CN116421995A - Rectifying equipment is used in processing of ultrapure aqueous ammonia that discharge rate is high - Google Patents
Rectifying equipment is used in processing of ultrapure aqueous ammonia that discharge rate is high Download PDFInfo
- Publication number
- CN116421995A CN116421995A CN202310684217.8A CN202310684217A CN116421995A CN 116421995 A CN116421995 A CN 116421995A CN 202310684217 A CN202310684217 A CN 202310684217A CN 116421995 A CN116421995 A CN 116421995A
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- Prior art keywords
- wall
- fixedly connected
- rectifying
- barrel
- plate
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- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 title claims abstract description 23
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims description 20
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 22
- 230000000694 effects Effects 0.000 claims abstract description 13
- 238000001125 extrusion Methods 0.000 claims abstract description 5
- 238000001914 filtration Methods 0.000 claims description 14
- 239000012535 impurity Substances 0.000 claims description 14
- 241000883990 Flabellum Species 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 38
- 238000000034 method Methods 0.000 abstract description 35
- 239000000463 material Substances 0.000 abstract description 34
- 238000003756 stirring Methods 0.000 abstract description 26
- 239000013590 bulk material Substances 0.000 abstract description 12
- 238000002156 mixing Methods 0.000 abstract description 10
- 238000005406 washing Methods 0.000 abstract description 2
- 230000007423 decrease Effects 0.000 description 7
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 230000000630 rising effect Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 238000004821 distillation Methods 0.000 description 2
- 239000004065 semiconductor Substances 0.000 description 2
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 230000000873 masking effect Effects 0.000 description 1
- 238000004377 microelectronic Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/30—Fractionating columns with movable parts or in which centrifugal movement is caused
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/836—Mixing plants; Combinations of mixers combining mixing with other treatments
- B01F33/8361—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating
- B01F33/83611—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating by cutting
Abstract
The utility model discloses rectifying equipment for processing ultra-pure ammonia water with high discharge rate, and relates to the technical field of rectifying equipment. The utility model provides a high ultrapure ammonia water rectification apparatus for processing of discharge rate, water through lifter plate upper portion is risen by the extrusion, the in-process that rises accelerates the mixing of various materials in the aquatic, the follow-up rectification of being convenient for, lifter plate rises in-process and pumps the water in the filter equipment, make water rise to the rectifying vessel after the filter screen, the bulk material of water through the filter screen bottom in the flow in-process, the washing of rivers can accelerate the crushing of bulk material, the toper mouth is the toper setting, rivers are spouted from the toper mouth, the blowout of rivers can play the stirring effect to the rectifying vessel in.
Description
Technical Field
The utility model relates to the technical field of rectifying equipment, in particular to rectifying equipment for processing ultra-pure ammonia water with high discharge rate.
Background
Ultra-pure ammonia is the main material of microelectronic silicon nitride masking films, and in recent years, the global information industry has rapidly developed, and doping very small amounts of impurity elements into pure semiconductor products can cause the resistivity of the products to change greatly, so the semiconductor industry has high requirements on the purity of chemical materials.
The Chinese patent with publication number of CN218248580U discloses an ultrapure ammonia rectification device, and belongs to the field of ultrapure ammonia water processing treatment. It solves the problems of low distillation efficiency and low distillation discharge rate of the existing ultra-pure ammonia water. The utility model provides an ultrapure ammonia rectifying device, includes rectifying still casing, the lateral part of casing still is provided with the heating cabinet, the heating pipe is still installed to the casing inside, and the heating pipe is connected with the heating cabinet, air inlet and inlet have still been seted up respectively to the both sides of casing, stirring mechanism is still installed to the casing inside, the casing upper end still is provided with the blast pipe, one side of casing still is provided with and connects the case, connect still be provided with the support directly over the case, and the support links firmly the lateral part at the casing, the tip of blast pipe is located the support, and still installs condensation subassembly on the support.
In the process of rectifying the ultra-pure ammonia and other materials, because certain impurities exist in the materials, the rectification efficiency can be influenced in the rectification process, and the impurities exist in rectification equipment and are difficult to remove.
Disclosure of Invention
Aiming at the defects of the prior art, the utility model provides rectifying equipment for processing ultra-pure ammonia water with high discharge rate, so as to solve the problems in the prior art.
In order to achieve the above purpose, the utility model is realized by the following technical scheme:
the rectification equipment for processing the ultra-pure ammonia water with high discharge rate comprises a rectification barrel, wherein the bottom of the rectification barrel is fixedly connected with a rectification device, the outer wall of the rectification barrel is fixedly connected with a treatment device, and the rectification device is an existing device on the market and can achieve the rectification effect on materials;
the processing device comprises:
the lifting device is of a circular structure, is fixedly connected to the bottom of the rectifying barrel, has an extrusion effect, is provided with a feed inlet at a position, far away from the bottom of the filter screen, on the rectifying barrel, and can be used for adding ultrapure ammonia and other materials to be rectified into the rectifying barrel through the feed inlet;
the filter equipment, filter equipment is rectangular structure, filter equipment fixed connection is in the bottom of rectifying still, filter equipment has the effect of storage impurity, at lifter plate decline in-process, can extrude the water in the rectifying still to the bin in, when rivers are impacted upward from the bottom of fly leaf, the impact of rivers can drive the fly leaf rotatory, then the rising of lifter plate can extract the water in the bin again, when rivers remove the below from the top of filter, the filter filters the impurity in the rivers, makes impurity storage in the bin.
Preferably, elevating gear includes the filter screen, filter screen fixed connection is at the inner wall of rectifying barrel, the rectifying device outer wall is located the position fixedly connected with telescoping machine of rectifying barrel bottom, the axle center swing joint of telescoping machine is on the telescopic shaft, the telescopic shaft is pegged graft in rectifying barrel bottom, the top fixedly connected with lifter plate of telescopic shaft, the setting of filter screen intercepts bulk material, and the bulk material of interception rises to the inside of rectifying barrel, has avoided influencing the rectification effect at rectifying barrel middle part, and the telescoping machine starts the in-process and drives the telescopic shaft and stretch out and draw back from top to bottom, and the telescopic shaft is located the rectifying barrel and stretches out and draws back, drives the lifter plate in the telescopic process and follow and remove, and the lifter plate is located when rising in the rectifying barrel because the outer lane of lifter plate is very little with the inner wall interval of rectifying barrel.
Preferably, the telescopic shaft is inserted in the outer wall of the filter screen, the lifting plate is located at the top of the filter screen, water in the rectifying barrel is extruded to rise in the lifting plate rising process, water on the upper portion of the lifting plate is extruded to rise, mixing of various materials in the water is accelerated in the rising process, water in the filter device is pumped in the lifting plate rising process, water rises into the rectifying barrel after passing through the filter screen, and dispersion of the bulk materials is accelerated in the flushing process.
Preferably, the outer wall fixedly connected with reducing mechanism of telescopic shaft, reducing mechanism includes the elastic plate, elastic plate fixedly connected with is at the outer wall of telescopic shaft, the outer wall fixedly connected with of elastic plate two straight-bars, the end of two straight-bars is all fixedly connected with third bearing, the straight-bar is connected with the cutting pole through the third bearing rotation, the bottom fixedly connected with swash plate of filter screen is kept away from to the rectifying barrel inner wall, the guiding groove has been seted up to the outer wall of swash plate, and the decline of lifter drives rivers and descends, then makes bulk material fall on the swash plate, descends the position of guiding groove along the slope of swash plate, and the decline of cutting pole cuts bulk material on the guiding groove this moment, makes the material smash.
Preferably, the cutting rod is in movable contact with the guide groove, the outer wall of the cutting rod is provided with a groove, when water flows through the conical opening, the flow of the water flow can drive the fan blade to rotate, the fan blade drives the rotating rod and the stirring rod to rotate, the stirring rod is used for stirring in the rectifying barrel in the rotating process of the stirring rod, the stirring of the stirring rod accelerates the mixing of materials, and the telescopic shaft can drive the straight rod to move along with the stirring rod in the extending process.
Preferably, the outer wall fixedly connected with agitating unit of lifter plate, agitating unit includes the toper mouth, the outer wall at the lifter plate is seted up to the toper mouth, the inner wall fixedly connected with second bearing of toper mouth, the inner wall rotation of second bearing is connected with the rotary rod, the bottom fixedly connected with flabellum of rotary rod, the top fixedly connected with puddler of rotary rod, the toper mouth is the toper setting, so when the lifter plate risees, rivers can follow the toper mouth blowout, and the blowout of rivers can play the stirring effect to the rectifying tank, accelerates the various stirring efficiency of material in the rectifying tank.
Preferably, the filter device comprises a storage box fixedly connected to the bottom of the rectifying barrel, the storage box is communicated with the inside of the rectifying barrel, a first bearing is fixedly connected to the inner wall of the storage box, a movable plate is rotatably connected to the outer wall of the first bearing, a filter plate is fixedly connected to the outer wall of the movable plate, a spring is fixedly connected between the outer wall of the movable plate and the inner wall of the storage box, the spring is elastic, and the movable plate can be jacked up to descend under the elasticity of the spring when water flow stops impacting the movable plate.
The utility model provides a rectifying device for processing ultra-pure ammonia water with high discharge rate. The beneficial effects are as follows:
1. this high rectification apparatus for ultrapure aqueous ammonia processing of discharge rate, the water through lifter plate upper portion is risen by the extrusion, the in-process that rises accelerates the mixing of aquatic various materials, the follow-up rectification of being convenient for, lifter plate rises in-process and pumps the water in the filter equipment, make water rise to the rectifying vessel after the filter screen, the water is through the bulk material of filter screen bottom in the flow process, the washing of rivers can accelerate the crushing of bulk material, moreover the flow of rivers also can accelerate the mixing between the material.
2. This rectifying device is used in ultrapure aqueous ammonia processing that discharge rate is high, through the toper setting of bell mouth toper, rivers are from the bell mouth blowout, and the blowout of rivers can play the stirring effect to the rectifying vessel in, accelerates the various stirring efficiency of material in the rectifying vessel, and the blowout of rivers makes the rivers flow moreover, has avoided the material to pile up bottom position, has ensured the mixture of material.
3. This rectifying device is used in processing of ultrapure aqueous ammonia that discharge rate is high, through the flow of rivers, when the rivers pass through the bell mouth, the flow of rivers can drive the rotation of flabellum, and the puddler rotation in-process stirs the rectifying barrel, and the stirring of puddler has accelerated the mixture of material, and the intensive mixing of material has increased the discharge rate.
4. This rectifying device is used in ultrapure aqueous ammonia processing that discharge rate is high, rise and decline all can drive the flow of rivers through the lifter plate, rise and decline in-process all produce different effects moreover, the decline of lifter plate drives the rivers and descends, the slope setting of swash plate has played the guide effect to bulk material, then the cooperation cutting rod cuts bulk material, make the material smash, the crushing of bulk material has been accelerated, and then guaranteed the mixing of material, the intensive mixing of material has increased the discharge rate.
5. This rectifying device is used in processing of ultrapure aqueous ammonia that discharge rate is high, through the decline that utilizes the lifter plate, can extrude the water in the rectifying tank to the bin, the rising of lifter plate can extract the water in the bin again, when rivers remove the below from the top of filter, the filter filters the impurity in the rivers, make impurity storage in the bin, the effect of collecting that impurity in the rectifying tank played, the existence of impurity has been reduced, even in addition, when partial bulk material was stored in the bin, the scouring of rivers also can make the material mix in the bin.
Drawings
FIG. 1 is a schematic view of a shaft-side perspective of the present utility model;
FIG. 2 is a schematic diagram of an explosive structure according to the present utility model;
FIG. 3 is a schematic diagram of a motion flow of a processing apparatus according to the present utility model;
FIG. 4 is an enlarged view of the portion A of FIG. 3 according to the present utility model;
FIG. 5 is an enlarged view of the portion B of FIG. 3 according to the present utility model;
FIG. 6 is a schematic diagram of the motion flow path structure of the stirring device of the utility model;
FIG. 7 is a schematic diagram of the motion flow path structure of the filtering device of the present utility model.
In the figure: 1. a rectifying barrel; 2. a rectifying device; 3. a processing device; 31. a lifting device; 311. a lifting plate; 312. a filter screen; 313. a telescopic shaft; 314. a telescoping machine; 32. a filtering device; 321. a storage box; 322. a movable plate; 323. a first bearing; 324. a filter plate; 325. a spring; 33. a stirring device; 331. a stirring rod; 332. a conical mouth; 333. a rotating rod; 334. a second bearing; 335. a fan blade; 34. a pulverizing device; 341. an elastic plate; 342. a straight rod; 343. a third bearing; 344. cutting the rod; 345. a guide groove; 346. and a sloping plate.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments.
Examples of the embodiments are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to like or similar elements throughout or elements having like or similar functionality. The embodiments described below by referring to the drawings are illustrative and intended to explain the present utility model and should not be construed as limiting the utility model.
Example 1
Referring to fig. 1-3, the present utility model provides a technical solution: the rectification equipment for processing the ultra-pure ammonia water with high discharge rate comprises a rectification barrel 1, wherein the bottom of the rectification barrel 1 is fixedly connected with a rectification device 2, and the outer wall of the rectification barrel 1 is fixedly connected with a treatment device 3;
the processing device 3 includes:
the lifting device 31, the lifting device 31 is of a round structure, the lifting device 31 is fixedly connected to the bottom of the rectifying barrel 1, and the lifting device 31 has an extrusion function;
the filtering device 32, the filtering device 32 is rectangular structure, the filtering device 32 is fixedly connected to the bottom of the rectifying barrel 1, and the filtering device 32 has the function of storing impurities.
The lifting device 31 comprises a filter screen 312, the filter screen 312 is fixedly connected to the inner wall of the rectifying barrel 1, a telescopic machine 314 is fixedly connected to the outer wall of the rectifying device 2 at the bottom of the rectifying barrel 1, the axis of the telescopic machine 314 is movably connected to a telescopic shaft 313, the telescopic shaft 313 is inserted into the bottom of the rectifying barrel 1, and a lifting plate 311 is fixedly connected to the top of the telescopic shaft 313.
The telescopic shaft 313 is inserted in the outer wall of the filter screen 312, and the lifting plate 311 is positioned at the top of the filter screen 312.
When the rectifying device 2 is used, the rectifying device 2 is placed at a required position, the rectifying barrel 1 is arranged on the rectifying device 2, the position, away from the bottom of the filter screen 312, of the rectifying barrel 1 is provided with a feed inlet, ultrapure ammonia and other materials to be rectified can be added into the rectifying barrel 1 through the feed inlet, the filter screen 312 is arranged to intercept blocky materials, the intercepted materials rise into the rectifying barrel 1, the rectifying effect in the middle of the rectifying barrel 1 is prevented from being influenced, the telescopic shaft 313 is driven to stretch up and down in the starting process of the telescopic machine 314, the telescopic shaft 313 is positioned in the rectifying barrel 1 to stretch out and draw back in the telescopic process, the lifting plate 311 is driven to move along, when the lifting plate 311 is positioned in the rectifying barrel 1, the outer ring of the lifting plate 311 is very small in distance from the inner wall of the rectifying barrel 1, so that the lifting plate 311 is positioned in the rectifying barrel 1, the movement of the rectifying barrel is similar to a 'beating' structure, water in the lifting process of the lifting plate 311 is extruded in the lifting process, water in the lifting part of the lifting plate 311 is extruded and lifted in the lifting process, the lifting process of the blocky materials are accelerated in the lifting process, the mixing of the materials in the lifting process of the lifting plate 311 is accelerated, the materials in the lifting process of the lifting process, the lifting plate 311 is driven to move up and the water in the filtering barrel 32 in the process of the water after the filtering device is lifted in the lifting the water, and the water in the process of the filtering barrel 1 is pumped up and the water in the process of the filtering device.
Example two
Referring to fig. 1-6, the present utility model provides a technical solution based on the first embodiment:
the outer wall fixedly connected with reducing mechanism 34 of telescopic shaft 313, reducing mechanism 34 includes elastic plate 341, elastic plate 341 fixed connection is at the outer wall of telescopic shaft 313, and the outer wall fixedly connected with of elastic plate 341 has two straight-bars 342, and the end of two straight-bars 342 is all fixedly connected with third bearing 343, and straight-bar 342 rotates through third bearing 343 and is connected with cutting rod 344, and the bottom fixedly connected with swash plate 346 that filter screen 312 was kept away from to rectifying barrel 1 inner wall, and guiding groove 345 has been seted up to the outer wall of swash plate 346.
The cutting bar 344 is movably contacted with the guide groove 345, and the outer wall of the cutting bar 344 is provided with a groove.
The outer wall fixedly connected with agitating unit 33 of lifter plate 311, agitating unit 33 include the toper mouth 332, and the outer wall at lifter plate 311 is seted up to toper mouth 332, and the inner wall fixedly connected with second bearing 334 of toper mouth 332, the inner wall rotation of second bearing 334 is connected with rotary rod 333, the bottom fixedly connected with flabellum 335 of rotary rod 333, the top fixedly connected with puddler 331 of rotary rod 333.
When the device is used, the conical opening 332 is arranged in a conical manner, so when the lifting plate 311 ascends, water flow is sprayed out from the top of the conical opening 332, the spraying of the water flow can play a role in stirring the rectifying barrel 1, various stirring efficiencies of materials in the rectifying barrel 1 are accelerated, when the water flow passes through the conical opening 332, the flow of the water flow can drive the fan blade 335 to rotate, the fan blade 335 drives the rotating rod 333 and the stirring rod 331 to rotate, the stirring rod 331 stirs the rectifying barrel 1 in the rotating process of the stirring rod 331, the stirring of the stirring rod 331 accelerates the mixing of the materials, the telescopic shaft 313 drives the straight rod 342 to move along in the telescoping process, the descending of the lifting plate 311 drives the water flow to descend, then the blocky materials fall onto the inclined plate 346, the slope of the inclined plate 346 descends to the position of the guide groove 345, and the descending of the cutting rod 344 cuts the blocky materials on the guide groove 345, so that the materials are crushed.
Example III
Referring to fig. 1-7, the present utility model provides a technical solution based on the first embodiment and the second embodiment:
the filter 32 includes storage box 321, and storage box 321 fixed connection is in the bottom of rectifying tank 1, and storage box 321 communicates with rectifying tank 1's inside, and the inner wall fixedly connected with first bearing 323 of storage box 321, the outer wall rotation of first bearing 323 are connected with fly leaf 322, and the outer wall fixedly connected with filter 324 of fly leaf 322, fixedly connected with spring 325 between the outer wall of fly leaf 322 and the inner wall of storage box 321.
When the lifting plate 311 is used, water in the rectifying barrel 1 is extruded into the storage tank 321 in the descending process, when water flow impacts from the bottom of the movable plate 322 to the upper surface, the impact of the water flow can drive the movable plate 322 to rotate, then the lifting plate 311 ascends to extract water in the storage tank 321, and when the water flow moves from the upper side to the lower side of the filter plate 324, the filter plate 324 filters impurities in the water flow, so that the impurities are stored in the storage tank 321.
The foregoing is only a preferred embodiment of the present utility model, but the scope of the present utility model is not limited thereto, and any person skilled in the art, who is within the scope of the present utility model, should make equivalent substitutions or modifications according to the technical scheme of the present utility model and the inventive concept thereof, and should be covered by the scope of the present utility model.
Claims (7)
1. The utility model provides a rectification apparatus is used in processing of ultrapure aqueous ammonia that discharge rate is high, includes rectifying barrel (1), its characterized in that: the bottom of the rectifying barrel (1) is fixedly connected with a rectifying device (2), and the outer wall of the rectifying barrel (1) is fixedly connected with a processing device (3);
the processing device (3) comprises:
the lifting device (31) is of a round structure, the lifting device (31) is fixedly connected to the bottom of the rectifying barrel (1), and the lifting device (31) has an extrusion effect;
the filtering device (32), the filtering device (32) is rectangular structure, filtering device (32) fixed connection is in the bottom of rectifying barrel (1), filtering device (32) have the effect of storage impurity.
2. The high-discharge-rate rectification apparatus for processing ultra-pure ammonia water according to claim 1, wherein: lifting device (31) are including filter screen (312), filter screen (312) fixed connection is in the inner wall of rectifying barrel (1), the position fixedly connected with telescoping machine (314) that rectifying device (2) outer wall is located rectifying barrel (1) bottom, the axle center swing joint of telescoping machine (314) is in telescopic shaft (313), telescopic shaft (313) are pegged graft in rectifying barrel (1) bottom, the top fixedly connected with lifter plate (311) of telescopic shaft (313).
3. The high-discharge-rate rectification apparatus for processing ultra-pure ammonia water according to claim 2, wherein: the telescopic shaft (313) is inserted into the outer wall of the filter screen (312), and the lifting plate (311) is positioned at the top of the filter screen (312).
4. The high-discharge-rate rectification apparatus for processing ultra-pure ammonia water according to claim 2, wherein: the utility model discloses a grinding device for the high-pressure oil of the rectification barrel, including telescopic shaft (313), outer wall fixedly connected with reducing mechanism (34) of telescopic shaft (313), reducing mechanism (34) include elastic plate (341), elastic plate (341) fixedly connected with is at the outer wall of telescopic shaft (313), the outer wall fixedly connected with of elastic plate (341) two straight-bars (342), the end of two straight-bars (342) all fixedly connected with third bearing (343), straight-bar (342) are connected with cutting rod (344) through third bearing (343) rotation, bottom fixedly connected with swash plate (346) are kept away from to rectification barrel (1) inner wall, guiding groove (345) have been seted up to the outer wall of swash plate (346).
5. The high-discharge-rate rectification apparatus for processing ultra-pure ammonia water according to claim 4, wherein: the cutting rod (344) is movably contacted with the guide groove (345), and the outer wall of the cutting rod (344) is provided with a groove.
6. The high-discharge-rate rectification apparatus for processing ultra-pure ammonia water according to claim 2, wherein: the outer wall fixedly connected with agitating unit (33) of lifter plate (311), agitating unit (33) are including toper mouth (332), the outer wall at lifter plate (311) is seted up to toper mouth (332), the inner wall fixedly connected with second bearing (334) of toper mouth (332), the inner wall rotation of second bearing (334) is connected with rotary rod (333), the bottom fixedly connected with flabellum (335) of rotary rod (333), the top fixedly connected with puddler (331) of rotary rod (333).
7. The high-discharge-rate rectification apparatus for processing ultra-pure ammonia water according to claim 1, wherein: the filter device (32) comprises a storage box (321), the storage box (321) is fixedly connected to the bottom of the rectifying barrel (1), the storage box (321) is communicated with the inside of the rectifying barrel (1), a first bearing (323) is fixedly connected to the inner wall of the storage box (321), a movable plate (322) is rotatably connected to the outer wall of the first bearing (323), a filter plate (324) is fixedly connected to the outer wall of the movable plate (322), and a spring (325) is fixedly connected between the outer wall of the movable plate (322) and the inner wall of the storage box (321).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310684217.8A CN116421995B (en) | 2023-06-12 | 2023-06-12 | Rectifying equipment is used in processing of ultrapure aqueous ammonia that discharge rate is high |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310684217.8A CN116421995B (en) | 2023-06-12 | 2023-06-12 | Rectifying equipment is used in processing of ultrapure aqueous ammonia that discharge rate is high |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN116421995A true CN116421995A (en) | 2023-07-14 |
| CN116421995B CN116421995B (en) | 2023-08-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202310684217.8A Active CN116421995B (en) | 2023-06-12 | 2023-06-12 | Rectifying equipment is used in processing of ultrapure aqueous ammonia that discharge rate is high |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2187800A (en) * | 1986-03-13 | 1987-09-16 | Alexander Robert Powell | Crankcase compression operated fuel injection system |
| FR2702390A1 (en) * | 1993-03-08 | 1994-09-16 | Gantzer Robert | Waste recovery plant with waste. |
| CN209378889U (en) * | 2018-12-28 | 2019-09-13 | 无锡市英波化工有限公司 | A kind of environment-friendly type aqueous paint dispersing and filtering equipment |
| CN218248580U (en) * | 2022-08-29 | 2023-01-10 | 浙江英德赛半导体材料股份有限公司 | Ultra-pure ammonia rectification equipment |
-
2023
- 2023-06-12 CN CN202310684217.8A patent/CN116421995B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2187800A (en) * | 1986-03-13 | 1987-09-16 | Alexander Robert Powell | Crankcase compression operated fuel injection system |
| FR2702390A1 (en) * | 1993-03-08 | 1994-09-16 | Gantzer Robert | Waste recovery plant with waste. |
| CN209378889U (en) * | 2018-12-28 | 2019-09-13 | 无锡市英波化工有限公司 | A kind of environment-friendly type aqueous paint dispersing and filtering equipment |
| CN218248580U (en) * | 2022-08-29 | 2023-01-10 | 浙江英德赛半导体材料股份有限公司 | Ultra-pure ammonia rectification equipment |
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| Publication number | Publication date |
|---|---|
| CN116421995B (en) | 2023-08-11 |
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