CN105688571A - Oil recovery and processing system - Google Patents
Oil recovery and processing system Download PDFInfo
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- CN105688571A CN105688571A CN201610161310.0A CN201610161310A CN105688571A CN 105688571 A CN105688571 A CN 105688571A CN 201610161310 A CN201610161310 A CN 201610161310A CN 105688571 A CN105688571 A CN 105688571A
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- water separator
- oil
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- oil water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/40—Combinations of devices covered by groups B01D45/00 and B01D47/00
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0211—Separation of non-miscible liquids by sedimentation with baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/10—Treatment of sludge; Devices therefor by pyrolysis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/16—Treatment of sludge; Devices therefor by de-watering, drying or thickening using drying or composting beds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Analytical Chemistry (AREA)
- Developing Agents For Electrophotography (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention relates to an oil recovery and processing system, which comprises a cyclone dust remover, a spraying processing tower and an oil-water separator, wherein the cyclone dust remover is connected in front of the spraying processing tower through a gas conveying pipe; the oil-water separator is arranged right under the spraying processing tower, and comprises a conical inlet, a vertical passage, a conical outlet and a conical separation plate; an annular outlet is formed between the conical separation plate and the vertical passage; the lower end of the oil-water separator is provided with a sedimentation chamber; the lowest end of the sedimentation chamber is provided with a water discharge passage; the water discharge passage is connected onto a spray head arranged in the spraying processing tower; the outer surface of the cyclone dust remover is provided with a heating sleeve; a heating coil is arranged between the heating sleeve and the cyclone dust remover. The oil recovery and processing system solves the problem that heavy oil and light oil cannot be directly separated; the heavy oil, the light oil and dust can be more thoroughly removed from smoke gas, so that the equipment operation is smoother.
Description
Technical field
The present invention relates to a kind of Oil recovery and process system, particularly relate to the equipment that a kind of high-temperature flue gas that oily sludge is produced in mummification and pyrolysis charring process processes。
Background technology
According to statistics, the generation amount of the oil recovery business oily sludge of China is more than million tons。Containing bulk petroleum hydro carbons in oily sludge, if not utilizing, not only wasting petroleum resources, and because moisture content is higher, sludge volume is relatively larger, it is necessary to takies large-area soil and carries out storing or filling, easily to environment。Treatment technology for oily sludge has burning, biological treatment and pyrolysis etc. both at home and abroad。The pyrolysis charring of oily sludge is adopted by industry gradually as the comparatively effective resource treatment technique of one。
Application number disclosed in 29 days July in 2015 be 201520099383.2 innovation and creation disclose a kind of smoke processing system, it utilizes treating column, spray thrower and oil scraping mechanism etc. to complete three phase separation, solve pyrolysis gas in entering the process entering pipeline after condensation process, be susceptible to the problem of blocking, and utilize oil scraping mechanism to reclaim mink cell focus and light oil。But, mink cell focus and the light oil collected due to these innovation and creation are not easily separated, mix, cause separately utilizing in the occasion of mink cell focus and light oil at many needs, the special equipment mink cell focus to collecting and light oil is needed to be easily separated, adding man-hour, improve cost, utilization rate of equipment and installations is not high；And, in use finding, these innovation and creation are not thorough to the collection of dust and oil point, and blockage problem still can occur, and the properly functioning generation harmful effect to equipment, even if increasing cyclone dust collector, effect is also unsatisfactory。
Summary of the invention
It is an object of the invention to for the deficiencies in the prior art part, overcome mink cell focus and problem that light oil can not be made directly separation, mink cell focus and light oil is made to be done directly separation at collection phase, and more thoroughly mink cell focus and light oil and dust are removed from flue gas, the operating making equipment is more smoothly。
A kind of Oil recovery processes system, including cyclone dust extractor, spray treating column and oil water separator, being provided with smoke feed pipe on described cyclone dust extractor, described cyclone dust extractor is connected to by air shooter before spray treating column, and described oil water separator is arranged on immediately below spray treating column；The outer wall of described oil water separator and described spray treating column is tubular and is coaxially disposed, and air shooter is arranged between spray treating column and oil water separator；Described oil water separator includes tapered inlet, Vertical Channel, conical outlet and conical baffle, and described tapered inlet is arranged on directly over conical outlet, and described Vertical Channel upper end connects with tapered inlet, and described Vertical Channel lower end connects with conical outlet；Described conical baffle lower end is connected to the inside outer wall of described oil water separator, and described conical baffle upper end is between tapered inlet lower end and conical baffle lower end；Ring exit is formed between described conical baffle and described Vertical Channel；Described oil water separator lower end is provided with expansion chamber, and described expansion chamber is that inverted cone is connected with the outer wall of oil water separator, the axis of described expansion chamber and the dead in line of oil water separator；Described expansion chamber bottom is provided with drainage channel, and described drainage channel is connected on the shower nozzle in spray treating column；Described cyclone dust extractor outer surface is provided with and adds hot jacket, described in add and between hot jacket and cyclone dust extractor, be provided with heating coil。
As improvement, the inside outer wall of described oil water separator is provided with sensor；Being provided with light oil outlet and mink cell focus outlet on the outer wall of described oil water separator, described light oil exports between described conical baffle top and bottom, and described mink cell focus exports between conical baffle lower end and expansion chamber upper end。
As improvement, being provided with rotation element in described conical outlet, described rotation element is disc, the axis of described rotation element and the dead in line of Vertical Channel；Described rotation element is between conical outlet top and bottom。
As improvement, being provided with discharge duct in described Vertical Channel, described discharge duct upper end is that circular arc is bent downwardly；Described discharge duct upper end open is between tapered inlet top and bottom, and described discharge duct lower end is in Vertical Channel lower end and rotates between element upper end。
As improvement, described sensor can be pressure transducer, described pressure transducer at least two, and two pressure transducers are between conical baffle lower end and expansion chamber upper end；Two pressure transducers are vertically arranged up and down, lay respectively on the upper end of mink cell focus outlet and under the lower end of mink cell focus outlet。
As improvement, being provided with horizontal comb in described spray treating column, described horizontal comb is arranged on spray treating column inside outer wall, is positioned on air shooter；At least provided with a shower nozzle in described spray treating column, described shower nozzle is arranged on described horizontal comb top；Being provided with packing layer on described horizontal comb, described packing layer upper end is positioned under described shower nozzle。
As improvement, described spray treating column top offers gas passage mouth, and described gas passage mouth connects gas passage, is provided with condensation plate in described gas passage, and described condensation plate is a kind of fold-line-shaped plate with holes, and described condensation plate is positioned at gas passage mouth place。
As improvement, described ring exit and described Vertical Channel coaxial line；The dead in line of the axis of described Vertical Channel and described oil water separator。
Beneficial effects of the present invention:
(1) present invention utilizes the special construction of oil water separator, make mink cell focus and light oil autologous density can be relied on to make mink cell focus and light oil be able to separate collection in the oil-water separation stage, avoid increasing subsequent technique and man-hour the mink cell focus to collecting and light oil be easily separated, decrease man-hour, reduce cost, improve the utilization ratio of equipment, and spray treating column, oil water separator, expansion chamber and conical baffle coaxial line, it is ensured that stability when spray treating column and oil water separator operating。
(2) oil water separator of the present invention conical outlet in arrange rotate element the liquid in oil water separator can be stirred, while acceleration mink cell focus separates with light oil, rotate when element rotates and may also reach up the unforeseeable effect of such a:, when rotating element rotation, rotate member upper and can form low-pressure area, facilitate the liquid in Vertical Channel to circulate downwards；Additionally, rotate and can also apply pressure to rotating element lower portions liquid when element rotates, force liquid below conical outlet to flow to oil water separator surrounding so that it is in mink cell focus and light oil float up, it is to avoid part mink cell focus and light oil are trapped near conical outlet to be difficult to discharge。
(3) it is provided with discharge duct in the Vertical Channel of the present invention, it is to avoid build-up of air in conical outlet, hinders downward liquid flow in Vertical Channel。
(4) present invention utilizes heating coil that cyclone dust extractor is heated, make to be higher than flue gas dew point temperature with the surface temperature of high-temperature flue gas contact surface in cyclone dust extractor, avoid the generation of leak source corrosion phenomenon, ensure that flue gas maintains higher temperature in two stage treatment tower simultaneously, the a large amount of vaporific water droplet produced when utilizing the water that high-temperature flue gas sprays out with shower nozzle to contact, composition condensable in flue gas is carried out condensation adsorption, condensable composition is condensed by endothermic reaction when simultaneously moisture can also be utilized to evaporate, additionally, utilize and heating-up temperature can be had more flexible control during heating coils heat。
(5) present invention first pass through cyclone dust extractor carry out independent dust removal process again through spray treating column in shower nozzle carried out spray process, and dust is very easily adhere to a large amount of mink cell focus and light oil composition, first carry out mink cell focus and light oil composition that independent dust removal process is equivalent to remove in flue gas one step ahead, thus the mink cell focus more thoroughly removed in flue gas and light oil composition, dust itself is also able to more remove thoroughly simultaneously。
(6) packing layer that the present invention adopts makes the gas of rising longer with the time of contact of the ejecting liquid of decline, contact more abundant, what in gas, the condensation process of mink cell focus and light oil composition carried out is more abundant, and mink cell focus and lightweight oil separating are more thorough。
(7) high-temperature flue gas is through the process of cyclone dust extractor of the present invention, in gas, solid content is few, therefore the moisture in expansion chamber can be circulated utilization, it is to avoid often the water in expansion chamber is carried out purified treatment, while having saved water resource, decrease cost；Simultaneously containing part mink cell focus and light oil in recirculated water, this part mink cell focus and light oil with water when packing layer declines, stickiness by oil itself can reduce the speed that liquid declines in packing layer, thus increasing the time of contact of liquid and uprising gas, make contact more abundant, in gas, the condensation process of mink cell focus and light oil composition is more abundant, and mink cell focus and lightweight oil separating are more thorough。
Accompanying drawing explanation
For clearer explanation technical scheme, below the accompanying drawing used required during embodiment is described is briefly described, apparently, drawings discussed below is only some embodiments of the present invention, for those of ordinary skill in the art, under the premise not paying creative work, it is also possible to obtain other accompanying drawings according to these accompanying drawings。
Fig. 1 is that Oil recovery processes system schematic。
Fig. 2 is cyclone dust extractor schematic diagram。
Fig. 3 is spray treating column and oil water separator schematic diagram。
Label declaration:
1. smoke feed pipe, 2. cyclone dust extractor, 20. add hot jacket, 21. air shooter, 22. heating coil, 3. spray treating columns, 30. outer wall, 31. horizontal combs, 32. packing layers, 33. shower nozzle, 34. gas passage mouths, 35. gas passages, 36. condensation plate, 4. oil water separator, 4a. expansion chamber, 4b. sensor, 41. tapered inlet, 42. Vertical Channel, 43. conical outlet, 44. conical baffle, 45. ring exits, 46. light oil outlets, 47. mink cell focus exports, 48. drainage channel, 49. discharge ducts, 410. rotate element。
Detailed description of the invention
Below in conjunction with accompanying drawing, technical scheme is illustrated clearly and completely。
Embodiment
Fig. 1 is that Oil recovery processes system schematic, Fig. 2 is cyclone dust extractor schematic diagram, Fig. 3 is spray treating column and oil water separator schematic diagram。As shown in Figure 1, Figure 2 and Figure 3, the present embodiment provides a kind of Oil recovery and processes system, including cyclone dust extractor 2, spray treating column 3 and oil water separator 4, described cyclone dust extractor 2 is provided with smoke feed pipe 1, described cyclone dust extractor 2 is connected to by air shooter 21 before spray treating column 3, and described oil water separator 4 is arranged on immediately below spray treating column 3；The outer wall 30 of described oil water separator 4 and described spray treating column 3 for tubular and is coaxially disposed, and air shooter 21 is arranged between spray treating column 3 and oil water separator 4；Described oil water separator 4 includes tapered inlet 41, Vertical Channel 42, conical outlet 43 and conical baffle 44, described tapered inlet 41 is arranged on directly over conical outlet 43, described Vertical Channel 42 upper end connects with tapered inlet 41, and described Vertical Channel 42 lower end connects with conical outlet 43；Described conical baffle 44 lower end is connected to inside the outer wall 30 of described oil water separator 4, and described conical baffle 44 upper end is between tapered inlet 41 lower end and conical baffle 44 lower end；Ring exit 45 is formed between described conical baffle 44 and described Vertical Channel 42；It is that inverted cone is connected with the outer wall 30 of oil water separator 4 that described oil water separator 4 lower end is provided with expansion chamber 4a, described expansion chamber 4a, the axis of described expansion chamber 4a and the dead in line of oil water separator 4；Described expansion chamber 4a bottom is provided with drainage channel 48, and described drainage channel 48 is connected on the shower nozzle 33 in spray treating column 3；Described cyclone dust extractor 2 outer surface is provided with and adds hot jacket 20, described in add be provided with between hot jacket 20 and cyclone dust extractor 2 heating coil 22；It is provided with sensor 4b inside the outer wall 30 of described oil water separator 4；Being provided with light oil outlet 46 and mink cell focus outlet 47 on the outer wall 30 of described oil water separator 4, the outlet 46 of described light oil is between described conical baffle 44 top and bottom, and the outlet 47 of described mink cell focus is between conical baffle 44 lower end and expansion chamber 4a upper end；Being provided with rotation element 410 in described conical outlet 43, described rotation element (410) is disc, the axis of described rotation element 410 and the dead in line of Vertical Channel 42；Described rotation element 410 is between conical outlet 43 top and bottom；Being provided with discharge duct 49 in described Vertical Channel 42, described discharge duct 49 upper end is that circular arc is bent downwardly；Described discharge duct 49 upper end open is between tapered inlet 41 top and bottom, and described discharge duct 49 lower end is in Vertical Channel 42 lower end and rotates between element 410 upper end；Described sensor 4b can be pressure transducer, described pressure transducer at least two, and two pressure transducers are between conical baffle 44 lower end and expansion chamber 4a upper end；Two pressure transducers are vertically arranged up and down, lay respectively on the upper end of mink cell focus outlet 47 and under the lower end of mink cell focus outlet 47；Being provided with horizontal comb 31 in described spray treating column 3, described horizontal comb 31 is arranged on inside spray treating column 3 outer wall 30, is positioned on air shooter 21；At least provided with a shower nozzle 33 in described spray treating column 3, described shower nozzle is arranged on described horizontal comb 31 top；Being provided with packing layer 32 on described horizontal comb 31, described packing layer 32 upper end is positioned under described shower nozzle 33；Described spray treating column 3 top offers gas passage mouth 34, described gas passage mouth 34 connects gas passage 35, being provided with condensation plate 36 in described gas passage 35, described condensation plate 36 is a kind of fold-line-shaped plate with holes, and described condensation plate 36 is positioned at gas passage mouth 34 place；Described ring exit 45 and described Vertical Channel 42 coaxial line；The dead in line of the axis of described Vertical Channel 42 and described oil water separator 4；Described mink cell focus outlet 47 and light oil export in 46 pipelines and are provided with valve；The valve liquid level in order to regulate in oil water separator it is provided with in described drainage channel 48。
Work process: the high-temperature flue gas that oily sludge produces in mummification and pyrolysis charring process first enters cyclone dust extractor 2 from smoke feed pipe 1, remove the dust granules carried in smoke, flue gas enters spray treating column 3 through air shooter 21 after cyclone dust extractor 2, flue gas passes upward through horizontal comb 31 and packing layer 32, contact with downward ejecting liquid in packing layer, condensable part flows to expansion chamber 4a with ejecting liquid through oil water separator 4, ejecting liquid flows out conical outlet 43 from Vertical Channel 42 through the stirring of over-rotation element 410, the light oil that density is little exports 46 through ring exit 45 from light oil and separates；The slightly larger mink cell focus of density is stayed and is exported 47 from mink cell focus under conical baffle 44 and separate。It is exactly specifically: reach pressure P set in advance when mink cell focus exports pressure transducer 4b above, when the pressure below sensor of mink cell focus outlet simultaneously reaches P+ Δ p, opens mink cell focus outlet valve, make mink cell focus separate。When mink cell focus exports pressure transducer above not up to pressure P set in advance, or when mink cell focus exports pressure below sensor more than P+ Δ p, close mink cell focus outlet valve。The moisture of expansion chamber lower floor flows to shower nozzle 33 through drainage channel 48。It is pointed out that described Δ p is described mink cell focus pressure differential between said two pressure transducer 4b in described oil water separator 4；Regulate the valve in drainage channel 48 can the displacement that drainage channel 48 is discharged be finely tuned。Flue gas can not condensation portion enter in gas passage 35 from gas passage mouth 34。In flue gas can not condensation portion through condensation plate 36 time, the condensation plate 36 that smoke contacts temperature containing a large amount of water vapour is relatively low, making a large amount of water vapour be condensed into droplet, the mink cell focus in flue gas and light oil composition are condensed in flowing downward entrance spray treating column 3 along condensation plate 36 by droplet；Additionally, droplet on condensation plate 36 also has a unforeseeable effect, that is: the globule on condensation plate 36 is not before falling within spray treating column 3, forms, on condensation plate 36, the effect being similar to cascade, it is possible to mink cell focus and light oil composition to a small amount of non-total condensation condense。
The above; being only the present invention preferably detailed description of the invention, but protection scope of the present invention is not limited thereto, any those familiar with the art is in the technical scope that the invention discloses; the change that can readily occur in or replacement, all should be encompassed within protection scope of the present invention。Therefore, protection scope of the present invention should be as the criterion with the protection domain of claims。
Claims (8)
1. an Oil recovery processes system, it is characterized in that: include cyclone dust extractor (2), spray treating column (3) and oil water separator (4), described cyclone dust extractor (2) is provided with smoke feed pipe (1), described cyclone dust extractor (2) is connected to by air shooter (21) before spray treating column (3), and described oil water separator (4) is arranged on immediately below spray treating column (3)；The outer wall (30) of described oil water separator (4) and described spray treating column (3) for tubular and is coaxially disposed, and air shooter (21) is arranged between spray treating column (3) and oil water separator (4)；Described oil water separator (4) includes tapered inlet (41), Vertical Channel (42), conical outlet (43) and conical baffle (44), described tapered inlet (41) is arranged on directly over conical outlet (43), described Vertical Channel (42) upper end connects with tapered inlet (41), and described Vertical Channel (42) lower end connects with conical outlet (43)；Described conical baffle (44) lower end is connected to outer wall (30) inner side of described oil water separator (4), and described conical baffle (44) upper end is positioned between tapered inlet (41) lower end and conical baffle (44) lower end；Ring exit (45) is formed between described conical baffle (44) and described Vertical Channel (42)；Described oil water separator (4) lower end is provided with expansion chamber (4a), described expansion chamber (4a) is connected with the outer wall of oil water separator (4) (30) in inverted cone, the dead in line of the axis of described expansion chamber (4a) and oil water separator (4)；Described expansion chamber (4a) bottom is provided with drainage channel (48), and described drainage channel (48) is connected on the shower nozzle (33) in spray treating column (3)；Described cyclone dust extractor (2) outer surface is provided with and adds hot jacket (20), described in add be provided with between hot jacket (20) and cyclone dust extractor (2) heating coil (22)。
2. a kind of Oil recovery as claimed in claim 1 processes system, it is characterised in that: outer wall (30) inner side of described oil water separator (4) is provided with sensor (4b)；The outer wall (30) of described oil water separator (4) is provided with light oil outlet (46) and mink cell focus outlet (47), described light oil outlet (46) is positioned between described conical baffle (44) top and bottom, and described mink cell focus outlet (47) is positioned between conical baffle (44) lower end and expansion chamber (4a) upper end。
3. a kind of Oil recovery as claimed in claim 1 processes system, it is characterized in that: in described conical outlet (43), be provided with rotation element (410), described rotation element (410) is disc, the axis of described rotation element (410) and the dead in line of Vertical Channel (42)；Described rotation element (410) is positioned between conical outlet (43) top and bottom。
4. a kind of Oil recovery as claimed in claim 3 processes system, it is characterised in that: being provided with discharge duct (49) in described Vertical Channel (42), described discharge duct (49) upper end is that circular arc is bent downwardly；Described discharge duct (49) upper end open is positioned between tapered inlet (41) top and bottom, and described discharge duct (49) lower end is positioned at Vertical Channel (42) lower end and rotates between element (410) upper end。
5. a kind of Oil recovery as claimed in claim 2 processes system, it is characterized in that: described sensor (4b) can be pressure transducer, described pressure transducer at least two, two pressure transducers are positioned between conical baffle (44) lower end and expansion chamber (4a) upper end；Two pressure transducers are vertically arranged up and down, lay respectively on the upper end of mink cell focus outlet (47) and under the lower end of mink cell focus outlet (47)。
6. a kind of Oil recovery as claimed in claim 1 processes system, it is characterized in that: in described spray treating column (3), be provided with horizontal comb (31), described horizontal comb (31) is arranged on spray treating column (3) outer wall (30) inner side, is positioned on air shooter (21)；At least provided with a shower nozzle (33) in described spray treating column (3), described shower nozzle is arranged on described horizontal comb (31) top；Being provided with packing layer (32) on described horizontal comb (31), described packing layer (32) upper end is positioned under described shower nozzle (33)。
7. a kind of Oil recovery as claimed in claim 1 processes system, it is characterized in that: described spray treating column (3) top offers gas passage mouth (34), described gas passage mouth (34) connects gas passage (35), described gas passage (35) is provided with condensation plate (36), described condensation plate (36) is a kind of fold-line-shaped plate with holes, and described condensation plate (36) is positioned at gas passage mouth (34) place。
8. a kind of Oil recovery as claimed in claim 1 processes system, it is characterised in that: described ring exit (45) and described Vertical Channel (42) coaxial line；The dead in line of the axis of described Vertical Channel (42) and described oil water separator (4)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610161310.0A CN105688571A (en) | 2016-03-21 | 2016-03-21 | Oil recovery and processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610161310.0A CN105688571A (en) | 2016-03-21 | 2016-03-21 | Oil recovery and processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105688571A true CN105688571A (en) | 2016-06-22 |
Family
ID=56232193
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610161310.0A Withdrawn CN105688571A (en) | 2016-03-21 | 2016-03-21 | Oil recovery and processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105688571A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106823578A (en) * | 2017-03-03 | 2017-06-13 | 北京朗净时代环境科技有限公司 | A kind of cyclone demisting dust arrester |
| CN107617299A (en) * | 2017-10-31 | 2018-01-23 | 湖北力帝机床股份有限公司 | Disintegrating machine fire prevention dust pelletizing system |
| CN113088316A (en) * | 2021-03-27 | 2021-07-09 | 西南石油大学 | Oil-water mixed steam condensing system containing drilling cutting dust and condensing method |
-
2016
- 2016-03-21 CN CN201610161310.0A patent/CN105688571A/en not_active Withdrawn
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106823578A (en) * | 2017-03-03 | 2017-06-13 | 北京朗净时代环境科技有限公司 | A kind of cyclone demisting dust arrester |
| CN107617299A (en) * | 2017-10-31 | 2018-01-23 | 湖北力帝机床股份有限公司 | Disintegrating machine fire prevention dust pelletizing system |
| CN113088316A (en) * | 2021-03-27 | 2021-07-09 | 西南石油大学 | Oil-water mixed steam condensing system containing drilling cutting dust and condensing method |
| CN113088316B (en) * | 2021-03-27 | 2022-04-12 | 西南石油大学 | Oil-water mixed steam condensing system containing drilling cutting dust and condensing method |
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