CN207438156U - Buffer tank - Google Patents
Buffer tank Download PDFInfo
- Publication number
- CN207438156U CN207438156U CN201721266670.3U CN201721266670U CN207438156U CN 207438156 U CN207438156 U CN 207438156U CN 201721266670 U CN201721266670 U CN 201721266670U CN 207438156 U CN207438156 U CN 207438156U
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- China
- Prior art keywords
- tank body
- liquid
- equalizing reservoir
- tank
- surge tank
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- 239000007788 liquid Substances 0.000 claims abstract description 121
- 238000001816 cooling Methods 0.000 claims abstract description 41
- 239000012530 fluid Substances 0.000 claims abstract description 17
- 238000012545 processing Methods 0.000 claims abstract description 7
- 238000009833 condensation Methods 0.000 claims description 32
- 230000005494 condensation Effects 0.000 claims description 32
- 238000007689 inspection Methods 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 238000003912 environmental pollution Methods 0.000 abstract description 6
- 238000000926 separation method Methods 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract description 2
- 230000000149 penetrating effect Effects 0.000 abstract 1
- 238000007701 flash-distillation Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000004576 sand Substances 0.000 description 6
- 238000000605 extraction Methods 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 238000001727 in vivo Methods 0.000 description 3
- 239000003129 oil well Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000003139 buffering effect Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model provides a buffer tank, buffer tank includes: the tank body is provided with a liquid inlet pipe for introducing fluid in a penetrating way, the top of the tank body is provided with an air outlet, and the bottom of the tank body is provided with a liquid outlet; cooling unit, cooling unit's at least part sets up internally at the jar to going into jar internal fluid by the feed liquor pipe and cooling down the processing in order to isolate gas and liquid, the gas of separation rises to the top of the jar body and flows out by the gas outlet, and the liquid of separation falls to the bottom of the jar body and flows out by the liquid outlet. The utility model discloses a buffer tank has solved the viscous crude thermal recovery in-process among the prior art and can produce the extravagant and environmental pollution's of energy problem.
Description
Technical field
The utility model is related to field of petroleum exploitation, in particular to a kind of surge tank.
Background technology
At present, conventional Heavy Oil thermal recovery is using well site, block station, treating stations three-level cloth station gathering and transferring process.In heavy crude heat extraction mistake
Cheng Zhong, measuring station storage tank to carry out liquid temperature degree higher, a large amount of high temp oil gas mixtures are overflowed from measuring station storage tank tank mouth, cause the energy
The problems such as waste and surrounding enviroment pollution.
In addition, winter in order to ensure the mobility of Produced Liquid, convenient for collect it is defeated, steam is just being mixed into Produced Liquid into before tank
Heat is mixed, has been further exacerbated by waste and contamination phenomenon.
Utility model content
The main purpose of the utility model is that a kind of surge tank is provided, to solve heavy crude heat extraction process of the prior art
In can lead to the problem of energy waste and environmental pollution.
To achieve these goals, the utility model provides a kind of surge tank, including：Tank body is worn on tank body useful
Gas outlet is provided at the top of the inlet tube being passed through for fluid, tank body, the bottom of tank body is provided with liquid outlet；Cooling component,
Cooling component is at least partially disposed in tank body, to carry out cooling processing to entering the in vivo fluid of tank by inlet tube to separate
Go out gas and liquid, the gas isolated rises to the top of tank body and flowed out by gas outlet, and the liquid isolated drops to tank
It is simultaneously flowed out by liquid outlet the bottom of body.
Further, cooling component includes：Equalizing reservoir, equalizing reservoir are arranged in tank body and connect with the cavity of tank body
Logical, the inlet of inlet tube is located at the outside of tank body, and the liquid outlet of inlet tube is stretched into equalizing reservoir, so as to be entered by inlet tube
Fluid flash-off of steam and liquid in equalizing reservoir, the steam flashed off flow after equalizing reservoir towards the top of tank body,
The liquid flashed off is after equalizing reservoir towards the flows of tank body.
Further, equalizing reservoir is tubulose, and the liquid outlet of inlet tube penetrates equalizing reservoir from the tube wall of equalizing reservoir
Interior, a nozzle of equalizing reservoir is set towards the top of tank body, and the bottom of another nozzle towards the tank body of equalizing reservoir is set
It puts.
Further, cooling component further includes：Condensation tube bank condenses being at least partially disposed in tank body and positioned at flat for tube bank
The top of weighing apparatus container, so that the condensed tube bank of the steam stream flowed out out of equalizing reservoir is condensed with being condensed out gas and condensed water
The gas gone out is flowed out by gas outlet, and the condensed water being condensed out is towards the flows of tank body.
Further, condensation tube bank includes multiple pipeline sections being arranged in parallel, and multiple pipeline sections are perpendicular to the axis of tank body.
Further, condensation tube bank inspection hole is provided on tank body, to be located at tank body by condensing tube bank inspection hole inspection
The surface condition of the pipeline section of interior condensation tube bank.
Further, surge tank further includes：Liquid level gauge, liquid level gauge are arranged on the outside of tank body, first are provided on tank body
Take over and taken over second, first take over second take over along tank body axis direction arrangement, the first first end taken over and second
The first end taken over is connected with tank body, and the first second end taken over and the second second end taken over are connected with liquid level gauge, with
Liquid level gauge is made to detect the in vivo liquid level of tank.
Further, surge tank includes cylinder, the upper cover that is located on the nozzle of cylinder upper end of lid and lid and is located under cylinder
Hold the low head on nozzle；Gas outlet is arranged on upper cover, and liquid outlet is arranged on low head.
Further, low head is taper, and the big opening end of low head and the lower end nozzle of cylinder connect, the osculum of low head
End is connected with liquid outlet.
Further, surge tank further includes bearing, and seat supports are in the bottom of tank body.
The surge tank of the utility model is by setting tank body and cooling component so as to be completed into the Produced Liquid in surge tank
Phase-change heat-exchange can be applied to heavy crude heat extraction production process.Wherein, the inlet tube for being passed through for fluid is equipped on tank body,
Gas outlet is provided at the top of tank body, the bottom of tank body is provided with liquid outlet；Cooling component is at least partially disposed in tank body,
To carry out cooling processing to entering the in vivo fluid of tank by inlet tube to isolate gas and liquid, the gas isolated rises to
The top of tank body is simultaneously flowed out by gas outlet, and the liquid isolated drops to the bottom of tank body and flowed out by liquid outlet.The surge tank
Cooling component is arranged in tank body, Produced Liquid enters lower buffer in surge tank from inlet tube, using phase-change heat-exchange principle, adopts
Go out liquid to pass through flash distillation in surge tank under the action of cooling component and exchange heat, gas the going out from tank body top at final separation
Gas port is discharged, and liquid is discharged from the liquid outlet of tank body lower part.
Description of the drawings
The accompanying drawings which form a part of this application are used to provide a further understanding of the present invention, this practicality
New schematic description and description does not form the improper restriction to the utility model for explaining the utility model.
In the accompanying drawings：
Fig. 1 shows the structure diagram of the embodiment of surge tank according to the present utility model.
Wherein, above-mentioned attached drawing is marked including the following drawings：
10th, tank body；11st, inlet tube；111st, inlet；12nd, gas outlet；13rd, liquid outlet；14th, first take over；15th, second
It takes over；16th, cylinder；17th, upper cover；18th, low head；19th, Produced Liquid inspection hole；20th, equalizing reservoir；30th, condensation tube bank；31、
Condensation tube bank inspection hole；32nd, inlet；33rd, liquid outlet；40th, liquid level gauge；50th, bearing.
Specific embodiment
It should be noted that in the case where there is no conflict, the feature in embodiment and embodiment in the application can phase
Mutually combination.The utility model will be described in detail below with reference to the accompanying drawings and embodiments.
The utility model provides a kind of surge tank, please refers to Fig.1, and surge tank includes：Tank body 10 is equipped on tank body 10
For the inlet tube 11 being passed through for fluid, the top of tank body 10 is provided with gas outlet 12, and the bottom of tank body 10 is provided with liquid outlet
13；Cooling component, cooling component are at least partially disposed in tank body 10, with to entering the fluid in tank body 10 by inlet tube 11
Cooling processing is carried out to isolate gas and liquid, the gas isolated rises to the top of tank body 10 and flowed by gas outlet 12
Go out, the liquid isolated drops to the bottom of tank body 10 and flowed out by liquid outlet 13.
The surge tank of the utility model is by setting tank body 10 and cooling component so that complete into the Produced Liquid in surge tank
Into phase-change heat-exchange, heavy crude heat extraction production process can be applied to.Wherein, the feed liquor for being passed through for fluid is equipped on tank body 10
Pipe 11, the top of tank body 10 are provided with gas outlet 12, and the bottom of tank body 10 is provided with liquid outlet 13；At least part of cooling component
It is arranged in tank body 10, to isolate gas and liquid to carrying out cooling processing into the fluid in tank body 10 by inlet tube 11
Body, the gas isolated rise to the top of tank body 10 and are flowed out by gas outlet 12, and the liquid isolated drops to tank body 10
It is simultaneously flowed out by liquid outlet 13 bottom.Cooling component is arranged in tank body by the surge tank, and Produced Liquid enters surge tank from inlet tube
Interior lower buffer, using phase-change heat-exchange principle, Produced Liquid passes through flash distillation and heat exchange under the action of cooling component in surge tank,
Gas at final separation is discharged from the gas outlet on tank body top, and liquid is discharged from the liquid outlet of tank body lower part.
This surge tank carries out flash distillation cooling and phase-change heat-exchange by Produced Liquid in surge tank so that medium outlet temperature is steady
It is fixed controllable, and then damage of the high-temperature produced liquid to oil transfer pump is effectively reduced, avoid the wasting of resources and environmental pollution；Also,
Produced Liquid is directly entered surge tank and is changed by flashing to cool down rather than flow through in heat exchanger tube by wall-type heat exchange with managing outer low-temperature receiver
Heat drop temperature so that the defeated resistance of collection of Produced Liquid is small, and oil well production is steady.
In the present embodiment, cooling component includes equalizing reservoir 20, and equalizing reservoir 20 is arranged in tank body 10 and and tank body
10 cavity connection, the inlet 111 of inlet tube 11 are located at the outside of tank body 10, and the liquid outlet of inlet tube 11 stretches into equalizing reservoir
In 20, so that by inlet tube 11 into the fluid flash-off of steam and liquid in equalizing reservoir 20, the steam flashed off is through balance
It is flowed after container 20 towards the top of tank body 10, the liquid flashed off is after equalizing reservoir 20 towards the flows of tank body 10.
The setting of equalizing reservoir 20 can make the Produced Liquid liquid level outside equalizing reservoir 20, in tank body 10 keep stablizing, and be conducive to liquid level
Measurement.
When it is implemented, also having carried out thickening design inside equalizing reservoir 20, such setting slows down Produced Liquid and takes sand
Caused by abrasion.
When it is implemented, equalizing reservoir 20 is tubulose, the liquid outlet of inlet tube 11 is penetrated from the tube wall of equalizing reservoir 20
In equalizing reservoir 20, a nozzle of equalizing reservoir 20 is set towards the top of tank body 10, another nozzle of equalizing reservoir 20
It is set towards the bottom of tank body 10.
In the present embodiment, cooling component further includes condensation tube bank 30, and condensation tube bank 30 is at least partially disposed at tank body 10
Top interior and positioned at equalizing reservoir 20, so that the steam stream of outflow is condensed out of equalizing reservoir 20 restrains 30 to condense outlet
Body and condensed water, the gas being condensed out are flowed out by gas outlet 12, and the condensed water being condensed out is towards the flows of tank body 10.
In the present embodiment, as shown in Figure 1, condensation tube bank 30 has inlet 32 and liquid outlet 33, condensation tube bank 30
Inlet 32 and the liquid outlet 33 of condensation tube bank 30 are respectively positioned on the outside of tank body.
When it is implemented, condensation tube bank 30 includes multiple pipeline sections being arranged in parallel, multiple pipeline sections are perpendicular to the axis of tank body 10
Line.
When it is implemented, being built-in with heat exchanger tube in condensation tube bank 30, heat exchanger tube uses light pipe, condensation 30 structure types of tube bank
Using coiled, velocity of medium in pipe can be increased, mitigate heat-transfer surface pollution, increase heat exchange efficiency, be effectively reduced cleaning frequency
Rate.
In the present embodiment, condensation tube bank inspection hole 31 is provided on tank body 10, to be examined by condensing tube bank inspection hole 31
Look into the surface condition of the pipeline section of the condensation tube bank 30 in tank body 10.Inspection hole is restrained by the condensation for being arranged on tank body top
Observation condensation surface soiled condition can be restrained when shutting down, such as find that the dirty steam that is passed through is cleaned, reduce outside pipe
Dirtiness resistance ensure that heat transfer effect, add the service life of tube bank.
Preferably, the center of condensation tube bank 30 and the axis of condensation tube bank inspection hole 31 are located in same level.
In the present embodiment, surge tank further includes liquid level gauge 40, and liquid level gauge 40 is arranged on the outside of tank body 10, on tank body 10
The first take over 14 and the second take over 15 are provided with, the first take over 14 and the second take over 15 are arranged along the axis direction of tank body 10, the
The first end of one take over 14 and the first end of the second take over 15 are connected with tank body 10, and the second end of the first take over 14 and second connects
The second end of pipe 15 is connected with liquid level gauge 40, so that liquid level gauge 40 detects the liquid level in tank body 10.
Preferably, the combination of magnetic double level gauge and differential pressure levelmeter may be employed in liquid level gauge 40, and then ensures that liquid level is surveyed
It measures accurate.
In addition, in the present embodiment, surge tank includes cylinder 16, lid be located at the upper cover 17 on 16 upper end nozzle of cylinder with
And lid is located at the low head 18 on 16 lower end nozzle of cylinder；Gas outlet 12 is arranged on upper cover 17, and liquid outlet 13 is arranged on down
On end socket 18.
Preferably, condensation tube bank inspection hole 31 is welded to connect with cylinder 16.
Preferably, the first take over 14 and the second take over 15 are welded to connect with cylinder 16.
Preferably, inlet tube 11 is welded to connect with cylinder 16.
Preferably, the big opening end of low head 18 and the lower end of cylinder 16 are welded to connect, and the osculum end of low head 18 is with going out liquid
Mouth 13 is welded to connect.
Preferably, upper cover 17 and the lower end of cylinder 16 are welded to connect, and gas outlet 12 is welded to connect with upper cover 17.
When it is implemented, low head 18 is taper, the big opening end of low head 18 is connected with the lower end nozzle of cylinder 16, lower envelope
First 18 osculum end is connected with liquid outlet 13, and low head 18 is designed with for taper beneficial to the discharge that sand is taken in Produced Liquid.
When it is implemented, as shown in Figure 1, surge tank further includes Produced Liquid inspection hole 19, Produced Liquid inspection hole 19 is arranged on
The outside of low head 18, to check that 18 inner wall of low head takes the hardened situation of sand by Produced Liquid inspection hole 19.When shutting down, pass through
Produced Liquid inspection hole 19 checks that low head inner wall takes the hardened situation of sand, and as found, taking sand hardened phenomenon can easily be cleared up,
Liquid outlet is avoided to block, ensures Produced Liquid smoothly outer row so that equipment can be run with security and stability.
Preferably, Produced Liquid inspection hole 19 is welded to connect with low head 18.
In order to allow support and fixed surge tank, surge tank further include bearing 50, bearing 50 is supported on the bottom of tank body 10.
When it is implemented, bearing 50 uses supporting leg type bearing, facilitate the connection of the external pipeline in surge tank lower part.
Preferably, bearing 50 is welded to connect with low head 18.
The production process of the utility model：
Produced Liquid enters lower buffer in surge tank from inlet tube, utilizes phase-change heat-exchange principle：Produced Liquid is under surge tank
Portion flashes, liquid cooling therein；On the vapour mixture (containing water vapor and associated gas) that flash separation comes out from Produced Liquid
It rises by condensation tube bank, the cooling media for heat exchange with condensation tube bank internal circulation flow, vapour mixture is condensed and cooled down；After cooling
Residual gas (associated gas and a small amount of uncooled vapor) exchange heat again in gas outlet, after final vapour mixture condensation
Liquid after the condensed water of generation and flash distillation cooling is discharged together from the liquid outlet of tank body lower part.
The beneficial effects of the utility model：
(1) surge tank developed using the principle of flash distillation cooling and phase-change heat-exchange has controllable Produced Liquid outlet temperature
Degree, recycling flash-off steam and its heat, the defeated resistance of Produced Liquid collection are small, anti-wear, cleaning is convenient, are not easy the multiple functions such as long-pending sand,
It effectively prevents gas outlet and takes environmental pollution caused by oil vapour escapes, while also achieve UTILIZATION OF VESIDUAL HEAT IN, save Liao Zhan areas and protect
Temperature vapour.
(2) media outlet stability of flow is made into row buffering using tank volume.
(3) Produced Liquid carries out flash distillation cooling and phase-change heat-exchange in surge tank, and medium outlet temperature is stably and controllable, effectively subtracts
Damage of the high-temperature produced liquid to oil transfer pump is lacked.
(4) Produced Liquid is directly entered surge tank and is cooled down by flashing rather than flow through and pass through wall-type heat exchange in heat exchanger tube
Cool down with low-temperature receiver heat exchange outside pipe, the defeated resistance of Produced Liquid collection is small, and oil well production is steady.
(5) flash-off steam and its heat are received back and forth using condensation tube bank, avoid the wasting of resources and environmental pollution.
It can be seen from the above description that the above embodiments of the present invention achieve the following technical effects：
The surge tank of the utility model is by setting tank body 10 and cooling component so that complete into the Produced Liquid in surge tank
Into phase-change heat-exchange, heavy crude heat extraction production process can be applied to.Wherein, the feed liquor for being passed through for fluid is equipped on tank body 10
Pipe 11, the top of tank body 10 are provided with gas outlet 12, and the bottom of tank body 10 is provided with liquid outlet 13；At least part of cooling component
It is arranged in tank body 10, to isolate gas and liquid to carrying out cooling processing into the fluid in tank body 10 by inlet tube 11
Body, the gas isolated rise to the top of tank body 10 and are flowed out by gas outlet 12, and the liquid isolated drops to tank body 10
It is simultaneously flowed out by liquid outlet 13 bottom.Cooling component is arranged in tank body by the surge tank, and Produced Liquid enters surge tank from inlet tube
Interior buffering, using phase-change heat-exchange principle, Produced Liquid passes through flash distillation and heat exchange under the action of cooling component in surge tank, finally
Gas at separation is discharged from the gas outlet on tank body top, and liquid is discharged from the liquid outlet of tank body lower part.
This surge tank carries out flash distillation cooling and phase-change heat-exchange by Produced Liquid in surge tank so that medium outlet temperature is steady
It is fixed controllable, and then damage of the high-temperature produced liquid to oil transfer pump is effectively reduced, avoid the wasting of resources and environmental pollution；Also,
Produced Liquid is directly entered surge tank and is changed by flashing to cool down rather than flow through in heat exchanger tube by wall-type heat exchange with managing outer low-temperature receiver
Heat drop temperature so that the defeated resistance of collection of Produced Liquid is small, and oil well production is steady.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, for this
For the technical staff in field, various modifications and changes may be made to the present invention.It is all in the spirit and principles of the utility model
Within, any modifications, equivalent replacements and improvements are made should be included within the scope of protection of this utility model.
Claims (10)
1. a kind of surge tank, which is characterized in that including：
Tank body (10) is equipped with the inlet tube (11) for being passed through for fluid, the top of the tank body (10) on the tank body (10)
Portion is provided with gas outlet (12), and the bottom of the tank body (10) is provided with liquid outlet (13)；
Cooling component, the cooling component is at least partially disposed in the tank body (10), with to by the inlet tube (11)
Cooling processing is carried out to isolate gas and liquid into the fluid in the tank body (10), and the gas isolated rises to described
The top of tank body (10) simultaneously by the gas outlet (12) flow out, the liquid isolated drop to the bottom of the tank body (10) and by
Liquid outlet (13) outflow.
2. surge tank according to claim 1, which is characterized in that the cooling component includes：
Equalizing reservoir (20), the equalizing reservoir (20) are arranged in the tank body (10) and connect with the cavity of the tank body (10)
Logical, the inlet (111) of the inlet tube (11) is located at the outside of the tank body (10), and the liquid outlet of the inlet tube (11) is stretched
Enter in the equalizing reservoir (20), so as to flash to steam into the fluid in the equalizing reservoir (20) by the inlet tube (11)
Vapour and liquid, the steam flashed off are flowed towards the top of the tank body (10) after the equalizing reservoir (20), flashed off
Liquid is after the equalizing reservoir (20) towards the flows of the tank body (10).
3. surge tank according to claim 2, which is characterized in that the equalizing reservoir (20) be tubulose, the inlet tube
(11) liquid outlet is penetrated from the tube wall of the equalizing reservoir (20) in the equalizing reservoir (20), the equalizing reservoir (20)
A nozzle set towards the top of the tank body (10), another nozzle of the equalizing reservoir (20) is towards the tank body
(10) bottom is set.
4. surge tank according to claim 2, which is characterized in that the cooling component further includes：
Condensation tube bank (30), the condensation tube bank (30) are at least partially disposed in the tank body (10) and hold positioned at the balance
The top of device (20), so that the steam of outflow flows through the condensation tube bank (30) to condense outlet out of the equalizing reservoir (20)
Body and condensed water, the gas being condensed out are flowed out by the gas outlet (12), and the condensed water being condensed out is towards the tank body (10)
Flows.
5. surge tank according to claim 4, which is characterized in that the condensation tube bank (30) includes multiple be arranged in parallel
Pipeline section, multiple pipeline sections are perpendicular to the axis of the tank body (10).
6. surge tank according to claim 4, which is characterized in that condensation tube bank inspection hole is provided on the tank body (10)
(31), check that the pipeline section of (30) is restrained in the condensation being located in the tank body (10) to restrain inspection hole (31) by the condensation
Surface condition.
7. surge tank according to claim 1, which is characterized in that the surge tank further includes：
Liquid level gauge (40), the liquid level gauge (40) are arranged on the outside of the tank body (10), and is provided on the tank body (10)
One, which takes over (14) and second, takes over (15), and described first, which takes over (14) and described second, takes over the axis of (15) along the tank body (10)
Line direction arranges, described first take over the first end of (14) and described second take over the first end of (15) with the tank body (10)
Connection, described first, which takes over the second end of (14) and described second, takes over the second end of (15) with the liquid level gauge (40) even
It is logical, so that the liquid level gauge (40) detects the liquid level in the tank body (10).
8. surge tank according to claim 1, which is characterized in that described in the surge tank includes cylinder (16), lid is located at
Upper cover (17) and lid on the nozzle of cylinder (16) upper end are located at the low head (18) on the nozzle of the cylinder (16) lower end；Institute
It states gas outlet (12) to be arranged on the upper cover (17), the liquid outlet (13) is arranged on the low head (18).
9. surge tank according to claim 8, which is characterized in that the low head (18) be taper, the low head
(18) big opening end is connected with the lower end nozzle of the cylinder (16), osculum end and the liquid outlet of the low head (18)
(13) connect.
10. surge tank according to claim 1, which is characterized in that the surge tank further includes bearing (50), the bearing
(50) it is supported on the bottom of the tank body (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721266670.3U CN207438156U (en) | 2017-09-28 | 2017-09-28 | Buffer tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721266670.3U CN207438156U (en) | 2017-09-28 | 2017-09-28 | Buffer tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207438156U true CN207438156U (en) | 2018-06-01 |
Family
ID=62295545
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721266670.3U Active CN207438156U (en) | 2017-09-28 | 2017-09-28 | Buffer tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207438156U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111043008A (en) * | 2018-10-11 | 2020-04-21 | 河南顺达新能源科技有限公司 | Large-volume buffer tank with noise reduction and vibration reduction functions |
-
2017
- 2017-09-28 CN CN201721266670.3U patent/CN207438156U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111043008A (en) * | 2018-10-11 | 2020-04-21 | 河南顺达新能源科技有限公司 | Large-volume buffer tank with noise reduction and vibration reduction functions |
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