CN102071056A - Recovery treatment device for aging oil of oil fields - Google Patents
Recovery treatment device for aging oil of oil fields Download PDFInfo
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- CN102071056A CN102071056A CN2010105917517A CN201010591751A CN102071056A CN 102071056 A CN102071056 A CN 102071056A CN 2010105917517 A CN2010105917517 A CN 2010105917517A CN 201010591751 A CN201010591751 A CN 201010591751A CN 102071056 A CN102071056 A CN 102071056A
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- 238000011084 recovery Methods 0.000 title abstract description 8
- 230000002431 foraging effect Effects 0.000 title abstract 2
- 230000032683 aging Effects 0.000 claims abstract description 57
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000000926 separation method Methods 0.000 claims abstract description 26
- 238000000034 method Methods 0.000 claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 239000002893 slag Substances 0.000 claims abstract description 14
- 239000010865 sewage Substances 0.000 claims abstract description 10
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 238000001914 filtration Methods 0.000 claims abstract description 3
- 238000004064 recycling Methods 0.000 claims description 15
- 230000003068 static effect Effects 0.000 claims description 14
- 235000011888 snacks Nutrition 0.000 claims description 8
- 229940126680 traditional chinese medicines Drugs 0.000 claims description 8
- 239000003814 drug Substances 0.000 claims description 5
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 230000008878 coupling Effects 0.000 claims description 2
- 238000010168 coupling process Methods 0.000 claims description 2
- 238000005859 coupling reaction Methods 0.000 claims description 2
- 239000003921 oil Substances 0.000 abstract description 90
- 239000010779 crude oil Substances 0.000 abstract description 9
- 239000003599 detergent Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 230000004899 motility Effects 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 238000004945 emulsification Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 230000005611 electricity Effects 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- 239000013043 chemical agent Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 241000406668 Loxodonta cyclotis Species 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000004087 circulation Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000002734 clay mineral Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000007764 o/w emulsion Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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Abstract
The invention discloses a recovery treatment device for aging oil of oil fields, which is mainly used for the centralized treatment for difficultly treated aging oil of oil and gas fields, and the recovery of crude oil resources. According to the sequence of process flow, the recovery treatment device for the aging oil mainly comprises a material hoisting system, a filtration system, a material-adding system, a heating/heat exchange system, a solid-liquid separation centrifuge, a slag collection box, an oil-water buffer tank and an oil-water separator. Heating/heat exchange and solid-liquid separation treatment processes can be selected according to the specific situation of aging oil to be treated; due to a skid-mounted design, the device is high in motility; the process can effectively treat the aging oil of oil field stations, recover effluent oil, and meter treated oil and water to count recovery efficiency; the recovered sewage can enter a sewage treatment system; and the water content ratio of recovered oil can reach the standard of detergent oil.
Description
Technical field
The present invention relates to a kind of ageing oil recycling and processing device of oilfield exploitation industry, be applicable to the various aging oil handling of land and offshore oil and gas field.
Background technology
Along with oilfield exploitation enters the middle and later periods, a large amount of reluctant ageing oils appears in each oil field, big land and offshore production platform in succession, has caused the waste of device processes capacity, brings hidden danger to system simultaneously.The ageing oil main source has three approach, the recovery sump oil of treatment systems such as sewage sedimentation, flotation, the profit transition layer in the water trap, the sump oil in the height emulsive crude oil emulsion in drilling well, operation and the transport process and the oil that lands, sewage/sump oil pond for recovering.According to above source analysis, ageing oil milk sap composition is extremely complicated, mainly comprises following characteristics:
Contain mechanical impuritys such as many clays, colloidal state FeS, mainly from the oily collection of landing of each oil field, sump oil recovery system etc., the existence of clay mineral can increase the emulsification depth that electricity takes off interior transition layer, height-increasing device electroconductibility to this part component.
The inorganic salts that water treatment system is introduced, mainly the oil slick from water treatment system reclaims, the type ageing oil has been carried the various inorganic water conditioner that adds in a large amount of water treatment systems secretly, add chemical agents such as the various sterilizations added in oil recovery, the defeated process of collection, scale inhibition, inhibiter, oil in water emulsion electroconductibility is big, particularly moisture high slightly, the ageing oil that the emulsification degree is high.
The light constituent volatilization is serious.Each elephant ageing oil is the process that long-term collection is handled again at present, this has just produced the volatilization of ageing oil light constituent, and colloid, bituminous matter component substantially exceed ordinary crude oils, adsorbs with solia particle, acting in conjunction has strengthened emulsification degree and dehydration difficulty to a greater degree in water-oil interface.
More than the problem degree difference of these problems in different ageing oils, component concentration is also different, the existence of these component characteristics can cause that self-cleaning oil is moisture to exceed standard, deviating from oil content of wastewater exceeds standard, and because ageing oil contains inorganic salt ionogen, clay etc., bring very big hidden danger for the dehydrating of crude oil treatment facility, cause that easily electricity takes off tripping operation, strides accident such as electric field, has shortened the work-ing life of equipment; A large amount of ageing oil transition layers exist in system, have wasted the useful space of treatment facility, have a strong impact on the ordinary production in oil field.
At present, the inherent ageing oil processing of industry aspect, there is not special processing unit to solve problem, more solution is to adopt back the mode of mixing processing, but this mode can not be dealt with problems at all, do not approved widely yet, it is very strong to return the contaminative of mixing ageing oil, the emulsification degree of meeting increase system crude oil, cause new electricity to take off problem, having result of study to claim back to mix aging oil mass can not surpass 10%, preferably is controlled at 5%, and this art breading efficient is very low, and mostly is ageing oil circulations in system.Patent CN200410013673.7, CN200620091934.1, CN200320126151.9 all discloses ageing oil and has handled new technology, but all rely on follow-up electro-dewatering technology, the pretreatment technology or the equipment that belong to ageing oil, only the ageing oil at certain type characteristic has proposed solution, and the ageing oil of inapplicable other component type, as high conduction high emulsibility ageing oil.
Summary of the invention
In view of These characteristics and present situation, the purpose of this invention is to provide a kind of oil field ageing oil recycling and processing device, effectively the independent system of treatment of aged oil is not relied on follow-up electro-dewatering technology fully, realize the thorough processing of crude oil, break away from of the puzzlement of each component of ageing oil original dewatering system.
For achieving the above object, technical scheme of the present invention is:
A kind of oil field ageing oil recycling and processing device, major function unit comprise ageing oil lifting system, filtering system, heating/heat-transmission system, solid-liquid centrifuge separator, slag trapping box, profit surge tank and oily water separation whizzer; Above-mentioned each functional unit is set up into sledge according to process sequence; According to the technical process order, ageing oil is lifted into sledge through screw rod lift pump 1,1 outlet of screw rod lift pump is connected with strainer 2 through pipe, strainer 2 is established bypass line, strainer 2 outlets connect under meter 3 through pipe, connect medicament static mixer 5 behind the under meter 3,5 outlets of medicament static mixer connect separation heat exchanging device 6 inlets through pipe, ageing oil enters solid-liquid separation centrifuge 16 after heat exchange, whizzer 16 slag-drip openings are through vertically being flexible coupling to mobile slag trapping box 11, whizzer 16 liquid outlets connect profit surge tank 13 through pipe, and surge tank 13 water outlets are promoted to oily water separation whizzer 10 inlets via screw rod lift pump 17, and the outlet of whizzer 10 profits is connected to respectively through pipe and purifies oil tank and Sewage treatment systems.
Described a kind of oil field ageing oil recycling and processing device, reserving hot water water mixing interface 15 on the trunk main of equipment, access point are located between under meter 3 outlets and static mixer 5 inlets.
Described a kind of oil field ageing oil recycling and processing device, equipment is furnished with chemicals dosing plant 14, add snack made with traditional Chinese medicines 4 be located under meter 3 and between between the static mixer 5, add snack made with traditional Chinese medicines 19 and be located in the profit surge tank.
Described a kind of oil field ageing oil recycling and processing device, the profit outlet of oily water separation whizzer is equipped with under meter 8,9.
Described a kind of oil field ageing oil recycling and processing device, described slag trapping box 11 adopts the airtight design of packaged type, and fast-open type deslagging side door 12 is established in the casing side.
Described a kind of oil field ageing oil recycling and processing device is provided with the bypass line 7 that selectivity is used solid-liquid separation centrifuge 16, slag trapping box 11 and profit buffer module 12 between the inlet of whizzer 16 and oily water separation whizzer 10 inlets.
The present invention has the following advantages: each equipment is assembled into sledge according to process sequence, adopts the packaged type design, and the assembling moving is convenient, can adapt to the probabilistic characteristics in short period, intermittence, place that ageing oil is handled; Fully taken into account the component difference of different ageing oils, had hot water water mixing mouth and solid-liquid separation system, to be suitable for different components ratio ageing oil; Adopted independently treatment process system, broken away from follow-up electro-dewatering technology, can not bring new problem, handled crude oil and reach the self-cleaning oil standard, disposed of sewage to Sewage treatment systems.
Description of drawings
Fig. 1 is a process flow sheet of the present invention
Number among the figure: 1 ageing oil lift pump, 2 strainers, 3 under meters, 4 add snack made with traditional Chinese medicines, 5 static mixers, 6 heated separators, 7 bypass pipes, 8 produce water ga(u)ge, 9 self-cleaning oil under meters, 10 oily water separation whizzers, 11 slag trapping box, 12 open side door soon, 13 profit surge tanks, 14 grug feeding jars, 15 mix the hot water mouth, 16 solid-liquid separation centrifuges, 17 profit lift pumps, 18 slag-drip openings, 19 add snack made with traditional Chinese medicines.
Embodiment
Below in conjunction with example explanation embodiments of the present invention shown in Figure 1, but the present invention is not limited to following example:
Embodiment one: ageing oil is lifted into sledge by screw rod lift pump 1, and pressure increases to 0.4MPa, and spiral pump 1 outlet is connected with blue formula strainer 2 through pipe, and strainer is established bypass line, and filter outlet connects under meter 3 through pipe, the about 2～3m of system handles flow
3/ h, Trunk Line is provided with hot water water mixing mouth 15 behind the under meter, draw from on-the-spot 100 ℃ of electro-dewatering water outlets, temperature rises to 50 ℃ and laggardly goes into Trunk Line medicine-feeding agent static mixer 5, the hot water that makes emulsion splitter and mix thorough mixing in system, adding snack made with traditional Chinese medicines 4 is located between water mixing mouth and the static mixer, the static mixer outlet connects separation heat exchanging device 6 inlets through pipe, crude oil temperature is promoted to by 50 ℃ and is higher than 85 ℃, the heat exchanger entrance tangential direction enters, be provided with slag-drip opening 18 at the bottom of the interchanger, to remove the solid slag that pre-separation goes out, high temperature ageing oil enters solid-liquid separation centrifuge 16 after heat exchange, the whizzer slag-drip opening is connected to mobile slag trapping box 11 through vertical tube, this sludge box adopts the design of shifting roller formula, but hand propelled moves concentrated outward transport after body refuse is collected; The whizzer liquid outlet connects profit surge tank 13 through pipe, add chemical agent in the surge tank, and be provided with whipping appts and tank level control system, with 17 interlocks of profit lift pump, the surge tank water outlet is promoted to vortex oily water separation whizzer 10 inlets via the profit lift pump, and the outlet of whizzer profit is connected to respectively through pipe and purifies oil tank and Sewage treatment systems.Be respectively equipped with under meter 8,9 at whizzer oil export and water out, with the profit amount that metering is produced, statistical treatment efficient, the body refuse component of trace is got rid of in sepn process simultaneously.Chemicals dosing plant and main process unit all are assembled into sledge in the system.Native system can effectively be handled the high slightly ageing oil of solid content, and solid-liquid separation is produced the slag oleaginousness less than 2%, produces the water oil-containing less than 1000mg/L, produces the fuel-displaced moisture self-cleaning oil standard that reaches.
Embodiment two: ageing oil is lifted into sledge by screw rod lift pump 1, and pressure increases to 0.5MPa, and spiral pump 1 outlet is connected with blue formula strainer 2 through pipe, and strainer is established bypass line, and filter outlet connects under meter 3 through pipe, the about 2m of system handles flow
3/ h, be provided with behind the under meter and add snack made with traditional Chinese medicines, enter medicament static mixer 5 on the Trunk Line afterwards, the hot water that makes emulsion splitter and mix thorough mixing in system, the static mixer outlet connects separation heat exchanging device 6 inlets through pipe, crude oil temperature is promoted to by 40 ℃ and is higher than 75 ℃, the heat exchanger entrance tangential direction enters, be provided with slag-drip opening 18 at the bottom of the interchanger, to remove a spot of solid slag in the ageing oil, after bypass line 7 directly enters vortex oily water separation whizzer 10, the outlet of whizzer profit is connected to respectively through pipe and purifies oil tank and Sewage treatment systems high temperature ageing oil through heat exchange.Be respectively equipped with under meter 8,9 at whizzer oil export and water out, with the profit amount that metering is produced, statistical treatment efficient is discharged a spot of body refuse component in the sepn process simultaneously.Chemicals dosing plant and main process unit all are assembled into sledge in the system.Native system can effectively be handled the low low relatively ageing oil of solid emulsification degree that contains, and produces the water oil-containing less than 500mg/L, produces the fuel-displaced moisture self-cleaning oil standard that reaches.
Claims (6)
1. oil field ageing oil recycling and processing device, it is characterized in that: this device major function unit comprises ageing oil lifting system, filtering system, heating/heat-transmission system, solid-liquid centrifuge separator, slag trapping box, profit surge tank and oily water separation whizzer; Above-mentioned each functional unit is set up into sledge according to process sequence; According to the technical process order, ageing oil is lifted into sledge through screw rod lift pump (1), screw rod lift pump (1) outlet is connected with strainer (2) through pipe, strainer (2) is established bypass line, strainer (2) outlet connects under meter (3) through pipe, connect medicament static mixer (5) behind the under meter (3), medicament static mixer (5) outlet connects separation heat exchanging device (6) inlet through pipe, ageing oil enters solid-liquid separation centrifuge (16) after heat exchange, whizzer (16) slag-drip opening is through vertically being flexible coupling to mobile slag trapping box (11), whizzer (16) liquid outlet connects profit surge tank (13) through pipe, surge tank (13) water outlet is promoted to oily water separation whizzer (10) inlet via screw rod lift pump (17), and the outlet of whizzer (10) profit is connected to respectively through pipe and purifies oil tank and Sewage treatment systems.
2. a kind of oil field according to claim 1 ageing oil recycling and processing device is characterized in that: reserving hot water water mixing interface (15) on the trunk main of equipment, access point are located between under meter (3) outlet and static mixer (5) inlet.
3. a kind of oil field according to claim 1 ageing oil recycling and processing device, it is characterized in that: equipment is furnished with chemicals dosing plant (14), add snack made with traditional Chinese medicines (4) be located under meter (3) and between between the static mixer (5), add snack made with traditional Chinese medicines (19) and be located in the profit surge tank.
4. a kind of oil field according to claim 1 ageing oil recycling and processing device is characterized in that: the profit outlet of oily water separation whizzer is equipped with under meter (8,9).
5. a kind of oil field according to claim 1 ageing oil recycling and processing device is characterized in that: described slag trapping box (11) adopts the airtight design of packaged type, and fast-open type deslagging side door (12) is established in the casing side.
6. a kind of oil field according to claim 1 ageing oil recycling and processing device is characterized in that: be provided with the bypass line (7) that selectivity is used solid-liquid separation centrifuge (16), slag trapping box (11) and profit buffer module (12) between the inlet of whizzer (16) and oily water separation whizzer (10) inlet.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010105917517A CN102071056A (en) | 2010-12-16 | 2010-12-16 | Recovery treatment device for aging oil of oil fields |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010105917517A CN102071056A (en) | 2010-12-16 | 2010-12-16 | Recovery treatment device for aging oil of oil fields |
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| CN102071056A true CN102071056A (en) | 2011-05-25 |
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| CN2010105917517A Pending CN102071056A (en) | 2010-12-16 | 2010-12-16 | Recovery treatment device for aging oil of oil fields |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106435785A (en) * | 2016-10-24 | 2017-02-22 | 中复神鹰碳纤维有限责任公司 | Oiling device and method for improving stability of oil agent |
| CN107090305A (en) * | 2017-02-23 | 2017-08-25 | 西南石油大学 | A kind of ageing oil in oil filed recycling and processing device and technique |
| CN107673503A (en) * | 2016-08-02 | 2018-02-09 | 中国石油化工股份有限公司 | A kind of recovery method of clear tank oil |
| CN112226247A (en) * | 2020-10-22 | 2021-01-15 | 东北石油大学 | Ageing oil dehydration processing system |
| CN114590925A (en) * | 2022-03-13 | 2022-06-07 | 郑凯 | Oil field station oil-water pollutant reduction optimization treatment method |
| CN114716073A (en) * | 2022-05-19 | 2022-07-08 | 克拉玛依市三达新技术股份有限公司 | Oil field aging oil treatment system and treatment method thereof |
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|---|---|---|---|---|
| JPS5337495A (en) * | 1976-09-18 | 1978-04-06 | Takashi Ooshimo | Method of determination of the quality of aged oil |
| CN2677000Y (en) * | 2003-12-11 | 2005-02-09 | 陈国信 | Complete equipment for treating oil field ageing oil |
| CN101386790A (en) * | 2008-10-17 | 2009-03-18 | 胜利油田胜利工程设计咨询有限责任公司 | Ground crude oil dewatering treater |
| CN201276539Y (en) * | 2008-10-15 | 2009-07-22 | 中国石油天然气股份有限公司 | Aged crude oil treatment device |
| CN201334378Y (en) * | 2009-01-14 | 2009-10-28 | 李继凤 | Hydrous heavy dirty oil treatment device in oil field |
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2010
- 2010-12-16 CN CN2010105917517A patent/CN102071056A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5337495A (en) * | 1976-09-18 | 1978-04-06 | Takashi Ooshimo | Method of determination of the quality of aged oil |
| CN2677000Y (en) * | 2003-12-11 | 2005-02-09 | 陈国信 | Complete equipment for treating oil field ageing oil |
| CN201276539Y (en) * | 2008-10-15 | 2009-07-22 | 中国石油天然气股份有限公司 | Aged crude oil treatment device |
| CN101386790A (en) * | 2008-10-17 | 2009-03-18 | 胜利油田胜利工程设计咨询有限责任公司 | Ground crude oil dewatering treater |
| CN201334378Y (en) * | 2009-01-14 | 2009-10-28 | 李继凤 | Hydrous heavy dirty oil treatment device in oil field |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107673503A (en) * | 2016-08-02 | 2018-02-09 | 中国石油化工股份有限公司 | A kind of recovery method of clear tank oil |
| CN106435785A (en) * | 2016-10-24 | 2017-02-22 | 中复神鹰碳纤维有限责任公司 | Oiling device and method for improving stability of oil agent |
| CN107090305A (en) * | 2017-02-23 | 2017-08-25 | 西南石油大学 | A kind of ageing oil in oil filed recycling and processing device and technique |
| CN107090305B (en) * | 2017-02-23 | 2018-09-11 | 西南石油大学 | A kind of ageing oil in oil filed recycling and processing device and technique |
| CN112226247A (en) * | 2020-10-22 | 2021-01-15 | 东北石油大学 | Ageing oil dehydration processing system |
| CN114590925A (en) * | 2022-03-13 | 2022-06-07 | 郑凯 | Oil field station oil-water pollutant reduction optimization treatment method |
| CN114590925B (en) * | 2022-03-13 | 2023-12-15 | 大庆中道易成石油科技有限公司 | Oil field station oil-water pollutant reduction optimization treatment method |
| CN114716073A (en) * | 2022-05-19 | 2022-07-08 | 克拉玛依市三达新技术股份有限公司 | Oil field aging oil treatment system and treatment method thereof |
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Application publication date: 20110525 |