CN204756431U - Liquefied gas raffinate vapourizing unit among oil liquefied gas pipeline - Google Patents
Liquefied gas raffinate vapourizing unit among oil liquefied gas pipeline Download PDFInfo
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- CN204756431U CN204756431U CN201520385378.8U CN201520385378U CN204756431U CN 204756431 U CN204756431 U CN 204756431U CN 201520385378 U CN201520385378 U CN 201520385378U CN 204756431 U CN204756431 U CN 204756431U
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- raffinate
- liquid gas
- liquefied gas
- hole
- gas flow
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Abstract
The utility model relates to a liquefied gas raffinate vapourizing unit among oil liquefied gas pipeline, including casing, raffinate sediment box, porous liquefied gas circulation board and siphon, the casing has a same diameter with oil liquefied gas pipeline, and both ends are connected with oil liquefied gas pipeline through the flange respectively, and casing below intercommunication has the raffinate sediment box, establishes porous liquefied gas circulation board in the casing on raffinate sediment box upper portion, and the raffinate sediment box feeds through respectively through a plurality of vaporization access openings that a plurality of siphons and porous liquefied gas circulated on the board, and the nozzle is established at the siphon top. Compared with the prior art, the beneficial effects of the utility model are that: based on hydrodynamics principles of design, outside power need not to exert, and the fluid pressure that have certainly when passing through pipeline through the oil liquefied gas vaporize the raffinate suction, simple structure, simple to operate, the use need not artificial intervention, and raffinate vaporization effect is good, has filled in a blank in the technique of this area.
Description
Technical field
The utility model relates to a kind of device for vaporizing liquid gas raffinate, particularly relates to a kind of device for vaporizing liquid gas raffinate of liquefied petroleum gas conveyance conduit.
Background technique
At present, in liquefied petroleum gas conveyance conduit, device can only be stored up, then periodic collection by subsection setup liquid petroleum gas residual liquid in the duct for the processing method of liquefied gas residue, then process.The shortcoming of this way is, regularly will carry out the collection work of liquid petroleum gas residual liquid, and process is loaded down with trivial details, time-consuming.
Summary of the invention
The utility model provides device for vaporizing liquid gas raffinate in a kind of liquefied petroleum gas conveyance conduit, design based on fluid mechanics principle, without the need to applying external impetus, raffinate sucking-off is vaporized by hydrodynamic pressure own during conveyance conduit by liquefied petroleum gas, structure is simple, and easy for installation, using process is without the need to manual intervention, raffinate vaporization effect is good, has filled up a blank in art technology.
In order to achieve the above object, the utility model realizes by the following technical solutions:
Device for vaporizing liquid gas raffinate in a kind of liquefied petroleum gas conveyance conduit, comprise housing, raffinate sediment box, porous liquid gas flow plate and syphon tube, described housing has the diameter identical with liquefied petroleum gas conveyance conduit, two ends are connected with liquefied petroleum gas conveyance conduit respectively by flange, raffinate sediment box is communicated with below housing, porous liquid gas flow plate is established in the housing on raffinate sediment box top, raffinate sediment box is communicated with the multiple vaporization port holes on porous liquid gas flow plate respectively by multiple syphon tube, and syphon tube top is provided with nozzle.
Be provided with multiple liquid gas flow through hole to described porous liquid gas flow plate upper dense, be provided with to lower dense multiple vaporization port hole, liquid gas flow through hole is evenly arranged in the horizontal direction with vaporization port hole, is staggered along short transverse, and liquid gas flow through hole is identical with vaporization port hole diameter.
Described liquid gas flow through hole is demarcated along housing horizontal axis with vaporization port hole, more than horizontal axis is liquid gas flow through hole, be vaporization port hole, and vaporization port hole is 2 rows below horizontal axis.
Described vaporization port hole and syphon tube one_to_one corresponding, the nozzle of syphon tube upper end is conical vaporization nozzles, and lower end extends to bottom raffinate sediment box, and pipe end offers scarf, and filter screen is housed.
Compared with prior art, the beneficial effects of the utility model are:
Design based on fluid mechanics principle, without the need to applying external impetus, raffinate sucking-off is vaporized by hydrodynamic pressure own during conveyance conduit by liquefied petroleum gas, structure is simple, easy for installation, using process is without the need to manual intervention, and raffinate vaporization effect is good, has filled up a blank in art technology.
Accompanying drawing explanation
Fig. 1 is three-dimensional cutaway view of the present utility model.
Fig. 2 is main pseudosection of the present utility model.
Fig. 3 is the left view of Fig. 2.
In figure: 1. housing 2. flange 3. raffinate sediment box 4. porous liquid gas flow plate 41. liquid gas flow through hole 42. is vaporized port hole 5. syphon tube 6. nozzle
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described further:
See Fig. 1-Fig. 3, it is structural representation of the present utility model, device for vaporizing liquid gas raffinate in a kind of liquefied petroleum gas conveyance conduit of the utility model, comprise housing 1, raffinate sediment box 3, porous liquid gas flow plate 4 and syphon tube 5, described housing 1 has the diameter identical with liquefied petroleum gas conveyance conduit, two ends are connected with liquefied petroleum gas conveyance conduit respectively by flange 2, raffinate sediment box 3 is communicated with below housing 1, porous liquid gas flow plate 4 is established in the housing 1 on raffinate sediment box 3 top, raffinate sediment box 3 is communicated with the multiple vaporization port holes 42 on porous liquid gas flow plate 4 respectively by multiple syphon tube 5, syphon tube 5 top is provided with nozzle 6.
Be provided with multiple liquid gas flow through hole 41 to described porous liquid gas flow plate 4 upper dense, be provided with to lower dense multiple vaporization port hole 42, liquid gas flow through hole 41 is evenly arranged in the horizontal direction with vaporization port hole 42, be staggered along short transverse, liquid gas flow through hole 41 is identical with vaporization port hole 42 diameter.
Described liquid gas flow through hole 41 is demarcated along housing 1 horizontal axis with vaporization port hole 42, more than horizontal axis is liquid gas flow through hole 41, be vaporization port hole 42, and vaporization port hole 42 is 2 rows below horizontal axis.
Described vaporization port hole 42 and syphon tube 5 one_to_one corresponding, the nozzle 6 of syphon tube 5 upper end is conical vaporization nozzles, and lower end extends to bottom raffinate sediment box 3, and pipe end offers scarf, and filter screen is housed.
The main component of liquid petroleum gas residual liquid is butane, pentane, hydrogen sulfide etc. containing not easily vaporizing under the condition that carbon value is higher, ambient temperature is low, also has other impurity.Porous liquid gas flow plate 4 offers gasification channel hole 42, when liquid gas in liquefied petroleum gas conveyance conduit is by this hole traveling through nozzle 6, nozzle 6 place is made to produce negative pressure, by syphon tube 5 by the liquefied gas residue sucking-off bottom raffinate sediment box 3, then sprayed by vaporization nozzles 6 and taken out of vaporization by the L. P. G entraining air stream with hydrodynamic pressure, liquefied gas residue after vaporization is with L. P. G entraining air stream continuous Flows backward, thus automatic evaporation under achieving liquefied gas residue external power-free situation.
In the utility model, liquid gas flow through hole 41 is principal flow passage of liquid gas in pipeline, and liquid gas flow through hole 41 is identical with the aperture of vaporization port hole 42, can ensure each hole internal pressure balance.
Claims (4)
1. device for vaporizing liquid gas raffinate in a liquefied petroleum gas conveyance conduit, it is characterized in that, comprise housing, raffinate sediment box, porous liquid gas flow plate and syphon tube, described housing has the diameter identical with liquefied petroleum gas conveyance conduit, two ends are connected with liquefied petroleum gas conveyance conduit respectively by flange, raffinate sediment box is communicated with below housing, porous liquid gas flow plate is established in the housing on raffinate sediment box top, raffinate sediment box is communicated with the multiple vaporization port holes on porous liquid gas flow plate respectively by multiple syphon tube, syphon tube top is provided with nozzle.
2. device for vaporizing liquid gas raffinate in a kind of liquefied petroleum gas conveyance conduit according to claim 1, it is characterized in that, be provided with multiple liquid gas flow through hole to described porous liquid gas flow plate upper dense, be provided with to lower dense multiple vaporization port hole, liquid gas flow through hole is evenly arranged in the horizontal direction with vaporization port hole, be staggered along short transverse, liquid gas flow through hole is identical with vaporization port hole diameter.
3. device for vaporizing liquid gas raffinate in a kind of liquefied petroleum gas conveyance conduit according to claim 1 and 2, it is characterized in that, described liquid gas flow through hole is demarcated along housing horizontal axis with vaporization port hole, it more than horizontal axis is liquid gas flow through hole, be vaporization port hole below horizontal axis, and vaporization port hole is 2 rows.
4. device for vaporizing liquid gas raffinate in a kind of liquefied petroleum gas conveyance conduit according to claim 1, it is characterized in that, described vaporization port hole and syphon tube one_to_one corresponding, the nozzle of syphon tube upper end is conical vaporization nozzles, lower end extends to bottom raffinate sediment box, and pipe end offers scarf, and filter screen is housed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520385378.8U CN204756431U (en) | 2015-06-08 | 2015-06-08 | Liquefied gas raffinate vapourizing unit among oil liquefied gas pipeline |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520385378.8U CN204756431U (en) | 2015-06-08 | 2015-06-08 | Liquefied gas raffinate vapourizing unit among oil liquefied gas pipeline |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204756431U true CN204756431U (en) | 2015-11-11 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520385378.8U Expired - Fee Related CN204756431U (en) | 2015-06-08 | 2015-06-08 | Liquefied gas raffinate vapourizing unit among oil liquefied gas pipeline |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204756431U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105333429A (en) * | 2015-11-25 | 2016-02-17 | 襄阳宏伟航空器有限责任公司 | Burner siphon device for fire balloon |
-
2015
- 2015-06-08 CN CN201520385378.8U patent/CN204756431U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105333429A (en) * | 2015-11-25 | 2016-02-17 | 襄阳宏伟航空器有限责任公司 | Burner siphon device for fire balloon |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20151111 Termination date: 20160608 |