CN209451571U - A kind of rotating circulating adsorption desorption integration acquirer - Google Patents
A kind of rotating circulating adsorption desorption integration acquirer Download PDFInfo
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- CN209451571U CN209451571U CN201821079817.2U CN201821079817U CN209451571U CN 209451571 U CN209451571 U CN 209451571U CN 201821079817 U CN201821079817 U CN 201821079817U CN 209451571 U CN209451571 U CN 209451571U
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Abstract
A kind of rotating circulating adsorption desorption integration acquirer it include cylindrical tube (43), adsorbed gas import (1), purified gas outlet (2), cooling gas import (3), cooling gas exports (4), desorption gas exports (5), solid absorbent import (6, 7, 8), solid absorbent outlet (9, 10, 11), there are center rotating shaft (15) at cylindrical tube (43) center, there are three pieces of partitions (35 between center rotating shaft (15) and cylindrical tube (43), 36, 37), by partition (35, 36, 37) cylindrical tube (43) is divided into the absorber (20) of identical three fan-shaped cylinders, regenerator (21) and cooler (22), absorber (20), regenerator (21) and cooler (22) are to be recycled.The utility model realizes continuous absorption, the regeneration, cooling cycle of gas, realizes the continuity of adsorption operations, makes the advantages of adsorption separation process is from intermittently becoming continuous, shortening the adsorption-desorption period.
Description
Technical field
The utility model belongs to a kind of rotating circulating adsorption desorption integration acquirer.
Background technique
Solid absorption method is the selective reversible adsorption using solid adsorbent to the light concentration gas in material mixed gas
It acts on separating and recovering.Under low temperature or high pressure, these solid absorbents adsorption of Low Concentration gas from gaseous mixture, in high temperature
Or be desorbed out again under low pressure, so as to separating low concentration gas, while solid absorbent can be regenerated.Absorption method tool
Have that technological operation is simple, process is short, small investment, operating flexibility are big, the good advantage of environmental benefit, always by the blueness of researcher
It looks at.
Current most of light concentration gas reclaimers are all to pass through interval on two or more fixed-bed adsorbers
Formula absorption-desorption technique, and conventional pressure-swing desorption or alternating temperature desorption, the recycling of Lai Shixian light concentration gas.The absorber is inhaled
Attached-desorption period is long, and desorption is not thorough, and purification efficiency is unstable, high operation requirements and complexity, and investment is big, occupied area
Greatly；It is desorbed especially with pressure-swing desorption or alternating temperature, the investment of system and energy consumption are all very big.In recent years, researcher, which proposed, follows
Ring fluidized bed adsorbing and trapping device, although broad-minded gas absorption can be handled, operation is relatively complicated, and adsorbs again
The raw time is not easy to control, therefore, selects a kind of absorption regeneration adsorbent equipment for improving operating condition, reducing operation energy consumption, green
Colour circle guarantor etc. has great importance.Huang Weiqiu et al. refers to lead in Oil-gas Separation in patent 201120435125.9
Domain application rotary type adsorber device, realize inner cylinder rotation to achieve the purpose that Oil-gas Separation, but in inner cylinder by
In with the presence of a large amount of solid absorbents, lead to the larger problem of transmission device energy consumption, then have its application range relatively narrow, does not have universal
Applicability.
Summary of the invention
That the purpose of the utility model is to provide a kind of structures is simple, treating capacity is big, occupied area is small, heat-transfer effect is good, suitable
Rotating circulating adsorption-desorption integration acquirer for various normal pressure light concentration gas.
Technical solutions of the utility model are as follows:
A kind of rotating circulating adsorption desorption integration acquirer of the utility model, it includes cylindrical tube, adsorbed gas import,
Purified gas outlet, cooling gas import, cooling gas outlet, desorption gas outlet, solid absorbent import, solid absorbent
Outlet, has center rotating shaft at cylindrical tube center, there is three pieces of partitions between center rotating shaft and cylindrical tube, will by partition
Cylindrical tube is divided into absorber, regenerator and the cooler of identical three fan-shaped cylinders, the upper surface and overhead of cylindrical tube
Heart cylinder ring fixed plate is welded to connect, and the lower end surface of cylindrical tube and lower open circles band of column fixed plate are welded to connect, upper hollow
Between cylinder ring fixed plate and absorber, regenerator and cooler with upper rotation circular baffle plate, in lower open circles band of column fixed plate
Have lower rotation circular baffle plate between absorber, regenerator and cooler, upper rotation circular baffle plate and lower rotation circular baffle plate with
Center rotating axis connection, cylindrical tube and upper rotation circular baffle plate are connected by the recessed circle of upper movable sealing, cylindrical tube and backspin
Turn to connect between circular baffle plate by the recessed circle of lower movable sealing, lower open circles band of column fixed plate has lower hollow cylinder outer ring, lower sky
Heart cylinder middle ring and lower hollow cylinder inner ring, upper hollow cylinder ring fixed plate have upper hollow cylinder outer ring, upper hollow cylinder middle ring,
Upper hollow cylinder inner ring, upper hollow cylinder outer ring, upper hollow cylinder middle ring, upper hollow cylinder inner ring are kept off with upper rotation circle respectively
It is connected between plate by upper activity O-ring seal, lower hollow cylinder outer ring, lower hollow cylinder middle ring and lower hollow cylinder inner ring point
It is not connect between lower rotation circular baffle plate by lower activity O-ring seal, lower rotation circular baffle plate is located at outside lower hollow cylinder
There is the first circular hole at ring, there is third circular hole at lower hollow cylinder inner ring, the first circular hole and third circular hole adhere to two sectors separately
Cylinder, lower hollow cylinder outer ring have an adsorbed gas import, and lower hollow cylinder inner ring has a cooling gas import, adsorbed gas import with
First circular hole communicates, and cooling gas import is communicated with third circular hole, and upper rotation circular baffle plate, which is located at upper hollow cylinder outer ring, to be had
Second circular hole has the 5th circular hole at upper hollow cylinder inner ring, is located at the 4th circular hole at upper hollow cylinder middle ring, the second circle
Hole, the 5th circular hole and the 4th circular hole adhere to three fan-shaped cylinders separately, and upper hollow cylinder outer ring has purified gas outlet, upper hollow cylinder
Middle ring has desorption gas outlet, upper hollow cylinder inner ring to have cooling gas outlet, purified gas outlet to communicate with the second circular hole, cold
But gas vent is communicated with the 4th circular hole, and desorption gas outlet is communicated with the 5th circular hole, and center rotating shaft is connected with driving equipment,
The medial surface of cylindrical tube arranges 3 groups of heating rods, and solid absorbent import is installed on the top of cylindrical tube, and lower part is installed solid and inhaled
Attached dose of outlet.
Silk screen under further being installed between lower rotation circular baffle plate and absorber, regenerator and cooler, in upper rotation
Silk screen is installed between circular baffle plate and absorber, regenerator and cooler, to prevent adsorbent material leakage.
Absorber (20), regenerator (21) and cooler (22) are to be recycled.
By adjust driving equipment realize be rotated up and down the revolving speed of circular baffle plate realize gas continuous absorption, regenerate,
Cooling circulation.
Adsorbent described further includes organic, organic and inorganic, inorganic solid absorbent.Wherein organic adsorbs
Agent specifically includes that the amines such as tetraethylenepentamine (TEPA), polyethyleneimine (PEI), pentaethylene hexamine (PEHA), six ethylene, seven amine
Material；Organic and inorganic adsorbent mainly includes: TEPA support type, PEI support type, PEHA support type, six ethylene, seven amine support type
(porous materials such as carrier MCM-41, SBA15, mesoporous silicon) TEPA grafting-type, PEI grafting-type, PEHA grafting-type, six ethylene seven
Amine grafting-type and metal organic framework (MOF) (Mg-MOF-74, Ni-MOF-74, grafting amine type MOF material)；Inorganic absorption
Agent specifically includes that modified activated carbon, molecular sieve, houghite, alkali carbonate, alkaline earth metal carbonate, potassium/magnesium-based load
Type adsorbent (carrier Al2O3, the materials such as mesoporous silicon).
The utility model is suitable for the purified treatment of various normal pressure light concentration gas, especially suitable for carbonated, two
The purified treatment of the gases such as sulfur oxide, hydrogen sulfide, nitrogen oxides and organic pollutant (VOCs).
The step adsorbed gas and adsorbent as described above adsorption temp in cylindrical tube absorber is 50-80oC；Again
Desorption temperature is 100-400 in raw device oC, temperature can be controlled by the power of heating rod；Temperature in cooler is 50-80oC, can be by the flow control of cooling gas.
The utility model has the advantages that
(1) using novel rotating circulating adsorption-desorption integration acquirer may be implemented gas it is continuous absorption, regenerate,
Cooling cycle realizes the continuity of adsorption operations, makes adsorption separation process from intermittently becoming continuous, shortens adsorption-desorption week
Phase, high degree of automation.
(2) a kind of method and device for being generally applicable to gas purification is provided, the scope of application is wider.
(3) operation of equipment, letter easy to use are realized by adjusting the revolving speed of driving equipment realization rotation circular baffle plate
It is single, reduce investment outlay and reduce operation energy consumption.
Detailed description of the invention
Fig. 1 is novel rotating circulating adsorption-desorption integration acquirer structural schematic diagram；
Fig. 2 is A-A view in Fig. 1；
Fig. 3 is B-B view in Fig. 1；
Fig. 4 is the process flow diagram that gas purification is carried out using rotating circulating adsorption-desorption integration acquirer.
It is as shown in the figure:
1 it is adsorbed gas import, 2 be purified gas outlet, 3 be cooling gas import, 4 be cooling gas outlet, 5 is de-
Attached gas vent, 6(7,8) be solid absorbent import, 9(10,11) be solid absorbent outlet, 12(13,14) it is hand hole, 15
Be center rotating shaft, 16 be electrically heated rod, 17 be bracket, 18 be driving equipment, 19 be lower rotation circular baffle plate, 20 be absorption
Device, 21 be regenerator, 22 be cooler, 23 be lower hollow cylinder outer ring, 24 be lower hollow cylinder middle ring, 25 be lower hollow cylinder
Inner ring, 26 be upper rotation circular baffle plate, 27 be upper hollow cylinder outer ring, 28 be upper hollow cylinder middle ring, 29 be upper hollow cylinder
Inner ring, 30 be lower open circles band of column fixed plate, 31 be the recessed circle of lower movable sealing, 32 be the recessed circle of upper movable sealing, 33(34) be axis
Hold, 35(36,37) be partition, 38 be lower activity O-ring seal, 39 be upper activity O-ring seal, 40 be lower screen cloth, 41 be on
Sieve composition, 42 are upper hollow cylinder ring fixed plates.
It is purification gas, c be cooling gas, d be that cooling gas, e are desorption gas, a1 is out that a, which is mixed gas, b,
It is third circular hole, d4 be the 4th circular hole, e5 is the 5th circular hole that one circular hole, b2, which are the second circular hole, c3,.
Specific embodiment
The integrated acquirer of Novel rotary circulation absorption desorption of the invention is described with reference to the drawings as follows:
Embodiment 1:
A kind of rotating circulating adsorption desorption integration acquirer of the utility model, it includes cylindrical tube 43, adsorbed gas into
Mouth 1, purified gas outlet 2, cooling gas import 3, cooling gas outlet 4, desorption gas export 5, solid absorbent import 6
(7,8), solid absorbent export 9(10,11), have center rotating shaft 15 at 43 center of cylindrical tube, center rotating shaft 15 with
There are three pieces of partition 35(36,37) between cylindrical tube 43, is divided into identical three fans by partition 35(36,37) by cylindrical tube 43
Absorber 20, regenerator 21 and the cooler 22 of shape cylinder, the upper surface of cylindrical tube 43 and upper hollow cylinder ring fixed plate 42
It is welded to connect, the lower end surface of cylindrical tube 43 and lower open circles band of column fixed plate 30 are welded to connect, and are fixed in upper hollow cylinder ring
Between plate 42 and absorber 20, regenerator 21 and cooler 22 with upper rotation circular baffle plate 26, in lower open circles band of column fixed plate
There are lower rotation circular baffle plate 19, upper rotation circular baffle plate 26 and backspin between 30 and absorber 20, regenerator 21 and cooler 22
Turn circular baffle plate 19 to connect with center rotating shaft 15, cylindrical tube 43 and upper rotation circular baffle plate 26 pass through the recessed circle of upper movable sealing
32 connections pass through recessed 31 connection of circle of lower movable sealing, the lower open circles band of column between cylindrical tube 43 and lower rotation circular baffle plate 19
Fixed plate 30 has lower hollow cylinder outer ring 23, lower hollow cylinder middle ring 24 and lower hollow cylinder inner ring 25, and upper hollow cylinder ring is solid
Fixed board 42 have upper hollow cylinder outer ring 27, upper hollow cylinder middle ring 28, upper hollow cylinder inner ring 29,
Upper hollow cylinder outer ring 27, upper hollow cylinder middle ring 28, upper hollow cylinder inner ring 29 are kept off with upper rotation circle respectively
It is connected between plate 26 by upper activity O-ring seal 39, lower hollow cylinder outer ring 23, lower hollow cylinder middle ring 24 and lower open circles
Column inner ring 25 is connect between lower rotation circular baffle plate 19 by lower activity O-ring seal 38 respectively, lower rotation circular baffle plate 19
There is the first circular hole a1 at lower hollow cylinder outer ring 23, there is third circular hole c3, the first circle at lower hollow cylinder inner ring 25
Hole a1 and third circular hole c3 adheres to two fan-shaped cylinders separately, and lower hollow cylinder outer ring 23 has an adsorbed gas import 1, in lower hollow cylinder
Ring 25 has cooling gas import 3, and adsorbed gas import 1 is communicated with the first circular hole a1, cooling gas import 3 and third circular hole c3 phase
Logical, upper rotation circular baffle plate 26, which is located at upper hollow cylinder outer ring 27, the second circular hole b2, is located at upper hollow cylinder inner ring 29
There is the 5th circular hole e5, is located at the 4th circular hole d4, the second circular hole b2, the 5th circular hole e5 and the 4th circular hole at upper hollow cylinder middle ring 28
D4 adheres to three fan-shaped cylinders separately, and upper hollow cylinder outer ring 27 has purified gas outlet 2, upper hollow cylinder middle ring 28 to have desorption gas
Outlet 5, upper hollow cylinder inner ring 29 have cooling gas outlet 4, purified gas outlet 2 to communicate with the second circular hole b2, cooling gas
Outlet 4 is communicated with the 4th circular hole d4, and desorption gas outlet 5 is communicated with the 5th circular hole e5, center rotating shaft 15 and driving equipment 18
It is connected, medial surface 3 groups of heating rods 16 of arrangement of cylindrical tube, the top installation solid absorbent import 6(7 of cylindrical tube 43,
8), lower part installation solid absorbent outlet 9(10,11).
Silk screen under further being installed between lower rotation circular baffle plate 19 and absorber 20, regenerator 21 and cooler 22
40, silk screen 41 is installed between upper rotation circular baffle plate 26 and absorber 20, regenerator 21 and cooler 22, to prevent from adsorbing
Agent material leakage.
The revolving speed of circular baffle plate is rotated up and down by the adjusting realization of driving equipment 18 to realize that the continuous of gas adsorbs, again
Raw, cooling circulation.
60 Nm of this example proposed adoption3The flue gas of/h carries out decarburization experiment (CO2: 15 vol%, air: 85vol%), adsorbent
For pentaethylene hexamine support type (PEHA) adsorbent, adsorption temp 60 oC, desorption temperature is 100 in regenerator oC, cooling air
Using air, cooling temperature 60 oC.This example outside cylinder barrel diameter is 1500 mm, height: 1000 mm；Upper and lower open circles
The height of the band of column is 250 mm, and the diameter of the inner ring of the upper and lower open circles band of column, middle ring and outer ring is followed successively by 600 mm, 900 mm
With 1200 mm；Being rotated up and down the time that circular baffle plate rotation is turned around is 15 min, can be carried out continuously absorption, regeneration and cooling
Circular integration operation.It is 100 mm, the diameter of e5 that the pore size for being rotated up and down circular baffle plate, which is the diameter of a1, b2, c3, d4,
For 50 mm.
60 Nm3The mixed flue gas a of/h is entered in lower open circles band of column outer ring 23 by adsorbed gas import 1, then passes through backspin
The circular hole a1 corresponding with adsorbed gas import 1 for turning to open up in circular baffle plate 19 enters in the absorber 20 of cylindrical tube, with
PEHA type CO2Solid absorbent contact, adsorption temp 60oC, the CO in flue gas2It is adsorbed by adsorbent, purified flue gas b
By opening up circular hole b2 corresponding with purified gas outlet 2 in upper rotation circular baffle plate 26 into upper hollow cylinder ring outer ring 27
In, it is emptied by purified gas outlet 2, the CO in purifying smoke at this time2For concentration less than 1 vol%, adsorption time is 5 min；
The adsorbent of adsorption saturation at this time enters regeneration stage, and regeneration heat source is provided by heating rod 16, and desorption temperature is controlled 100 oC,
The CO of absorption2Due to being heated disengaging adsorbent, the gas e of desorption is discharged by hole e5 in upper rotation circular baffle plate 26
In open circles band of column middle ring 28, recycled by 5 discharge of desorption gas outlet, CO in desorption gas at this time2Concentration is greater than 95
Vol%, desorption time are 5 min；The adsorbent finished is desorbed and enters cooling stage, cooling gas c passes through cooling gas import 3
Into in lower open circles band of column inner ring 25, enters in cooler 22 by the hole c3 in lower rotation circular baffle plate 19, pass through cooling
Adsorbent is purged, by adjusting cooling gas flow, the temperature of adsorbent is made to be reduced to 60 oC, gas d after cooling is through upper rotation
The hole d4 turned in circular baffle plate 26 enters in upper hollow cylinder ring inner ring 29, and by 4 emptying of cooling gas outlet, cooling time is
5 min；Adsorbent after cooling just with corresponding circular hole a1, b2 in rotation circular baffle plate 19,26 to upper, repeats at this time
The continuous absorption of circulation, cooling and detachment assays (see attached drawing 4).
Embodiment 2:
Novel rotary circulation absorption desorbs integrated acquirer structure with example 1
50 Nm of this example proposed adoption3The flue gas of/h carries out desulfurization (SO2: 2000 ppm, remaining be air), adsorbent
For acticarbon, adsorption temp 70 oC, desorption temperature is 120 in regenerator oC, cooling temperature 70 oC.Rotation follows
Ring adsorption-desorption integration acquirer outer barrel diameter is determined according to gaseous mixture treating capacity, this example outside cylinder barrel diameter is
1000 mm, height: 600 mm；The height of the upper and lower open circles band of column is 200 mm, the inner ring of the upper and lower open circles band of column, middle ring with
And the diameter of outer ring is followed successively by 400 mm, 600 mm and 800 mm；Being rotated up and down the time that circular baffle plate rotation is turned around is 24
Min can be carried out continuously the circular integration operation of absorption, regeneration and cooling.Be rotated up and down circular baffle plate pore size be a1,
The diameter of b2, c3, d4 are 50 mm, and the diameter of e5 is 25 mm.
50 Nm3The mixed flue gas a of/h is entered in lower open circles band of column outer ring 23 by adsorbed gas import 1, passes through lower rotation
The circular hole a1 corresponding with adsorbed gas import 1 opened up in circular baffle plate 19 enters in the absorber 20 of cylindrical tube, with work
Property charcoal solid absorbent contact, adsorption temp 70oC, the SO in flue gas2It is adsorbed by adsorbent, purified flue gas b passes through upper
Circular hole b2 corresponding with purified gas outlet 2 is opened up in rotation circular baffle plate 26 to enter in upper hollow cylinder ring outer ring 27, is led to
Cross the emptying of purified gas outlet 2, the SO in purifying smoke at this time2For concentration less than 2 ppm, adsorption time is 8 min；It inhales at this time
The adsorbent of attached saturation enters regeneration stage, and regeneration heat source is provided by heating rod 16, and desorption temperature is controlled 120 oC, absorption
SO2Due to being heated disengaging adsorbent, the gas e of desorption is discharged into upper open circles by hole e5 in upper rotation circular baffle plate 26
In column middle ring 28, recycled by 5 discharge of desorption gas outlet, SO in desorption gas at this time2Concentration is greater than 1995 ppm, desorption
Time is 8 min；The adsorbent finished is desorbed and enters cooling stage, cooling gas c is hollow under being entered by cooling gas import 3
In cylinder inner ring 25, enter in cooler 22 by the hole c3 in lower rotation circular baffle plate 19, purges adsorbent by cooling, lead to
Cooling gas flow is overregulated, the temperature of adsorbent is made to be reduced to 70 oC, gas d after cooling are through in upper rotation circular baffle plate 26
Hole d4 enter upper hollow cylinder inner ring 29 in, by cooling gas outlet 4 emptying, cooling time be 8 min；Suction after cooling
Attached dose, at this time just with corresponding circular hole a1, b2 in rotation circular baffle plate 19,26 to upper, repeats to recycle continuous absorption, cold
But with detachment assays (see attached drawing 4).
Embodiment 3:
Novel rotary circulation absorption desorbs integrated acquirer structure with example 1
20 Nm of this example proposed adoption3The flue gas of/h carry out desulfurization (toluene: 1000 ppm, remaining be nitrogen), absorption
Agent is molecular sieve MCM41, adsorption temp 30 oC, desorption temperature is 150 in regenerator oC, cooling temperature 70 oC.Rotation follows
Ring adsorption-desorption integration acquirer outer barrel diameter is determined according to gaseous mixture treating capacity, this example outside cylinder barrel diameter is
800 mm, height: 500 mm；The height of the upper and lower open circles band of column is 150 mm, the inner ring of the upper and lower open circles band of column, middle ring and
The diameter of outer ring is followed successively by 320 mm, 480 mm and 640 mm；Being rotated up and down the time that circular baffle plate rotation is turned around is 27 min,
The circular integration operation of absorption, regeneration and cooling can be carried out continuously.Be rotated up and down circular baffle plate pore size be a1, b2,
The diameter of c3, d4 are 40 mm, and the diameter of e5 is 20 mm.
20 Nm3The mixing VOCs gas a of/h is entered in lower hollow cylinder outer ring 23 by adsorbed gas import 1, passes through backspin
The circular hole a1 corresponding with adsorbed gas import 1 for turning to open up in circular baffle plate 19 enters in the absorber 20 of cylindrical tube, with
The contact of molecular sieve MCM41 solid absorbent, adsorption temp 30oC, the toluene mixed in VOCs is adsorbed by adsorbent, after purification
Gas b by opening up circular hole b2 corresponding with purified gas outlet 2 in upper rotation circular baffle plate 26 into upper hollow cylinder
It in outer ring 27, is emptied by purified gas outlet 2, less than 5 ppm, adsorption time is the toluene concentration in purification gas at this time
9 min；The adsorbent of adsorption saturation at this time enters regeneration stage, and regeneration heat source is provided by heating rod 16, and desorption temperature control exists
150 oThe toluene of C, absorption are arranged due to being heated disengaging adsorbent, the gas e of desorption by hole e5 in upper rotation circular baffle plate 26
Enter in upper hollow cylinder middle ring 28 out, is recycled by 5 discharge of desorption gas outlet, toluene concentration is big in desorption gas at this time
In 990 ppm, desorption time is 9 min；The adsorbent finished is desorbed and enters cooling stage, cooling gas c passes through cooling gas
Import 3 enters in lower hollow cylinder inner ring 25, enters in cooler 22 by the hole c3 in lower rotation circular baffle plate 19, by cold
But adsorbent is purged, by adjusting cooling gas flow, the temperature of adsorbent is made to be reduced to 30 oC, gas d after cooling is through upper
The hole d4 rotated in circular baffle plate 26 enters in upper hollow cylinder inner ring 29, and by 4 emptying of cooling gas outlet, cooling time is
9 min；Adsorbent after cooling just with corresponding circular hole a1, b2 in rotation circular baffle plate 19,26 to upper, repeats at this time
The continuous absorption of circulation, cooling and detachment assays (see attached drawing 4).
Claims (3)
1. a kind of rotating circulating adsorption desorption integration acquirer, it includes cylindrical tube (43), adsorbed gas import (1), purification
Gas vent (2), cooling gas import (3), cooling gas outlet (4), desorption gas outlet (5), solid absorbent import (6,
7,8), solid absorbent outlet (9,10,11), it is characterised in that have center rotating shaft (15) at cylindrical tube (43) center,
There are three pieces of partitions (35,36,37) between center rotating shaft (15) and cylindrical tube (43), by partition (35,36,37) by cylindrical drum
Body (43) is divided into absorber (20), regenerator (21) and the cooler (22) of identical three fan-shaped cylinders, cylindrical tube (43)
Upper surface and upper hollow cylinder ring fixed plate (42) be welded to connect, the lower end surface of cylindrical tube (43) and the lower open circles band of column are solid
Fixed board (30) is welded to connect, in upper hollow cylinder ring fixed plate (42) and absorber (20), regenerator (21) and cooler (22)
Between have upper rotation circular baffle plate (26), in lower open circles band of column fixed plate 30 and absorber (20), regenerator (21) and cooling
There are lower rotation circular baffle plate (19), upper rotation circular baffle plate (26) and lower rotation circular baffle plate (19) and center to turn between device (22)
Moving axis (15) connection, cylindrical tube (43) are connect with upper rotation circular baffle plate 26 by the recessed circle (32) of upper movable sealing, cylindrical drum
It is connect between body (43) and lower rotation circular baffle plate (19) by the recessed circle (31) of lower movable sealing, lower open circles band of column fixed plate
(30) there are lower hollow cylinder outer ring (23), lower hollow cylinder middle ring (24) and lower hollow cylinder inner ring (25), upper hollow cylinder ring
Fixed plate (42) has upper hollow cylinder outer ring (27), upper hollow cylinder middle ring (28), upper hollow cylinder inner ring (29), upper open circles
Column outer ring (27), upper hollow cylinder middle ring (28), upper hollow cylinder inner ring (29) are respectively between upper rotation circular baffle plate (26)
It is connected by upper activity O-ring seal (39), lower hollow cylinder outer ring (23), lower hollow cylinder middle ring (24) and lower hollow cylinder
Inner ring (25) is connect between lower rotation circular baffle plate (19) by lower activity O-ring seal (38) respectively, the round gear of lower rotation
Plate (19), which is located at lower hollow cylinder outer ring (23), the first circular hole (a1), and being located at lower hollow cylinder inner ring (25) has third circle
Hole (c3), the first circular hole (a1) and third circular hole (c3) adhere to two fan-shaped cylinders separately, and lower hollow cylinder outer ring (23) has adsorbed gas
Body import (1), lower hollow cylinder inner ring (25) have cooling gas import (3), adsorbed gas import (1) and the first circular hole (a1) phase
Logical, cooling gas import (3) is communicated with third circular hole (c3), and upper rotation circular baffle plate (26) is located at upper hollow cylinder outer ring (27)
Place has the second circular hole (b2), and being located at upper hollow cylinder inner ring (29) has the 5th circular hole (e5), is located at upper hollow cylinder middle ring
(28) the 4th circular hole (d4) at, the second circular hole (b2), the 5th circular hole (e5) and the 4th circular hole (d4) adhere to three fan-shaped cylinders separately, on
Hollow cylinder outer ring (27) has purified gas outlet (2), upper hollow cylinder middle ring (28) to have desorption gas outlet (5), upper hollow
Cylinder inner ring (29) has cooling gas outlet (4), purified gas outlet (2) to communicate with the second circular hole (b2), cooling gas outlet
(4) it is communicated with the 4th circular hole (d4), desorption gas outlet (5) is communicated with the 5th circular hole (e5), center rotating shaft (15) and driving
Equipment (18) is connected, and the medial surface of cylindrical tube arranges 3 groups of heating rods (16), and solid absorption is installed on the top of cylindrical tube (43)
Solid absorbent outlet (9,10,11) is installed in agent import (6,7,8), lower part.
2. a kind of rotating circulating adsorption desorption integration acquirer as described in claim 1, it is characterised in that the lower round gear of rotation
Lower silk screen (40) are installed, in upper rotation circular baffle plate between plate (19) and absorber (20), regenerator (21) and cooler (22)
(26) silk screen (41) are installed between absorber (20), regenerator (21) and cooler (22).
3. a kind of rotating circulating adsorption desorption integration acquirer as described in claim 1, it is characterised in that absorber (20), again
Raw device (21) and cooler (22) are to be recycled.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821079817.2U CN209451571U (en) | 2018-07-09 | 2018-07-09 | A kind of rotating circulating adsorption desorption integration acquirer |
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| CN201821079817.2U CN209451571U (en) | 2018-07-09 | 2018-07-09 | A kind of rotating circulating adsorption desorption integration acquirer |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113330958A (en) * | 2021-06-25 | 2021-09-03 | 西安交通大学 | Greenhouse carbon dioxide concentration adjusting system and method based on carbon capture |
| CN116348412A (en) * | 2020-06-09 | 2023-06-27 | 全球温控营运有限责任公司 | Continuous motion direct air trapping system |
-
2018
- 2018-07-09 CN CN201821079817.2U patent/CN209451571U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116348412A (en) * | 2020-06-09 | 2023-06-27 | 全球温控营运有限责任公司 | Continuous motion direct air trapping system |
| CN113330958A (en) * | 2021-06-25 | 2021-09-03 | 西安交通大学 | Greenhouse carbon dioxide concentration adjusting system and method based on carbon capture |
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