CN214513723U - Buffer tank with dust removal effect for octane bis (fluoroborate) production - Google Patents
Buffer tank with dust removal effect for octane bis (fluoroborate) production Download PDFInfo
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- CN214513723U CN214513723U CN202022459223.8U CN202022459223U CN214513723U CN 214513723 U CN214513723 U CN 214513723U CN 202022459223 U CN202022459223 U CN 202022459223U CN 214513723 U CN214513723 U CN 214513723U
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- air duct
- chamber
- tank body
- welded
- partition plate
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- 230000000694 effects Effects 0.000 title claims abstract description 33
- 239000000428 dust Substances 0.000 title claims abstract description 31
- -1 octane bis (fluoroborate) Chemical compound 0.000 title claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 title abstract description 20
- 238000005192 partition Methods 0.000 claims abstract description 43
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- 238000000034 method Methods 0.000 claims description 3
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 238000012423 maintenance Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 11
- 239000012535 impurity Substances 0.000 description 7
- 238000005457 optimization Methods 0.000 description 3
- MJHHIPFNTVWXDN-UHFFFAOYSA-N B(O)(F)F.CCCCCCCC Chemical compound B(O)(F)F.CCCCCCCC MJHHIPFNTVWXDN-UHFFFAOYSA-N 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000007086 side reaction Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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Abstract
The utility model provides a buffer tank is used in production of octane difluoride borate with dust removal effect, include: a tank body, an exhaust pipe and a diaphragm plate; the tank body is in a hollow cylindrical shape, and an exhaust pipe is welded in the middle of the top end of the tank body; two transverse partition plates which are symmetrical up and down are welded at the middle part inside the tank body, a vertical partition plate is welded between the two transverse partition plates, and the vertical partition plate is welded and fixed with the tank body; an upper chamber, a middle chamber and a lower chamber are arranged in the tank body through a transverse partition plate, the upper chamber and the lower chamber are two reaction chambers, and the middle chamber is provided with a left buffer chamber and a right buffer chamber through a vertical partition plate; the utility model has the advantages of rational in infrastructure, it is better to derive the effect, and production efficiency and plant maintenance efficiency are higher, thereby effectual solution the utility model provides a problem and not enough.
Description
Technical Field
The utility model relates to an octane difluoride borate production technical field, more specifically say, especially relate to an octane difluoride borate production buffer tank with dust removal effect.
Background
A buffer tank is needed in the production process of the octane bis-fluoroborate, and a dust removal filter is generally arranged at an air inlet of the buffer tank and used for purifying hydrogen fluoride gas entering the buffer tank.
When the existing buffer tank for producing octane bis (fluoroborate) is used, the diversion effect of the interior of the buffer tank on gas after reaction is poor, and the production efficiency is reduced; in the process of maintaining inside the buffer tank, impurities settled in the tank are inconvenient to be led out, the equipment maintenance efficiency is low, and an improved space exists.
In view of the above, the present invention provides a buffer tank for producing octane bis fluoroborate with a dust removal effect, which aims to solve the problems and improve the practical value by the technology.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an octane difluoride borate production buffer tank with dust removal effect to solve the problem that proposes in the above-mentioned background art and not enough.
In order to achieve the above object, the utility model provides a buffer tank is used in production of octane difluoride borate with dust removal effect is reached by following specific technological means:
a buffer tank with dust removal effect for producing octane bis (fluoroborate) comprises: the device comprises a tank body, an exhaust pipe, a transverse partition plate, a vertical partition plate, a reaction chamber, a buffer chamber, a discharge pipe, a first air duct, a first shunt pipe, an air inlet pipe, a dust removal filter, a second air duct, a second shunt pipe and a third air duct; the tank body is in a hollow cylindrical shape, and an exhaust pipe is welded in the middle of the top end of the tank body; two transverse partition plates which are symmetrical up and down are welded at the middle part inside the tank body, a vertical partition plate is welded between the two transverse partition plates, and the vertical partition plate is welded and fixed with the tank body; an upper chamber, a middle chamber and a lower chamber are arranged in the tank body through a transverse partition plate, the upper chamber and the lower chamber are two reaction chambers, and the middle chamber is provided with a left buffer chamber and a right buffer chamber through a vertical partition plate; the bottom of the right side of the reaction chamber, the bottom of the left side buffer chamber and the left side of the bottom of the rear side of the right side buffer chamber are respectively provided with a discharge pipe, and the discharge pipes are welded on the side part of the tank body; a first air duct is arranged in the reaction chamber and is in an inverted U shape; the left end of the bottom of the first air duct is welded with a circular first shunt pipe, and the first shunt pipe is horizontally suspended above the transverse partition plate at the upper side; the right end of the bottom of the first air duct is embedded on the transverse partition plate at the upper side, and the surface of the side part of the right end of the bottom of the first air duct is tangent to the right end face of the vertical partition plate; the first air duct is welded and fixed with the upper side diaphragm plate and is communicated with the inside of the right buffer chamber; an air inlet pipe is horizontally arranged at the top of the left side buffer chamber in a penetrating manner, and the air inlet pipe is welded and fixed with the side part of the tank body; the left end of the air inlet pipe is connected with a dust removal filter through a flange, and the dust removal filter is arranged outside the left buffer chamber; the left buffer chamber is communicated with the lower side reaction chamber through a second air duct; the second air duct vertically penetrates through the lower lateral clapboard, and the second air duct is welded and fixed with the lower lateral clapboard; the top end of the second air duct is in a horn mouth shape, and a circular second shunt tube is welded at the bottom end of the second air duct; the second shunt pipe is horizontally suspended above the bottom end in the tank body; the right buffer chamber is communicated with the lower side reaction chamber through a third air duct; the third air duct vertically wears to establish on the downside cross slab, and the lateral part surface of third air duct is tangent with the lateral part surface of jar internal portion to second air duct and downside cross slab welded fastening.
As the further optimization of this technical scheme, the utility model relates to a buffer tank is used in production of octane difluoride borate with dust removal effect the top of the jar body is the toper form, and the bottom of the jar body is the slope form of high left low right.
As a further optimization of this technical scheme, the utility model relates to a buffer tank is used in production of octane difluoride borate with dust removal effect the slope form of upside cross slab for the height from left to right low, and the bottom face of the right-hand member of upside cross slab and first air duct bottom aligns.
As a further optimization of this technical scheme, the utility model relates to a buffer tank is used in production of octane difluoride borate with dust removal effect the downside cross slab establishes to the high slope form in the low right side in a left side, and the bottom face of downside cross slab and third air duct aligns.
Because of above-mentioned technical scheme's application, compared with the prior art, the utility model have the following advantage:
1. the utility model discloses a top that sets up the jar body is the toper form, and the upside cross slab establishes to the slope form of high left and low right side to the downside cross slab establishes to the slope form of low right side height in a left side, makes the better entering right side surge chamber of gas ability in the downside reaction chamber, follows the better entering reaction chamber of right side surge chamber again, from the better exhaust of gas vent at last, and gaseous water conservancy diversion effect is better, has improved production efficiency.
2. The utility model discloses a set up the slope form that the upside cross slab established to the height in the left side low in the right side, and the downside cross slab establishes to the height in the left side high in the right side high slope form to the bottom of the jar body is the slope form of the height in the left side low in the right side, is convenient for with the better derivation jar body of the impurity on jar internal portion bottom and the cross slab, improves the maintenance efficiency of jar internal portion.
3. The utility model discloses an improvement to a buffer tank is used in production of octane difluoride borate with dust removal effect has rational in infrastructure, derives the effect better, and production efficiency and the higher advantage of machine maintenance efficiency to effectual solution the utility model discloses the problem that proposes in background art one with not enough.
Drawings
The accompanying drawings, which are incorporated in and constitute a part of this application, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification. In the drawings:
fig. 1 is a schematic structural view of the present invention;
fig. 2 is a schematic view of a partial structure of the present invention.
In the figure: the device comprises a tank body 1, an exhaust pipe 2, a transverse partition plate 3, a vertical partition plate 4, a reaction chamber 5, a buffer chamber 6, a discharge pipe 7, a first air duct 8, a first shunt pipe 9, an air inlet pipe 10, a dust removal filter 11, a second air duct 12, a second shunt pipe 13 and a third air duct 14.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments.
It is to be noted that, in the description of the present invention, "a plurality" means two or more unless otherwise specified; the terms "upper", "lower", "left", "right", "inner", "outer", "front", "rear", "head", "tail", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are merely for convenience of description and simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention.
Furthermore, the terms "first," "second," "third," and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
Meanwhile, in the description of the present invention, unless otherwise explicitly specified or limited, the terms "connected" and "connected" should be interpreted broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; the connection can be mechanical connection or electrical connection; may be directly connected or indirectly connected through an intermediate. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
Referring to fig. 1 to 2, the present invention provides a specific technical implementation of a buffer tank for producing octane bis (fluoroborate) with dust removal effect:
a buffer tank with dust removal effect for producing octane bis (fluoroborate) comprises: the device comprises a tank body 1, an exhaust pipe 2, a transverse partition plate 3, a vertical partition plate 4, a reaction chamber 5, a buffer chamber 6, a discharge pipe 7, a first air duct 8, a first shunt pipe 9, an air inlet pipe 10, a dust removal filter 11, a second air duct 12, a second shunt pipe 13 and a third air duct 14; the tank body 1 is in a hollow cylindrical shape, and an exhaust pipe 2 is welded in the middle of the top end of the tank body 1; two transverse clapboards 3 which are symmetrical up and down are welded at the middle part inside the tank body 1, a vertical clapboard 4 is welded between the two transverse clapboards 3, and the vertical clapboard 4 is welded and fixed with the tank body 1; an upper chamber, a middle chamber and a lower chamber are arranged in the tank body 1 at intervals through a transverse partition plate 3, the upper chamber and the lower chamber are arranged into two reaction chambers 5, and the middle chamber is provided with a left buffer chamber and a right buffer chamber 6 at intervals through a vertical partition plate 4; the bottom of the right side of the reaction chamber 5, the bottom of the left side buffer chamber 6 and the left side of the bottom of the rear side of the right side buffer chamber 6 are all provided with a discharge pipe 7, and the discharge pipe 7 is welded on the side part of the tank body 1; a first air duct 8 is arranged in the reaction chamber 5, and the first air duct 8 is in an inverted U shape; the left end of the bottom of the first air duct 8 is welded with a circular first shunt tube 9, and the first shunt tube 9 is horizontally suspended above the upper transverse clapboard 3; the right end of the bottom of the first air duct 8 is embedded on the transverse partition plate 3 at the upper side, and the surface of the side part of the right end of the bottom of the first air duct 8 is tangent to the right end surface of the vertical partition plate 4; the first air duct 8 is welded and fixed with the upper side diaphragm plate 3, and the first air duct 8 is communicated with the inside of the right side buffer chamber 6; an air inlet pipe 10 horizontally penetrates through the top of the left side of the left buffer chamber 6, and the air inlet pipe 10 is welded and fixed with the side part of the tank body 1; the left end of the air inlet pipe 10 is connected with a dust removal filter 11 through a flange, and the dust removal filter 11 is arranged outside the left buffer chamber 6; the left buffer chamber 6 is communicated with the lower reaction chamber 5 through a second air duct 12; the second gas-guide tube 12 vertically penetrates through the lower transverse clapboard 3, and the second gas-guide tube 12 is welded and fixed with the lower transverse clapboard 3; the top end of the second air duct 12 is in a bell mouth shape, and a second circular shunt pipe 13 is welded on the bottom end of the second air duct 12; the second shunt pipe 13 is horizontally suspended above the bottom end in the tank body 1; the right buffer chamber 6 is communicated with the lower reaction chamber 5 through a third air duct 14; the third air duct 14 vertically penetrates through the lower lateral diaphragm plate 3, the lateral surface of the third air duct 14 is tangent to the lateral surface inside the tank body 1, and the second air duct 12 is welded and fixed with the lower lateral diaphragm plate 3.
Specifically, referring to fig. 1, the top end of the tank 1 is tapered to improve the effect of the gas flowing to the bottom end of the exhaust port 2, and the bottom end of the tank 1 is inclined in a horizontal direction to improve the effect of guiding out the impurities in the tank 1.
Specifically, please refer to fig. 2, the upper transverse partition plate 3 is set to be inclined with a high left and a low right, and the upper transverse partition plate 3 is aligned with the bottom end face of the right end of the bottom of the first air duct 8, so as to improve the effect of the gas flowing to the right end of the bottom of the first air duct 8, and improve the effect of the impurities on the upper transverse partition plate 3 flowing to the discharge pipe 7, so as to facilitate the discharge.
Specifically, referring to fig. 2, the lower diaphragm plate 3 is designed to be inclined with a lower left and a higher right, and the lower diaphragm plate 3 is aligned with the bottom end surface of the third gas-guide tube 14, so as to improve the effect of gas flowing to the bottom end of the third gas-guide tube 14, and improve the effect of impurities on the lower diaphragm plate 3 flowing to the discharge tube 7, thereby facilitating the discharge.
The method comprises the following specific implementation steps:
the top of jar body 1 is the toper form, and upside cross slab 3 is the slope form of height from the left to the right, and downside cross slab 3 is the slope form of height from the left to the right for the gas in the downside reacting chamber 5 can be better gets into right side buffer chamber 6, from the better entering reacting chamber 5 of right side buffer chamber 6 again, from the better exhaust of gas vent 2 at last, and gaseous water conservancy diversion effect is better, has improved production efficiency.
Upside cross slab 3 is the slope form of the height in the left right side low, and downside cross slab 3 is the slope form of the height in the left side low right side high, and the bottom of jar body 1 is the slope form of the height in the left side low in the right side, is convenient for with jar body 1 of leading out that impurity on 1 inside bottom of jar and the cross slab 3 is better, improves the maintenance efficiency of 1 inside of jar body.
In summary, the following steps: according to the buffer tank with the dust removal effect for producing the octane bis (fluoroborate), the top end of the tank body is in a conical shape, the transverse partition plate on the upper side is in an inclined shape with the height from left to right and the transverse partition plate on the lower side is in an inclined shape with the height from left to right, so that gas in the reaction chamber on the lower side can better enter the buffer chamber on the right side, then better enters the reaction chamber from the buffer chamber on the right side, and finally better exhausts from the exhaust port, the gas flow guide effect is better, and the production efficiency is improved; the upper transverse partition plate is arranged to be in an inclined shape with the left higher and the right lower, the lower transverse partition plate is arranged to be in an inclined shape with the left lower and the right higher, and the bottom end of the tank body is in an inclined shape with the left higher and the right lower, so that impurities at the bottom end in the tank body and on the transverse partition plate can be guided out of the tank body better, and the maintenance efficiency of the interior of the tank body is improved; the utility model discloses an improvement to a buffer tank is used in production of octane difluoride borate with dust removal effect has rational in infrastructure, derives the effect better, and production efficiency and higher advantage of machine maintenance efficiency to effectual solution the utility model provides a problem and not enough.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (4)
1. A buffer tank with dust removal effect for producing octane bis (fluoroborate) comprises: the device comprises a tank body (1), an exhaust pipe (2), a transverse partition plate (3), a vertical partition plate (4), a reaction chamber (5), a buffer chamber (6), a discharge pipe (7), a first air duct (8), a first shunt pipe (9), an air inlet pipe (10), a dust removal filter (11), a second air duct (12), a second shunt pipe (13) and a third air duct (14); the method is characterized in that: the tank body (1) is in a hollow cylindrical shape, and an exhaust pipe (2) is welded in the middle of the top end of the tank body (1); two transverse partition plates (3) which are symmetrical up and down are welded at the middle part inside the tank body (1), a vertical partition plate (4) is welded between the two transverse partition plates (3), and the vertical partition plate (4) is welded and fixed with the tank body (1); an upper chamber, a middle chamber and a lower chamber are arranged in the tank body (1) at intervals through a transverse partition plate (3), the upper chamber and the lower chamber are two reaction chambers (5), and the middle chamber is provided with a left buffer chamber and a right buffer chamber (6) at intervals through a vertical partition plate (4); a discharge pipe (7) is arranged at the bottom of the right side of the reaction chamber (5), at the bottom of the left side buffer chamber (6) and at the left side of the bottom of the rear side of the right side buffer chamber (6), and the discharge pipe (7) is welded on the side part of the tank body (1); a first air duct (8) is arranged in the reaction chamber (5), and the first air duct (8) is in an inverted U shape; the left end of the bottom of the first air duct (8) is welded with a circular first shunt pipe (9), and the first shunt pipe (9) is horizontally suspended above the upper transverse clapboard (3); the right end of the bottom of the first air duct (8) is embedded on the transverse partition plate (3) at the upper side, and the surface of the side part of the right end of the bottom of the first air duct (8) is tangent to the right end face of the vertical partition plate (4); the first air duct (8) is welded and fixed with the upper side diaphragm plate (3), and the first air duct (8) is communicated with the inside of the right side buffer chamber (6); an air inlet pipe (10) is horizontally arranged at the top of the left side buffer chamber (6) in a penetrating manner, and the air inlet pipe (10) is welded and fixed with the side part of the tank body (1); the left end of the air inlet pipe (10) is connected with a dust removal filter (11) through a flange, and the dust removal filter (11) is arranged outside the left buffer chamber (6); the left buffer chamber (6) is communicated with the lower reaction chamber (5) through a second air duct (12); the second air duct (12) vertically penetrates through the lower transverse clapboard (3), and the second air duct (12) is welded and fixed with the lower transverse clapboard (3); the top end of the second air duct (12) is in a bell mouth shape, and a circular second shunt pipe (13) is welded at the bottom end of the second air duct (12); the second shunt pipe (13) is horizontally suspended above the bottom end in the tank body (1); the right buffer chamber (6) is communicated with the lower reaction chamber (5) through a third air duct (14); the third air duct (14) vertically penetrates through the lower side diaphragm plate (3), the side surface of the third air duct (14) is tangent to the side surface inside the tank body (1), and the second air duct (12) is welded and fixed with the lower side diaphragm plate (3).
2. The buffer tank with dust removal effect for producing octane bis (fluoroborate) according to claim 1, wherein: the top of the tank body (1) is in a conical shape, and the bottom of the tank body (1) is in an inclined shape with a high left and a low right.
3. The buffer tank with dust removal effect for producing octane bis (fluoroborate) according to claim 1, wherein: the upper side diaphragm plate (3) is designed to be inclined in a left-high and right-low manner, and the lower end face of the right end of the upper side diaphragm plate (3) is aligned with the bottom end face of the first air duct (8).
4. The buffer tank with dust removal effect for producing octane bis (fluoroborate) according to claim 1, wherein: the lower side diaphragm plate (3) is designed to be an inclined shape with a lower left and a higher right, and the lower side diaphragm plate (3) is aligned with the bottom end surface of the third air duct (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022459223.8U CN214513723U (en) | 2020-10-30 | 2020-10-30 | Buffer tank with dust removal effect for octane bis (fluoroborate) production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022459223.8U CN214513723U (en) | 2020-10-30 | 2020-10-30 | Buffer tank with dust removal effect for octane bis (fluoroborate) production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214513723U true CN214513723U (en) | 2021-10-29 |
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ID=78229871
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022459223.8U Expired - Fee Related CN214513723U (en) | 2020-10-30 | 2020-10-30 | Buffer tank with dust removal effect for octane bis (fluoroborate) production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214513723U (en) |
-
2020
- 2020-10-30 CN CN202022459223.8U patent/CN214513723U/en not_active Expired - Fee Related
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| 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: 20211029 |