CN209060839U - A kind of zeolite molecular sieve runner Adsorption Concentration device - Google Patents
A kind of zeolite molecular sieve runner Adsorption Concentration device Download PDFInfo
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- CN209060839U CN209060839U CN201821751672.6U CN201821751672U CN209060839U CN 209060839 U CN209060839 U CN 209060839U CN 201821751672 U CN201821751672 U CN 201821751672U CN 209060839 U CN209060839 U CN 209060839U
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- fixedly installed
- runner
- molecular sieve
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Abstract
The utility model discloses a kind of zeolite molecular sieve runner Adsorption Concentration devices, including pedestal and shell, the upper surface of pedestal is fixedly installed with shell, the interior side of shell is fixedly installed with coarse strainer, and the outer surface of shell offers air inlet close to the side of coarse strainer, the inside of shell is fixedly installed with fie screen close to the side of coarse strainer, and the inside of shell is fixedly installed with drying layer close to the side of fie screen；The utility model is cooled down by the way that the hot gas that heating response device is discharged in circulating cooling pipe is arranged, first so that air-flow is turned cold after cool down to the zeolite in rotary wheel device, second water can heat up after absorbing heat to by pretreated exhaust gas, and exhaust gas is made to meet the temperature requirement of runner absorption；Drying layer is added on rear side of fie screen, reduces the humidity of organic exhaust gas, it is made to meet runner absorption humidity requirement, and the circulating cooling pipe of setting utilizes extra heat well, reduces energy consumption.
Description
Technical field
The utility model relates to waste gas purifications to handle correlative technology field, and specially a kind of zeolite molecular sieve runner absorption is dense
Compression apparatus.
Background technique
Molecular sieve is a kind of with uniform micro, the absorption being mainly made of silicon, aluminium, oxygen and some other metal cation
Agent or film substance, aperture is suitable with general molecular size, and various fluid molecules are sieved according to its effective aperture.Zeolite point
Son sieve refers to those natural and artificial synthesized crystalline aluminosilicates with molecular sieve effect.In desorption process, due to boiling
Stone is after hot-air blowing is desorbed, and temperature gets higher that organic matter can not be adsorbed, and needing to cool down zeolite at this time makes
It drops to room temperature, guarantees its adsorption efficiency.For this purpose, the utility model proposes a kind of zeolite molecular sieve runner Adsorption Concentration device use
In solving the above problems.
Utility model content
The purpose of this utility model is to provide a kind of zeolite molecular sieve runner Adsorption Concentration devices, to solve above-mentioned background
The problem of being proposed in technology.
To achieve the above object, the utility model provides the following technical solutions: a kind of zeolite molecular sieve runner Adsorption Concentration
Device, including pedestal and shell, the upper surface of the pedestal are fixedly installed with shell, and the interior side of the shell is fixedly mounted
There is coarse strainer, and the outer surface of shell offers air inlet close to the side of coarse strainer, the inside of the shell is close to coarse strainer
Side be fixedly installed with fie screen, the inside of the shell is fixedly installed with drying layer close to the side of fie screen, described outer
The inside of shell is fixedly installed with runner outer casing frame far from the side of drying layer, and the runner outer casing frame is internally provided with runner dress
It sets, the lateral wall of rotary wheel device is fixedly connected with the inner sidewall of runner outer casing frame, is leaned in the middle part of the outer surface of the runner outer casing frame
The side of nearly drying layer is fixedly installed with desorption blower, and the outer surface of the runner outer casing frame side opposite with blower is desorbed is fixed
Heating response device is installed, the lower end that the upper surface of the pedestal is located at heating response device is fixedly installed with air-exhausting duct, and air draft
The outer surface of pipe is fixedly connected with absorption blower far from the side of runner outer casing frame, and the output end of the heating response device is fixed to be connected
It is connected to connecting pipe, and connecting pipe leads to the inside of shell, the end of connecting pipe and desorption wind across the upper surface of shell
The input terminal of machine is fixedly connected, and the outer surface spiral winding of the connecting pipe has circulating cooling pipe, and circulating cooling pipe is in spiral shell
Rotation shape is fixedly mounted between the inside and outside wall of shell.
Preferably, the rotary wheel device includes adsorption zone, desorption area, renewing zone and gear ring, and the side of rotary wheel device is logical
It crosses partition and is divided into adsorption zone, desorption area and renewing zone, desorption area renewing zone size is identical, the fixed peace in the outer surface of rotary wheel device
Equipped with gear ring.
Preferably, the interior lower end of the runner outer casing frame is fixedly installed with driving device, and the output end of driving device
Shaft outer surface is fixedly installed with pinion gear, and pinion gear is engaged with the gear ring of rotary wheel device outer surface.
Preferably, the water inlet end of the circulating cooling pipe close to heating response device side and pass through water pump and outer tank
It is fixedly connected, the water outlet of circulating cooling pipe is located between the lower end inside and outside wall of shell.
Preferably, the output end of the desorption blower is fixedly connected with the shell of rotary wheel device, and the output of blower is desorbed
Holding corresponding part is the region that area and renewing zone is desorbed and collectively constitutes.
Compared with prior art, the utility model has the beneficial effects that
1. cooled down by the way that circulating cooling pipe hot gas that heating response device is discharged is arranged, first so that air-flow is turned cold after it is right
Zeolite in rotary wheel device cools down, and the second water can heat up after absorbing heat to by pretreated exhaust gas, makes to give up
Gas meets the temperature requirement of runner absorption；
2. adding drying layer on rear side of fie screen, the humidity of organic exhaust gas is reduced, so that it is met runner absorption humidity and wants
It asks, the circulating cooling pipe of setting utilizes extra heat well, reduces energy consumption.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model；
Fig. 2 is this practical rotary wheel device side view.
In figure: 1 pedestal, 2 shells, 3 air inlets, 4 coarse strainers, 5 fie screens, 6 drying layers, 7 runner outer casing frames, 8 desorption wind
Machine, 9 heating response devices, 10 air-exhausting ducts, 11 absorption blowers, 12 connecting pipes, 13 circulating cooling pipes, 14 rotary wheel devices, 141 absorption
Area, 142 desorption areas, 143 renewing zones, 144 gear rings, 15 driving devices.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Fig. 1 to Fig. 2 is please referred to, the utility model provides a kind of technical solution: a kind of zeolite molecular sieve runner Adsorption Concentration
Device, as shown in Figure 1, the zeolite molecular sieve runner Adsorption Concentration device of the present embodiment, including pedestal 1 and shell 2, pedestal 1
Upper surface is fixedly installed with shell 2, and the interior side of shell 2 is fixedly installed with coarse strainer 4, and the outer surface of shell 2 is close to thick
The side of strainer 4 offers air inlet 3, and the inside of shell 2 is fixedly installed with fie screen 5, shell 2 close to the side of coarse strainer 4
Inside be fixedly installed with drying layer 6 close to the side of fie screen 5, the inside of shell 2 is fixedly mounted far from the side of drying layer 6
There is runner outer casing frame 7, runner outer casing frame 7 is internally provided with rotary wheel device 14, the lateral wall and runner shell of rotary wheel device 14
The inner sidewall of frame 7 is fixedly connected, and the side in the middle part of the outer surface of runner outer casing frame 7 close to drying layer 6 is fixedly installed with desorption wind
Machine 8, and the outer surface of runner outer casing frame 7 and the opposite side of desorption blower 8 are fixedly installed with heating response device 9, pedestal 1 it is upper
The lower end that surface is located at heating response device 9 is fixedly installed with air-exhausting duct 10, and the outer surface of air-exhausting duct 10 is far from runner outer casing frame 7
Side be fixedly connected with absorption blower 11, the output end of heating response device 9 is fixedly connected with connecting pipe 12, and connecting pipe
The inside of shell 2, the fixed company of input terminal of the end and desorption blower 8 of connecting pipe 12 are led in 12 upper surfaces for passing through shell 2
It connects, the outer surface spiral winding of connecting pipe 12 has circulating cooling pipe 13, and circulating cooling pipe 13 is fixedly mounted in the shape of a spiral
Between the inside and outside wall of shell 2.
Further, rotary wheel device 14 includes adsorption zone 141, desorption area 142, renewing zone 143 and gear ring 144, runner
The side of device 14 is divided into adsorption zone 141, desorption area 142 and renewing zone 143 by partition, and desorption 142, area renewing zone 143 is big
Small identical, the outer surface of rotary wheel device 14 is fixedly installed with gear ring 144, and the corresponding fan angle of adsorption zone 141 is 300 degree,
Area 142 is desorbed and the corresponding fan angle in renewing zone 143 is 30 degree.
Further, the interior lower end of runner outer casing frame 7 is fixedly installed with driving device 15, and the output of driving device 15
End shaft outer surface be fixedly installed with pinion gear, pinion gear is engaged with the gear ring 144 of 14 outer surface of rotary wheel device, pinion gear and
The gear ratio of gear ring 144 is 1 to 5, drives rotary wheel device 14 by gear drive.
Further, the water inlet end of circulating cooling pipe 13 close to heating response device 9 side and pass through water pump and external water
Case is fixedly connected, and the water outlet of circulating cooling pipe 13 is located between the lower end inside and outside wall of shell 2, and circulating cooling pipe 13 is by connecting tube
The heat of 12 inside hot gas of road is taken away, and is allowed to cool, while the circulating cooling pipe 13 after heating transfers heat in shell 2
Exhaust gas heats up to it, and heat is recycled.
Further, the output end that blower 8 is desorbed is fixedly connected with the shell of rotary wheel device 14, and the defeated of blower 8 is desorbed
The corresponding part of outlet is the region that area 142 and renewing zone 143 is desorbed and collectively constitutes, and the output end of desorption blower 8 is divided into two
Point, the hot wind of a part blowout comes out organic exhaust gas from desorption area 142 desorption, is burned and is purified by heating response device 9, makes to boil
Stone regenerating molecular sieve so recycles, and a part is that the cold air of 12 end of connecting pipe output carries out cooling drop to renewing zone 143
Temperature.
Working principle: organic exhaust gas enters the inside of shell 2 through air inlet 3, and zeolite molecular sieve runner Adsorption Concentration first leads to
It crosses coarse strainer 4 and fie screen 5 is removed the fine particle of exhaust gas, organic exhaust gas is made to meet the cleaning of the absorption of rotary wheel device 14
Degree requires, and the moisture in organic exhaust gas is dried in drying layer 6, then by cooling cycle pipe 13 to organic inside shell 2
Exhaust gas heats up, it is made to meet in main installation 14 temperature and humidity requirement, will be by pretreatment by adsorbing the effect of blower 11
Organic exhaust gas by the adsorption zone 141 of zeolite molecular sieve runner, organic molecule is captured by the distinctive adsorption hole of zeolite runner,
It adsorbs gas up to standard and is directly discharged into chimney, after adsorbing for a period of time, the meeting adsorption saturation of adsorption zone 141, at this point, passing through absorption
Blower 8 purges the desorption area 142 of rotary wheel device 14, and organic matter is burned only after being desorbed out in zeolite through heating response device 9
Change, make the zeolite regeneration of rotary wheel device 14, since zeolite is after hot-air blowing is desorbed, temperature gets higher not adsorbing organic
Object needs to cool down zeolite at this time that it is made to drop to room temperature, guarantees its adsorption efficiency, hot wind is through 12 row of connecting pipe
Out, the circulating cooling pipe 13 of 12 outer surface of connecting pipe cools down hot wind, the gas after cooling and desorption blower 8
Input terminal is fixedly connected, and is cooled down to renewing zone 142, and the circulating cooling pipe 13 after heating up is embedded in the inside and outside of shell 2
It heats up between layer to organic exhaust gas, it is made to meet the temperature requirement of adsorption zone 141.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (5)
1. a kind of zeolite molecular sieve runner Adsorption Concentration device, including pedestal (1) and shell (2), the upper surface of the pedestal (1)
It is fixedly installed with shell (2), it is characterised in that: the interior side of the shell (2) is fixedly installed with coarse strainer (4), and shell
(2) outer surface offers air inlet (3) close to the side of coarse strainer (4), and the inside of the shell (2) is close to coarse strainer (4)
Side be fixedly installed with fie screen (5), the inside of the shell (2) is fixedly installed with drying close to the side of fie screen (5)
Layer (6), the inside of the shell (2) is fixedly installed with runner outer casing frame (7) far from the side of drying layer (6), outside the runner
Cage (7) is internally provided with rotary wheel device (14), and the lateral wall of rotary wheel device (14) and the inner sidewall of runner outer casing frame (7) are solid
The outer surface middle part of fixed connection, the runner outer casing frame (7) is fixedly installed with desorption blower (8) close to the side of drying layer (6),
And the outer surface of runner outer casing frame (7) and desorption blower (8) opposite side are fixedly installed with heating response device (9), the bottom
The lower end that the upper surface of seat (1) is located at heating response device (9) is fixedly installed with air-exhausting duct (10), and the outer surface of air-exhausting duct (10)
Side far from runner outer casing frame (7) is fixedly connected with absorption blower (11), and the output end of the heating response device (9) is fixed to be connected
It is connected to connecting pipe (12), and connecting pipe (12) leads to the inside of shell (2), connecting pipe across the upper surface of shell (2)
(12) end is fixedly connected with the input terminal of desorption blower (8), and the outer surface spiral winding of the connecting pipe (12) follows
Ring cooling tube (13), and circulating cooling pipe (13) is fixedly mounted in the shape of a spiral between the inside and outside wall of shell (2).
2. a kind of zeolite molecular sieve runner Adsorption Concentration device according to claim 1, it is characterised in that: the runner dress
Setting (14) includes adsorption zone (141), desorption area (142), renewing zone (143) and gear ring (144), the side of rotary wheel device (14)
It is divided into adsorption zone (141), desorption area (142) and renewing zone (143) by partition, area (142) a renewing zone (143) size is desorbed
Identical, the outer surface of rotary wheel device (14) is fixedly installed with gear ring (144).
3. a kind of zeolite molecular sieve runner Adsorption Concentration device according to claim 1, it is characterised in that: outside the runner
The interior lower end of cage (7) is fixedly installed with driving device (15), and the output end shaft outer surface of driving device (15) is fixed
Pinion gear is installed, pinion gear is engaged with the gear ring (144) of rotary wheel device (14) outer surface.
4. a kind of zeolite molecular sieve runner Adsorption Concentration device according to claim 1, it is characterised in that: the circulation is cold
But manage (13) water inlet end close to heating response device (9) side and be fixedly connected by water pump with outer tank, circulating cooling
The water outlet of pipe (13) is located between the lower end inside and outside wall of shell (2).
5. a kind of zeolite molecular sieve runner Adsorption Concentration device according to claim 1, it is characterised in that: the desorption wind
The output end of machine (8) is fixedly connected with the shell of rotary wheel device (14), and the corresponding part of output end that blower (8) are desorbed is de-
The region that attached area (142) and renewing zone (143) collectively constitute.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821751672.6U CN209060839U (en) | 2018-10-28 | 2018-10-28 | A kind of zeolite molecular sieve runner Adsorption Concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821751672.6U CN209060839U (en) | 2018-10-28 | 2018-10-28 | A kind of zeolite molecular sieve runner Adsorption Concentration device |
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| Publication Number | Publication Date |
|---|---|
| CN209060839U true CN209060839U (en) | 2019-07-05 |
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ID=67096290
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821751672.6U Active CN209060839U (en) | 2018-10-28 | 2018-10-28 | A kind of zeolite molecular sieve runner Adsorption Concentration device |
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| CN (1) | CN209060839U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110465159A (en) * | 2019-07-25 | 2019-11-19 | 江苏苏净集团有限公司 | A kind of processing exhaust gas adsorption runner device |
| CN116216832A (en) * | 2023-02-23 | 2023-06-06 | 山东省鲁南地质工程勘察院(山东省地质矿产勘查开发局第二地质大队) | Fixed adsorption tube reactor for treating high-salt chemical wastewater |
-
2018
- 2018-10-28 CN CN201821751672.6U patent/CN209060839U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110465159A (en) * | 2019-07-25 | 2019-11-19 | 江苏苏净集团有限公司 | A kind of processing exhaust gas adsorption runner device |
| CN116216832A (en) * | 2023-02-23 | 2023-06-06 | 山东省鲁南地质工程勘察院(山东省地质矿产勘查开发局第二地质大队) | Fixed adsorption tube reactor for treating high-salt chemical wastewater |
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Address after: No.1-48, Beishi village, hi tech Zone, Zibo City, Shandong Province Patentee after: Shandong Baolan Environmental Protection Co.,Ltd. Address before: No.1-48, Beishi village, hi tech Zone, Zibo City, Shandong Province Patentee before: SHANDONG BAOLAN EP Co.,Ltd. |