CN104236378B - Spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement - Google Patents

Spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement Download PDF

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Publication number
CN104236378B
CN104236378B CN201410445069.5A CN201410445069A CN104236378B CN 104236378 B CN104236378 B CN 104236378B CN 201410445069 A CN201410445069 A CN 201410445069A CN 104236378 B CN104236378 B CN 104236378B
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Prior art keywords
crude oil
eddy current
cylindrical shell
heat exchanger
spiral heat
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CN201410445069.5A
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CN104236378A (en
Inventor
柳兰生
周凤娇
金万芸
王想文
丁永平
张磊
严如强
罗继英
刘力
张岩
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Lanzhou hi tech refinery Limited by Share Ltd
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Lanzhou Lanluo Oil Refinery & Chemical Processing Equipment Co Ltd
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  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The invention discloses spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement, comprise crude oil import adapter, eddy current drainage cylindrical shell, crude oil gathering sill, taper sediment outflow cylindrical shell and sewage draining exit, described eddy current drainage cylindrical shell is arranged on spiral heat exchanger bottom and is connected with described spiral heat exchanger lower surface outmost turns crude oil side open channels, described taper sediment outflow cylindrical shell is arranged on described eddy current drainage cylindrical shell bottom, described crude oil gathering sill is arranged in described eddy current drainage cylindrical shell, being close to described eddy current drainage cylinder inboard wall extends spirally, described crude oil gathering sill lowermost end is taken over and is connected with the crude oil import that stretches out described eddy current drainage cylindrical shell, described sewage outfalls setting is in described taper sediment outflow cylindrical shell bottom. spiral heat exchanger eddy current of the present invention, centrifugal sediment outflow interface arrangement, by the design to the each structure in spiral heat exchanger below, effectively realized separating of crude oil and silt, avoids oil-sand greasy filth to accumulate in spiral heat exchanger and result in blockage.

Description

Spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement
Technical field
The present invention relates to crude oil purification equipment technical field, especially a kind of spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement.
Background technology
Spiral heat exchanger, because heat exchange efficiency is high, has self-cleaning function after passage fouling, and the preheating conveying etc. that is widely used in crude oil is easily in fouling medium technique. But owing to containing a large amount of silt particles in crude oil, and the instability of flow of crude oil, when flow velocity is less than in the situation of 1m/s or intermitten service, silt particle in crude oil easily deposits in the passage of heat exchanger, result in blockage, have a strong impact on the normal operation of heat exchanger, cause very large difficulty to operation maintenance, heat exchanger tends to therefore reduce 50% service life.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement are proposed, by the design to the each structure in spiral heat exchanger below, effectively realize separating of crude oil and silt, avoid oil-sand greasy filth to accumulate in spiral heat exchanger and result in blockage.
In order to realize foregoing invention object, the invention provides following technical scheme:
Spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement, comprise crude oil import adapter, eddy current drainage cylindrical shell, crude oil gathering sill, taper sediment outflow cylindrical shell and sewage draining exit,
Described eddy current drainage cylindrical shell is arranged on spiral heat exchanger bottom and is connected with described spiral heat exchanger lower surface outmost turns crude oil side open channels,
Described taper sediment outflow cylindrical shell is arranged on described eddy current drainage cylindrical shell bottom,
Described crude oil gathering sill is arranged in described eddy current drainage cylindrical shell, is close to described eddy current drainage cylinder inboard wall and extends spirally, and described crude oil gathering sill lowermost end is taken over and is connected with the crude oil import that stretches out described eddy current drainage cylindrical shell,
Described sewage outfalls setting is in described taper sediment outflow cylindrical shell bottom.
Further, at described crude oil gathering sill end face, be evenly distributed with some oil outlets along described crude oil gathering sill length direction,
In described crude oil gathering sill bottom surface, be evenly distributed with some sand discharges hole along described crude oil gathering sill length direction.
Further, described crude oil import is taken over and is connected with described crude oil gathering sill with described eddy current drainage cylindrical shell cross section tangential direction.
Further, described crude oil gathering sill from its lowermost end to become 5 degree inclination angles upwards to extend spirally with horizontal plane.
Spiral heat exchanger eddy current of the present invention, centrifugal sediment outflow interface arrangement, by the design to the each structure in spiral heat exchanger below, effectively realized separating of crude oil and silt, avoids oil-sand greasy filth to accumulate in spiral heat exchanger and result in blockage.
Brief description of the drawings
Fig. 1 is that the master of spiral heat exchanger eddy current of the present invention, centrifugal sediment outflow interface arrangement looks schematic diagram, and wherein dotted line represents crude oil gathering sill;
Fig. 2 is that schematic diagram is looked on the right side of spiral heat exchanger eddy current of the present invention, centrifugal sediment outflow interface arrangement, and wherein dotted line represents crude oil import adapter;
Fig. 3 be in Fig. 1 D-D overlook cross-sectional schematic;
Fig. 4 is crude oil gathering sill cross sectional representation of the present invention.
Detailed description of the invention
Describe the present invention below in conjunction with accompanying drawing, the description of this part is only exemplary and explanatory, should not have any restriction to protection scope of the present invention.
Spiral heat exchanger eddy current as shown in Figures 1 to 4, centrifugal sediment outflow interface arrangement, comprise crude oil import adapter 1, eddy current drainage cylindrical shell 2, crude oil gathering sill 3, taper sediment outflow cylindrical shell 4 and sewage draining exit 5, and sewage draining exit 5 is removable,
Eddy current drainage cylindrical shell 2 is arranged on spiral heat exchanger 6 bottoms and is connected with spiral heat exchanger 6 lower surface outmost turns crude oil side open channels,
Taper sediment outflow cylindrical shell 4 is arranged on eddy current drainage cylindrical shell 2 bottoms,
Crude oil gathering sill 3 is arranged in eddy current drainage cylindrical shell 2, is close to eddy current drainage cylindrical shell 2 spiral inner walls and extends, and crude oil gathering sill 3 lowermost ends are taken over 1 with the crude oil import that stretches out eddy current drainage cylindrical shell 2 and are connected,
Taper sediment outflow cylindrical shell 4 is for being inverted shape cylinder cone, and sewage draining exit 5 is arranged on taper sediment outflow cylindrical shell 4 bottoms.
Crude oil gathering sill 3 cross sections are square, at its end face, be evenly distributed with some oil outlets 31 along crude oil gathering sill 3 length directions,
In crude oil gathering sill 3 bottom surfaces, be evenly distributed with some sand discharges hole 32 along crude oil gathering sill 3 length directions.
In the present embodiment, oil outlet 31 and sand discharge hole 32 diameters all arrange one around each 15 degree of eddy current drainage cylindrical shell 2 axis.
Crude oil import is taken over 1 and is connected with crude oil gathering sill 3 with eddy current drainage cylindrical shell 2 cross section tangential directions.
Crude oil gathering sill 3 from its lowermost end to become 5 degree inclination angles upwards to extend spirally with horizontal plane.
When use, crude oil is taken over 1 from crude oil import and is entered eddy current drainage cylindrical shell 2, is being directed at the interior formation spiral vortex of eddy current drainage cylindrical shell 2 by crude oil gathering sill 3. Under the effect of centrifugal force, the solids of heavy sand grains drops in taper sediment outflow cylindrical shell 4. Crude oil after desanding enters in spiral heat exchanger 6, after heat exchange, discharges. Taper sediment outflow cylindrical shell 4 can be by dismountable sewage draining exit 5 periodic cleanings.
Spiral heat exchanger eddy current of the present invention, centrifugal sediment outflow interface arrangement, by the design to the each structure in spiral heat exchanger below, effectively realized separating of crude oil and silt, avoids oil-sand greasy filth to accumulate in spiral heat exchanger and result in blockage.

Claims (3)

1. spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement, is characterized in that, comprises crude oil import adapter, eddy current drainage cylindrical shell, crude oil gathering sill, taper sediment outflow cylindrical shell and sewage draining exit,
Described eddy current drainage cylindrical shell is arranged on spiral heat exchanger bottom and is connected with described spiral heat exchanger lower surface outmost turns crude oil side open channels,
Described taper sediment outflow cylindrical shell is arranged on described eddy current drainage cylindrical shell bottom,
Described crude oil gathering sill is arranged in described eddy current drainage cylindrical shell, is close to described eddy current drainage cylinder inboard wall and extends spirally, and described crude oil gathering sill lowermost end is taken over and is connected with the crude oil import that stretches out described eddy current drainage cylindrical shell,
Described sewage outfalls setting is in described taper sediment outflow cylindrical shell bottom,
At described crude oil gathering sill end face, be evenly distributed with some oil outlets along described crude oil gathering sill length direction,
In described crude oil gathering sill bottom surface, be evenly distributed with some sand discharges hole along described crude oil gathering sill length direction.
2. spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement as claimed in claim 1, described crude oil import is taken over and is connected with described crude oil gathering sill with described eddy current drainage cylindrical shell cross section tangential direction.
3. spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement as claimed in claim 1, described crude oil gathering sill from its lowermost end to become 5 degree inclination angles upwards to extend spirally with horizontal plane.
CN201410445069.5A 2014-09-03 2014-09-03 Spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement Active CN104236378B (en)

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CN201410445069.5A CN104236378B (en) 2014-09-03 2014-09-03 Spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement

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CN104236378B true CN104236378B (en) 2016-05-04

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112225418A (en) * 2020-10-23 2021-01-15 连云港金驰生物科技有限公司 Novel heat exchange cyclone desanding device
CN116762608A (en) * 2023-08-04 2023-09-19 遵义师范学院 Promoting CO 2 And low cost greenhouse gas circulation system for heat circulation

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08200270A (en) * 1995-01-20 1996-08-06 Hitachi Ltd Air compressor oil separator
CN1820816A (en) * 2006-01-24 2006-08-23 薛国民 Helical pipe composite gas and liquid separator
CN203024518U (en) * 2012-12-13 2013-06-26 广东美的电器股份有限公司 Oil separator and air conditioner outdoor unit
CN203550700U (en) * 2013-11-21 2014-04-16 兰州兰洛炼化设备有限公司 Centrifugal filtration type crude oil spiral plate heat exchanger
CN204027411U (en) * 2014-09-03 2014-12-17 兰州兰洛炼化设备有限公司 Spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08200270A (en) * 1995-01-20 1996-08-06 Hitachi Ltd Air compressor oil separator
CN1820816A (en) * 2006-01-24 2006-08-23 薛国民 Helical pipe composite gas and liquid separator
CN203024518U (en) * 2012-12-13 2013-06-26 广东美的电器股份有限公司 Oil separator and air conditioner outdoor unit
CN203550700U (en) * 2013-11-21 2014-04-16 兰州兰洛炼化设备有限公司 Centrifugal filtration type crude oil spiral plate heat exchanger
CN204027411U (en) * 2014-09-03 2014-12-17 兰州兰洛炼化设备有限公司 Spiral heat exchanger eddy current, centrifugal sediment outflow interface arrangement

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
螺旋管油气水多相流动与原油管流除砂理论;郭烈锦;《工程热物理学报》;20020131;第23卷(第01期);第107~110页 *

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Address after: 730000 Lanzhou, Anning District, Gansu Jian Xi Road, No. 789

Patentee after: Lanzhou hi tech refinery Limited by Share Ltd

Address before: 730000 Lanzhou, Anning District, Gansu Jian Xi Road, No. 789

Patentee before: LANZHOU LANLUO OIL REFINERY & CHEMICAL PROCESSING EQUIPMENT CO., LTD.

CP01 Change in the name or title of a patent holder