CN206647093U - A kind of surface technology processing system of more series of strata yard different disposal scales - Google Patents
A kind of surface technology processing system of more series of strata yard different disposal scales Download PDFInfo
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- CN206647093U CN206647093U CN201720294453.9U CN201720294453U CN206647093U CN 206647093 U CN206647093 U CN 206647093U CN 201720294453 U CN201720294453 U CN 201720294453U CN 206647093 U CN206647093 U CN 206647093U
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Abstract
It the utility model is related to a kind of surface technology processing system of more series of strata yard different disposal scales, the coming oil manifold of each series of strata is sequentially connected ball collecting chamber, heating furnace, three phases separator, and the oil exports of all three phases separators connects crude oil output pipeline after being sequentially connected overflow settling tank, purification oil tank, oil transfer pump；Coming oil manifold, ball collecting chamber, heating furnace, the three phases separator of each series of strata are also connected by manifold with other series of strata；Valve is provided with all connection manifolds, the utility model passes through " connection in series-parallel of different layers position distinct device " and " with the connection in series-parallel of layer position distinct device ", solves " under the premise of bilayer system exploitation scale is uncertain; crude Treatment macro ratio distributes " problem, optimized the surface technology of more series of strata oil field gathering and transportation yards, energy consumption is reduced, surface construction investment is saved, improves oil field development comprehensive utilization benefit.
Description
Technical field
The utility model belongs to oil gas field exploitation technology field, and in particular to a kind of more series of strata yard different disposal rule
The surface technology processing system of mould, be specifically one kind be related in oilfield surface construction engineering oil-collecting in station, heating, dehydration,
The outer defeated defeated processing system of collection of crude oil supercharging.
Background technology
Due to Changqing oilfields Productivity Construction demand：Construction station is more, scale is big（Nearly more than 10 seat multi-purpose station, 50 are built every year
Remaining seat block station）, rhythm is fast, deployment adjustment is frequent, more series of strata overlapping development modes（It is related to double-deck system and more series of strata yards is up to
More than half）, while using rolling development pattern, while exploitation, while recognize, side adjust, uncertain factor is more, change greatly, cause
Make the treatment scale ratio of multiple layers of position can not determine.This uncertainty seriously governs multi-purpose station lectotype selection and technique stream
The selection of journey.In view of large and medium-sized yard reduces expropriation of land, reduces investment, one-stage completion is avoided transforming difficulty repeatedly, how adapted to
In the case of more series of strata oil field development scales are uncertain, the flow of dewatering system is rationally set, and meets different scales ratio
Flow assignment problem, it is desirable to must adapt to modification scenario change needs.
Utility model content
The purpose of this utility model is in order that the surface technology of more series of strata oil field gathering and transportation yards is optimized, and reduces energy
Consumption, surface construction investment is saved, improves oil field development comprehensive utilization benefit.
Therefore, the utility model provides a kind of surface technology processing system of more series of strata yard different disposal scales, bag
The coming oil manifold of more series of strata is included, the coming oil manifold of each series of strata is sequentially connected a ball collecting chamber, a heating furnace, an oil gas water
Three phase separator, the gas outlet of all three phases separators are connected to associated gas knockout, all oil gas water together
The water out of three phase separator is connected to water process dress system together, the oil exports of all three phases separators together according to
Crude oil output pipeline is connected after secondary connection overflow settling tank, purification oil tank, oil transfer pump；Described heating furnace also by manifold with
Overflow settling tank is directly connected, and the oil export of three phases separator is also directly connected by manifold with oil transfer pump；
The coming oil manifold of each series of strata is also connected by manifold with the ball collecting chamber of other series of strata；The ball collecting chamber of each series of strata is also
Connected by manifold with the heating furnace of other series of strata；The heating furnace of each series of strata also passes through manifold and the oil gas water three of other series of strata
Phase separator or the connection of overflow settling tank；
Valve is provided with all connection manifolds.
The gas outlet of described associated gas knockout is to heating furnace.
A kind of surface technology processing system of bilayer system yard different disposal scale, including coming oil manifold A and coming oil manifold
B, coming oil manifold A are sequentially connected ball collecting chamber A, heating furnace A, three phases separator A, and coming oil manifold B is sequentially connected ball collecting chamber
B, heating furnace B, three phases separator B, three phases separator A and three phases separator B gas outlet are together
It is connected to associated gas knockout；Three phases separator A and three phases separator B water out are connected at water together
Manage dress system；Three phases separator A and three phases separator B oil exports are sequentially connected overflow settling tank, purification oil
Crude oil output pipeline is connected after storage tank, oil transfer pump；
Described heating furnace A and heating furnace B is also directly connected by manifold with overflow settling tank, three phases separator
A and three phases separator B oil export are also directly connected by manifold with oil transfer pump；
Described coming oil manifold A is also connected by manifold with ball collecting chamber B, and described coming oil manifold B is also by manifold with receiving
Ball cylinder A is connected；Described ball collecting chamber A is also connected by manifold with heating furnace B, and described ball collecting chamber B also passes through manifold and heating
Stove A is connected；Described heating furnace A is also connected by manifold with three phases separator B, and described heating furnace B also passes through pipe
Remittance connects with three phases separator A；
Valve is provided with all connection manifolds.
The gas outlet of described associated gas knockout is respectively communicated to heating furnace A and heating furnace B.
The surface technology processing systems of this more series of strata yard different disposal scales provided by the utility model and method
Beneficial effect：
1st, this technology processing system realizes the totally-enclosed processing of more series of strata.
2nd, this technology processing system passes through " different layers position distinct device（Heating furnace, three phases separator, overflow are sunk
Tank drops）Connection in series-parallel " and " with layer position distinct device（Three phases separator, overflow settling tank）Connection in series-parallel ", solve
" under the premise of bilayer system exploitation scale is uncertain, the distribution of crude Treatment macro ratio " problem.
3rd, this technology processing system by realize valve member adjust, improve yard adaptability, reduce the construction period and
Construction investment.
4th, production operation is convenient, saves furnace fuel.
Brief description of the drawings
The utility model is described in further details below with reference to accompanying drawing.
Fig. 1 is system structure diagram of the present utility model.
Description of reference numerals：1st, coming oil manifold；2nd, ball collecting chamber；3rd, heating furnace；4th, three phases separator；5th, associated gas
Knockout；6th, overflow settling tank；7th, oil tank is purified；8th, oil transfer pump.
Embodiment
Embodiment 1：
The present embodiment provides a kind of surface technology processing system of more series of strata yard different disposal scales, as shown in figure 1, bag
The coming oil manifold 1 of more series of strata is included, the coming oil manifold 1 of each series of strata is sequentially connected 3, one, the heating furnace oil of ball collecting chamber 2, one
Gas-water separator 4, the gas outlet of all three phases separators 4 are connected to associated gas knockout 5, associated gas together
The gas outlet of knockout 5 is to heating furnace 3；The water out of all three phases separators 4 is connected to water process together
Dress system, the oil export of all three phases separators 4 are sequentially connected overflow settling tank 6, purify oil tank 7, be defeated together
Crude oil output pipeline is connected after oil pump 8；Described heating furnace 3 is also directly connected by manifold with overflow settling tank 6, oil gas water three
The oil export of phase separator 4 is also directly connected by manifold with oil transfer pump 8；
The coming oil manifold 1 of each series of strata is also connected by manifold with the ball collecting chamber 2 of other series of strata；The ball collecting chamber of each series of strata
2 are also connected by manifold with the heating furnace 3 of other series of strata；The heating furnace 3 of each series of strata also passes through manifold and the oil of other series of strata
Gas-water separator 4 or overflow settling tank 6 connect；
Valve is provided with all connection manifolds.
The present embodiment passes through " connection in series-parallel of different layers position distinct device " and " with the connection in series-parallel of layer position distinct device ", solution
Certainly problem " under the premise of bilayer system exploitation scale is uncertain, the distribution of crude Treatment macro ratio ", reduces energy consumption, saves
Surface construction is invested.
Embodiment 2：
As shown in figure 1, a kind of surface technology processing system of bilayer system yard different disposal scale, including coming oil manifold A
Ball collecting chamber A, heating furnace A, three phases separator A are sequentially connected with coming oil manifold B, coming oil manifold A, coming oil manifold B is successively
Connect ball collecting chamber B, heating furnace B, three phases separator B, three phases separator A and three phases separator B
Gas outlet is connected to associated gas knockout 5 together, and the gas outlet of associated gas knockout 5 is respectively communicated to heating furnace A and heating furnace
B；Three phases separator A and three phases separator B water out are connected to water process dress system together；Oil gas water three
Phase separator A and three phases separator B oil exports connect after being sequentially connected overflow settling tank 6, purification oil tank 7, oil transfer pump 8
Connect crude oil output pipeline；
Described heating furnace A and heating furnace B is also directly connected by manifold with overflow settling tank 6, oil gas water three phase separation
Device A and three phases separator B oil export are also directly connected by manifold with oil transfer pump 8；
Described coming oil manifold A is also connected by manifold with ball collecting chamber B, and described coming oil manifold B is also by manifold with receiving
Ball cylinder A is connected；Described ball collecting chamber A is also connected by manifold with heating furnace B, and described ball collecting chamber B also passes through manifold and heating
Stove A is connected；Described heating furnace A is also connected by manifold with three phases separator B, and described heating furnace B also passes through pipe
Remittance connects with three phases separator A；
Valve is provided with all connection manifolds.
A series of strata oil well is connected by pipeline valve component with coming oil manifold A, and coming oil manifold A passes through pipeline valve component again
It is connected with ball collecting chamber A entrances, ball collecting chamber A outlets access heating furnace A crude oil entrances, heating furnace A crude exports pass through pipeline valve
Component connect three phases separator A entrances, overflow settling tank 6 can also be directly entered, subsequently into purification oil tank 7,
Purification oil after purifying oil tank 7 enters oil transfer pump 8, transports to next gathering station outside.
B series of strata oil well is connected by pipeline valve component with coming oil manifold B, and coming oil manifold B passes through pipeline valve component again
It is connected with ball collecting chamber B entrances, ball collecting chamber B outlets access heating furnace B crude oil entrances, heating furnace B crude exports pass through pipeline valve
Component connect three phases separator B entrances, overflow settling tank 6 can also be directly entered, subsequently into purification oil tank 7,
Purification oil after purifying oil tank 7 enters oil transfer pump 8, transports to next gathering station outside.
After B scales diminish when A series of strata oil wells are larger, it is connected also by pipeline valve component with coming oil manifold A, coming oil
Manifold A is connected by pipeline valve component with ball collecting chamber A entrances again, ball collecting chamber A outlets access heating furnace B crude oil entrances, heating
Stove B crude exports connect three phases separator B entrances by pipeline valve component.
After A scales diminish when B series of strata oil wells are larger, it is connected, comes with coming oil manifold B also by pipeline valve component
Oil pipe remittance B is connected by pipeline valve component with ball collecting chamber B entrances again, ball collecting chamber B outlets access heating furnace A crude oil entrances, is added
Hot stove A crude exports connect three phases separator A entrances by pipeline valve component.
Three phases separator A, three phases separator the B qualified oil export connection entrance of oil transfer pump 8, oil transfer pump
8 outlet connection crude oil output pipelines.
Three phases separator A oil product is unqualified, then three phases separator A outlet enters overflow settling tank
6, carry out secondary settlement, the import of the outlet of overflow settling tank 6 access purification oil tank 7, the outlet connection oil transportation of purification oil tank 7
The entrance of pump 8, the outlet of oil transfer pump 8 connection crude oil output pipeline.
Three phases separator B oil product is unqualified, then three phases separator B outlet enters overflow settling tank
6, carry out secondary settlement, the import of the outlet of overflow settling tank 6 access purification oil tank 7, the outlet connection oil transportation of purification oil tank 7
The entrance of pump 8, the outlet of oil transfer pump 8 connection crude oil output pipeline.
Three phases separator A, three phases separator B gas outlet are connected is connected to associated gas knockout together
5, the outlet of associated gas knockout 5 is connected to heating furnace A, heating furnace B fuel gas inlet.
Three phases separator A, three phases separator B water out remove water treatment facilities.
Embodiment 3：
The present embodiment provides a kind of surface technology processing method of more series of strata yard different disposal scales, including following step
Suddenly：
1）Each series of strata coming oil manifold 1 receives the wet oil that the conveying of surrounding well site takes, then is entered by pipeline valve component and received
Ball cylinder 2 carries out receipts ball；
2）The well liquid that the well site conveying that temperature by ball collecting chamber 2 is 3 DEG C comes, 55 DEG C are heated into heating furnace 3；
3）Well liquid after the heating of heating furnace 3 enters three phases separator 4 or is directly entered overflow settling tank 6；
4）The associated gas for each series of strata isolated through three phases separator 4 enters associated gas knockout 5, association together
The associated gas that gas knockout is isolated is used as fuel into heating furnace 3；Each series of strata isolated through three phases separator 4
Deviate from water and enter the follow-up water process of water treatment system progress together, handle qualified rear re-injection；Separated through three phases separator 4
The purification oil of each series of strata gone out is outer after overflow settling tank 6, purification oil tank 7 and oil transfer pump 8 successively to transport to next gathering station.
Described step 4）The purification oil of the middle each series of strata isolated through three phases separator 4 be qualified oil product and
Slop oil, if the purification oil oil product separated is unqualified, oil is successively by overflow settling tank 6, purification oil tank 7 and
It is outer after oil transfer pump 8 to transport to next gathering station；If the purification oil oil product separated is qualified, oil transfer pump 8 is directly entered, process is defeated
Oil pump 8 is outer after being pressurized to transport to next gathering station.
The present embodiment is described in detail by taking bilayer system yard as an example, as shown in Figure 1：
A series of strata coming oil manifolds A receives the wet oil that the conveying of surrounding well site takes, and is 3 DEG C by temperature after ball collecting chamber A
Heating furnace A, which is sent into, after the well liquid mixing that well site conveying comes is heated to 55 DEG C；The well liquid that well site conveying after heating comes has two-way defeated
Go out, two-way is standby each other：
It is to be dehydrated according to three phase separator all the way, then is directly entered three phases separator A and carries out oil gas water three phase
Separation, the oil and gas and water that three phases separator A is isolated export for 3 tunnels.
Oil transfer pump 8 is directly entered after 1. the purification oil separated is qualified, it is outer after the supercharging of oil transfer pump 8 to transport to next collection
Defeated station.
The purification oil oil product separated is unqualified, then into overflow settling tank 6, subsequently into purification oil tank 7, passes through
Purification oil after purification oil tank 7 enters oil transfer pump 8, transports to next gathering station outside.
2. the gas outlet for the associated gas that three phases separator A, three phases separator B are separated is connected together
Associated gas knockout 5 is connected to, the outlet of associated gas knockout 5 is connected to heating furnace A, heating furnace B fuel gas inlet.
3. three phases separator A, three phases separator the B sewage separated go water process from water out
Device, handle qualified rear re-injection.
It is to be dehydrated using overflow settling tank all the way in addition, the well liquid that the well site conveying after heating comes is directly entered overflow sedimentation
Tank 6, subsequently into purification oil tank 7, the purification oil after purifying oil tank 7 enters oil transfer pump 8, it is defeated to transport to next collection outside
Stand.
Similarly, B series of strata also can all realize above-mentioned function.
Embodiment 4：
On the basis of embodiment, the present embodiment is further illustrated, and the coming oil manifold 1 in each series of strata is parallel with one another standby
With the oil gas in standby, each series of strata parallel with one another of heating furnace 3 in standby, each series of strata parallel with one another of ball collecting chamber 2 in, each series of strata
Water three-phase separator 4 is parallel with one another standby, when the change of a certain series of strata oil well well liquid scale is big, can be shunted by other series of strata.
By taking bilayer system yard as an example, after later stage A layer scale becomes greatly, after B scales diminish, A series of strata can pass through pipeline valve
The equipment component of door component access B series of strata is standby each other.
Such as 3 standby flow of heating furnace is as follows：
When A series of strata oil wells are larger, it is connected by pipeline valve component with the coming oil manifold A of A series of strata, coming oil manifold
A is connected by pipeline valve component with ball collecting chamber A entrances again, the well site that temperature is 3 DEG C is conveyed after the well liquid come mixes and is sent into
Heating furnace B is heated to 55 DEG C；The well liquid that well site conveying after heating comes has two-way output：
It is to be dehydrated according to three phase separator all the way, then is directly entered three phases separator A and carries out oil gas water three phase
Separation, the oil and gas and water that three phases separator A is isolated export for 3 tunnels.
It is to be dehydrated using overflow settling tank all the way in addition, the well liquid that the well site conveying after heating comes is directly entered overflow sedimentation
Tank 6, subsequently into purification oil tank 7, the purification oil after purifying oil tank 7 enters oil transfer pump 8, it is defeated to transport to next collection outside
Stand.
Equally, ball collecting chamber 2, three phases separator 4 can two series of strata each other stand-by equipment.
Similarly, B series of strata scale can also realize above-mentioned function entirely after becoming big.
In summary, the utility model provides a kind of technology processing system of more series of strata different scales, makes more series of strata oil
The surface technology of field gathering station field is optimized, and reduces energy consumption, saves surface construction investment, improves oil field development synthesis profit
Use benefit.
Exemplified as above is only for example, not forming to the scope of protection of the utility model to of the present utility model
Limitation, it is every to be belonged to the same or analogous design of the utility model within the scope of protection of the utility model.
Claims (4)
- A kind of 1. surface technology processing system of more series of strata yard different disposal scales, it is characterised in that：Come including more series of strata Oil pipe converges（1）, the coming oil manifold of each series of strata（1）It is sequentially connected a ball collecting chamber（2）, a heating furnace（3）, an oil gas water Three phase separator（4）, all three phases separator（4）Gas outlet be connected to associated gas knockout together（5）, own Three phases separator（4）Water out be connected to together water process dress system, all three phases separators（4） Oil export be sequentially connected overflow settling tank together（6）, purification oil tank（7）, oil transfer pump（8）After connect crude oil output pipeline； Described heating furnace（3）Also pass through manifold and overflow settling tank（6）Directly connect, three phases separator（4）Oil export Also pass through manifold and oil transfer pump（8）Directly connect；The coming oil manifold of each series of strata（1）Also pass through manifold and the ball collecting chamber of other series of strata（2）Connection；The ball collecting chamber of each series of strata （2）Also pass through manifold and the heating furnace of other series of strata（3）Connection；The heating furnace of each series of strata（3）Also pass through manifold and other layers The three phases separator of system（4）Or overflow settling tank（6）Connection；Valve is provided with all connection manifolds.
- 2. the surface technology processing system of more series of strata yard different disposal scales as claimed in claim 1, it is characterised in that：Institute The associated gas knockout stated（5）Gas outlet to heating furnace（3）.
- A kind of 3. surface technology processing system of bilayer system yard different disposal scale, it is characterised in that：Including coming oil manifold A and Coming oil manifold B, coming oil manifold A are sequentially connected ball collecting chamber A, heating furnace A, three phases separator A, and coming oil manifold B connects successively Connect ball collecting chamber B, heating furnace B, three phases separator B, three phases separator A and three phases separator B gas Outlet is connected to associated gas knockout together（5）；Three phases separator A and three phases separator B water out one Rise and be connected to water process dress system；Three phases separator A and three phases separator B oil exports are sequentially connected overflow and sunk Tank drops（6）, purification oil tank（7）, oil transfer pump（8）After connect crude oil output pipeline；Described heating furnace A and heating furnace B also passes through manifold and overflow settling tank（6）Directly connect, three phases separator A Also pass through manifold and oil transfer pump with three phases separator B oil export（8）Directly connect；Described coming oil manifold A is also connected by manifold with ball collecting chamber B, and described coming oil manifold B also passes through manifold and ball collecting chamber A Connection；Described ball collecting chamber A is also connected by manifold with heating furnace B, and described ball collecting chamber B is also connected by manifold and heating furnace A It is logical；Described heating furnace A is also connected by manifold with three phases separator B, and described heating furnace B also passes through manifold and oil Gas-water separator A is connected；Valve is provided with all connection manifolds.
- 4. the surface technology processing system of bilayer system yard different disposal scale as claimed in claim 3, it is characterised in that：Institute The associated gas knockout stated（5）Gas outlet be respectively communicated to heating furnace A and heating furnace B.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201720294453.9U CN206647093U (en) | 2017-03-24 | 2017-03-24 | A kind of surface technology processing system of more series of strata yard different disposal scales |
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| CN201720294453.9U CN206647093U (en) | 2017-03-24 | 2017-03-24 | A kind of surface technology processing system of more series of strata yard different disposal scales |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106837292A (en) * | 2017-03-24 | 2017-06-13 | 西安长庆科技工程有限责任公司 | A kind of the surface technology processing system and method for many series of strata yard different disposal scales |
| CN110331965A (en) * | 2019-07-29 | 2019-10-15 | 山东万泰油气装备科技股份有限公司 | A kind of continuous circularly-supercharged gas recovery facility |
-
2017
- 2017-03-24 CN CN201720294453.9U patent/CN206647093U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106837292A (en) * | 2017-03-24 | 2017-06-13 | 西安长庆科技工程有限责任公司 | A kind of the surface technology processing system and method for many series of strata yard different disposal scales |
| CN110331965A (en) * | 2019-07-29 | 2019-10-15 | 山东万泰油气装备科技股份有限公司 | A kind of continuous circularly-supercharged gas recovery facility |
| CN110331965B (en) * | 2019-07-29 | 2024-03-22 | 山东万泰压缩机有限公司 | Continuous circulation supercharging gas production equipment |
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