CN207641281U - Supergravity carbonator - Google Patents
Supergravity carbonator Download PDFInfo
- Publication number
- CN207641281U CN207641281U CN201720863177.3U CN201720863177U CN207641281U CN 207641281 U CN207641281 U CN 207641281U CN 201720863177 U CN201720863177 U CN 201720863177U CN 207641281 U CN207641281 U CN 207641281U
- Authority
- CN
- China
- Prior art keywords
- hypergravity
- flue gas
- supply unit
- carbonator
- alkaline matter
- 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.)
- Expired - Fee Related
Links
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000003546 flue gas Substances 0.000 claims abstract description 36
- 239000007787 solid Substances 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 23
- 238000000926 separation method Methods 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 13
- 230000000694 effects Effects 0.000 claims description 12
- 230000001105 regulatory effect Effects 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 6
- 238000001179 sorption measurement Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 4
- 230000005484 gravity Effects 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims 1
- 230000020477 pH reduction Effects 0.000 claims 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 26
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 12
- 239000001569 carbon dioxide Substances 0.000 abstract description 12
- 230000008901 benefit Effects 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 210000004027 cell Anatomy 0.000 description 19
- 229960004424 carbon dioxide Drugs 0.000 description 10
- 239000002910 solid waste Substances 0.000 description 4
- 230000001133 acceleration Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000005431 greenhouse gas Substances 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 239000010882 bottom ash Substances 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 210000000635 valve cell Anatomy 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The utility model relates to a catch device of carbon dioxide in flue gas, in particular to, it relates to an utilize hypergravity carbonator, with a component homodisperse that contains alkaline substance in the device, carry out the carbonation with a flue gas that contains carbon dioxide, form a through handling flue gas to reach the purpose of getting rid of carbon dioxide in the flue gas. The utility model comprises a supergravity carbonator, a mixing unit and a liquid-solid separating unit. The utility model has the advantages of higher carbonation efficiency, smaller device occupation area and lower operation cost.
Description
Technical field
The utility model is related to a kind of devices of capture carbon dioxide in flue gas, and hypergravity carbonic acid is utilized especially in regard to a kind of
Makeup is set, and a kind of component comprising alkaline matter is dispersed in the device, and wrapping carbonated flue gas with a kind of
Carbonation is carried out, formation is a kind of through handling flue gas, to achieve the purpose that remove carbon dioxide in flue gas.
Background technology
In industry or the flue gas that discharges of power plant, mostly containing greenhouse gases (such as：Carbon dioxide etc.), if this is contained
The flue gas of carbon dioxide is directly discharged into air, can probably aggravate the rate of global warming, therefore, before such flue gas emission, palpus
It is handled, carbon dioxide separation contained therein is captured, to reduce potential hazard of the greenhouse gases to environment by appropriate device.
On the other hand, industry or power plant are normal with a large amount of alkali solid waste outputs, such as：Clinker, flying dust, bottom ash and sludge
Deng, such alkali solid waste usually contain high-activity compound (such as：Free state calcium oxide, free state magnesia etc.),
Content is differed between 0.1% to 15%, and recycling must carry out a stabilization program before applying.
In recent years, carbonation reaction is accelerated to have attracted much attention, because it is in combination in such alkali solid waste and flue gas two
Carbonoxide, reduces the content of high-activity compound in alkali solid waste, and reduces the discharge of smoke carbon dioxide, has aobvious
Write environmental benefit.However, effectively to promote the rate and processing capacity that accelerate carbonation reaction, high temperature/height is often used in document
The high-pressure cooker of pressure, or be installed on using the slurry reactive tank of normal pressure up to being carried out under the time of a few hours, it can be only achieved
Preferable carbonation efficiencies.Such acceleration carbonator needs larger floor space more, and expends time and mass energy place to go
Reason, causes such device cost higher.
In view of above-mentioned, existing acceleration carbonator have the shortcomings that as greenhouse gases capture device it is above-mentioned, therefore
It is necessary to design acceleration carbonation apparatus that is a kind of novel and can solving at least one prior art disadvantage.
Invention content
The purpose of this utility model is to provide the devices that a kind of high efficiency captures carbon dioxide in flue gas, compare known
Accelerate carbonating capture carbon dioxide plant, this is novel have that carbonation efficiencies are higher, plant area is smaller and operating cost compared with
Low advantage.
Then, the utility model hypergravity carbonator, for a kind of component comprising alkaline matter to be dispersed in this
In device, carbonation is carried out with a kind of carbonated flue gas of packet, formation is a kind of through handling flue gas, to reach smoke abatement
The purpose of carbon dioxide in gas.The hypergravity carbonator includes：
One hypergravity carbonation reactor, including one overweight for being acted on the flue gas for the alkaline matter component
Power reative cell, and include one be connected to the hypergravity reative cell and for enter for the flue gas air inlet, one to be connected to this super
Gravity reative cell and for for this through handle flue gas discharge gas outlet, one be connected to the hypergravity reative cell and for for and this
The feed inlet and the basic species for being connected to the hypergravity reative cell and being used for after confession and flue gas effect that alkaline matter group enters
The discharge port of matter component discharge；
One mixed cell, including one is used for supplying the well-mixed unit of alkaline matter component, including a connection
The mixed cell and for convey the first supply unit of the solid-state alkalinity adsorption material, one connect the mixed cell and for defeated
Give the second supply unit and a feed inlet for connecting the hypergravity carbonation reactor and for conveying of the stripping liquid
The third supply unit of the alkaline matter component, the alkaline matter component are formed in the mixed cell；And
One liquid/solid separation unit, including one is used for carrying out solid-liquor separation for the alkaline matter component after flue gas effect
Separator, including one connect the mixed cell and for convey the stripping liquid the second supply unit and a company
Connect the discharge port and for conveying the 4th supply unit of the alkaline matter component after flue gas effect.
What the utility model reached has technical effect that：The hypergravity carbonator is implemented by structure design one
It is that the solid-state alkalinity adsorption material is delivered in the mixed cell through first supply unit in example, which should
Stripping liquid is delivered in the mixed cell, has by the mixed cell solid matter and liquid phase substance forming one uniformly
The function of phase is thoroughly mixed to form the alkaline matter.
Description of the drawings
Fig. 1 is a schematic diagram of embodiment described in the utility model.
Specific implementation mode
Fig. 1 is the preferred embodiment of the utility model hypergravity carbonator, wherein：
The unit of solid-liquor separation includes the connection mixed cell 2 and is used for conveying the second conveying list of the stripping liquid
First 32, discharge ports 15 for connecting the hypergravity carbonation reactor and for conveying the alkaline matter group after flue gas effect
Point the 4th supply unit 34, and for convey separation after solid-state alkalinity adsorption material the 6th supply unit 36.The solid-liquor separation
Unit 5 is installed on 1 lower section of hypergravity carbonation reactor, which is passed through gravity stream
Mode is sent via the 4th supply unit 34 to the liquid/solid separation unit 5 from the discharge port 15 of the hypergravity carbonation reactor.
In this embodiment, which is delivered to the solid-state alkalinity sorbing material in the mixed cell 2,
The stripping liquid is delivered in the mixed cell 2 by second supply unit 32, is had solid formation using the mixed cell 2
Matter is mixed to form homogeneous function with liquid phase substance, is sufficiently mixed and forms it into the alkaline matter component.Third conveying is single
The alkaline matter component 33 is delivered in the hypergravity reative cell 11 by member, and the alkali is allowed by the hypergravity carbonation reactor 1
Property material composition and the smoke contacts, and carbonation reaction is carried out in the hypergravity reative cell 11, while strengthening solid phase, liquid phase
And the microring array efficiency that gas phase etc. three is alternate so that the utility model hypergravity carbonator can within shorter time of contact,
High-carbon is obtained under normal pressure and is acidified efficiency, to reach the purpose of this utility model.
Preferably, can also be as needed, it is provided in the hypergravity carbonator conducive to solid-state alkalinity suction is conveyed
The device of enclosure material and the stripping liquid.Such as in this embodiment, the control mechanism 4 include one be mounted on this first
Supply unit 31 and for control the first regulating valuve unit 41, one of the flow of the solid-state alkalinity sorbing material be mounted on this
Two supply units 32 and to be mounted on the third defeated for controlling the second regulating valuve unit 42, one of the flow of the stripping liquid
It send unit 33 and is mounted on the 4th conveying for the third regulating valuve unit 43, one for controlling the flow of the alkaline matter component
Unit 34 and for control and the flue gas effect after alkaline matter component flow the 4th regulating valuve unit 44 and one peace
The 5th of the flow of alkaline matter component after should being acted on flue gas mounted in the 5th supply unit 35 and for control section adjusts
Save valve cell 45.
The driving device 6 is separately mounted to second supply unit 32 and is located at 5 downstream of liquid/solid separation unit and is used for
Accelerate the flowing of the stripping liquid, and after should being acted on flue gas mounted on the 5th supply unit 35 and for accelerating part
The flowing of alkaline matter component.The specific example of the driving device 6 is pump.
The temperature-adjusting device 7 is mounted on second supply unit 32 and positioned at 5 downstream of driving device and for adjusting
The temperature of the stripping liquid.The specific example of the temperature-adjusting device 7 is heat exchanger.
The above, only the embodiments of the present invention cannot limit the scope of the utility model, every basis with this
Simple equivalent changes and modifications made by the claims and description of the present utility model application, all still belong to
In the range of the utility model patent covers.
Claims (10)
1. a kind of hypergravity carbonator, for a kind of component comprising alkaline matter to be dispersed in the device, with
A kind of carbonated flue gas of packet carries out carbonation, is formed a kind of through handling flue gas, wherein the alkaline matter component by
Solid-state alkalinity sorbing material and stripping liquid are mixed and are formed, which includes：
One hypergravity carbonation reactor, including a hypergravity for being used for that the alkaline matter component is supplied to act on the flue gas are anti-
Answer room, and include one be connected to the hypergravity reative cell and for for the flue gas enter air inlet, one be connected to the hypergravity
Reative cell and for for this through handle flue gas discharge gas outlet, one be connected to the hypergravity reative cell and for for and the alkalinity
The feed inlet and an alkaline matter for being connected to the hypergravity reative cell and being used for after confession and flue gas effect that material composition enters
The discharge port of component discharge；
One mixed cell, including one is used for supplying the well-mixed unit of alkaline matter component, including one connects this and mixes
Close unit and for convey the first supply unit of the solid-state alkalinity adsorption material, one connect the mixed cell and for conveying this
Second supply unit of stripping liquid and a feed inlet for connecting the hypergravity carbonation reactor and for conveying the alkali
The third supply unit of property material composition, which formed in the mixed cell；And
One liquid/solid separation unit a, including point for being used for carrying out solid-liquor separation for the alkaline matter component after flue gas effect
From device, including one connects the mixed cell and should for the second supply unit and a connection for conveying the stripping liquid
Discharge port and the 4th supply unit for being used for conveying the alkaline matter component after flue gas effect.
2. hypergravity carbonator as described in claim 1, wherein the liquid/solid separation unit is installed on the hypergravity carbonic acid
Change below reactor, it is anti-from hypergravity carbonating by the alkaline matter component after being acted on flue gas by gravity stream mode
The discharge port of device is answered to be sent to the liquid/solid separation unit via the 4th supply unit.
3. hypergravity carbonator as described in claim 1 includes also a control mechanism, and the control mechanism further includes
One be mounted on first supply unit and for control the solid-state alkalinity adsorption material flow the first regulating valuve unit, one
Mounted on second supply unit and for control the stripping liquid flow the second regulating valuve unit and one be mounted on
The third supply unit and for control the alkaline matter component flow third regulating valuve unit.
4. hypergravity carbonator as described in claim 1, further includes one and be used for after transport portion should act on flue gas
Alkaline matter component the 5th supply unit.
5. hypergravity carbonator as claimed in claim 4, wherein the 5th supply unit is additionally coupled to the hypergravity carbon
The feed inlet of acidification reactor.
6. hypergravity carbonator as claimed in claim 4, wherein the 5th supply unit further includes one and is used for driving
The driving device of alkaline matter component after flue gas effect.
7. hypergravity carbonator as described in claim 1, wherein the mixed cell further include one be mounted on this second
Supply unit and the driving device for being located at the liquid/solid separation unit downstream and being used for that the stripping liquid is accelerated to flow.
8. hypergravity carbonator as claimed in claim 7, wherein the mixed cell further include one be mounted on this second
Supply unit and positioned at the driving device downstream and for control the stripping liquid temperature temperature-adjusting device.
9. hypergravity carbonator as described in claim 1, wherein the liquid/solid separation unit further includes one and is used for conveying
6th supply unit of solid-state alkalinity adsorption material after gained reacts after separation.
10. hypergravity carbonator as described in claim 1, wherein the mixed cell is a Venturi tube, a self-priming
Formula cast feeder or a stirred tank.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW106205213U TWM554378U (en) | 2017-04-14 | 2017-04-14 | High gravity carbonation equipment |
| TW106205213 | 2017-04-14 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207641281U true CN207641281U (en) | 2018-07-24 |
Family
ID=61729837
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720863177.3U Expired - Fee Related CN207641281U (en) | 2017-04-14 | 2017-07-17 | Supergravity carbonator |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN207641281U (en) |
| TW (1) | TWM554378U (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109603720B (en) * | 2019-01-08 | 2021-03-26 | 北京化工大学 | Hypergravity oxidation reactor device and application |
| CN109647315B (en) * | 2019-01-08 | 2021-03-26 | 北京化工大学 | Hypergravity device capable of fully utilizing energy, oxidation method and system |
-
2017
- 2017-04-14 TW TW106205213U patent/TWM554378U/en not_active IP Right Cessation
- 2017-07-17 CN CN201720863177.3U patent/CN207641281U/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| TWM554378U (en) | 2018-01-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2010139168A1 (en) | Digestion circulating fluidized bed flue gas desulfurization method and device | |
| CN207641281U (en) | Supergravity carbonator | |
| CN200980986Y (en) | Circulation fluidized bed dry method smoke desulphurizing device | |
| CN203469801U (en) | Desulfurized ash-limestone mixing and slurrying device | |
| CN112915749A (en) | Semi-dry desulfurization method and system for aluminum electrolysis flue gas | |
| CN105080329A (en) | Dust removal and flue gas desulfurization and purification process and device for coke oven | |
| US20130095018A1 (en) | Up-flow fluidized bed dry scrubber and method of operating same | |
| CN100460047C (en) | Circulation fluidized bed dry method flue gas desulfur device | |
| CN204699577U (en) | A kind of semidry process desulfurizer that can reduce calcium sulfur ratio | |
| CN201572600U (en) | Waste incineration gas purification dry deacidification system | |
| CN101804293A (en) | Flue gas desulfurization method of heating boiler and device thereof | |
| CN1185041C (en) | Circular suspension type semi-dry fume purifier | |
| CN101446416A (en) | Thermal power plant boiler tail flue gas dust removal and desulfurization treatment process and device thereof | |
| CN211659676U (en) | Semidry flue gas desulfurization dust collector | |
| CN217410334U (en) | Carbon calcining furnace flue gas treatment system | |
| CN110975554A (en) | Method for flue gas desulfurization of lime rotary kiln by using kiln tail ash | |
| CN216093000U (en) | Semi-dry desulfurization system for aluminum electrolysis flue gas | |
| CN221342169U (en) | Slaked lime storage and slurry preparation system | |
| CN101670237B (en) | Method and device for desulfurizing and dechlorinating flue gas of circulating fluidized bed | |
| CN218249506U (en) | Boiler flue gas wet desulphurization process system | |
| CN101036855A (en) | Circled dry phase flow tower flue gas desulphurizaion technique | |
| CN210993738U (en) | Semidry flue gas desulfurization dust collector | |
| CN115350573B (en) | High-sulfur flue gas desulfurization method | |
| CN217746472U (en) | Roasting flue gas desulfurization dust removal equipment | |
| CN201930710U (en) | Magnesium desulfurization system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180724 Termination date: 20190717 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |