CN220745798U - Reformate dechlorination tank with layered sampling function for clean production - Google Patents
Reformate dechlorination tank with layered sampling function for clean production Download PDFInfo
- Publication number
- CN220745798U CN220745798U CN202322425895.0U CN202322425895U CN220745798U CN 220745798 U CN220745798 U CN 220745798U CN 202322425895 U CN202322425895 U CN 202322425895U CN 220745798 U CN220745798 U CN 220745798U
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- China
- Prior art keywords
- tank
- hydrogenation
- dechlorination
- hydrogen
- storage tank
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- 238000006298 dechlorination reaction Methods 0.000 title claims abstract description 35
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 16
- 238000005070 sampling Methods 0.000 title claims abstract description 16
- 238000005984 hydrogenation reaction Methods 0.000 claims abstract description 50
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 239000001257 hydrogen Substances 0.000 claims abstract description 48
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 48
- 238000003756 stirring Methods 0.000 claims abstract description 16
- 238000000034 method Methods 0.000 claims abstract description 7
- 238000009434 installation Methods 0.000 claims abstract description 6
- 230000000712 assembly Effects 0.000 claims abstract description 3
- 238000000429 assembly Methods 0.000 claims abstract description 3
- 239000007789 gas Substances 0.000 claims description 7
- 239000007921 spray Substances 0.000 claims description 5
- 239000003208 petroleum Substances 0.000 abstract description 23
- 239000003921 oil Substances 0.000 description 25
- 238000010586 diagram Methods 0.000 description 9
- 150000001805 chlorine compounds Chemical class 0.000 description 4
- 239000002585 base Substances 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 2
- 239000003502 gasoline Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910001504 inorganic chloride Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- Devices For Use In Laboratory Experiments (AREA)
Abstract
The utility model discloses a reformate dechlorination tank with a layered sampling function for clean production, which belongs to the technical field of dechlorination tanks, and comprises a dechlorination tank, wherein the dechlorination tank comprises a storage tank assembly and a hydrogenation device, the hydrogenation device is assembled between the storage tank assemblies, the hydrogenation device comprises a hydrogenation mechanism and a hydrogenation head, an air inlet is opened to add hydrogen into the hydrogen tank when the hydrogenation device is used, petroleum is added into the oil tank through a connecting port, at the moment, an air pump is started, the hydrogen in the hydrogen tank is sucked into the collecting tray through a first connecting pipe and blown into the collecting tray through a second connecting pipe, the hydrogen is dispersed into each stirring pipe through the collecting tray and sprayed out from the hydrogenation head, all openings and installation directions of the connecting ports are consistent when sprayed out, the collecting tray is driven to rotate when sprayed out, the stirring pipe is used for stirring the petroleum in the oil tank, the hydrogen and the petroleum in the oil tank can be fully mixed, and the dechlorination process is increased.
Description
Technical Field
The utility model belongs to the technical field of dechlorination tanks, and particularly relates to a reformate dechlorination tank with a layered sampling function for clean production.
Background
Petroleum refers to a mixture of gaseous, liquid and solid hydrocarbons, which has a natural shape, is a viscous and dark brown liquid, is called as "industrial blood", has properties different from place to place, has a wide viscosity range and a large difference in solidifying point, has a boiling point range of normal temperature to more than five hundred degrees celsius, is soluble in various organic solvents, is insoluble in water, but forms an emulsion with water, although the components and appearance of petroleum in different oil fields can be greatly distinguished, petroleum is mainly used as fuel oil and gasoline, fuel oil and gasoline are one of the most important secondary energy sources, and some chlorides are doped in untreated petroleum, and the chlorides in petroleum are generally considered as two types, namely organic chlorides existing as chlorinated hydrocarbon and inorganic chlorides formed with alkali metals or alkaline earth metals, and the chlorides existing in the two forms can cause some harm to people and equipment in the petroleum processing process, so that hydrogen and petroleum need to be fully contacted for better chlorine removal during hydrodechlorination.
The existing dechlorination tank cannot be fully mixed with the petroleum in the dechlorination tank during hydrogenation, so that the internal dechlorination process becomes long, and the working efficiency becomes low.
Disclosure of Invention
Aiming at the problems that the existing dechlorination tank cannot be fully mixed with the petroleum in the interior during hydrogenation, which leads to the lengthening of the internal dechlorination process and the low working efficiency, the utility model provides the reformate dechlorination tank with the layered sampling function for clean production.
In order to solve the problems, the utility model adopts the following technical scheme.
The clean production is with reformate dechlorination jar that has layering sampling function, including the dechlorination jar, the dechlorination jar include holding vessel assembly and hydrogenation unit, hydrogenation unit assemble between the holding vessel assembly, hydrogenation unit include hydrogenation mechanism and hydrogenation head, hydrogenation mechanism on be equipped with a plurality of hydrogenation heads.
Preferably, the hydrogenation mechanism include the air pump, one end of air pump be equipped with first connecting pipe, the other side is equipped with the second connecting pipe, and the bottom of air pump is equipped with adjustable high base, one side upper end rotation of second connecting pipe is equipped with the collection dish, the inside cavity of collection dish and the upper and lower both ends of collection dish are equipped with a plurality of churns on being close to the position of outer wall, every churns all with collect the dish intercommunication, can disperse every churns inside through the churns with the hydrogen that the air pump carried.
Preferably, the hydrogenation head include the shower nozzle, the front of shower nozzle be provided with the shrinkage pool, be provided with symmetrical spout on the inner wall of shrinkage pool, the inside sliding connection of spout has the slider, the one end that the slider stretched out the spout is equipped with the connecting rod, the terminal of both sides connecting rod is equipped with the inserted block, the one end of inserted block is equipped with the blanking disc, and is equipped with the spring between slider and the spout, can make the inserted block insert the shrinkage pool inside sealed through the spring.
Preferably, the storage tank assembly comprises an oil storage tank, a connecting port is arranged at the upper end of the oil storage tank, a hydrogen tank is arranged on one side of the oil storage tank, an air filling port is arranged at the upper end of the hydrogen tank, a plurality of supporting legs are arranged at the bottoms of the oil storage tank and the air filling port, through holes are formed in the centers of the bottoms of the oil storage tank and the hydrogen tank, and the through holes through the bottoms of the oil storage tank and the hydrogen tank are used for connecting a hydrogenation device.
Preferably, the spray head is connected with the stirring pipe, the first connecting pipe is connected with the bottom through hole of the hydrogen tank, the second connecting pipe is connected with the bottom through hole of the oil storage tank, and the opening directions of all concave holes are consistent with the installation direction.
Advantageous effects
Compared with the prior art, the utility model has the beneficial effects that:
(1) According to the utility model, when the device is used, the gas adding port is opened to add hydrogen into the hydrogen tank, petroleum is added into the oil storage tank through the connecting port, the air pump is started at the moment, the hydrogen in the hydrogen tank is sucked through the first connecting pipe and blown to the collecting disc through the second connecting pipe, the hydrogen is dispersed into each stirring pipe through the collecting disc and sprayed out from the hydrogenation head, all openings and installation directions of the connecting port are consistent when the hydrogen is sprayed out, the collecting disc is driven to rotate when the hydrogen is sprayed out, the stirring pipe is used for stirring the petroleum in the oil storage tank, the hydrogen and the petroleum in the oil storage tank can be fully mixed, and the dechlorination process is increased.
(2) According to the utility model, the plug block can be inserted into the connection port through the spring when hydrogen is not added, the plug disc is blocked outside the concave hole, petroleum can be prevented from entering the concave hole, the plug disc and the plug block are pushed to move outwards through gas when hydrogen is sprayed out, the sliding block slides in the sliding groove and compresses the spring, and the plug block is reset through the spring when hydrogen is not added, so that petroleum can be prevented from leaking.
Drawings
FIG. 1 is a schematic diagram of a reformate dechlorination tank with layered sampling function for clean production in the utility model;
FIG. 2 is a schematic diagram of a storage tank assembly according to the present utility model;
FIG. 3 is a schematic view of the structure of the hydrogenation apparatus of the present utility model;
FIG. 4 is a schematic diagram of a hydrogen adding mechanism according to the present utility model;
FIG. 5 is a schematic view of the structure of the hydrogenation head according to the present utility model.
The correspondence between the reference numerals and the component names in the drawings is as follows:
1. a dechlorination tank;
2. a storage tank assembly; 21. an oil storage tank; 22. a connection port; 23. support legs; 24. a hydrogen tank;
25. an air inlet;
3. a hydrogenation unit; 31. a hydrogenation mechanism; 311. an air pump; 312. a first connection pipe; 313. a second connection pipe;
314. a collection tray; 315. a stirring tube; 32. a hydrogenation head; 321. a spray head; 322. concave holes; 323. a chute;
324. a blocking disc; 325. inserting blocks; 326. a connecting rod; 327. a slide block; 328. and (3) a spring.
Detailed Description
The utility model is further described in connection with the following specific utility model.
Example 1
Referring to fig. 1, a schematic diagram of a reformate dechlorination tank with layered sampling function for clean production according to a preferred embodiment of the present utility model is shown, where the reformate dechlorination tank with layered sampling function for clean production in this example includes a dechlorination tank 1, the dechlorination tank 1 includes a storage tank assembly 2 and a hydrogenation device 3, and the hydrogenation device 3 is assembled between the storage tank assemblies 2.
As shown in fig. 2, which is a schematic structural diagram of a storage tank assembly in the present utility model, the storage tank assembly 2 includes an oil storage tank 21, a connection port 22 is assembled at the upper end of the oil storage tank 21, a hydrogen tank 24 is disposed at one side of the oil storage tank 21, an air inlet 25 is assembled at the upper end of the hydrogen tank 24, a plurality of support legs 23 are assembled at the bottoms of the oil storage tank 21 and the air inlet 25, and a through hole is disposed at the bottom centers of the oil storage tank 21 and the hydrogen tank 24; the oil tank 21 and the hydrogen tank 24 can be supported by the support legs 23, and petroleum is charged through the connection port 22, and hydrogenation is performed through the gas charging port 25.
As shown in fig. 3, which is a schematic structural diagram of a hydrogenation device of the present utility model, the hydrogenation device 3 includes a hydrogenation mechanism 31 and a hydrogenation head 32, and the hydrogenation mechanism 31 is equipped with a plurality of hydrogenation heads 32; the hydrogenation mechanism 31 can be connected to the through holes in the bottoms of the oil tank 21 and the hydrogen tank 24, and the hydrogenation head 32 can hydrodechlorinate the inside of the oil tank 21.
As shown in fig. 4, which is a schematic structural diagram of a hydrogenation mechanism in the present utility model, the hydrogenation mechanism 31 includes an air pump 311, one end of the air pump 311 is equipped with a first connecting pipe 312, the other side is equipped with a second connecting pipe 313, the bottom of the air pump 311 is equipped with a base with adjustable height, the upper end of one side of the second connecting pipe 313 is rotatably equipped with a collecting tray 314, the interior of the collecting tray 314 is hollow, and a plurality of stirring pipes 315 are equipped at the positions of the upper end and the lower end of the collecting tray 314, which are close to the outer wall, and each stirring pipe 315 is communicated with the collecting tray 314; the height can be freely adjusted by the base at the bottom of the air pump 311 to match the oil tank 21 and the hydrogen tank 24.
As shown in fig. 5, which is a schematic diagram of the structure of the hydrogenation head in the present utility model, the hydrogenation head 32 includes a spray head 321, a concave hole 322 is provided on the front surface of the spray head 321, a symmetrical sliding groove 323 is provided on the inner wall of the concave hole 322, a sliding block 327 is slidably connected in the sliding groove 323, a connecting rod 326 is assembled at one end of the sliding block 327 extending out of the sliding groove 323, an insert 325 is assembled at the end of the connecting rod 326 at both sides, a plugging disc 324 is assembled at one end of the insert 325, and a spring 328 is assembled between the sliding block 327 and the sliding groove 323; the nozzle 321 is connected to the stirring tube 315, and hydrogen gas can be ejected through the concave hole 322.
The nozzle 321 is connected with the stirring pipe 315, the first connecting pipe 312 is connected with the bottom through hole of the hydrogen tank 24, the second connecting pipe 313 is connected with the bottom through hole of the oil tank 21, and the opening directions of all concave holes 322 are consistent with the installation direction.
Working principle: when the device is used, the gas adding port 25 is opened to add hydrogen into the hydrogen tank 24, petroleum is added into the oil storage tank 21 through the connecting port 22, the air pump 311 is started at the moment, the hydrogen in the hydrogen tank 24 is sucked through the first connecting pipe 312 and blown to the collecting disc 314 through the second connecting pipe 313, the hydrogen is dispersed into each stirring pipe 315 through the collecting disc 314 and is sprayed out from the hydrogenation head 32, all openings and installation directions of the connecting port 22 are consistent when the hydrogen is sprayed out, the collecting disc 314 is driven to rotate when the hydrogen is sprayed out, the stirring pipe 315 is used for stirring the petroleum in the oil storage tank 21, the hydrogen and the petroleum in the oil storage tank can be fully mixed, and the dechlorination process is increased.
Example 2
As shown in fig. 1 to 5, which are schematic diagrams of a reformate dechlorination tank with layered sampling function for clean production according to another preferred embodiment of the present utility model, the reformate dechlorination tank with layered sampling function for clean production of this example can enable the insert block 325 to be inserted into the inside of the connection port 22 when no hydrogen is added through the spring 328 on the basis of example 1, the plug disc 324 is blocked outside the concave hole 322, so that petroleum can be prevented from entering the inside of the concave hole 322, the plug disc 324 and the insert block 325 are pushed to move outwards through gas when hydrogen is sprayed, the slider 327 slides in the inside of the chute 323 and compresses the spring 328, and the slider 327 is reset through the spring 328 when no hydrogen is added, so that petroleum can be ensured not to leak.
The foregoing is a further elaboration of the present utility model in connection with the detailed description, and it is not intended that the utility model be limited to the specific embodiments shown, but rather that a number of simple deductions or substitutions be made by one of ordinary skill in the art without departing from the spirit of the utility model, should be considered as falling within the scope of the utility model as defined in the appended claims.
Claims (5)
1. The reformate dechlorination tank with the layered sampling function for clean production comprises a dechlorination tank (1), wherein the dechlorination tank (1) comprises a storage tank assembly (2) and a hydrogenation device (3), the hydrogenation device (3) is assembled between the storage tank assemblies (2),
the method is characterized in that:
the hydrogenation device (3) comprises a hydrogenation mechanism (31) and a hydrogenation head (32), wherein the hydrogenation mechanism (31) is provided with a plurality of hydrogenation heads (32).
2. The reformate dechlorination tank with layered sampling function for clean production of claim 1, characterized in that: the hydrogenation mechanism (31) include air pump (311), one end of air pump (311) be equipped with first connecting pipe (312), the other side is equipped with second connecting pipe (313), and the bottom of air pump (311) is equipped with the base that can increase, one side upper end rotation of second connecting pipe (313) is equipped with collection dish (314), collect and be equipped with a plurality of stirred tubes (315) on the position that the upper and lower both ends that dish (314) are close to the outer wall are just collected to the inside cavity of dish (314), every stirred tube (315) all with collect dish (314) intercommunication.
3. The reformate dechlorination tank with layered sampling function for clean production of claim 2, characterized in that: the hydrogenation head (32) include shower nozzle (321), the front of shower nozzle (321) be provided with shrinkage pool (322), be provided with symmetrical spout (323) on the inner wall of shrinkage pool (322), the inside sliding connection of spout (323) has slider (327), slider (327) stretches out the one end of spout (323) and is equipped with connecting rod (326), the end of both sides connecting rod (326) is equipped with inserted block (325), the one end of inserted block (325) is equipped with blanking plug (324), and is equipped with spring (328) between slider (327) and spout (323).
4. A reformate dechlorination tank with layered sampling function for clean production according to claim 3, characterized in that: the storage tank assembly (2) include oil storage tank (21), oil storage tank (21) upper end be equipped with connector (22), one side of oil storage tank (21) is provided with hydrogen tank (24), the upper end of hydrogen tank (24) is equipped with gas port (25), and the bottom of oil storage tank (21) and gas port (25) is equipped with a plurality of supporting legs (23), and the bottom center department of oil storage tank (21) and hydrogen tank (24) is provided with the through-hole.
5. The reformate dechlorination tank with layered sampling function for clean production of claim 4, characterized in that: the spray head (321) is connected with the stirring pipe (315), the first connecting pipe (312) is connected with a bottom through hole of the hydrogen tank (24), the second connecting pipe (313) is connected with a bottom through hole of the oil storage tank (21), and the opening directions of all concave holes (322) are consistent with the installation direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322425895.0U CN220745798U (en) | 2023-09-07 | 2023-09-07 | Reformate dechlorination tank with layered sampling function for clean production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322425895.0U CN220745798U (en) | 2023-09-07 | 2023-09-07 | Reformate dechlorination tank with layered sampling function for clean production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220745798U true CN220745798U (en) | 2024-04-09 |
Family
ID=90571232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322425895.0U Active CN220745798U (en) | 2023-09-07 | 2023-09-07 | Reformate dechlorination tank with layered sampling function for clean production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220745798U (en) |
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2023
- 2023-09-07 CN CN202322425895.0U patent/CN220745798U/en active Active
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