CN114082259A - Molecular sieve water-gas distributor - Google Patents
Molecular sieve water-gas distributor Download PDFInfo
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- CN114082259A CN114082259A CN202111300381.1A CN202111300381A CN114082259A CN 114082259 A CN114082259 A CN 114082259A CN 202111300381 A CN202111300381 A CN 202111300381A CN 114082259 A CN114082259 A CN 114082259A
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- molecular sieve
- bearing
- gas
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- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 49
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 48
- 238000000605 extraction Methods 0.000 claims abstract 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 238000005086 pumping Methods 0.000 claims description 13
- 239000007921 spray Substances 0.000 claims description 11
- 238000005485 electric heating Methods 0.000 claims description 9
- 230000000740 bleeding effect Effects 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 48
- 238000000034 method Methods 0.000 description 7
- 239000011148 porous material Substances 0.000 description 6
- 208000005156 Dehydration Diseases 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2411—Filter cartridges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/26—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies rotatable
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Geometry (AREA)
- Drying Of Gases (AREA)
Abstract
The invention discloses a molecular sieve water-gas distributor which comprises a base, a gas inlet channel, a first support, a connecting channel, a second support and a second gas extraction channel, wherein a bearing cylinder is fixed on one side of the upper end surface of the base, the gas inlet channel penetrates and is fixed on the rear side wall of the bearing cylinder, the gas inlet channel is positioned on the inner side of a cylindrical water-gas sieve, one end of the connecting channel is fixed at the bottom of the bearing cylinder through a bolt, the second support is fixed on the other side of the upper end surface of the base through a bolt, a first splicing pipeline and a second splicing pipeline are respectively fixed on two sides of the bearing channel, and a molecular sieve is fixed on the inner side of the bearing channel. This molecular sieve aqueous vapor distributor utilizes the tube-shape aqueous vapor sieve to separate out after the moisture in the gas, and the tube-shape aqueous vapor sieve can rotate along with the commentaries on classics board, can arrange to use aspiration pump, connecting tube, first bleed passage and the first steam of bleeding to take out steam when utilizing the electric plate stoving tube-shape aqueous vapor sieve to go up moisture, makes things convenient for used repeatedly tube-shape aqueous vapor sieve.
Description
Technical Field
The invention relates to the related technical field of molecular sieves, in particular to a water-gas distributor of a molecular sieve.
Background
The molecular sieve is an artificially synthesized hydrated aluminosilicate (zeolite) or natural zeolite with the function of screening molecules, and has a plurality of pore passages with uniform pore diameters and holes arranged in order in the structure, the molecular sieves with different pore diameters separate molecules with different sizes and shapes, and the molecular sieves with different pore diameters have high adsorption capacity, strong selectivity and high temperature resistance, are widely used in organic chemical industry and petrochemical industry, are also excellent adsorbents for gas dehydration, and are increasingly emphasized in waste gas purification.
Disclosure of Invention
The invention aims to provide a molecular sieve water-gas distributor, which solves the problems that the existing water-gas distributor in the prior art is inconvenient to reuse a water-gas sieve in the existing water-gas distributor, is difficult to perform continuous dehydration treatment on gas, has low working efficiency, and is difficult to use the molecular sieve repeatedly because one kind of molecules are adsorbed by the molecular sieve and then are inconvenient to be desorbed and extracted independently.
In order to achieve the purpose, the invention provides the following technical scheme: the molecular sieve water-gas distributor comprises a base, an air inlet channel, a first bracket, a connecting channel, a second bracket and a second air exhaust channel,
a bearing cylinder is fixed on one side of the upper end face of the base, an arc support plate is fixed on the rear inner wall of the bearing cylinder, and electric heating plates are fixed on the inner top of the bearing cylinder and the upper end face of the arc support plate;
the air inlet channel penetrates through and is fixed on the rear side wall of the bearing cylinder, the lower end face of the air inlet channel penetrates through and is fixed with the spray head, the air inlet channel is positioned on the inner side of the cylindrical moisture sieve, and the cylindrical moisture sieve is rotatably connected to the inner side of the bearing cylinder;
one end of the connecting channel is fixed at the bottom of the bearing cylinder through a bolt, the other end of the connecting channel is connected with the first splicing pipeline through a stud bolt, and a fan is fixed in the connecting channel;
the second support is fixed on the other side of the upper end face of the base through a bolt, a bearing channel is fixed at the top of the second support, a first splicing pipeline and a second splicing pipeline are respectively fixed on two sides of the bearing channel, and a molecular sieve is fixed on the inner side of the bearing channel.
By adopting the technical scheme, after the gas is led into the bearing cylinder, the cylindrical moisture sieve can sieve the moisture in the gas, at the moment, the moisture remains at the inner side of the cylindrical moisture sieve, the dehydrated gas enters the bearing channel through the connecting channel and the first splicing pipeline in sequence, the molecular sieve can adsorb molecules with one shape and size, the bearing channels with required number can be assembled on the right side of the bearing channel before the device is used, the pore diameter of the molecular sieve in each bearing channel is different, the molecules with different shapes and sizes can be conveniently adsorbed, in the process of separating the moisture by using the cylindrical moisture sieve, the cylindrical moisture sieve can rotate along with the rotating plate, the electric heating plate is matched to dry the moisture on the cylindrical moisture sieve, and the vapor generated in the process can be pumped away through the pumping head, the first pumping channel and the connecting pipeline in sequence under the action of the pumping pump, after the molecular sieve is used for adsorbing molecules, an air pump outside the second air pumping channel can be used for desorbing and pumping away the molecules in the molecular sieve.
Preferably, the first air exhaust channel is fixed on the inner top of the bearing cylinder and the upper end surface of the arc support plate, the first air exhaust channel is connected with the air exhaust pump through a connecting pipeline, and an air exhaust head penetrates through and is fixed on the inner end surface of the first air exhaust channel.
Through adopting above-mentioned technical scheme, utilize the electric heat board to carry out drying process's in-process to the tube-shape aqueous vapor sieve and can arrange to use aspiration pump, connecting tube, first bleed passage and the first vapor of bleeding to take out steam.
Preferably, the suction heads are distributed at equal distances over the first suction channel.
By adopting the technical scheme, the air pumps distributed at equal intervals can better pump away the water vapor.
Preferably, the spray heads are distributed equidistantly on the air inlet channel.
By adopting the technical scheme, the spray heads distributed equidistantly can enable gas to be more dispersed and comprehensively communicated into the bearing cylinder.
Preferably, the first support is fixed on the base through a bolt, a motor is fixed at the top of the first support, the output end of the motor is connected with the rotating plate through a motor shaft, and the rotating plate is fixed on the front side of the cylindrical water-gas screen through a bolt.
Through adopting above-mentioned technical scheme, when utilizing the tube-shape moisture sieve to separate moisture in the gas, the tube-shape moisture sieve can rotate along with the commentaries on classics board together, makes things convenient for the make full use of tube-shape moisture sieve.
Preferably, the cylindrical water-gas screen is rotatably connected to the inner side of the limiting ring, and the limiting ring is fixed on the rear inner wall of the bearing cylinder.
Through adopting above-mentioned technical scheme, the spacing ring plays the effect of spacing support at the pivoted in-process of tube-shape aqueous vapor sieve.
Preferably, the second pumping channel penetrates through and is fixed on the front side of the bearing channel, and a first electric valve is arranged in the second pumping channel.
Through adopting above-mentioned technical scheme, link together second bleed passage and outside air exhaust device and close first electrically operated valve can be opened after the second electrically operated valve in the first concatenation pipeline and the second electrically operated valve in the second concatenation pipeline, conveniently get off and take away the molecule desorption on the molecular sieve.
Preferably, the second spliced pipeline and the first spliced pipeline are symmetrically arranged on the bearing channel.
By adopting the technical scheme, the required number of the bearing channels can be continuously assembled on the right side of the bearing channel by utilizing the first splicing pipeline, the second splicing pipeline and the stud bolt before the device is used.
Preferably, second electric valves are arranged in the second splicing pipeline and the first splicing pipeline.
Through adopting above-mentioned technical scheme, need close the second electric valve in the first concatenation pipeline and the second electric valve in the second concatenation pipeline before carrying out desorption treatment to the molecule in the molecular sieve.
Compared with the prior art, the invention has the beneficial effects that: the water-gas distributor of the molecular sieve is provided with a water-gas distributor,
(1) after the gas is introduced into the bearing cylinder through the gas inlet channel and the spray head, the gas passes through the cylindrical water-gas sieve and then enters the bearing channel through the connecting channel and the first splicing pipeline, and the water doped in the gas is remained at the inner side of the cylindrical water-gas sieve, so that the dehydration effect is conveniently achieved;
(2) after the moisture in the gas is separated by the cylindrical water vapor screen, the cylindrical water vapor screen can rotate along with the rotating plate, and the water on the cylindrical water vapor screen is dried by the electric heating plate, and meanwhile, the water vapor can be pumped by the air pump, the connecting pipeline, the first air pumping channel and the air pumping head, so that the cylindrical water vapor screen can be conveniently and repeatedly used;
(3) after the dehydrated gas enters the bearing channels, the molecular sieve can adsorb molecules with one size and shape, the bearing channels with the required number can be continuously assembled rightwards by utilizing the first splicing pipeline, the second splicing pipeline and the stud bolt before the device is used, the pore diameter of the molecular sieve in each bearing channel is different, and the molecules with different sizes and shapes can be conveniently adsorbed;
(4) after the molecular sieve adsorbs molecules in a size shape, the second electric valve in the first splicing pipeline and the second electric valve in the second splicing pipeline are closed, the second air exhaust channel is connected with an external air exhaust device, and the molecules on the molecular sieve can be desorbed and exhausted after the first electric valve is opened, so that the molecular sieve can be reused conveniently.
Drawings
FIG. 1 is a schematic front sectional view of the present invention;
FIG. 2 is a schematic view of the front view of the present invention;
FIG. 3 is a rear view of the present invention;
FIG. 4 is a schematic left-side sectional view of the present invention;
FIG. 5 is a schematic view of the connection structure of the bearing cartridge, the electric heating plate, the first pumping channel and the pumping head according to the present invention;
FIG. 6 is a schematic view of the connection structure of the carrying channel, the first splicing pipeline, the molecular sieve, the second pumping channel, the first electric valve, the second splicing pipeline and the second electric valve.
In the figure: 1. the base, 2, bear a weight of the section of thick bamboo, 3, the arc extension board, 4, the electric plate, 5, the aspiration pump, 6, the connecting tube, 7, first bleed passage, 8, the head of bleeding, 9, the spacing ring, 10, inlet channel, 11, the shower nozzle, 12, first support, 13, the motor, 14, the motor shaft, 15, change the board, 16, tube-shape aqueous vapor sieve, 17, the connecting tube, 18, the fan, 19, the second support, 20, bear the weight of the passageway, 21, first concatenation pipeline, 22, the molecular sieve, 23, the second bleed passage, 24, first electric valve, 25, the second concatenation pipeline, 26, the second electric valve.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-6, the present invention provides a technical solution: a molecular sieve water vapor distributor is shown in figures 1 and 2, wherein a bearing cylinder 2 is fixed on one side of the upper end surface of a base 1, an arc support plate 3 is fixed on the rear inner wall of the bearing cylinder 2, an electric heating plate 4 is fixed on the inner top of the bearing cylinder 2 and the upper end surface of the arc support plate 3, a first air exhaust channel 7 is fixed on the inner top of the bearing cylinder 2 and the upper end surface of the arc support plate 3, the first air exhaust channel 7 is connected with an air exhaust pump 5 through a connecting pipeline 6, an air exhaust head 8 penetrates through the inner end surface of the first air exhaust channel 7, after moisture in gas is separated by using a cylindrical water vapor sieve 16, the cylindrical water vapor sieve 16 can rotate along with a rotating plate 15, the electric heating plate 4 can dry the cylindrical water vapor sieve 16, and water vapor generated in the drying process can be discharged through the air exhaust head 8, the first air exhaust channel 7 and the connecting pipeline 6 in sequence under the action of the air exhaust pump 5, the air exhaust heads 8 are distributed on the first air exhaust channel 7 at equal intervals, and the air exhaust heads 8 distributed at equal intervals can exhaust water vapor more comprehensively and uniformly.
As shown in fig. 1, 2 and 3, an air inlet passage 10 is fixed through the rear side wall of the mandrel 2, and the lower end surface of the air inlet channel 10 is fixedly penetrated with a spray head 11, the spray heads 11 are distributed on the air inlet channel 10 at equal intervals, after the air inlet channel 10 is connected with external ventilation equipment, the gas can enter the bearing cylinder 2 through the gas inlet passage 10 and the spray heads 11 in sequence, the spray heads 11 distributed at equal intervals can make the gas inlet effect more dispersed and comprehensive, the first bracket 12 is fixed on the base 1 through bolts, the top of the first bracket 12 is fixed with the motor 13, meanwhile, the output end of the motor 13 is connected with a rotating plate 15 through a motor shaft 14, the rotating plate 15 is fixed at the front side of the cylindrical water-air screen 16 through bolts, the rotating plate 15 can rotate under the action of the motor 13 and the motor shaft 14, thereby driving the cylindrical water-gas sieve 16 to rotate, and conveniently and fully utilizing the cylindrical water-gas sieve 16 to separate the water in the gas.
According to the drawings of fig. 1, 2, 3 and 4, the air inlet channel 10 is located on the inner side of the cylindrical water-gas screen 16, the cylindrical water-gas screen 16 is rotatably connected on the inner side of the bearing cylinder 2, the cylindrical water-gas screen 16 is rotatably connected on the inner side of the limiting ring 9, the limiting ring 9 is fixed on the rear inner wall of the bearing cylinder 2, and the limiting ring 9 plays a role of limiting and supporting in the rotating process of the cylindrical water-gas screen 16, so that the cylindrical water-gas screen 16 is more stable in rotation.
According to the drawings of fig. 1, 2, 3, 5 and 6, one end of the connecting channel 17 is fixed at the bottom of the bearing cylinder 2 by bolts, the other end of the connecting channel 17 is connected with the first splicing pipeline 21 by stud bolts, a fan 18 is fixed in the connecting channel 17, a second bracket 19 is fixed at the other side of the upper end surface of the base 1 by bolts, a bearing channel 20 is fixed at the top of the second bracket 19, a first splicing pipeline 21 and a second splicing pipeline 25 are respectively fixed at two sides of the bearing channel 20, a molecular sieve 22 is fixed at the inner side of the bearing channel 20, a second air suction channel 23 penetrates and is fixed at the front side of the bearing channel 20, a first electric valve 24 is arranged in the second air suction channel 23, molecules on the molecular sieve 22 can be desorbed and drawn away after the second electric valve 26 is closed and the first electric valve 24 is opened, the second splicing pipeline 25 and the first splicing pipeline 21 are symmetrically arranged on the bearing channel 20, usable first concatenation pipeline 21 before using the device, the required number of bearing channel 20 of second concatenation pipeline 25 and stud concatenation equipment is on the right side of bearing channel 20, the aperture of molecular sieve 22 is different in every bearing channel 20, conveniently adsorb the molecule of different shape size, all be provided with second electric valve 26 in second concatenation pipeline 25 and the first concatenation pipeline 21, need close second electric valve 26 in the first concatenation pipeline 21 and the second electric valve 26 in the second concatenation pipeline 25 when carrying out desorption treatment to the molecule on molecular sieve 22.
The working principle of the embodiment is as follows: when the molecular sieve water-gas distributor is used, firstly, the gas inlet channel 10 is connected with external ventilation equipment, then the first splicing pipeline 21, the second splicing pipeline 25 and the stud bolts are utilized to splice and assemble the required number of bearing channels 20 to the right, the bearing channels are connected to an external power supply, after gas is sequentially led into the bearing barrel 2 through the gas inlet channel 10 and the spray head 11, moisture doped in the gas is remained at the inner side of the cylindrical water-gas sieve 16, the dehydrated gas passes through the cylindrical water-gas sieve 16 and then enters the bearing channels 20 through the connecting channel 17 and the first splicing pipeline 21 under the action of the fan 18, each molecular sieve 22 can adsorb molecules with one size and one shape, after the motor 13 is started, the motor 13 drives the motor shaft 14 to rotate, so as to drive the rotating plate 15 to rotate, the cylindrical water-gas sieve 16 rotates along with the connecting channel, and simultaneously the electric heating plate 4 and the air suction pump 5 are started, the electric heating plate 4 can dry moisture on the cylindrical water-gas sieve 16, water vapor generated in the drying process can be discharged through the connecting pipeline 6, the first air-extracting channel 7 and the air-extracting head 8 in sequence under the action of the air-extracting pump 5, after the molecular sieve 22 is used for adsorbing molecules with a certain size and shape, the second electric valve 26 in the first splicing pipeline 21 and the second electric valve 26 in the second splicing pipeline 25 are closed, the second air-extracting channel 23 is connected with an external air-extracting device, and the first electric valve 24 is opened, so that the molecules on the molecular sieve 22 are desorbed and extracted, and the content which is not described in detail in the specification belongs to the prior art which is known by professionals in the field.
Although the present invention has been described in detail with reference to the preferred embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted without departing from the spirit and scope of the invention as defined in the appended claims. The techniques, shapes, and configurations not described in detail in the present invention are all known techniques.
The terms "central," "longitudinal," "lateral," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like are used in the orientation or positional relationship indicated in the drawings for simplicity of description only and are not intended to indicate or imply that the referenced devices or elements must be in a particular orientation, constructed and operative in a particular orientation, and are not to be considered limiting of the claimed invention.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that various changes in the embodiments and/or modifications of the invention can be made, and equivalents and modifications of some features of the invention can be made without departing from the spirit and scope of the invention.
Claims (9)
1. Molecular sieve aqueous vapor distributor, including base (1), inlet channel (10), first support (12), connecting channel (17), second support (19) and second pumping channel (23), its characterized in that:
a bearing cylinder (2) is fixed on one side of the upper end face of the base (1), an arc support plate (3) is fixed on the rear inner wall of the bearing cylinder (2), and an electric heating plate (4) is fixed on the inner top of the bearing cylinder (2) and the upper end face of the arc support plate (3);
the air inlet channel (10) penetrates and is fixed on the rear side wall of the bearing cylinder (2), the lower end face of the air inlet channel (10) penetrates and is fixed with the spray head (11), the air inlet channel (10) is located on the inner side of the cylindrical water-air sieve (16), and the cylindrical water-air sieve (16) is rotatably connected to the inner side of the bearing cylinder (2);
one end of the connecting channel (17) is fixed at the bottom of the bearing cylinder (2) through a bolt, the other end of the connecting channel (17) is connected with a first splicing pipeline (21) through a stud bolt, and a fan (18) is fixed in the connecting channel (17);
the second support (19) is fixed on the other side of the upper end face of the base (1) through bolts, a bearing channel (20) is fixed to the top of the second support (19), a first splicing pipeline (21) and a second splicing pipeline (25) are fixed to the two sides of the bearing channel (20) respectively, and a molecular sieve (22) is fixed to the inner side of the bearing channel (20).
2. The molecular sieve water gas distributor of claim 1, wherein: the first air exhaust channel (7) is fixed on the inner top of the bearing barrel (2) and the upper end face of the arc support plate (3), the first air exhaust channel (7) is connected with the air exhaust pump (5) through a connecting pipeline (6), and an air exhaust head (8) penetrates through and is fixed on the inner end face of the first air exhaust channel (7).
3. The molecular sieve water gas distributor of claim 1, wherein: the air extraction heads (8) are distributed on the first air extraction channel (7) at equal intervals.
4. The molecular sieve water gas distributor of claim 1, wherein: the spray heads (11) are distributed on the air inlet channel (10) at equal intervals.
5. The molecular sieve water gas distributor of claim 1, wherein: the first support (12) is fixed on the base (1) through bolts, the motor (13) is fixed at the top of the first support (12), meanwhile, the output end of the motor (13) is connected with the rotating plate (15) through the motor shaft (14), and the rotating plate (15) is fixed on the front side of the cylindrical water-gas screen (16) through bolts.
6. The molecular sieve water gas distributor of claim 1, wherein: the cylindrical water-gas screen (16) is rotatably connected to the inner side of the limiting ring (9), and the limiting ring (9) is fixed on the rear inner wall of the bearing cylinder (2).
7. The molecular sieve water gas distributor of claim 1, wherein: the second air exhaust channel (23) penetrates through and is fixed on the front side of the bearing channel (20), and a first electric valve (24) is arranged in the second air exhaust channel (23).
8. The molecular sieve water gas distributor of claim 1, wherein: the second splicing pipeline (25) and the first splicing pipeline (21) are symmetrically arranged on the bearing channel (20).
9. The molecular sieve water gas distributor of claim 1, wherein: and second electric valves (26) are arranged in the second splicing pipeline (25) and the first splicing pipeline (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111300381.1A CN114082259A (en) | 2021-11-04 | 2021-11-04 | Molecular sieve water-gas distributor |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111300381.1A CN114082259A (en) | 2021-11-04 | 2021-11-04 | Molecular sieve water-gas distributor |
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| CN114082259A true CN114082259A (en) | 2022-02-25 |
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Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1396032A (en) * | 1971-05-03 | 1975-05-29 | Air Liquide | Process and insta-lation for fractionating a gaseous mixture |
| GB1431845A (en) * | 1972-07-26 | 1976-04-14 | Grace W R & Co | Pressure equalisation adsorption systems |
| EP0225934A1 (en) * | 1985-12-16 | 1987-06-24 | Health Technologies, Inc. | Method and apparatus for separating gases and gaseous mixtures by employing molecular sieves |
| JPS63274430A (en) * | 1987-04-30 | 1988-11-11 | Kuraray Chem Kk | Pressure variation adsorption type nitrogen gas separation apparatus |
| CN1470312A (en) * | 2003-07-04 | 2004-01-28 | 黄公连 | Single-tower pressure-swing adsorption air-separating method |
| US20040060446A1 (en) * | 2002-09-26 | 2004-04-01 | Wolfgang Rittner | Device for enriching air with oxygen |
| CN202336263U (en) * | 2011-11-17 | 2012-07-18 | 辽宁省电力有限公司本溪供电公司 | Air-water separating device |
| CN102716634A (en) * | 2012-06-11 | 2012-10-10 | 柳州展维热工科技有限公司 | Gas-water separator with coarse-fine separation function |
| CN202715336U (en) * | 2012-09-07 | 2013-02-06 | 清远市联升空气液化有限公司 | Water separator device for air inlet of molecular sieve of large air separation plant |
| CN106276823A (en) * | 2016-10-14 | 2017-01-04 | 北京石油化工工程有限公司 | Low dew point swing adsorption nitrogen producing apparatus and technological process |
| CN206366270U (en) * | 2017-01-09 | 2017-08-01 | 浙江澳蓝环保科技有限公司 | A kind of automatic dehydration formula moisture separator |
| CN107817138A (en) * | 2017-10-20 | 2018-03-20 | 重庆美高科技有限公司 | A kind of device for trapping dust |
| CN208212822U (en) * | 2018-04-10 | 2018-12-11 | 上海宇薄实业有限公司 | A kind of gas-liquid separator |
| CN213253465U (en) * | 2020-09-10 | 2021-05-25 | 河北睿胜环保设备有限公司 | Filter cartridge cleaning device of filter cartridge dust remover |
| CN213527818U (en) * | 2020-09-27 | 2021-06-25 | 滁州天陆泓机械有限公司 | Quick replacement's air inlet filter core |
| CN214264298U (en) * | 2020-09-24 | 2021-09-24 | 韩延辉 | Split type large-diameter screen drum |
-
2021
- 2021-11-04 CN CN202111300381.1A patent/CN114082259A/en active Pending
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1396032A (en) * | 1971-05-03 | 1975-05-29 | Air Liquide | Process and insta-lation for fractionating a gaseous mixture |
| GB1431845A (en) * | 1972-07-26 | 1976-04-14 | Grace W R & Co | Pressure equalisation adsorption systems |
| EP0225934A1 (en) * | 1985-12-16 | 1987-06-24 | Health Technologies, Inc. | Method and apparatus for separating gases and gaseous mixtures by employing molecular sieves |
| JPS63274430A (en) * | 1987-04-30 | 1988-11-11 | Kuraray Chem Kk | Pressure variation adsorption type nitrogen gas separation apparatus |
| US20040060446A1 (en) * | 2002-09-26 | 2004-04-01 | Wolfgang Rittner | Device for enriching air with oxygen |
| CN1470312A (en) * | 2003-07-04 | 2004-01-28 | 黄公连 | Single-tower pressure-swing adsorption air-separating method |
| CN202336263U (en) * | 2011-11-17 | 2012-07-18 | 辽宁省电力有限公司本溪供电公司 | Air-water separating device |
| CN102716634A (en) * | 2012-06-11 | 2012-10-10 | 柳州展维热工科技有限公司 | Gas-water separator with coarse-fine separation function |
| CN202715336U (en) * | 2012-09-07 | 2013-02-06 | 清远市联升空气液化有限公司 | Water separator device for air inlet of molecular sieve of large air separation plant |
| CN106276823A (en) * | 2016-10-14 | 2017-01-04 | 北京石油化工工程有限公司 | Low dew point swing adsorption nitrogen producing apparatus and technological process |
| CN206366270U (en) * | 2017-01-09 | 2017-08-01 | 浙江澳蓝环保科技有限公司 | A kind of automatic dehydration formula moisture separator |
| CN107817138A (en) * | 2017-10-20 | 2018-03-20 | 重庆美高科技有限公司 | A kind of device for trapping dust |
| CN208212822U (en) * | 2018-04-10 | 2018-12-11 | 上海宇薄实业有限公司 | A kind of gas-liquid separator |
| CN213253465U (en) * | 2020-09-10 | 2021-05-25 | 河北睿胜环保设备有限公司 | Filter cartridge cleaning device of filter cartridge dust remover |
| CN214264298U (en) * | 2020-09-24 | 2021-09-24 | 韩延辉 | Split type large-diameter screen drum |
| CN213527818U (en) * | 2020-09-27 | 2021-06-25 | 滁州天陆泓机械有限公司 | Quick replacement's air inlet filter core |
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Application publication date: 20220225 |