CN203061053U - Continuous circulating spraying device for removing hydrogen sulfide from crude oil storage tank - Google Patents
Continuous circulating spraying device for removing hydrogen sulfide from crude oil storage tank Download PDFInfo
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- CN203061053U CN203061053U CN 201320101871 CN201320101871U CN203061053U CN 203061053 U CN203061053 U CN 203061053U CN 201320101871 CN201320101871 CN 201320101871 CN 201320101871 U CN201320101871 U CN 201320101871U CN 203061053 U CN203061053 U CN 203061053U
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- hydrogen sulfide
- jar
- sulfur elimination
- crude oil
- oil storage
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Abstract
The utility model relates to the technical field of devices for removing hydrogen sulfide from crude oil storage tanks and relates to a continuous circulating spraying device for removing the hydrogen sulfide from the crude oil storage tank. The device comprises a sulfur removing agent tank, an opening mixing treatment tank and a spraying head, wherein a sulfur removing agent pipeline is fixedly mounted at the bottom of the sulfur removing agent tank; an outlet of the sulfur removing agent pipeline is positioned above the opening mixing treatment tank; the spraying head is fixedly mounted at the outlet of the sulfur removing agent pipeline; a pump is fixedly mounted on the sulfur removing agent pipeline; a gas inlet is formed at the bottom end of the opening mixing treatment tank; a gas dispersing device vertically corresponding to the spraying head is fixed at the lower part, corresponding to the gas inlet, in the opening mixing treatment tank; and gas dispersing holes are formed in the gas dispersing device. The device is reasonable and compact in structure and convenient to use, can be used for continuously spraying the sulfur removing agent in the process of storing crude oil on site, controlling the adding amount of the sulfur removing agent easily, eliminating the hydrogen sulfide well, reducing personal injury of the hydrogen sulfide on workers on site, and reducing environmental pollution.
Description
Technical field
The utility model relates to crude oil storage tank removal of hydrogen sulfide device technique field, is the continuous circulating sprayer of a kind of crude oil storage tank removal of hydrogen sulfide.
Background technology
Development along with petroleum industry, exploitation to sulfur-bearing oil-gas reservoir is more and more, sulfur-bearing oil-gas reservoir is under the effect of various conditions such as HTHP and steam, sulfide in oil gas and the formation rock constantly is converted into hydrogen sulfide, and in the process of exploitation and conveying, separate out, thereby environment and personal safety are caused serious harm, and corroded equipment and pipeline.
Crude oil storage tank be crude oil after the pit shaft extraction, crude oil is carried out on-the-spot preserving, the storage tank that adopts and tank car often all have opening port, then the hydrogen sulfide gas in the crude oil overflows from opening port, and relevant operating personnel's life security is caused huge hidden danger.Therefore, must eliminate crude oil hydrogen sulfide gas in the storage tank in preserving process.
The method of the removal of hydrogen sulfide gas of current employing mainly is to remove hydrogen sulfide in the jar at crude oil storage tank mouth dress sprinkling equipment and hydrogen sulfide sensing apparatus, namely when crude oil storage tank mouth hydrogen sulfide induction instrument aratus detects the preset value of hydrogen sulfide content, sprinkling equipment begins to spray sulfur elimination, when the content that detects hydrogen sulfide to the hydrogen sulfide sensing apparatus is lower than the preset value of hydrogen sulfide content, sprinkling equipment quits work, but owing to have the complicated component of volatile sulfur-bearing oil gas thing in the crude oil, it can cause the damage of hydrogen sulfide sensing apparatus, and cause the control of sprinkling equipment malfunctioning, cause the big or halfway problem of sulphur removal of sulfur elimination consumption.
Summary of the invention
The utility model provides a kind of crude oil storage tank removal of hydrogen sulfide continuous circulating sprayer, overcome the deficiency of above-mentioned prior art, it can effectively solve the problem that is difficult to control sulfur elimination addition and removal of hydrogen sulfide gas poor effect that existing crude oil storage tank removal of hydrogen sulfide device exists in actual use.
The technical solution of the utility model realizes by following measure: the continuous circulating sprayer of a kind of crude oil storage tank removal of hydrogen sulfide comprises sulfur elimination jar, opening mixed processing jar and spray head; The bottom of sulfur elimination jar is installed with the sulfur elimination pipeline, the outlet of sulfur elimination pipeline is positioned at the top of opening mixed processing jar, the outlet of sulfur elimination pipeline is installed with spray head, be installed with pump on the sulfur elimination pipeline, there is gas feed the bottom of opening mixed processing jar, bottom in the opening mixed processing jar corresponding with gas feed fixedly has and spray head corresponding diffusing device of air up and down, on the diffusing device of air air dispelling hole is arranged, the top in the opening mixed processing jar is installed with the hydrogen sulfide gas checkout gear.
Be the further optimization and/or improvements to above-mentioned utility model technical scheme below:
Above-mentioned diffusing device of air can comprise cylindrical base and tapered air dispersing hood, air dispersing hood comprises at least three guide plates that cross section is triangular in shape, the lower end of at least three guide plate is separately fixed at the upper end of cylindrical base, the upper end of at least three guide plate is compiled and is fixed together, form runner between guide plate, be furnished with air dispelling hole in the top punishment of the triangle of each guide plate, the upper fixed of air dispelling hole has flashing board, and the diameter of base is less than the diameter of air dispersing hood bottom.
Can there be the groove that is circular the lower end of above-mentioned air dispersing hood, and there is the projection corresponding with groove the upper end of base, and projection is fixedly mounted in the groove.
The diameter of above-mentioned air dispelling hole can be between one centimetre to two centimetres.
Above-mentioned flashing board can be umbrella.
Above-mentioned sulfur elimination jar top can have sulfur elimination to add entrance, and the bottom of sulfur elimination jar is fixedly connected with blowdown pipeline and valve and communicates, and the sulfur elimination jar is fixedly connected with recovery line with the bottom of opening mixed processing jar and communicates, and fixedly there is flange in the gas feed place outside.
Above-mentioned sulfur elimination jar can be installed with the liquid level display tube.
The utility model reasonable and compact in structure, easy to use, it is in carrying out the process that the scene preserves to crude oil, spray sulfur elimination continuously, be easy to control the addition of sulfur elimination and removal of hydrogen sulfide gas preferably, reduce the personal injury of hydrogen sulfide gas to the field personnel, and reduced the pollution to environment.
Description of drawings
Accompanying drawing 1 is the schematic flow sheet of the utility model most preferred embodiment.
Accompanying drawing 2 is the main TV structure schematic diagram of loose device of air and base.
Accompanying drawing 3 is the local structure for amplifying schematic diagram at A place in the accompanying drawing 2.
Coding in the accompanying drawing is respectively: 1 is the sulfur elimination jar, and 2 is opening mixed processing jar, and 3 is spray head, 4 is the sulfur elimination pipeline, and 5 are gas feed, and 6 is air dispersing hood, 7 is air dispelling hole, and 8 is recovery line, and 9 is pump, 10 is base, and 11 for sulfur elimination adds entrance, and 12 is the liquid level display tube, 13 is blowdown pipeline and valve, and 14 is flashing board, and 15 is flange, 16 is guide plate, and 17 is runner.
The specific embodiment
The utility model is not subjected to the restriction of following embodiment, can determine concrete embodiment according to the technical solution of the utility model and actual conditions.
In the utility model, for convenience of description, the description of the relative position relation of each parts all is that the Butut mode according to Figure of description 1 is described, as: the position relation of forward and backward, upper and lower, left and right etc. is what to determine according to the Butut direction of Figure of description 1.
Below in conjunction with embodiment and accompanying drawing the utility model is further described:
Shown in accompanying drawing 1,2,3, the continuous circulating sprayer of this crude oil storage tank removal of hydrogen sulfide comprises sulfur elimination jar 1, opening mixed processing jar 2 and spray head 3; The bottom of sulfur elimination jar 1 is installed with sulfur elimination pipeline 4, the outlet of sulfur elimination pipeline 4 is positioned at the top of opening mixed processing jar 2, the outlet of sulfur elimination pipeline 4 is installed with spray head 3, be installed with pump 9 on the sulfur elimination pipeline 4, there is gas feed 5 bottom of opening mixed processing jar 2, bottom in the opening mixed processing jar 2 corresponding with gas feed 5 fixedly has and spray head corresponding diffusing device of air about in the of 3, on the diffusing device of air air dispelling hole 7 is arranged, the tops in the opening mixed processing jar 2 are installed with the hydrogen sulfide gas checkout gear.
Can according to actual needs the continuous circulated sprinkling head of above-mentioned crude oil storage tank removal of hydrogen sulfide be made further optimization and/or improvements:
Shown in accompanying drawing 2,3, diffusing device of air comprises cylindrical base 10 and tapered air dispersing hood 6, air dispersing hood 6 comprises at least three guide plates 16 that cross section is triangular in shape, the lower end of at least three guide plate 16 is separately fixed at the upper end of cylindrical base 10, the upper end of at least three guide plate 16 is compiled and is fixed together, 16 on guide plate forms runner 17, be furnished with air dispelling hole 7 in the top punishment of the triangle of each guide plate 16, the upper fixed of air dispelling hole 7 has flashing board 14, and the diameter of base 10 is less than the diameter of air dispersing hood 6 bottoms.The sulfur elimination that the setting of guide plate 16 and runner 17 can be conducive to have neither part nor lot in reaction falls in the opening mixed processing jar 2 along runner 17; The setting of flashing board 14 can prevent that sulfur elimination from falling in the air dispersing hood 6, prevents from polluting crude oil; The diameter of base 10 can prevent effectively that less than the setting of the diameter of gas dress cover 6 bottoms of loosing the sulfur elimination that drops on air dispersing hood 6 outsides from flowing into base 10 inside.
As shown in Figure 1, 2, there is the groove that is circular the lower end of air dispersing hood 6, and there is the projection corresponding with groove the upper end of base 10, and projection is fixedly mounted in the groove.
Shown in accompanying drawing 2,3, the diameter of air dispelling hole 7 is between one centimetre to two centimetres.
As shown in Figure 3, flashing board 14 is umbrella.The setting of the flashing board 14 of umbrella can prevent effectively further that sulfur elimination from falling in the device of air 6 that looses and guide sulfur elimination to fall in the runner 17 effectively.
As shown in Figure 1, sulfur elimination jar 1 top has sulfur elimination to add entrance 11, the bottom of sulfur elimination jar 1 is fixedly connected with blowdown pipeline and valve 13 and communicates, and sulfur elimination jar 1 is fixedly connected with recovery line 8 with the bottom of opening mixed processing jar 2 and communicates, and fixedly there is flange 15 in the outside, gas feed 5 places.The setting of recovery line 8 can be reclaimed not with the stink damp precursor reactant and be fallen into sulfur elimination in the opening mixed processing jar 2.
As shown in Figure 1, sulfur elimination jar 1 is installed with liquid level display tube 12.The setting of liquid level display tube 12 can situation facilitates in the sulfur elimination jar 1 for the staff observes.
Above technical characterictic has constituted most preferred embodiment of the present utility model, and it has stronger adaptability and best implementation result, can increase and decrease non-essential technical characterictic according to actual needs, satisfies the demand of different situations.
The use of the utility model most preferred embodiment: at first, opening mixed processing jar 2 is fixedly installed togather by flange 15 and oil storage tank, the staff is transported to sulfur elimination on the opening mixed processing jar 2 from sulfur elimination jar 1 by sulfur elimination pipeline 4 by pump 9, and by spray head 3 sulfur elimination is sprayed on the air dispersing hood 6, simultaneously, hydrogen sulfide gas in the petroleum tank enters in the air dispersing hood 6 and from air dispelling hole 7 from gas feed 5 and overflows, and the hydrogen sulfide gas and the sulfur elimination that continue to overflow react.
Claims (10)
1. the continuous circulating sprayer of crude oil storage tank removal of hydrogen sulfide is characterized in that comprising sulfur elimination jar, opening mixed processing jar and spray head; The bottom of sulfur elimination jar is installed with the sulfur elimination pipeline, the outlet of sulfur elimination pipeline is positioned at the top of opening mixed processing jar, the outlet of sulfur elimination pipeline is installed with spray head, be installed with pump on the sulfur elimination pipeline, there is gas feed the bottom of opening mixed processing jar, bottom in the opening mixed processing jar corresponding with gas feed fixedly has and spray head corresponding diffusing device of air up and down, on the diffusing device of air air dispelling hole is arranged, the top in the opening mixed processing jar is installed with the hydrogen sulfide gas checkout gear.
2. the continuous circulating sprayer of crude oil storage tank removal of hydrogen sulfide according to claim 1, the device of air that it is characterized in that loosing comprises cylindrical base and tapered air dispersing hood, air dispersing hood comprises at least three guide plates that cross section is triangular in shape, the lower end of at least three guide plate is separately fixed at the upper end of cylindrical base, the upper end of at least three guide plate is compiled and is fixed together, form runner between guide plate, be furnished with air dispelling hole in the top punishment of the triangle of each guide plate, the upper fixed of air dispelling hole has flashing board, and the diameter of base is less than the diameter of air dispersing hood bottom.
3. the continuous circulating sprayer of crude oil storage tank removal of hydrogen sulfide according to claim 2 is characterized in that there is the groove that is circular the lower end of air dispersing hood, and there is the projection corresponding with groove the upper end of base, and projection is fixedly mounted in the groove.
4. according to claim 1 or the continuous circulating sprayer of 2 or 3 described crude oil storage tank removal of hydrogen sulfide, the diameter that it is characterized in that air dispelling hole is between one centimetre to two centimetres.
5. according to claim 2 or the continuous circulating sprayer of 3 described crude oil storage tank removal of hydrogen sulfide, it is characterized in that flashing board is umbrella.
6. the continuous circulating sprayer of crude oil storage tank removal of hydrogen sulfide according to claim 4 is characterized in that flashing board is umbrella.
7. according to claim 1 or the continuous circulating sprayer of 2 or 3 described crude oil storage tank removal of hydrogen sulfide, it is characterized in that sulfur elimination jar top has sulfur elimination to add entrance, the bottom of sulfur elimination jar is fixedly connected with blowdown pipeline and valve and communicates, the sulfur elimination jar is fixedly connected with recovery line with the bottom of opening mixed processing jar and communicates, and fixedly there is flange in the gas feed place outside.
8. the continuous circulating sprayer of crude oil storage tank removal of hydrogen sulfide according to claim 4, it is characterized in that sulfur elimination jar top has sulfur elimination to add entrance, the bottom of sulfur elimination jar is fixedly connected with blowdown pipeline and valve and communicates, the sulfur elimination jar is fixedly connected with recovery line with the bottom of opening mixed processing jar and communicates, and fixedly there is flange in the gas feed place outside.
9. the continuous circulating sprayer of crude oil storage tank removal of hydrogen sulfide according to claim 6, it is characterized in that sulfur elimination jar top has sulfur elimination to add entrance, the bottom of sulfur elimination jar is fixedly connected with blowdown pipeline and valve and communicates, the sulfur elimination jar is fixedly connected with recovery line with the bottom of opening mixed processing jar and communicates, and fixedly there is flange in the gas feed place outside.
10. the continuous circulating sprayer of crude oil storage tank removal of hydrogen sulfide according to claim 9 is characterized in that the sulfur elimination jar is installed with the liquid level display tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320101871 CN203061053U (en) | 2013-03-06 | 2013-03-06 | Continuous circulating spraying device for removing hydrogen sulfide from crude oil storage tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320101871 CN203061053U (en) | 2013-03-06 | 2013-03-06 | Continuous circulating spraying device for removing hydrogen sulfide from crude oil storage tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203061053U true CN203061053U (en) | 2013-07-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320101871 Expired - Fee Related CN203061053U (en) | 2013-03-06 | 2013-03-06 | Continuous circulating spraying device for removing hydrogen sulfide from crude oil storage tank |
Country Status (1)
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| CN (1) | CN203061053U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105617822A (en) * | 2014-10-28 | 2016-06-01 | 中国石油天然气股份有限公司 | Elimination apparatus of hydrogen sulfide in crude oil storage tank, and elimination method thereof |
| CN109499287A (en) * | 2018-11-23 | 2019-03-22 | 北京润泰环保科技有限公司 | A kind of wet scrubber tower and medical wastes incineration acid gas processing method |
| CN116459634A (en) * | 2023-05-10 | 2023-07-21 | 江苏民生重工有限公司 | Hydrogen sulfide removing device |
-
2013
- 2013-03-06 CN CN 201320101871 patent/CN203061053U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105617822A (en) * | 2014-10-28 | 2016-06-01 | 中国石油天然气股份有限公司 | Elimination apparatus of hydrogen sulfide in crude oil storage tank, and elimination method thereof |
| CN109499287A (en) * | 2018-11-23 | 2019-03-22 | 北京润泰环保科技有限公司 | A kind of wet scrubber tower and medical wastes incineration acid gas processing method |
| CN116459634A (en) * | 2023-05-10 | 2023-07-21 | 江苏民生重工有限公司 | Hydrogen sulfide removing device |
| CN116459634B (en) * | 2023-05-10 | 2023-11-07 | 江苏民生重工有限公司 | Hydrogen sulfide removing device |
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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: 20130717 Termination date: 20160306 |