CN105758248A - Annular pipe type uniform distribution device of fluid - Google Patents
Annular pipe type uniform distribution device of fluid Download PDFInfo
- Publication number
- CN105758248A CN105758248A CN201610220848.4A CN201610220848A CN105758248A CN 105758248 A CN105758248 A CN 105758248A CN 201610220848 A CN201610220848 A CN 201610220848A CN 105758248 A CN105758248 A CN 105758248A
- Authority
- CN
- China
- Prior art keywords
- cylinder
- distribution device
- fluid distribution
- uniform fluid
- type uniform
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention relates to an annular pipe type uniform distribution device of fluid. The uniform distribution device is characterized by comprising a vertically arranged cylinder, wherein the upper end in the cylinder is connected with a collection disc with an opening in the bottom in a fastening way; a liquid collection cylinder with an open upper end and a sealed lower end is arranged at the lower part of the collection disc; a plurality of horizontally arranged branch pipes are arranged at the lower part of the liquid collection cylinder in a circumferential direction; one end of each branch pipe is communicated with the liquid collection cylinder; the other end of each branch pipe is connected with the cylinder in the fastening way; at least one cycle of annular pipe penetrated and communicated with each branch pipe is arranged at the exterior of the liquid collection cylinder; a plurality of fluid uniformizing holes are formed in the bottom of the annular pipe. Through the annular pipe type uniform distribution device of the fluids, the upper end in the cylinder is connected with the collection disc in the fastening way, and a liquid collection cylinder with the open upper end and the sealed lower end is formed in the lower part of the collection disc; after outside fluids enter the cylinder, a gas-phase fluid flows through the collection disc, is naturally and uniformly pressed and then diffuses and flows downwards; liquid-phase fluid freely falls into the liquid collection cylinder; gas-liquid-phase fluid uniform distribution channels are relatively independent and have an excellent uniform distribution effect on fluid with high gas content.
Description
Technical field
The present invention relates to a kind of annular tube type uniform fluid distribution device, belong to uniform fluid distribution technical field.
Background technology
Along with the continuous reinforcement of offshore oil and gas resource exploration, exploitation dynamics, LNG-FPSO (platform is unloaded in the storage of offshore natural gas Floating Production) quickly grows.Wrap-round tubular heat exchanger, as the key core equipment of Large LNG-FPSO, has that heat transfer area is big, design pressure is high, allow the advantages such as big different transfer of heat.But, the heat exchange property of wrap-round tubular heat exchanger is had large effect by marine special operation condition, outstanding behaviours is rock the wrap-round tubular heat exchanger shell side flow distribution caused not to be respectively formed bias current, thus causing that heat exchanger overall heat exchange efficiency declines, and even substantial deviation design conditions.It is thus desirable to liquid phase fluid is carried out uniform by arranging uniform fluid distribution device, but although existing even distribution device preferably resolves the uniform problem of liquid phase fluid, but anti-shake to swing performance not good, it is impossible to be applied to sea and rock wrap-round tubular heat exchanger design and the exploitation of operating mode.
Summary of the invention
For the problems referred to above, it is an object of the invention to provide a kind of annular tube type uniform fluid distribution device that can make uniform fluid distribution under the condition of rocking.
For achieving the above object, the present invention takes techniques below scheme: a kind of annular tube type uniform fluid distribution device, it is characterised in that: it includes a cylinder being vertically arranged, and is fastenedly connected the catch tray of a bottom opening in the upper end of described inner barrel；The liquid cylinder of a uncovered lower end closed in upper end it is arranged below at described catch tray；The bottom of described liquid cylinder is circumferentially arranged multiple horizontally disposed arm, and one end of each described arm connects with described liquid cylinder, and the other end of each described arm and described cylinder are fastenedly connected；The endless tube that at least one circle runs through and connects each described arm is set in the outside of described liquid cylinder；The bottom of described endless tube offers multiple equal discharge orifice.
The bottom opening of described catch tray is uncovered with the upper end of described liquid cylinder corresponding；Described collector tray bottom opening diameter is less than the uncovered diameter in the upper end of described liquid cylinder.
It is fastenedly connected a guide pipe connecting with described catch tray and downwardly extending at the bottom opening place of described catch tray.
A collecting tank in inverted cone shape it is fastenedly connected at the top of described liquid cylinder.
Described arm adopts pipe or rectangular tube.
Described equal discharge orifice adopts circular hole, square hole or slit-aperture type hole.
Due to the fact that and take above technical scheme, it has the advantage that 1, due to the fact that and be fastenedly connected a catch tray in the upper end of inner barrel, it is arranged below at catch tray that a upper end is uncovered, the liquid cylinder of lower end closed, therefore external fluid enters after in cylinder, gaseous fluid is by naturally all pressing and downward diffusional flow after catch tray, liquid phase fluid free-falling enters in liquid cylinder, and the uniform passage of fluid liquid phase is relatively independent, and the fluid that void fraction is big has better uniform effect.2, due to the fact that circumferentially arranged in the bottom of liquid cylinder has multiple horizontally disposed arm, at least one circle that arranges radially outside at liquid cylinder runs through arm and the endless tube connected with each arm, offer multiple equal discharge orifice in the bottom of endless tube, therefore liquid phase fluid arm, endless tube and equal discharge orifice realize being uniformly distributed of liquid phase fluid.3, in the liquid cylinder of the present invention, liquid phase fluid is played cofferdam effect by storage space, its internal flow minimum liquid level only need to be controlled during application, achieve that uniform fluid distribution function under the condition of rocking, efficiently solve sea and rock the flow distribution problem of non-uniform of wrap-round tubular heat exchanger shell side under working condition.4, the present invention adopts integrated design, equipment no-movable part, and simple and compact for structure, cost is low.
Accompanying drawing explanation
Fig. 1 is the overall structure schematic diagram of the present invention；
Fig. 2 is the structural representation of the endless tube of the present invention.
Detailed description of the invention
Below in conjunction with drawings and Examples, the present invention is described in detail.
It is vertically arranged and the cylinder 1 of open at both ends as it is shown in figure 1, the present invention includes one, is fastenedly connected one in the upper end within cylinder 1 in inverted cone shape and the catch tray 2 of bottom opening.The liquid cylinder 3 of a uncovered lower end closed in upper end it is arranged below at catch tray 2.The bottom of liquid cylinder 3 is circumferentially arranged multiple horizontally disposed arm 4, and one end of each arm 4 all connects with liquid cylinder 3, and the other end of each arm 4 is all connected with cylinder 1 inner wall tightening.As in figure 2 it is shown, at least one circle that arranges radially outside at liquid cylinder 3 runs through arm 4 and the endless tube 5 connected with each arm 4.Offer multiple equal discharge orifice (not shown) in the bottom of endless tube 5, for enabling, the liquid phase fluid in endless tube 5 is uniform to flow out.
In above-described embodiment, the bottom opening of catch tray 2 is uncovered with the upper end of liquid cylinder 3 corresponding, and catch tray 2 bottom opening diameter is less than the uncovered diameter in the upper end of liquid cylinder 3, for making the liquid phase fluid collected by catch tray 2 can enter in liquid cylinder 3, it is prevented that leak outside.
In above-described embodiment, a guide pipe 6 connecting with catch tray 2 and downwardly extending it is fastenedly connected at the bottom opening place of catch tray 2, for controlling the flow of the liquid phase fluid collected by catch tray 2, enable liquid phase fluid following current in liquid cylinder 3, it is prevented that liquid phase fluid outwards splashes.
In above-described embodiment, it is fastenedly connected a collecting tank 7 in inverted cone shape at the top of liquid cylinder 3, for collecting the liquid phase fluid sputtered from catch tray 2 bottom opening edge.
In above-described embodiment, arm 4 can adopt pipe or rectangular tube.
In above-described embodiment, the current-sharing well format offered bottom endless tube 5 can adopt circular hole, square hole or slit-aperture type hole.
The present invention is operationally, extraneous liquid phase fluid after catch tray 2 is collected and is confluxed through guide pipe 6 vertical drop, in gaseous fluid freely uniform cylinder 1 to catch tray 2, liquid phase fluid is flowed in liquid cylinder 3 through collecting tank 7, realizes being uniformly distributed of liquid phase fluid by arm 4, endless tube 5 and equal discharge orifice.Meanwhile, when at sea rocking operating mode, in liquid cylinder 3, liquid phase fluid is played cofferdam effect by storage space, only needs fluid minimum liquid level in domination set fluid cylinder 3 during application, so that it may realize rocking uniform fluid distribution function under condition.
The various embodiments described above are merely to illustrate the present invention, and wherein the structure of each parts, connected mode etc. all can be varied from, every equivalents carried out on the basis of technical solution of the present invention and improvement, all should not get rid of outside protection scope of the present invention.
Claims (10)
1. an annular tube type uniform fluid distribution device, it is characterised in that: it includes a cylinder being vertically arranged, and is fastenedly connected the catch tray of a bottom opening in the upper end of described inner barrel；The liquid cylinder of a uncovered lower end closed in upper end it is arranged below at described catch tray；The bottom of described liquid cylinder is circumferentially arranged multiple horizontally disposed arm, and one end of each described arm connects with described liquid cylinder, and the other end of each described arm and described cylinder are fastenedly connected；The endless tube that at least one circle runs through and connects each described arm is set in the outside of described liquid cylinder；The bottom of described endless tube offers multiple equal discharge orifice.
2. a kind of annular tube type uniform fluid distribution device as claimed in claim 1, it is characterised in that: the bottom opening of described catch tray is uncovered with the upper end of described liquid cylinder corresponding；Described collector tray bottom opening diameter is less than the uncovered diameter in the upper end of described liquid cylinder.
3. a kind of annular tube type uniform fluid distribution device as claimed in claim 1, it is characterised in that: it is fastenedly connected a guide pipe connecting with described catch tray and downwardly extending at the bottom opening place of described catch tray.
4. a kind of annular tube type uniform fluid distribution device as claimed in claim 2, it is characterised in that: it is fastenedly connected a guide pipe connecting with described catch tray and downwardly extending at the bottom opening place of described catch tray.
5. a kind of annular tube type uniform fluid distribution device as claimed in claim 1 or 2 or 3 or 4, it is characterised in that: a collecting tank in inverted cone shape it is fastenedly connected at the top of described liquid cylinder.
6. a kind of annular tube type uniform fluid distribution device as claimed in claim 1 or 2 or 3 or 4, it is characterised in that: described arm adopts pipe or rectangular tube.
7. a kind of annular tube type uniform fluid distribution device as claimed in claim 5, it is characterised in that: described arm adopts pipe or rectangular tube.
8. a kind of annular tube type uniform fluid distribution device as claimed in claim 1 or 2 or 3 or 4, it is characterised in that: described equal discharge orifice adopts circular hole, square hole or slit-aperture type hole.
9. a kind of annular tube type uniform fluid distribution device as claimed in claim 5, it is characterised in that: described equal discharge orifice adopts circular hole, square hole or slit-aperture type hole.
10. a kind of annular tube type uniform fluid distribution device as claimed in claim 6, it is characterised in that: described equal discharge orifice adopts circular hole, square hole or slit-aperture type hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610220848.4A CN105758248A (en) | 2016-04-11 | 2016-04-11 | Annular pipe type uniform distribution device of fluid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610220848.4A CN105758248A (en) | 2016-04-11 | 2016-04-11 | Annular pipe type uniform distribution device of fluid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105758248A true CN105758248A (en) | 2016-07-13 |
Family
ID=56333749
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610220848.4A Pending CN105758248A (en) | 2016-04-11 | 2016-04-11 | Annular pipe type uniform distribution device of fluid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105758248A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109001246A (en) * | 2018-07-11 | 2018-12-14 | 中国石油大学(华东) | A kind of experimental rig of FLNG wound tube heat exchanger flowing and Research on Heat Transfer Characteristics |
| CN111895846A (en) * | 2020-06-11 | 2020-11-06 | 中海石油气电集团有限责任公司 | Disc type gas-liquid two-phase fluid uniform distribution device |
| CN113280650A (en) * | 2021-07-22 | 2021-08-20 | 四川空分设备(集团)有限责任公司 | Gas-liquid two-phase fluid uniform distribution device |
| CN114705077A (en) * | 2022-03-22 | 2022-07-05 | 中海石油气电集团有限责任公司 | Refrigerant uniform distribution system of LNG (liquefied Natural gas) coiled tube heat exchanger |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101837199A (en) * | 2010-04-06 | 2010-09-22 | 浙江工业大学 | Linear liquid distributor |
| CN202387443U (en) * | 2011-11-04 | 2012-08-22 | 联化科技股份有限公司 | Distributor in halogenated aromatic hydrocarbon ammoxidation fluidized bed reactor |
| CN204735227U (en) * | 2015-03-20 | 2015-11-04 | 杭州华泽医药科技有限公司 | Filled tower liquid distributor |
| CN205027198U (en) * | 2015-10-13 | 2016-02-10 | 唐山瑞丰钢铁（集团）有限公司 | Cooling tower water distribution uniformity device |
-
2016
- 2016-04-11 CN CN201610220848.4A patent/CN105758248A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101837199A (en) * | 2010-04-06 | 2010-09-22 | 浙江工业大学 | Linear liquid distributor |
| CN202387443U (en) * | 2011-11-04 | 2012-08-22 | 联化科技股份有限公司 | Distributor in halogenated aromatic hydrocarbon ammoxidation fluidized bed reactor |
| CN204735227U (en) * | 2015-03-20 | 2015-11-04 | 杭州华泽医药科技有限公司 | Filled tower liquid distributor |
| CN205027198U (en) * | 2015-10-13 | 2016-02-10 | 唐山瑞丰钢铁（集团）有限公司 | Cooling tower water distribution uniformity device |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109001246A (en) * | 2018-07-11 | 2018-12-14 | 中国石油大学(华东) | A kind of experimental rig of FLNG wound tube heat exchanger flowing and Research on Heat Transfer Characteristics |
| CN111895846A (en) * | 2020-06-11 | 2020-11-06 | 中海石油气电集团有限责任公司 | Disc type gas-liquid two-phase fluid uniform distribution device |
| CN113280650A (en) * | 2021-07-22 | 2021-08-20 | 四川空分设备(集团)有限责任公司 | Gas-liquid two-phase fluid uniform distribution device |
| CN114705077A (en) * | 2022-03-22 | 2022-07-05 | 中海石油气电集团有限责任公司 | Refrigerant uniform distribution system of LNG (liquefied Natural gas) coiled tube heat exchanger |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105758248A (en) | Annular pipe type uniform distribution device of fluid | |
| CN105865247B (en) | A kind of disc type uniform fluid distribution device | |
| CN205690066U (en) | A kind of separator for liquefied natural gas aerating machine | |
| CN202813776U (en) | Electric water heater inlet pipe | |
| CN201775987U (en) | Industrial oil-water separating system | |
| CN208966249U (en) | A kind of compact coaxial double-pipe injection-production well mouth device | |
| CN203134391U (en) | Double-chamber cylindrical type supercritical water cooled reactor steam chamber structure and pressure container | |
| CN205277395U (en) | Submarine pipeline gas -liquid section plug flow entrapment separator | |
| CN203678022U (en) | Air eliminator | |
| CN201343534Y (en) | Marsh gas generator with top-mounted hydraulic room | |
| CN111895846B (en) | Disc type gas-liquid two-phase fluid uniform distribution device | |
| CN204535487U (en) | With the heat exchanger of distributing disc | |
| CN105047374B (en) | Helical tube cycle cooling transformer | |
| CN202762277U (en) | Cylindrical block hole type graphite falling film absorber | |
| CN103816698A (en) | Eliminator | |
| CN205445977U (en) | Feed liquor valve prevents that row of burying adopts pump | |
| CN104748588A (en) | Heat exchanger with distribution discs | |
| CN106122749A (en) | A kind of automatic drain diverter | |
| CN217929927U (en) | Device for gasifying low-boiling-point medium by using waste heat of corrosive medium | |
| CN212745446U (en) | Flange assembly | |
| CN107744670A (en) | A kind of evaporator | |
| CN220392145U (en) | Oil gas recovery device of asphalt tank | |
| CN117266825B (en) | Open flow test device for high-temperature high-pressure geothermal well | |
| CN112113353B (en) | Heat collector constant-pressure tube spacing optimization design method | |
| CN209621289U (en) | Air-water separate injection device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 100010 Chaoyangmen North Street, Dongcheng District, Dongcheng District, Beijing Applicant after: China Offshore Oil Group Co., Ltd. Applicant after: CNOOC Gas & Power Group Applicant after: Kaifeng Air Separation Group Co., Ltd. Address before: 100010 Chaoyangmen North Street, Dongcheng District, Dongcheng District, Beijing Applicant before: China National Offshore Oil Corporation Applicant before: CNOOC Gas & Power Group Applicant before: Kaifeng Air Separation Group Co., Ltd. |
|
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160713 |