CN207667168U - Reboiler in propane production line - Google Patents
Reboiler in propane production line Download PDFInfo
- Publication number
- CN207667168U CN207667168U CN201721825367.2U CN201721825367U CN207667168U CN 207667168 U CN207667168 U CN 207667168U CN 201721825367 U CN201721825367 U CN 201721825367U CN 207667168 U CN207667168 U CN 207667168U
- Authority
- CN
- China
- Prior art keywords
- shell
- heating tube
- tube group
- diversion cans
- reboiler
- 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
Links
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses the reboilers in a kind of propane production line, including diversion cans, heater and shell;The heater includes heating tube group and connecting plate;U-tube in heating tube group is bellows;And heating tube group is saved by least two along the sequentially connected unit pipeline section group in heater length direction.Reboiler in the utility model propane production line, heating tube group and shell are made of several dismountable elementary sections so that the space occupied smaller needed for dismounting heating tube group and shell, dismounting are more convenient;And its shape pipe is bellows, under same diameter, the surface area bigger of the surface area ratio light pipe of bellows, therefore the heat exchange efficiency of the heating tube group in the utility model is than the heat exchange efficiency higher of heating tube in existing reboiler.
Description
Technical field
The utility model is related to a kind of chemical industry equipment, more particularly to the reboiler in a kind of high-purity propane production line.
Background technology
The mainstream refrigerant of domestic market be containing fluorinated refrigerant, such as R22, R410A and R407, but they cause it is smelly
The environmental problems such as oxygen layer destruction, greenhouse effects.For the environmental protection refrigerant R290 for obtaining natural, high-purity propane production technology is ground
Study carefully the research and development focus as refrigeration industry.
At present using the low-purity propane from natural gas or crude oil as raw material, through pretreatment of raw material, saturated hydrogenation, separation essence
The process of ultra-pure propane is made in the technical process such as system, has preferable development prospect.
In the technique separation and purification include to reaction product carry out de- light processing and it is de- handle again, in de- light processing and de- weight
In processing procedure, lightness-removing column and the mating setting reboiler of weight-removing column will be given.
Existing reboiler generally uses shell and tube reboiler, but the volume of shell and tube reboiler is larger, needed for dismounting
The space wanted is big, is unfavorable for the processing such as dismounting it, repair.And the heat exchanger tube that existing shell and tube reboiler uses is all
It is light pipe, heat exchange efficiency is relatively low.
Utility model content
In view of this, the purpose of this utility model is to provide the reboiler in a kind of propane production line, it is existing to solve
Tubulation keeps reboiler volume big, does not dismount cheaply and the more low technical problem of heat exchange efficiency.
Reboiler in the utility model propane production line, including diversion cans, heater and shell;
It is provided with partition board in the middle part of the diversion cans, the inner cavity of diversion cans is separated into oil inlet epicoele and fuel-displaced by the partition board
Cavity of resorption, is provided with the inlet connector being connected to oil inlet epicoele at the top of diversion cans, the bottoms of diversion cans be provided with it is fuel-displaced under
The oil returning pipe joint of chamber connection;
The heater include the heating tube group that forms of U-tube being arranged in parallel by several and be fixedly connected on plus
The connecting plate of heat pipe heat end;The connecting plate by the oral area of bolt and diversion cans connect, the oil inlet of heating tube group with point
The oil inlet epicoele connection of tank is flowed, the oil discharge outlet of heating tube group is connected to the fuel-displaced cavity of resorption of diversion cans;
The U-tube is bellows;
The heating tube group is made of at least two sections along the sequentially connected unit pipeline section in heater length direction, the unit
Buttcover plate is fixedly welded on the end of pipeline section, the buttcover plate on adjacent cells pipeline section is bolted;
The shell is connect by bolt with the connecting plate on heater, and the shell is also by least two sections along outer cover length
The sequentially connected cell enclosure section composition in direction, adjacent cells shell section pass through flanged joint;
The mouth end bottom of the shell is provided with feed liquor pipe fitting, is provided with exhaust fitting at the top of the tail end of shell, outside
The tail end bottom of shell is provided with drain pipe fitting, and liquid barrier is additionally provided in shell, and the drain pipe fitting setting is in gear liquid
Between plate and shell tail end.
Further, it is additionally provided in the middle part of the heating tube group and hangs circle, the inside top of the shell is provided with hanging ring, institute
It states and hangs circle and connected by hoist cable with hanging ring.
The beneficial effects of the utility model:
1, the reboiler in the utility model propane production line, heating tube group and shell are by several dismountable units
Duan Zucheng so that the space occupied smaller needed for dismounting heating tube group and shell, dismounting are more convenient.
2, the reboiler in the utility model propane production line, U-tube is bellows, under same diameter, bellows
Surface area ratio light pipe surface area bigger, therefore the heat exchange efficiency of the heating tube group in the utility model is than in existing reboiler
The heat exchange efficiency higher of heating tube.
Description of the drawings
Fig. 1 is the structural schematic diagram of reboiler in propane production line in embodiment;
Fig. 2 is the partial structural diagram of U-tube.
Specific implementation mode
The utility model is further described with reference to the accompanying drawings and examples.
As shown, the reboiler in the present embodiment in propane production line, including diversion cans 1, heater 2 and shell 3.
Partition board 4 is provided in the middle part of the diversion cans, the inner cavity of diversion cans is separated into oil inlet epicoele 5 and gone out by the partition board
Oily cavity of resorption 6 is provided with the inlet connector 7 being connected to oil inlet epicoele at the top of diversion cans, and the bottom of diversion cans is provided with and goes out
The oil returning pipe joint 8 of oily cavity of resorption connection.
The heater 2 includes the heating tube group 201 and be fixedly connected that the U-tube being arranged in parallel by several forms
Connecting plate 202 in heating tube group end;The connecting plate is connected by the oral area of bolt and diversion cans, the oil inlet of heating tube group
Mouth is connected to the oil inlet epicoele of diversion cans, and the oil discharge outlet of heating tube group is connected to the fuel-displaced cavity of resorption of diversion cans.
The U-tube is bellows.
The heating tube group 201 is made of at least two sections along the sequentially connected unit pipeline section in heater length direction, this reality
It is specially two sections to apply unit pipeline section in example.Buttcover plate 9 is fixedly welded on the end of the unit pipeline section, on adjacent cells pipeline section
Buttcover plate be bolted.
The shell 3 is connect by bolt with the connecting plate 202 on heater, and the shell is also by least two sections along shell
The sequentially connected cell enclosure section of length direction forms, and cell enclosure section is specially two sections in the present embodiment.Adjacent cells shell section passes through
Flange 10 connects.
The mouth end bottom of the shell is provided with feed liquor pipe fitting 11, and exhaust fitting is provided at the top of the tail end of shell
12, the tail end bottom of shell is provided with drain pipe fitting 13, and liquid barrier 14 is additionally provided in shell, and the drain pipe fitting is set
It sets between liquid barrier and shell tail end.The product of gasification is drained through exhaust fitting, and unvaporized product overflows across liquid barrier
It is discharged from drain pipe fitting 13 behind upper end.
Reboiler in the present embodiment in propane production line, heating tube group and shell are by several dismountable elementary sections
Composition so that the space occupied smaller needed for dismounting heating tube group and shell, dismounting are more convenient.
And the reboiler in the present embodiment in propane production line, U-tube is bellows, under same diameter, ripple
The surface area bigger of the surface area ratio light pipe of pipe, therefore the heat exchange efficiency of the heating tube group in the utility model is than existing reboiler
The heat exchange efficiency higher of middle heating tube.
It is additionally provided in the middle part of the heating tube group as a further modification of the present embodiment, and hangs circle 15, the inside of the shell
Top is provided with hanging ring 16, and circle and the hanging ring of hanging is connected by hoist cable 17.Since the length of tubular is larger, heating tube group
Weight it is larger, the interconnecting piece of tubular and connecting plate can bear larger moment of flexure so that the company of tubular and connecting plate
Socket part is susceptible to destruction crackle.This improvement by setting hang circle 15 pairs of heating tube groups be supported, can improve tubular with
The stressing conditions of the interconnecting piece of connecting plate are avoided that destructive crackle occurs in the position, can extend the service life of heater.
Finally illustrate, above example is merely intended for describing the technical solutions of the present application, but not for limiting the present application, although ginseng
The utility model is described in detail according to preferred embodiment, it will be understood by those of ordinary skill in the art that, it can be to this
The technical solution of utility model is modified or replaced equivalently, without departing from the objective and model of technical solutions of the utility model
It encloses, should all cover in the right of the utility model.
Claims (2)
1. the reboiler in a kind of propane production line, it is characterised in that:Including diversion cans, heater and shell;
Be provided with partition board in the middle part of the diversion cans, the partition board by the inner cavity of diversion cans be separated into oil inlet epicoele and it is fuel-displaced under
Chamber is provided with the inlet connector being connected to oil inlet epicoele at the top of diversion cans, and the bottom of diversion cans is provided with and fuel-displaced cavity of resorption
The oil returning pipe joint of connection;
The heater includes the heating tube group and be fixedly connected on heating tube that the U-tube being arranged in parallel by several forms
The connecting plate of group end;The connecting plate is connected by the oral area of bolt and diversion cans, the oil inlet and diversion cans of heating tube group
The connection of oil inlet epicoele, the oil discharge outlet of heating tube group is connected to the fuel-displaced cavity of resorption of diversion cans;
The U-tube is bellows;
The heating tube group is made of at least two sections along the sequentially connected unit pipeline section in heater length direction, the unit pipeline section
End on be fixedly welded with buttcover plate, the buttcover plate on adjacent cells pipeline section is bolted;
The shell is connect by bolt with the connecting plate on heater, and the shell is also by least two sections along outer cover length direction
Sequentially connected cell enclosure section composition, adjacent cells shell section pass through flanged joint;
The mouth end bottom of the shell is provided with feed liquor pipe fitting, and exhaust fitting is provided at the top of the tail end of shell, shell
Tail end bottom is provided with drain pipe fitting, and liquid barrier is additionally provided in shell, drain pipe fitting setting liquid barrier with
Between shell tail end.
2. the reboiler in propane production line according to claim 1, it is characterised in that:The middle part of the heating tube group is also
It is provided with and hangs circle, the inside top of the shell is provided with hanging ring, and the circle that hangs is connected with hanging ring by hoist cable.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721825367.2U CN207667168U (en) | 2017-12-22 | 2017-12-22 | Reboiler in propane production line |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721825367.2U CN207667168U (en) | 2017-12-22 | 2017-12-22 | Reboiler in propane production line |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207667168U true CN207667168U (en) | 2018-07-31 |
Family
ID=62970071
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721825367.2U Expired - Fee Related CN207667168U (en) | 2017-12-22 | 2017-12-22 | Reboiler in propane production line |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207667168U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110075554A (en) * | 2019-05-08 | 2019-08-02 | 上海蓝滨石化设备有限责任公司 | A kind of concatenated multi-fluid reboiler in still dome |
-
2017
- 2017-12-22 CN CN201721825367.2U patent/CN207667168U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110075554A (en) * | 2019-05-08 | 2019-08-02 | 上海蓝滨石化设备有限责任公司 | A kind of concatenated multi-fluid reboiler in still dome |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN207667168U (en) | Reboiler in propane production line | |
CN103884213A (en) | Corrosion-resistant shell and tube heat exchanger | |
CN203687669U (en) | Acid gas condenser | |
CN203837537U (en) | Liquid chlorine vaporizer device of continuous sleeve type | |
CN203389486U (en) | Efficient vapor-liquid separator | |
CN208779986U (en) | A kind of etch-proof tubular heat exchanger | |
CN203525344U (en) | Tubular falling-film evaporator | |
CN202860502U (en) | Vertical type water-cooled tube reactor | |
CN216654502U (en) | Radial isothermal ammonia synthesis reactor | |
CN103071305B (en) | Vacuum tube type solar solution regenerator | |
CN213375167U (en) | Electric heating kettle type evaporator for sulfuric acid concentration | |
CN204115528U (en) | A kind of lower supporting type graphite heat exchanger | |
CN209166145U (en) | A kind of glass pipe bundle condenser | |
CN101769650A (en) | Intercommunicated full-glass vacuum solar heat-collecting tube | |
CN202020940U (en) | Three-phase separating device for catalytic hydrogenation generation oil based on coal tar | |
CN207478002U (en) | A kind of refining titanic chloride increase evaporation and heat-exchange efficient appliances | |
CN206724757U (en) | A kind of anticorrosion tubular heat exchanger | |
CN201973931U (en) | Heat exchange water tank of solar water heater | |
CN218846097U (en) | Integrated waste heat recovery device | |
CN202909473U (en) | Negative pressure distillation tower for extracting crude benzene | |
CN216687968U (en) | Immunoglobulin salting-out separation device for antibody production | |
CN110793351A (en) | Horizontal multi-connected tube bundle heavy oil heat exchanger | |
CN211435145U (en) | Low-carbon rectifying tower | |
CN215756532U (en) | Multistage series evaporator | |
CN219217569U (en) | Hydrogen separation device of electrolytic tank |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180731 Termination date: 20191222 |