equipment of claim 2, it is characterized in that: the probe tube (30) that is connected with the strap brake valve on the pipeline (19) between described supercharging rear pump (8) and the 9th gate valve (18).
7. according to the described oil and water separation equipment of claim 2, it is characterized in that: the pipeline (19) of described first gate valve (9) entrance point is provided with the 14 gate valve (31), pipeline (19) between described first gate valve (9) and the 14 gate valve (31) is gone up and is connected with grug feeding jar (33) through the 3rd arm (32), the 3rd arm also is provided with the 14 gate valve (34), water pump (35) and the 15 gate valve (36) on (32), and wherein water pump (35) is positioned between the 14 gate valve (34) and the 15 gate valve (36).
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| Application Number | Priority Date | Filing Date | Title |
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| CN2009101042782A CN101607146B (en) | 2009-07-07 | 2009-07-07 | Oil and water separation system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009101042782A CN101607146B (en) | 2009-07-07 | 2009-07-07 | Oil and water separation system |
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| CN101607146A CN101607146A (en) | 2009-12-23 |
| CN101607146B true CN101607146B (en) | 2011-11-02 |
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|---|---|---|---|---|
| US4324209A (en) * | 1978-12-26 | 1982-04-13 | Gerry Martin E | Fuel and water homogenizer and vaporizer and method therefor |
| CN1095311A (en) * | 1993-05-14 | 1994-11-23 | 郭三福 | The water-oil mixing method of low pollution, high burning efficiency and equipment thereof |
| CN1694946A (en) * | 2002-10-16 | 2005-11-09 | 朴吉远 | Apparatus for producing water-in-oil emulsified fuel and supplying the same |
| CN201454433U (en) * | 2009-07-07 | 2010-05-12 | 重庆明珠机电有限公司 | Oil separation system |
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2009
- 2009-07-07 CN CN2009101042782A patent/CN101607146B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4324209A (en) * | 1978-12-26 | 1982-04-13 | Gerry Martin E | Fuel and water homogenizer and vaporizer and method therefor |
| CN1095311A (en) * | 1993-05-14 | 1994-11-23 | 郭三福 | The water-oil mixing method of low pollution, high burning efficiency and equipment thereof |
| CN1694946A (en) * | 2002-10-16 | 2005-11-09 | 朴吉远 | Apparatus for producing water-in-oil emulsified fuel and supplying the same |
| CN201454433U (en) * | 2009-07-07 | 2010-05-12 | 重庆明珠机电有限公司 | Oil separation system |
Non-Patent Citations (1)
| Title |
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| JP特开2000-266012A 2000.09.26 |
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| CN101607146A (en) | 2009-12-23 |
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