CN108079750A - A kind of gas absorption capturing device - Google Patents
A kind of gas absorption capturing device Download PDFInfo
- Publication number
- CN108079750A CN108079750A CN201810000452.8A CN201810000452A CN108079750A CN 108079750 A CN108079750 A CN 108079750A CN 201810000452 A CN201810000452 A CN 201810000452A CN 108079750 A CN108079750 A CN 108079750A
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- CN
- China
- Prior art keywords
- liquid
- tank body
- tube
- controller
- forcing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 99
- 238000005273 aeration Methods 0.000 claims abstract description 26
- 239000003463 adsorbent Substances 0.000 claims abstract description 19
- 239000012530 fluid Substances 0.000 claims abstract description 17
- 238000001179 sorption measurement Methods 0.000 claims abstract description 17
- 238000009826 distribution Methods 0.000 claims abstract description 12
- 230000005540 biological transmission Effects 0.000 claims description 9
- 238000001727 in vivo Methods 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 2
- 230000000274 adsorptive effect Effects 0.000 abstract description 15
- 230000000630 rising effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 30
- 229910000831 Steel Inorganic materials 0.000 description 14
- 239000010959 steel Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000002440 industrial waste Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 241000790917 Dioxys <bee> Species 0.000 description 1
- 241000277275 Oncorhynchus mykiss Species 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 210000005239 tubule Anatomy 0.000 description 1
Classifications
-
- 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
- B01D53/14—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 absorption
- B01D53/1412—Controlling the absorption process
-
- 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
- B01D53/14—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 absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
Abstract
The invention discloses a kind of gas absorption capturing devices, are made of air outlet pipe, liquid-level controller, head cover, outlet tube, sponge adsorbent equipment, inlet tube, filter screen, fluid cushion area, liquid outlet groove, aeration tube, gas absorption area, collection chamber, air inlet pipe, check-valves, force (forcing) pump, controller, conducting wire, tank body, check-valves and liquid distribution plate；Force (forcing) pump is controlled by controller, adsorptive liquid to be controlled to be flowed from bottom to top in adsorption tanks, the adsorptive liquid of overflow is flowed out at the top of adsorption tanks by outlet tube through go out liquid house steward；It is delivered gas to by aeration tube in adsorption tanks, during rising, is adsorbed and collected by sponge adsorbent equipment, and carry out subsequent processing；Gas not to be adsorbed excludes to collect after in collection chamber collecting through air outlet pipe, and carries out subsequent processing, meanwhile, the inside and outside air pressure balance of tank body is adjusted by air outlet pipe.
Description
Technical field
The present invention relates to a kind of devices for being used to adsorbing and trapping ease of solubility gas in laboratory or actual production.
Background technology
In recent years, due to industrial expansion and social progress, industrial waste gas is more and more, the dioxy discharged such as chemical fertilizer factory
Change nitrogen, hydrogen sulfide, the sulfur dioxide of smeltery's discharge, carbon monoxide, carbon dioxide etc..Industrial waste gas is to the destruction of environment
It is well-known.These substances enter the internal of people by different approach respiratory tracts, and some directly generates harm, and some also has
Cumulative effect, can the more serious health for endangering people.At present, industry is mainly three kinds to the administering method of industrial waste gas.The
First, absorption process, is exactly using the pollutant in liquid handling flue gas exhaust gas, exhaust gas is made to be contacted with liquid, in admixture of gas
One or more components are dissolved in liquid, achieve the purpose that purification.Such method device therefor is miscellaneous absorption tower.
Since various toxic and harmful gas properties are different, different solubility, it is impossible to fundamentally solve the problems, such as to remove exhaust gas.Second
It is dynamic wave against spray rinsing method, from industrial smoke from top to bottom into the reverse jet tube of straight barrel type, and absorbing liquid is from bottom to top
Injection, inversely contacts with gas, and froth zone is formed in tower, and flue gas passes through foam contacting, and absorbing liquid constantly cycles.It is anti-according to user
It reflects, such method operating cost is high, and still emission is in air.The third is electron radiation-chemicalpurification, utilizes height
Each component in the activation of energy electron ray, ionization, cracking exhaust gas, so as to which the series of chemical such as oxidation occur, by pollutant
It is converted into uncontamination object.Such method is equally of high cost, it is impossible to is widely accepted, it is difficult to promotion and implementation.To solve above-mentioned ask
Topic, therefore, the present invention develop a kind of gas absorption capturing device, and the apparatus structure is simple, economic and environment-friendly, convenient for promoting the use of.
The content of the invention
It is an object of the invention to develop one kind in laboratory or actual production for adsorbing and trap ease of solubility gas
Device, device low manufacture cost, operation is easy, applied widely, uses and promotes convenient for popularization.
To achieve these goals, agent structure of the invention includes air outlet pipe, liquid-level controller, head cover, outlet tube, sea
Continuous adsorbent equipment, inlet tube, filter screen, fluid cushion area, liquid outlet groove, aeration tube, gas absorption area, collection chamber, top aeration
Hole, bottom solarization air cap, inlet manifold, air inlet, check-valves, force (forcing) pump, controller, conducting wire, tank body, check-valves and liquid distribution plate group
Into：One tank body is set, one inlet tube is set in the bottom of tank body, a check-valves is set before inlet tube, only
It returns and a force (forcing) pump is set before valve, one filter screen is set in the in vivo inlet tube exit of tank, is pacified in the bottom of tank body
A liquid distribution plate is filled, tank body is divided into fluid cushion area and gas adsorption zone two parts, is opened up out on liquid distribution plate by liquid distribution plate
Liquid bath sets an aeration tube in the top of each liquid outlet groove, and the solarization air cap at the top of the setting of the upper surface of aeration tube is exposing
The lower surface of tracheae sets bottom solarization air cap, compared with the solarization air cap of top, arrangement and the arrangement relatively sparse one of bottom solarization air cap
A bit.One check-valves on each aeration tube on the outside of tank body is all set, an inlet manifold is set, by air inlet with exposing
Tracheae is connected, and in the top of aeration tube sponge adsorbent equipment arranged in a crossed manner, an outlet tube is set above tank body, in tank body
Top sets a head cover, and a fluid level controller is set in the lower part of arch head cover, and arch head cover and fluid level controller enclose
Into a collection chamber, fluid level controller is connected by conducting wire with controller, and controller is connected by conducting wire with force (forcing) pump, works as tank body
Interior liquid level after controller is connected to the alarm signal of liquid-level controller, is transmitted to force (forcing) pump and instructed, lead to more than after liquid-level controller
It overregulates the uninterrupted of force (forcing) pump or opens, stops controlling the in vivo liquid of tank, prevent liquid from largely entering collection chamber.Encircleing
The top of shape head cover sets an air outlet pipe, for excluding the residual gas after adsorbing and trapping.
Sponge adsorbent equipment is by going out liquid branch pipe, liquid collection opening, collecting pipe, control shaft, cavernous body, motor, transmission device and hair
Tubule forms, wherein, transmission device is made of driven gear and driving gear；One driving gear is set, in driving gear
Both sides all set a driven gear respectively, one control shaft of rigidity installation on each driven gear, in each control
One cavernous body is all installed, two cavernous bodies are in inverted v-shaped on axis.The positive and negative rotation of driving gear can drive driven gear
It rotates, and then the swing of cavernous body is driven by control shaft, opened so as to fulfill the inverted v-shaped structure that two cavernous bodies enclose
And closure.Some capillaries are set in each cavernous body, and capillary surface sets many ventholes, all capillaries
It is connected by liquid collection opening with collecting pipe, all by going out liquid branch pipe, to import out liquid total for the outlet tube on all collecting pipe and tank body
Pipe is collected by go out liquid house steward and discharged.Motor, the quantity of motor and the sponge adsorbent equipment of tank interior are installed in the outside of tank body
It corresponds, by the shaft of motor after transmission device adjusts rotating speed, is rigidly connected with driving gear, the positive and negative rotation of motor
The positive and negative rotation of driving gear can be driven, and then the inverted v-shaped structure opening and closing that two cavernous bodies is controlled to enclose.
When carrying out gas absorption trapping work, adsorptive liquid, the liquid level liquid level of adsorptive liquid are filled in tank body
Controller flushes, and force (forcing) pump is controlled by controller, and to control the flowing of adsorptive liquid, the adsorptive liquid in fluid cushion room leads to
It crosses liquid outlet groove and enters adsorption tanks, flowed from bottom to top in adsorption tanks, the adsorptive liquid of overflow is at the top of adsorption tanks by going out
Liquid pipe is flowed out through go out liquid house steward, and carries out subsequent processing；By the driving gear of sponge adsorbent equipment and driven gear by sponge
Body is adjusted to best angle, meanwhile, delivered gas to by aeration tube in adsorption tanks, and by solarization air cap come accelerate gas with
The mixing of liquid during gas and adsorptive liquid rise in adsorption tanks, is adsorbed and collected by sponge adsorbent equipment, sea
Adsorptive liquid in continuous body successively through capillary, collecting pipe, go out liquid branch pipe and go out liquid house steward flows out, and carry out subsequent processing；Not
The gas adsorbed excludes to collect after in collection chamber collecting through air outlet pipe, and carries out subsequent processing, meanwhile, by air outlet pipe come
Adjust the inside and outside air pressure balance of tank body.
Description of the drawings
Fig. 1 is the agent structure principle schematic of the present invention.
Fig. 2 is the agent structure A-A sectional views of the present invention.
Fig. 3 is the aeration tube top view of the present invention.
Fig. 4 is the aeration tube bottom view of the present invention.
Fig. 5 is the agent structure B-B sectional views of the present invention.
Fig. 6 is the sponge adsorbent equipment principle schematic diagram of the present invention.
Fig. 7 is the sponge adsorbent equipment side view of the present invention.
Specific embodiment
Below in conjunction with the accompanying drawings and pass through embodiment and be further described.
Embodiment：
The agent structure of the present embodiment include air outlet pipe 1, liquid-level controller 2, head cover 3, outlet tube 4, sponge adsorbent equipment 5, into
Liquid pipe 6, filter screen 7, fluid cushion area 8, liquid outlet groove 9, aeration tube 10, gas absorption area 11, collection chamber 12, top solarization air cap
21st, bottom solarization air cap 22, inlet manifold 26, air inlet 27, check-valves 28, force (forcing) pump 29, controller 30, conducting wire 31, tank body 32,
Check-valves 33 and liquid distribution plate 34 form：The steel tank 32 of 3000cm wide 2000cm high 3000cm one long is set, in tank body 32
Bottom set a diameter 30cm steel inlet tube 6, before inlet tube 6 set a check-valves 33, in check-valves
The force (forcing) pump 29 of 50cm wide 50cm high 50cm one long is set before 33, and 6 exit of inlet tube in tank body 32 sets one
The steel filter net 7 of a diameter 30cm installs the steel cloth liquid of 3000cm wide 2000cm thickness 2cm one long in the bottom of tank body 32
Tank body 32 is divided into 11 two parts of fluid cushion area 8 and gas adsorption zone, six is opened up on liquid distribution plate 34 by plate 34, liquid distribution plate 34
The liquid outlet groove 9 of the long 1600cm wide 20cm of item sets the steel of a root long 1800cm diameters 25cm in the top of each liquid outlet groove 9
Aeration tube 10 processed sets the top solarization air cap 21 of diameter 3cm in the upper surface of aeration tube 10, is set in the lower surface of aeration tube 10
The bottom solarization air cap 22 of diameter 3.5cm, compared with top solarization air cap 21, arrangement and the arrangement relatively sparse one of bottom solarization air cap 22
A bit.A check-valves 28 is all set on each aeration tube 10 in 32 outside of tank body, the air inlet for setting a diameter 50cm is total
Pipe 26 is connected by the air inlet 27 of diameter 25cm with aeration tube 10,17 arranged in a crossed manner long in the top of aeration tube 10
The sponge adsorbent equipment 5 of 1900cm wide 30cm sets the steel outlet tube 4 of a diameter 30cm, in tank body above tank body 32
32 top sets the arc steel head cover 3 of an arc length 4000cm high 50cm, is set in the lower part of arch head cover 3 one long
The fluid level controller 2 of 3000cm wide 20cm, arch head cover 3 and fluid level controller 2 enclose a collection chamber 12, fluid level controller
2 are connected by conducting wire 31 with the controller 30 of long 1000cm wide 500cm high 1000cm, and controller 30 passes through conducting wire 31 and force (forcing) pump
29 are connected, after the liquid level in tank body 32 is more than liquid-level controller 2, after controller 30 is connected to the alarm signal of liquid-level controller 2,
It transmits and instructs to force (forcing) pump 29, by adjusting the uninterrupted of force (forcing) pump 29 or opening, stop controlling the liquid in tank body 32, prevent
Liquid largely enters collection chamber 12.The air outlet pipe 1 of one diameter 45cm is set at the top of arch head cover 3, for excluding to pass through
Cross the later residual gas of adsorbing and trapping.
Sponge adsorbent equipment 5 by go out liquid branch pipe 14, liquid collection opening 15, collecting pipe 16, control shaft 17, cavernous body 18, motor 19,
Transmission device 20 and capillary 23 form, wherein, transmission device 20 is made of driven gear 24 and driving gear 25；Set one
The steel driving gear 25 of diameter 8cm all sets the steel driven gear of a diameter 4cm in the both sides of driving gear respectively
24, rigidity installs the steel control shaft 17 of 3cm wide 4cm one long on each driven gear 24, in each control shaft 17
On the cavernous body 18 of 1900cm wide 10cm one long is all installed, two cavernous bodies 18 are in inverted v-shaped.The rotating of driving gear 25
The dynamic rotation that can drive driven gear 24, and then by the swing of the drive cavernous body 18 of control shaft 14, so as to fulfill two seas
The inverted v-shaped structure opening and closing that continuous body 18 encloses.Some long 15cm diameters 2cm are set in each cavernous body 18
Steel capillary 23,23 surface of capillary sets many ventholes, the liquid collection opening 15 that all capillaries 23 pass through diameter 2cm
It is connected with the steel collecting pipe 16 of diameter 3cm, the outlet tube 4 on all collecting pipe 16 and tank body 32 all passes through diameter 5cm's
Steel goes out the steel go out liquid house steward 13 that liquid branch pipe 14 imports diameter 45cm, and discharge is collected by go out liquid house steward 13.In the outer of tank body 32
The steel motor 19 of 17 diameter 6cm is installed in side, and the quantity of motor 19 and the sponge adsorbent equipment 5 one inside tank body 32 are a pair of
Should, by the shaft of motor 19 after transmission device 20 adjusts rotating speed, it is rigidly connected with driving gear 25, the rotating of motor 19
Kinetic energy drives the positive and negative rotation of driving gear 25, and then the inverted v-shaped structure open and close that two cavernous bodies 18 is controlled to enclose
It closes.
When carrying out gas absorption trapping work, adsorptive liquid, the liquid level liquid of adsorptive liquid are filled in tank body 32
Face controller 2 flushes, and force (forcing) pump 29 is controlled by controller 30, to control the flowing of adsorptive liquid, the suction in liquid damper chamber 8
Attached liquid body enters adsorption tanks 11 by liquid outlet groove 9, is flowed from bottom to top in adsorption tanks 11, the adsorptive liquid of overflow is in adsorption tanks
11 top is flowed out by outlet tube 4 through go out liquid house steward 13, and carries out subsequent processing；Pass through the driving tooth of sponge adsorbent equipment 5
Cavernous body 18 is adjusted to best angle by wheel 25 and driven gear 24, meanwhile, adsorption tanks are delivered gas to by aeration tube 10
In 11, and accelerate the mixing of gas and liquid by solarization air cap, in the mistake that gas and adsorptive liquid rise in adsorption tanks 11
Cheng Zhong is adsorbed and collected by sponge adsorbent equipment 5, the adsorptive liquid in cavernous body 18 successively through capillary 23, collecting pipe 16, go out
Liquid branch pipe 14 and go out liquid house steward 13 flow out, and carry out subsequent processing；Gas not to be adsorbed collect in collection chamber 12 after through going out
Tracheae 1 excludes to collect, and carries out subsequent processing, meanwhile, 32 inside and outside air pressure balance of tank body is adjusted by air outlet pipe 1.
Claims (2)
1. a kind of gas absorption capturing device, which is characterized in that inhaled by air outlet pipe, liquid-level controller, head cover, outlet tube, sponge
Adsorption device, inlet tube, filter screen, fluid cushion area, liquid outlet groove, aeration tube, gas absorption area, collection chamber, top solarization air cap, bottom
Portion's solarization air cap, inlet manifold, air inlet, check-valves, force (forcing) pump, controller, conducting wire, tank body, check-valves and liquid distribution plate composition：If
A tank body is put, one inlet tube is set in the bottom of tank body, a check-valves is set before inlet tube, in check-valves
Front sets a force (forcing) pump, sets a filter screen in the in vivo inlet tube exit of tank, one is installed in the bottom of tank body
Tank body is divided into fluid cushion area and gas adsorption zone two parts, liquid outlet groove is opened up on liquid distribution plate by liquid distribution plate, liquid distribution plate,
The top of each liquid outlet groove sets an aeration tube, the solarization air cap at the top of the setting of the upper surface of aeration tube, in aeration tube
Lower surface sets bottom solarization air cap, and compared with the solarization air cap of top, the arrangement of bottom solarization air cap is relatively more sparse with arranging；In tank
A check-valves is all set on each aeration tube of external side, an inlet manifold is set, passes through air inlet and aeration tube phase
Even, in the top of aeration tube sponge adsorbent equipment arranged in a crossed manner, an outlet tube above tank body is set, is set at the top of tank body
A head cover is put, one fluid level controller is set in the lower part of arch head cover, arch head cover and fluid level controller enclose one
Collection chamber, fluid level controller are connected by conducting wire with controller, and controller is connected by conducting wire with force (forcing) pump, when the in vivo liquid of tank
It after controller is connected to the alarm signal of liquid-level controller, transmits and instructs to force (forcing) pump, pass through adjusting more than after liquid-level controller in face
The uninterrupted of force (forcing) pump is opened, stops controlling the in vivo liquid of tank, prevents liquid from largely entering collection chamber；In arch head cover
Top set an air outlet pipe, for excluding the residual gas after adsorbing and trapping.
2. a kind of gas absorption capturing device according to claim 1, which is characterized in that sponge adsorbent equipment is by going out liquid branch
Pipe, liquid collection opening, collecting pipe, control shaft, cavernous body, motor, transmission device and capillary composition, wherein, transmission device is by driven
Gear and driving gear composition；One driving gear is set, one driven gear is all set respectively in the both sides of driving gear,
One control shaft of rigidity installation, installs a cavernous body, two sponges in each control shaft on each driven gear
Body is in inverted v-shaped；The positive and negative rotation of driving gear can drive the rotation of driven gear, and then drive cavernous body by control shaft
Swing, the inverted v-shaped structure opening and closing enclosed so as to fulfill two cavernous bodies；It is set in each cavernous body
Some capillaries, capillary surface set many ventholes, and all capillaries are connected by liquid collection opening with collecting pipe, all
Outlet tube on collecting pipe and tank body all imports go out liquid house steward by going out liquid branch pipe, is collected and discharged by go out liquid house steward；In tank body
Motor is installed in outside, and the quantity of motor and the sponge adsorbent equipment of tank interior correspond, by the shaft of motor by transmission
After device adjustment rotating speed, it is rigidly connected with driving gear, the positive and negative rotation of motor can drive the positive and negative rotation of driving gear, and then
The inverted v-shaped structure opening and closing that two cavernous bodies of control enclose.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810000452.8A CN108079750A (en) | 2018-01-02 | 2018-01-02 | A kind of gas absorption capturing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810000452.8A CN108079750A (en) | 2018-01-02 | 2018-01-02 | A kind of gas absorption capturing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108079750A true CN108079750A (en) | 2018-05-29 |
Family
ID=62181478
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810000452.8A Pending CN108079750A (en) | 2018-01-02 | 2018-01-02 | A kind of gas absorption capturing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108079750A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115112787A (en) * | 2022-05-31 | 2022-09-27 | 永春县产品质量检验所(福建省香产品质量检验中心、国家燃香类产品质量监督检验中心(福建)) | Polycyclic aromatic hydrocarbon detection method |
| CN117205718A (en) * | 2023-08-21 | 2023-12-12 | 青岛理工大学 | Capturing and fixing CO 2 Composite material of (2), preparation method and CO 2 Absorption device |
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| CN1443593A (en) * | 2002-03-07 | 2003-09-24 | 刘乃瑞 | Gas cleaning device and its method |
| US6652627B1 (en) * | 2002-10-30 | 2003-11-25 | Velocys, Inc. | Process for separating a fluid component from a fluid mixture using microchannel process technology |
| CN101757835A (en) * | 2009-12-29 | 2010-06-30 | 西南大学 | Vibrating gas collector |
| CN104383709A (en) * | 2014-11-27 | 2015-03-04 | 天津奥展兴达化工技术有限公司 | Low-resistance efficient column tray |
| CN104492210A (en) * | 2014-11-22 | 2015-04-08 | 中北大学 | Flue gas desulfurization and dust removal technology and integrated apparatus applicable to ship |
| CN207871862U (en) * | 2018-01-02 | 2018-09-18 | 青岛理工大学 | A kind of gas absorption capturing device |
-
2018
- 2018-01-02 CN CN201810000452.8A patent/CN108079750A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1443593A (en) * | 2002-03-07 | 2003-09-24 | 刘乃瑞 | Gas cleaning device and its method |
| US6652627B1 (en) * | 2002-10-30 | 2003-11-25 | Velocys, Inc. | Process for separating a fluid component from a fluid mixture using microchannel process technology |
| CN101757835A (en) * | 2009-12-29 | 2010-06-30 | 西南大学 | Vibrating gas collector |
| CN104492210A (en) * | 2014-11-22 | 2015-04-08 | 中北大学 | Flue gas desulfurization and dust removal technology and integrated apparatus applicable to ship |
| CN104383709A (en) * | 2014-11-27 | 2015-03-04 | 天津奥展兴达化工技术有限公司 | Low-resistance efficient column tray |
| CN207871862U (en) * | 2018-01-02 | 2018-09-18 | 青岛理工大学 | A kind of gas absorption capturing device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115112787A (en) * | 2022-05-31 | 2022-09-27 | 永春县产品质量检验所(福建省香产品质量检验中心、国家燃香类产品质量监督检验中心(福建)) | Polycyclic aromatic hydrocarbon detection method |
| CN115112787B (en) * | 2022-05-31 | 2024-01-12 | 永春县产品质量检验所(福建省香产品质量检验中心、国家燃香类产品质量监督检验中心(福建)) | Detection method of polycyclic aromatic hydrocarbon |
| CN117205718A (en) * | 2023-08-21 | 2023-12-12 | 青岛理工大学 | Capturing and fixing CO 2 Composite material of (2), preparation method and CO 2 Absorption device |
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