CN208081887U - A kind of efficient Petroleum Production fractionating column - Google Patents

A kind of efficient Petroleum Production fractionating column Download PDF

Info

Publication number
CN208081887U
CN208081887U CN201820042250.5U CN201820042250U CN208081887U CN 208081887 U CN208081887 U CN 208081887U CN 201820042250 U CN201820042250 U CN 201820042250U CN 208081887 U CN208081887 U CN 208081887U
Authority
CN
China
Prior art keywords
fractionating column
mouth
petroleum production
downspout
filtering table
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.)
Expired - Fee Related
Application number
CN201820042250.5U
Other languages
Chinese (zh)
Inventor
沙马尔干
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujian Sumaitong E Commerce Co Ltd
Original Assignee
Fujian Sumaitong E Commerce Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Fujian Sumaitong E Commerce Co Ltd filed Critical Fujian Sumaitong E Commerce Co Ltd
Priority to CN201820042250.5U priority Critical patent/CN208081887U/en
Application granted granted Critical
Publication of CN208081887U publication Critical patent/CN208081887U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The utility model discloses a kind of efficient Petroleum Production fractionating columns,Its structure includes condenser,Gas vent,Solvent hydraulic fluid port,Gasoline mouth,Kerosene mouth,Oil gas mouth,Steam port,First residue exports,Second residue exports,Crude oil import,Evaporator,Pipeline,Tray apparatus,Fractionating column,The top of gas vent is installed below condenser,Gas vent is connected by external pipe with fractionating column,The left side insertion of solvent hydraulic fluid port is installed on the inside of fractionating column,The lower surface of gasoline mouth and the upper surface of kerosene mouth are mutually parallel,The right side of fractionating column is installed on the left of kerosene mouth,The left side of oil gas mouth is connected with fractionating column,The left side insertion of steam port is installed on the inside of fractionating column,The upper left corner of first residue outlet is installed on the lower section of fractionating column,A kind of efficient Petroleum Production fractionating column of the utility model,Tray apparatus is provided in its structure,Make to reduce impurity when its filtering,Make to be not easy to plug in filter process.

Description

A kind of efficient Petroleum Production fractionating column
Technical field
The utility model is a kind of efficient Petroleum Production fractionating column, belongs to petroleum production art.
Background technology
Fractionating column is a kind of tower vapour-liquid device distilled, and also known as destilling tower, fractionating column has plate column and filler Two kinds of main Types of tower, two kinds of continuous rectification tower and intermittent fractionation tower can be divided into according to action type again.
Prior art discloses application No. is:A kind of plate and fractionating column of CN201621106181.7, fractionating column Disk includes column plate and downflow weir, and fractionating column includes fractionating column cylinder, plate and riser, and fractionating column cylinder carries for fractionation For space, plate is fixed therein on wall.Plate is staggered in fractionating column cylinder;Fractionating column cylinder inboard wall and The cavity that plate is formed is riser, but impurity is more when the prior art filtering, is caused easily stifled in filter process Plug.
Utility model content
In view of the deficienciess of the prior art, the utility model aim is to provide a kind of efficient Petroleum Production fractionation Tower, impurity is more when solving prior art filtering, leads to the susceptible to plugging problem in filter process.
To achieve the goals above, the utility model is to realize by the following technical solutions:A kind of efficient oil Production fractionating column, structure include condenser, gas vent, solvent hydraulic fluid port, gasoline mouth, kerosene mouth, oil gas mouth, steam port, The outlet of first residue, the second residue outlet, crude oil import, evaporator, pipeline, tray apparatus, fractionating column, the condenser Lower section be installed on the top of gas vent, the gas vent is connected by external pipe with fractionating column, the solvent naphtha The left side insertion of mouth is installed on the inside of fractionating column, and the lower surface and the upper surface of kerosene mouth of the gasoline mouth are mutually parallel, institute The right side that fractionating column is installed on the left of kerosene mouth is stated, the left side of the oil gas mouth is connected with fractionating column, the steam port Left side is embedded in the inside for being installed on fractionating column, and the upper left corner of the first residue outlet is installed on the lower section of fractionating column, described It is connected below the upper left side of second residue outlet and evaporator, the left side of the evaporator is equipped with crude oil import, described The lower section of the upper surface tray apparatus of pipeline, the tray apparatus are assisted by support ring, triangle bubble promoting device, multiple branch Downspout, downspout, descending liquid tube support plate, composite holes miniature valve, tower wall, filtering table composition, the outside installation of the support ring In on the inside of tower wall, the lower surface of the triangle bubble promoting device is installed on the top of filtering table, and the multiple branch is auxiliary Downspout is helped to be installed on the inside of tower wall, the upper surface of the downspout is installed on the lower section of filtering table, the downspout support The inside of plate is connected with downspout, and the lower surface of the composite holes miniature valve fits in the top of filtering table.
Further, the solvent hydraulic fluid port is cylindrical structure, a diameter of 3cm of the pipeline.
Further, the lower surface of the solvent hydraulic fluid port and the upper surface of steam port are mutually parallel.
Further, the top of pipeline is installed below the filtering table.
Further, the filtering table is connected by tower wall with fractionating column.
Further, the pipeline is made of pvc, has the effect of at low cost.
Further, the descending liquid tube support plate is made of stainless steel, and has the effect of antirust.
Advantageous effect
A kind of efficient Petroleum Production fractionating column of the utility model, is provided with tray apparatus in its structure, and oil exists Inside fractionating column, it is tiny that the air-flow for flowing out a valve using the mechanical structure on its periphery is divided into multiply diameter by composite holes miniature valve Air-flow, increase gas liquid interfacial area, reduce liquid foam entrainment, then assisted under downspout flow direction by downspout and multiple branch The composite holes miniature valve of level-one is being reacted, and triangle bubble promoting device is carrying out blistering reaction, the support of descending liquid tube support plate Its stability in descending liquid makes to block in descending liquid, and support ring supports held stationary, makes to reduce impurity when its filtering, Make to be not easy to plug in filter process.
Description of the drawings
Upon reading the detailed description of non-limiting embodiments with reference to the following drawings, other spies of the utility model Sign, objects and advantages will become more apparent upon:
Fig. 1 is a kind of structural schematic diagram of efficient Petroleum Production fractionating column of the utility model;
Fig. 2 is a kind of efficient Petroleum Production fractionating plate device internal structure schematic diagram of the utility model.
In figure:Condenser -1, gas vent -2, solvent hydraulic fluid port -3, gasoline mouth -4, kerosene mouth -5, oil gas mouth -6, steam The -7, first residue of mouth exports the -8, second residue outlet -9, crude oil import -10, evaporator -11, pipeline -12, tower tray dress Set -13, fractionating column -14, support ring -1301, triangle bubble promoting device -1302, multiple branch auxiliary downspout -1303, drop Liquid pipe -1304, descending liquid tube support plate -1305, composite holes miniature valve -1306, tower wall -1307.
Specific implementation mode
To make the technical means, creative features, achievement of purpose, and effectiveness of the utility model be easy to understand, below In conjunction with specific implementation mode, the utility model is expanded on further.
It please refers to Fig.1, Fig. 2, the utility model provides a kind of efficient Petroleum Production fractionating column technical solution:Its structure Go out including condenser 1, gas vent 2, solvent hydraulic fluid port 3, gasoline mouth 4, kerosene mouth 5, oil gas mouth 6, steam port 7, the first residue The 8, second residue of mouth outlet 9, crude oil import 10, evaporator 11, pipeline 12, tray apparatus 13, fractionating column 14, the condenser 1 lower section is installed on the top of gas vent 2, and the gas vent 2 is connected by external pipe with fractionating column 14, described molten The left side insertion of agent hydraulic fluid port 3 is installed on the inside of fractionating column 14, the lower surface of the gasoline mouth 4 and the upper surface phase of kerosene mouth 5 Mutually parallel, the left side of the kerosene mouth 5 is installed on the right side of fractionating column 14, and the left side of the oil gas mouth 6 is connected with fractionating column 14 It connects, the left side insertion of the steam port 7 is installed on the inside of fractionating column 14, the upper left corner installation of the first residue outlet 8 It is connected with the lower section of evaporator 11 in the upper left side of the lower section of fractionating column 14, the second residue outlet 9, the evaporator 11 left side is equipped with crude oil import 10, and the lower section of the upper surface tray apparatus 13 of the pipeline 12, the tray apparatus 13 is by propping up Pushing out ring 1301, triangle bubble promoting device 1302, multiple branch auxiliary downspout 1303, downspout 1304, descending liquid tube support plate 1305, composite holes miniature valve 1306, tower wall 1307, filtering table 1308 form, and the outside of the support ring 1301 is installed on tower wall On 1307 inside, the lower surface of the triangle bubble promoting device 1302 is installed on the top of filtering table 1308, described more points Branch type auxiliary downspout 1303 is installed on the inside of tower wall 1307, and the upper surface of the downspout 1304 is installed on filtering table 1308 Lower section, the inside of the descending liquid tube support plate 1305 is connected with downspout 1304, under the composite holes miniature valve 1306 Surface fits in the top of filtering table 1308, and the solvent hydraulic fluid port 3 is cylindrical structure, a diameter of 3cm of the pipeline 12, institute The lower surface and the upper surface of steam port 7 for stating solvent hydraulic fluid port 3 are mutually parallel, and the lower section of the filtering table 1308 is installed on pipeline 12 Top, the filtering table 1308 is connected by tower wall 1307 with fractionating column 14, and the pipeline 12 is made of pvc, have at This low effect, the descending liquid tube support plate 1305 are made of stainless steel, and have the effect of antirust.
It is with pipe, pipe that tray apparatus 13 described in this patent, which also has two kinds of made of one piece and sectional type, the pipeline 12, The device for conveying gas, liquid or the fluid with solid particle that connector and valve etc. are connected into.
When being used, inside fractionating column, composite holes miniature valve 1306 will be flowed oil using the mechanical structure on its periphery The air-flow for going out a valve is divided into the tiny air-flow of multiply diameter, increases gas liquid interfacial area, reduces liquid foam entrainment, then passes through drop The composite holes miniature valve 1306 that liquid pipe 1304 and multiple branch auxiliary downspout 1303 flow to next stage is being reacted, triangle Bubble promoting device 1302 supports its stability in descending liquid, makes in descending liquid in progress blistering reaction, descending liquid tube support plate 1305 Shi Buhui is blocked, and support ring 1301 supports held stationary.
Impurity is more when the utility model solves prior art filtering, leads to the susceptible to plugging problem in filter process, The utility model is combined with each other by above-mentioned component, and tray apparatus is provided in its structure, makes to reduce impurity when its filtering, Make to be not easy to plug in filter process.
The advantages of basic principles and main features and the utility model of the utility model have been shown and described above, for For those skilled in the art, it is clear that the present invention is not limited to the details of the above exemplary embodiments, and without departing substantially from this In the case of the spirit or essential attributes of utility model, the utility model can be realized in other specific forms.Therefore, no matter From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the utility model is by institute Attached claim rather than above description limit, it is intended that will fall within the meaning and scope of the equivalent requirements of the claims All changes are embraced therein.Any reference numeral in claim should not be considered as to the involved right of limitation It is required that.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art The other embodiment being appreciated that.

Claims (5)

1. a kind of efficient Petroleum Production fractionating column, it is characterised in that:Its structure include condenser (1), gas vent (2), Solvent hydraulic fluid port (3), gasoline mouth (4), kerosene mouth (5), oil gas mouth (6), steam port (7), the first residue outlet (8), second remain Excess exports (9), crude oil import (10), evaporator (11), pipeline (12), tray apparatus (13), fractionating column (14), the condensation The top of gas vent (2) is installed below device (1), the gas vent (2) passes through external pipe and fractionating column (14) phase Connection, the left side insertion of the solvent hydraulic fluid port (3) are installed on the inside of fractionating column (14), the lower surface of the gasoline mouth (4) with The upper surface of kerosene mouth (5) is mutually parallel, and the right side of fractionating column (14), the oil gas are installed on the left of the kerosene mouth (5) The left side of mouth (6) is connected with fractionating column (14), and the left side insertion of the steam port (7) is installed on the inside of fractionating column (14), The upper left corner of the first residue outlet (8) is installed on the lower section of fractionating column (14), a left side for the second residue outlet (9) It is connected below top and evaporator (11), the left side of the evaporator (11) is equipped with crude oil import (10), the pipeline (12) lower section of upper surface tray apparatus (13), the tray apparatus (13) is bubbled by support ring (1301), triangle to be promoted Device (1302), multiple branch auxiliary downspout (1303), downspout (1304), descending liquid tube support plate (1305), composite holes are miniature Valve (1306), tower wall (1307), filtering table (1308) form, and tower wall (1307) is installed on the outside of the support ring (1301) On inside, the lower surface of the triangle bubble promoting device (1302) is installed on the top of filtering table (1308), the multiple-limb Type auxiliary downspout (1303) is installed on the inside of tower wall (1307), and the upper surface of the downspout (1304) is installed on filtering table (1308) inside of lower section, the descending liquid tube support plate (1305) is connected with downspout (1304), and the composite holes are miniature The lower surface of valve (1306) fits in the top of filtering table (1308).
2. a kind of efficient Petroleum Production fractionating column according to claim 1, it is characterised in that:The solvent hydraulic fluid port (3) it is cylindrical structure, a diameter of 3cm of the pipeline (12).
3. a kind of efficient Petroleum Production fractionating column according to claim 1, it is characterised in that:The solvent hydraulic fluid port (3) upper surface of lower surface and steam port (7) is mutually parallel.
4. a kind of efficient Petroleum Production fractionating column according to claim 1, it is characterised in that:The filtering table (1308) top of pipeline (12) is installed below.
5. a kind of efficient Petroleum Production fractionating column according to claim 1, it is characterised in that:The filtering table (1308) it is connected with fractionating column (14) by tower wall (1307).
CN201820042250.5U 2018-01-11 2018-01-11 A kind of efficient Petroleum Production fractionating column Expired - Fee Related CN208081887U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820042250.5U CN208081887U (en) 2018-01-11 2018-01-11 A kind of efficient Petroleum Production fractionating column

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820042250.5U CN208081887U (en) 2018-01-11 2018-01-11 A kind of efficient Petroleum Production fractionating column

Publications (1)

Publication Number Publication Date
CN208081887U true CN208081887U (en) 2018-11-13

Family

ID=64065545

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820042250.5U Expired - Fee Related CN208081887U (en) 2018-01-11 2018-01-11 A kind of efficient Petroleum Production fractionating column

Country Status (1)

Country Link
CN (1) CN208081887U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109260749A (en) * 2018-11-29 2019-01-25 方文星 Distilling filled tower is used in a kind of separation of chemical material
CN110180202A (en) * 2019-07-05 2019-08-30 黄河三角洲京博化工研究院有限公司 The production system and production method of a kind of low coloration high boiling aromatic hydrocarbon solvent of width boiling range
WO2021178301A1 (en) * 2020-03-06 2021-09-10 Uop Llc Bubble promoter

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109260749A (en) * 2018-11-29 2019-01-25 方文星 Distilling filled tower is used in a kind of separation of chemical material
CN110180202A (en) * 2019-07-05 2019-08-30 黄河三角洲京博化工研究院有限公司 The production system and production method of a kind of low coloration high boiling aromatic hydrocarbon solvent of width boiling range
CN110180202B (en) * 2019-07-05 2021-10-26 黄河三角洲京博化工研究院有限公司 Production system and production method of wide-distillation-range low-chroma high-boiling-point aromatic solvent
WO2021178301A1 (en) * 2020-03-06 2021-09-10 Uop Llc Bubble promoter
CN115243777A (en) * 2020-03-06 2022-10-25 环球油品有限责任公司 Bubble promoting device
US11554328B2 (en) 2020-03-06 2023-01-17 Uop Llc Bubble promoter

Similar Documents

Publication Publication Date Title
CN208081887U (en) A kind of efficient Petroleum Production fractionating column
CN103877752B (en) A kind of online degas method of pipeline fluid and device
CN104528206B (en) Wellhead oil collecting tank of carbon dioxide flooding well
CN203281068U (en) Multifunctional extraction concentration recycling set
BR0307480A (en) Apparatus in method for degassing liquids
CN204121795U (en) A kind of novel packed tower suppressing gas fractionation unit to block liquid
CN104524801B (en) A kind of dispersion descending liquid sieve-plate tower
CN100398174C (en) Tower plate with sinker in downcomer
CN202569671U (en) Oil-sand separating device for settlement plate type wellhead
CN103706138A (en) Distributor for packed tower
CN204723990U (en) A kind of packed tower of uniform liquid distribution
CN205528614U (en) Improve diesel oil vacuum dehydration system of diesel oil water content
CN107557058B (en) Compact combined flash crude oil degassing method and device
CN204699428U (en) A kind of practical packed tower
CN201271518Y (en) Steam-liquid distributor of packing tower
CN103301645B (en) A kind of High-flux plate-type tower
CN204848349U (en) A oil -water separator for coal tar hydrogenation equipment accident pond
CN208448683U (en) A kind of plated tower
CN204727863U (en) Improve the volatile oil extractor of distillate pipe
CN207933308U (en) A kind of reaction unit of separation of extractive distillation normal heptane and ethyl acetate
CN210543431U (en) Rectifying tower
CN206355622U (en) A kind of PETROLEUM PROCESSING rectifying column
CN203803525U (en) Distiller
CN202096770U (en) Side-draw or middle feeding device placed in packing layer
CN204447414U (en) Oil water separator

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20181113

Termination date: 20190111

CF01 Termination of patent right due to non-payment of annual fee