CN106466551A - A kind of apparatus system being applied to flue gas and powder hybrid reaction - Google Patents
A kind of apparatus system being applied to flue gas and powder hybrid reaction Download PDFInfo
- Publication number
- CN106466551A CN106466551A CN201510500745.9A CN201510500745A CN106466551A CN 106466551 A CN106466551 A CN 106466551A CN 201510500745 A CN201510500745 A CN 201510500745A CN 106466551 A CN106466551 A CN 106466551A
- Authority
- CN
- China
- Prior art keywords
- powder
- nozzle
- flue gas
- storage tank
- reactor
- 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.)
- Granted
Links
Abstract
The present invention relates to flue gases purification field is and in particular to a kind of apparatus system being applied to flue gas and powder hybrid reaction.A kind of apparatus system being applied to flue gas and powder hybrid reaction, including reactor, its top is provided with powder entrance, bottom is provided with powder outlet, the sheathed chuck of outer wall, it is provided with the air-flow chamber for flue gas circulation between the inwall of chuck and the outer wall of reactor, reactor inner chamber passes through bottom opening UNICOM air-flow chamber, the top of reactor side wall is provided with gas approach, and the top of jacket side wall is provided with exhanst gas outlet；Chuck bottom opening connects downwards blanking pipe, is provided with the adsorbent chamber of Venturi tube, the outside steam line of Venturi tube air inlet connection, gas outlet UNICOM feeding pipe below blanking pipe.Due to adopting technique scheme, present invention, avoiding mechanical gas lock short life, easily blocking, easily produced the problem of corrosion after vapour corrosion, the broken bridge effect of storage tank ensure that storing quality and conveying effect.
Description
Technical field
The present invention relates to flue gases purification field is and in particular to one kind is applied to flue gas and powder mixing is anti-
The apparatus system answered.
Background technology
In the existing apparatus system for powder with flue gas hybrid reaction, the storage tank depositing powder is in powder
Fall and carry out in external transport process, powder is easily deposited in tank base, be particularly easy to moisture absorption
Powder easily forms lump after being moistened so that accumulation situation is particularly acute.For this in traditional scheme
The solution of problem is generally dredged using compressed-air blows or mechanical agitation, and this kind of scheme exists
Following shortcoming：1) in the mode short time of compressed-air blows, there is certain effect, but because compression is empty
Moisture can be mixed into unavoidably in gas, blow long lasting for supply, after so that moisture is accumulated in tank body with
In tank, powder mixes and gradually absorbs for it, thus aggravating the powder caking situation in tank body；2) machinery stirs
Although mixing mode effect preferably, the design of its apparatus structure is complicated, volume is larger, longtime running energy consumption
Height, initial stage input cost and longtime running cost using mechanical agitation mode are all higher.
In addition, the powder body being used in conventional apparatus system in powder and the reactor of flue gas mixing is in circulation
It is circulated the airtight of pipeline and the control of powder carry distribution frequently with mechanical type gas lock.This structure exists
Following shortcoming：1), when adopting obturation effect preferable mechanical type gas lock, the processing for gas lock and cooperation are smart
Degree requires higher, easily causes that gas lock is stuck or accelerated wear test in the case that lump formed by powder；2)
During using the general or poor mechanical type gas lock of crudy and quality of fit, obturation effect is poor, holds
It is also easy to produce gas leak phenomenon.
Content of the invention
It is an object of the invention to, a kind of apparatus system being applied to flue gas and powder hybrid reaction is provided,
Solve above technical problem.
Technical problem solved by the invention can employ the following technical solutions to realize：
A kind of apparatus system being applied to flue gas and powder hybrid reaction, including a reactor, powder and cigarette
Gas reacts after the mixing of its inner chamber, and the harmful substance in flue gas is eliminated in the reaction, and its feature exists
In described reactor is the reactor of upright tubular structure, and its top is provided with the powder for inputting powder
Entrance, its bottom be provided with for export powder powder outlet, the sheathed chuck of its outer wall, chuck interior
Form an air-flow chamber supplying flue gas circulation, reaction after keeping at a certain distance away between wall and the outer wall of reactor
Kettle inner chamber passes through bottom opening UNICOM air-flow chamber, and the top of reactor side wall is provided with to be easy to input flue gas extremely
The gas approach of reactor inner chamber, the top of jacket side wall is provided with the external flue gas discharging reacted flue gas
Outlet, the flue gas containing harmful substance from gas approach enter after reactor inner chamber powder in it occur anti-
Should, the cleaning flue gases producing after reaction flow through air-flow chamber via after the discharge of reactor bottom powder outlet,
Finally discharge from exhanst gas outlet；
Chuck bottom is in the funnel structure of inverted cone body, and the lower openings of its funnel structure connect downwards one
The blanking pipe being vertically arranged, have neither part nor lot in reactor reaction or reaction incomplete residue powder from
Powder outlet falls in blanking pipe in falling on the way after discharging, and the lower section of blanking pipe is provided with a Venturi tube,
The adsorbent chamber entrance of described Venturi tube connects up described blanking pipe, the air inlet of described Venturi tube
UNICOM one is used for conveying one end of the feeding pipe of powder to the right the outside steam line of UNICOM, gas outlet to the left,
The top through circulating line UNICOM reactor for the other end of feeding pipe, is easy to, and has neither part nor lot in and reacts or anti-
Answer incomplete residue powder to come back to and in reactor, continue to participate in reaction.
The operation principle of the present invention is：The air inlet of Venturi tube after outside steam line insufflation gas,
Because Venturi effect produces negative pressure in downward pipe in blanking pipe, gas approach and exhanst gas outlet pass through
Negative pressure in direction kettle upwards is produced in reactor, in two negative pressure and kettle and blanking after setting difference in flow
The comprehensive function of the powder deadweight in pipeline determines the direction of motion of powder：1) when in pipe negative pressure and powder from
When the comprehensive function of weight is not enough to the effect of negative pressure in equilibrium still, powder is maintained at reactor and blanking pipe
Interior it is impossible to continue to drop；2) when the comprehensive function that negative pressure in pipe is conducted oneself with dignity with powder is more than the work of negative pressure in kettle
Used time, powder is inhaled into the adsorbent chamber of Venturi tube, then is ejected in feeding pipe, through circulation
Turn again to continue to participate in reaction after pipeline in reactor.Compare more conventionally employed setting in blanking pipe
Mechanical type gas lock come to limit powder whereabouts structure, the present invention has better seal performance, without load
The problem that the heart causes mechanical type gas lock stuck and weares and teares because of the moist situation with powder caking.
Described Venturi tube connects described outside steam line by flow control valve, adjusts literary composition will pass through
The air inflow of venturi is controlling the vacuum magnitude in blanking pipe.
Described feeding pipe is provided with a powder input interface, and described feeding pipe is inputted by described powder
Interface UNICOM one is used for depositing the storage tank of powder, carries out timely feed supplement will pass through storage tank to reactor.
The bottom of described storage tank is in the funnel structure of inverted cone body shape, the inclination of described storing pot bottom
Inwall is provided with the nozzle to delivery air in storage tank, and described nozzle connects an intermittence and supplies to nozzle
Pulse gas supplying device, by set interval time make pulse gas supplying device intermittent work realize nozzle to
Supply gas in a pulsed fashion in storage tank, the powder piled up using the loose inner tank wall of air pulse, and internally
On wall, the powder lump of caking carries out break process.
Described pulse gas supplying device adopts pneumatic operated valve.Before present invention work, first adjust pulse gas supplying device
Operating interval, thus supply to nozzle by pulse gas supplying device intermittence, by nozzle to storage tank
Inside supply gas in a pulsed fashion.
Described nozzle adopts nozzle between 10 degree～35 degree for the spray angle scope, it is preferred to use jet angle
Spend the nozzle for 15 degree～25 degree.
Highly it is provided with spray described at least two positioned at same level on the inwall of the funnel structure of storing pot bottom
Mouth, and the nozzle positioned at same level height is distributed in the broken bridge layer of composition one after storage tank bottom interior wall, uses
In the heap powder-deposit in storage tank is carried out loose and to powder caking crush；
The spacing distance between adjacent nozzle on same broken bridge layer is equal.
Described broken bridge layer is provided with least 2 layers.
Preferably, described broken bridge layer is provided with 2 layers～3 layers, and the spacer up and down between adjacent broken bridge layer
From equal.
Preferably, the nozzle quantity on arbitrary described broken bridge layer is 3～5.
Nozzle on same broken bridge layer is all connected with same pulse gas supplying device, by same pulse gas supplying
Device supplies, i other words, the pulse gas supplying device that working time of same broken bridge layer is connected by this layer of nozzle
Working time depending on.
The operating interval of neighbouring broken bridge layer differs 1 second～3 seconds, is 1.5 seconds preferably by difference.
Described nozzle adopts following structure setting in storage tank bottom interior wall：The centrage of arbitrary nozzle with
Angular range between the outer tangent line of circumference of broken bridge layer that it is located for this nozzle is 10 degree～75 degree, preferably
55 degree～70 degree；The centrage of arbitrary nozzle is 15 degree～35 degree with the angular range of horizontal plane, preferably
30 degree.
On vertical direction, the distance between neighbouring broken bridge layer is equal.
On neighbouring broken bridge layer, between the nozzle quantity of setting and adjacent nozzle, spacing distance is all consistent, on
Under adjacent broken bridge layer be to be dislocatedly distributed, i other words, the arbitrary nozzle on underlying arbitrary broken bridge layer
Set location the set location of corresponding nozzle is clockwise or counter-clockwise on the broken bridge layer in side thereon relatively
Turn over a special angle, the scope turning over angle is at 40 degree～130 degree, preferably 45 degree～120 degree.
The present invention by broken bridge layer is dislocatedly distributed, setting angle on each broken bridge layer for the fit with nozzle
Degree it is achieved that creating a spiral air flow environment in storage tank to realize brokenly bridge effect during nozzle operation, with
Will pass through spiral air flow realize stirring rod effect come to pile up and caking powder dredge, not only may be used
To play more preferable pulverizing and loose effect, can also effectively reduce the Blind-spot of nozzle.
When the present invention uses, it is right to realize after as needed the power cycles of pulse gas supplying device being set
The intermittent supply of nozzle, nozzle not only exists after spraying to the helical flow that the air-flow of storage tank inner chamber is formed
Ensure that brokenly bridge effect on the basis of reducing gas consumption, and be favorably improved the use of pulse gas supplying device
In the life-span, the reliability increasing system is moreover it is possible to avoid persistently supplying the problem that the powder leading to bubbles in tank.
The junction of described storage tank and described feeding pipe is provided with a metering screw conveyer, its entrance to
Upper UNICOM storage tank inner chamber, outlet downward UNICOM feeding pipe, the powder in storage tank first flows through when falling
Metering screw conveyer, more measured conveying worm delivers in feeding pipe on one's own initiative, during this,
Accurately being recorded by flow of powder, is easy to control feed supplement amount and the feeding time of storage tank.
It is provided with a valve, for controlling storage tank between described storage tank and described metering screw conveyer
Opening and closing, described valve preferably employs electromagnetic valve.
Beneficial effect：Due to adopting technique scheme, the present invention compares more traditional flue gas powder reaction dress
The system of putting has the advantage that：
1) control negative pressure amount controlling the powder in reactor to fall, it is to avoid the mechanical gas lock life-span
Short, easy blocking, easily produced the problem of corrosion after vapour corrosion；
2) the gas lock effect that Venturi tube produces is better than traditional mechanical gas lock in precision and sealing；
3) supply gas into storage tank using intermittence to form the broken bridge effect of spiral air flow and guarantee powder
Material is difficult to pile up caking it is ensured that the storing quality of storage tank and conveying effect in tank.
Brief description
Fig. 1 is the overall structure diagram of the present invention；
Fig. 2 is the partial structural diagram of Fig. 1.
Specific embodiment
In order that technological means, creation characteristic, reached purpose and effect that the present invention realizes are readily apparent from
Solution, is expanded on further the present invention with reference to being specifically illustrating.
With reference to Fig. 1, a kind of apparatus system being applied to flue gas and powder hybrid reaction, including a upright barrel shape
The reactor 1 of structure, its top is provided with powder entrance, bottom is provided with powder outlet, the sheathed chuck of outer wall,
Form the air flow chamber for flue gas circulation after keeping at a certain distance away between the outer wall of the inwall of chuck and reactor 1
Room 2, reactor inner chamber passes through bottom opening UNICOM air-flow chamber 2, and the top of reactor side wall is provided with flue gas
Import 101, the top of jacket side wall is provided with exhanst gas outlet 201.The undressed cigarette containing harmful substance
Gas inputs reactor 1 inner chamber from gas approach 101, reacts through mixing with powder therein, cigarette
Harmful substance in gas is eliminated in the reaction, and the reacted kettle bottom opening of the clean flue gas after process flows through
Air-flow chamber 2, then discharge from exhanst gas outlet 201.Chuck bottom is in the funnel structure of inverted cone body, its
The lower openings of funnel structure connect downwards the blanking pipe 3 being vertically arranged.The lower section of blanking pipe 3 is provided with
Venturi tube 4, the adsorbent chamber entrance of Venturi tube 4 connects up blanking pipe 3, the entering of Venturi tube 4
QI KOU connects outside steam line 5, gas outlet by flow control valve 501 to the left, and UNICOM is used for conveying to the right
One end of the feeding pipe 6 of powder, the other end of feeding pipe 6 is through circulating line UNICOM reactor 1
Top.Part have neither part nor lot in reaction or unreacted completely powder in clean flue gas from reactor 1 to air-flow
Drop in chamber 2 course of conveying and focus on chuck bottom and fall into again in blanking pipe 3.Feeding pipe 6
Be used for depositing the storage tank 7 of powder by powder input interface UNICOM thereon, with will pass through storage tank 7,
Feeding pipe 6, circulating line carry out timely feed supplement to reactor 1.Between feeding pipe 6 and storage tank 7
It is provided with metering screw conveyer 9, be provided with keying storage tank between metering screw conveyer 9 and storage tank 7 defeated
Go out the valve 601 of passage, valve 601 preferably employs electromagnetic valve.Have neither part nor lot in reaction or reaction is incomplete
Remaining powder comes back in reactor 1 through feeding pipe 6 and circulating line and continues to participate in reaction,
In powder circulation transport process, conveying pipeline sent into by the measured conveying worm 9 of supplementary powder of storage tank 7
In road 6, react or react incomplete residue powder with having neither part nor lot in and mix in entrance reactor 1
Participate in the reaction of next round flue gas powder.
The operation principle of the present invention is：The air inlet of Venturi tube after outside steam line insufflation gas,
Because Venturi effect produces negative pressure in downward pipe in blanking pipe, gas approach and exhanst gas outlet pass through
Negative pressure in direction kettle upwards is produced in reactor, in two negative pressure and kettle and blanking after setting difference in flow
The comprehensive function of the powder deadweight in pipeline determines the direction of motion of powder：1) when in pipe negative pressure and powder from
When the comprehensive function of weight is not enough to the effect of negative pressure in equilibrium still, powder is maintained at reactor and blanking pipe
Interior it is impossible to continue to drop；2) when the comprehensive function that negative pressure in pipe is conducted oneself with dignity with powder is more than the work of negative pressure in kettle
Used time, powder is inhaled into the adsorbent chamber of Venturi tube, then is ejected in feeding pipe, through circulation
Turn again to continue to participate in reaction after pipeline in reactor.Compare more conventionally employed setting in blanking pipe
Mechanical type gas lock come to limit powder whereabouts structure, the present invention has better seal performance, without load
The problem that the heart causes mechanical type gas lock stuck and weares and teares because of the moist situation with powder caking.
The bottom of storage tank 7 is in the funnel structure of inverted cone body shape, and its tilt internal wall is provided with to storing
The nozzle 8 of tank inner chamber delivery air, nozzle 8 connects the pulse gas supplying device that an intermittence supplies to nozzle 8,
Pulse gas supplying device adopts pneumatic operated valve.Before present invention work, first adjust the working time of pulse gas supplying device
Interval, thus being supplied to nozzle 8 by pulse gas supplying device intermittence, by nozzle 8 into storage tank with arteries and veins
The mode of punching is supplied gas, the powder piled up using air pulse loose inner tank wall, and to caking on inwall
Powder lump carries out break process.The spray angle scope of nozzle 8, between 10 degree～35 degree, is preferably adopted
The nozzle being 15 degree～25 degree with spray angle.It is located at same on the inwall of the funnel structure of storing pot bottom
Level height is provided with least two nozzles 8, and the nozzle 8 positioned at same level height is distributed in storage tank bottom
The broken bridge layer of composition one after portion's inwall, for carrying out to the heap powder-deposit in storage tank 7 loose and powder being tied
Block is crushed；The spacing distance between adjacent nozzle 8 on same broken bridge layer is equal.Broken bridge layer is provided with
At least 2 layers.Preferably, broken bridge layer is provided with 2 layers～3 layers, and between adjacent broken bridge layer between the upper and lower every
Apart from equal.Preferably, nozzle 8 quantity on arbitrary broken bridge layer is 3～5.Positioned at same broken bridge
Nozzle 8 on layer is all connected with same pulse gas supplying device, is supplied by same pulse gas supplying device, is
Say, the working time of pulse gas supplying device that working time of same broken bridge layer is connected by this layer of nozzle 8 and
Fixed.The operating interval of neighbouring broken bridge layer differs 1 second～3 seconds, is 1.5 seconds preferably by difference.
With reference to Fig. 2, nozzle 8 adopts following structure setting in storage tank bottom interior wall：Arbitrary nozzle 8
Centrage and this nozzle 8 angular range between the outer tangent line of circumference of broken bridge layer that it is located is 10 degree～75
Degree, preferably 55 degree～70 degree；The centrage of arbitrary nozzle 8 and the angular range of horizontal plane be 15 degree～
35 degree, preferably 30 degree.On vertical direction, the distance between neighbouring broken bridge layer is equal.Neighbouring
On broken bridge layer, between nozzle 8 quantity of setting and adjacent nozzle 8, spacing distance is all consistent, neighbouring
Broken bridge layer is to be dislocatedly distributed, i other words, the setting of the arbitrary nozzle 8 on underlying arbitrary broken bridge layer
On the relatively square thereon broken bridge layer in position, the set location of corresponding nozzle 8 turns over clockwise or counter-clockwise
One special angle, the scope turning over angle is at 40 degree～130 degree, preferably 45 degree～120 degree.By inciting somebody to action
Broken bridge layer is dislocatedly distributed, and setting angle on each broken bridge layer for the fit with nozzle 8 is it is achieved that nozzle 8
Create spiral air flow environment during work to realize brokenly bridge effect, will pass through spiral air flow in storage tank 7
The effect realizing stirring rod the powder piled up and lump is dredged, and not only can play more preferable powder
Broken and loose effect, can also effectively reduce the Blind-spot of nozzle.
When the present invention uses, it is right to realize after as needed the power cycles of pulse gas supplying device being set
The intermittent supply of nozzle, nozzle not only exists after spraying to the helical flow that the air-flow of storage tank inner chamber is formed
Ensure that brokenly bridge effect on the basis of reducing gas consumption, and be favorably improved the use of pulse gas supplying device
In the life-span, the reliability increasing system is moreover it is possible to avoid persistently supplying the problem that the powder leading to bubbles in tank.
The above has been shown and described ultimate principle, principal character and the advantages of the present invention of the present invention.
It should be understood by those skilled in the art that, the present invention is not restricted to the described embodiments, above-described embodiment and
Merely illustrating the principles of the invention described in description, in the premise without departing from spirit and scope of the invention
Under, the present invention also has various changes and modifications, and these changes and improvements both fall within claimed this
In bright scope.Claimed scope is by appending claims and its equivalent thereof.
Claims (10)
1. a kind of apparatus system being applied to flue gas and powder hybrid reaction, is used for making powder and cigarette including one
Gas its inner chamber mixing react after by flue gas harmful substance remove reactor it is characterised in that
Described reactor is the reactor of upright tubular structure, its top be provided with for input powder powder entrance,
Its bottom be provided with for export powder powder outlet, the sheathed chuck of its outer wall, the inwall of chuck with anti-
Form an air-flow chamber supplying flue gas circulation, reactor inner chamber after keeping at a certain distance away between the outer wall answering kettle
By bottom opening UNICOM air-flow chamber, the top of reactor side wall is provided with to be easy to input flue gas to reactor
The gas approach of inner chamber, the top of jacket side wall is provided with the external exhanst gas outlet discharging reacted flue gas；
Chuck bottom is in the funnel structure of inverted cone body, and the lower openings of its funnel structure connect downwards one
The blanking pipe being vertically arranged, the lower section of blanking pipe is provided with a Venturi tube, the suction of described Venturi tube
Attached chamber entrance connects up described blanking pipe, the air inlet outside supply of UNICOM to the left of described Venturi tube
Pipeline, gas outlet to the right UNICOM one be used for convey powder feeding pipe one end, feeding pipe another
The top through circulating line UNICOM reactor for the end.
2. a kind of apparatus system being applied to flue gas and powder hybrid reaction according to claim 1,
It is characterized in that, described feeding pipe is provided with a powder input interface, and described feeding pipe passes through described
Powder input interface UNICOM one is used for depositing the storage tank of powder；
The bottom of described storage tank is in the funnel structure of inverted cone body shape, the inclination of described storing pot bottom
Inwall is provided with the nozzle to delivery air in storage tank, and described nozzle connects an intermittence and supplies to nozzle
Pulse gas supplying device.
3. a kind of apparatus system being applied to flue gas and powder hybrid reaction according to claim 2,
It is characterized in that, described nozzle adopts nozzle between 10 degree～35 degree for the spray angle scope.
4. a kind of apparatus system being applied to flue gas and powder hybrid reaction according to claim 2,
It is characterized in that, the inwall of the funnel structure of storing pot bottom is highly provided with least two positioned at same level
Individual described nozzle, and be located at same level height nozzle be distributed in storage tank bottom interior wall after form a use
In carrying out to the heap powder-deposit in storage tank loose and broken broken bridge layer being carried out to powder caking, same broken
The spacing distance between adjacent nozzle on bridge layer is equal.
5. a kind of apparatus system being applied to flue gas and powder hybrid reaction according to claim 4,
It is characterized in that, described broken bridge layer is provided with least 2 layers, the nozzle on same broken bridge layer all with same
Pulse gas supplying device connects, and is supplied by same pulse gas supplying device, i other words, the work of same broken bridge layer
Depending on the working time of pulse gas supplying device that time is connected by this layer of nozzle.
6. a kind of apparatus system being applied to flue gas and powder hybrid reaction according to claim 5,
It is characterized in that, the operating interval of neighbouring broken bridge layer differs 1 second～3 seconds.
7. a kind of apparatus system being applied to flue gas and powder hybrid reaction according to claim 6,
It is characterized in that, described nozzle adopts following structure setting in storage tank bottom interior wall：Arbitrary nozzle
Centrage and this nozzle angular range between the outer tangent line of circumference of broken bridge layer that it is located is 10 degree～75
Degree；
The centrage of arbitrary nozzle is 15 degree～35 degree with the angular range of horizontal plane.
8. a kind of apparatus system being applied to flue gas and powder hybrid reaction according to claim 7,
It is characterized in that, on vertical direction, the distance between neighbouring broken bridge layer is equal.
9. a kind of apparatus system being applied to flue gas and powder hybrid reaction according to claim 8,
It is characterized in that, on neighbouring broken bridge layer, between the nozzle quantity of setting and adjacent nozzle, spacing distance is equal
Unanimously, neighbouring broken bridge layer is to be dislocatedly distributed, i other words, on underlying arbitrary broken bridge layer
The set location of arbitrary nozzle relatively thereon on the broken bridge layer in side the set location of corresponding nozzle clockwise or
Person turns over a special angle counterclockwise, and the scope turning over angle is at 40 degree～130 degree.
10. a kind of according to any one of claim 2 to 9 is applied to flue gas and powder hybrid reaction
Apparatus system is it is characterised in that described storage tank is provided with a metering spiral shell with the junction of described feeding pipe
Rotation conveyer, its entrance UNICOM's storage tank inner chamber, outlet downward UNICOM feeding pipe upwards；
It is provided with one between described storage tank and described metering screw conveyer to be used for controlling the opening and closing of storage tank
Valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510500745.9A CN106466551B (en) | 2015-08-14 | 2015-08-14 | A kind of apparatus system suitable for flue gas and powder hybrid reaction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510500745.9A CN106466551B (en) | 2015-08-14 | 2015-08-14 | A kind of apparatus system suitable for flue gas and powder hybrid reaction |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106466551A true CN106466551A (en) | 2017-03-01 |
| CN106466551B CN106466551B (en) | 2019-06-25 |
Family
ID=58214810
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510500745.9A Expired - Fee Related CN106466551B (en) | 2015-08-14 | 2015-08-14 | A kind of apparatus system suitable for flue gas and powder hybrid reaction |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106466551B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109225115A (en) * | 2018-09-17 | 2019-01-18 | 沈阳化工大学 | A kind of impact flow reactor of adjustable nozzle spacing |
| CN111621298A (en) * | 2020-06-05 | 2020-09-04 | 中国环境科学研究院 | Preparation process and equipment of biochar for soil improvement |
| CN115950244A (en) * | 2022-12-26 | 2023-04-11 | 广东微容电子科技有限公司 | Solid phase reaction device |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1467016A (en) * | 2002-07-12 | 2004-01-14 | 清华大学 | Flue gas desulfurizing and desaltpeterizing down flow bed reactor |
| CN101962108A (en) * | 2010-09-27 | 2011-02-02 | 中冶赛迪工程技术股份有限公司 | Tornado blowing method and cyclone device thereof |
| CN102120142A (en) * | 2010-12-22 | 2011-07-13 | 浙江天蓝环保技术有限公司 | Direct injection ash supplying device in dry powder desulfurizing agent tower |
-
2015
- 2015-08-14 CN CN201510500745.9A patent/CN106466551B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1467016A (en) * | 2002-07-12 | 2004-01-14 | 清华大学 | Flue gas desulfurizing and desaltpeterizing down flow bed reactor |
| CN101962108A (en) * | 2010-09-27 | 2011-02-02 | 中冶赛迪工程技术股份有限公司 | Tornado blowing method and cyclone device thereof |
| CN102120142A (en) * | 2010-12-22 | 2011-07-13 | 浙江天蓝环保技术有限公司 | Direct injection ash supplying device in dry powder desulfurizing agent tower |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109225115A (en) * | 2018-09-17 | 2019-01-18 | 沈阳化工大学 | A kind of impact flow reactor of adjustable nozzle spacing |
| CN109225115B (en) * | 2018-09-17 | 2024-04-16 | 沈阳化工大学 | Impinging stream reactor with adjustable nozzle spacing |
| CN111621298A (en) * | 2020-06-05 | 2020-09-04 | 中国环境科学研究院 | Preparation process and equipment of biochar for soil improvement |
| CN115950244A (en) * | 2022-12-26 | 2023-04-11 | 广东微容电子科技有限公司 | Solid phase reaction device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106466551B (en) | 2019-06-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5877250B2 (en) | Carbonation apparatus and carbonation method using the same | |
| CN106466551A (en) | A kind of apparatus system being applied to flue gas and powder hybrid reaction | |
| CN106232218A (en) | For the method making powder or bulk material and the mixture of liquid | |
| CN206374035U (en) | A kind of concrete mixer of anti-airborne dust | |
| CN205007847U (en) | Device system suitable for flue gas and powder mixing reaction | |
| CN106695576A (en) | Pre-mixing type pulsed abrasive gas-jet erosion method and device | |
| CN107142200B (en) | Dry-wet combined integrated anaerobic fermentation device and anaerobic fermentation process | |
| CN206150125U (en) | Livestock -raising automatic feed device | |
| CN208761716U (en) | A kind of ash-storing bin ash exhauster | |
| CN211944647U (en) | Storage tank | |
| KR200413773Y1 (en) | Hopper with air chamber | |
| CN206255856U (en) | A kind of powdery water treatment agent strength dosing system | |
| CN207071473U (en) | A kind of dusting device | |
| CN110871029A (en) | Desulfurization water circulating system | |
| JP3743725B2 (en) | Activated carbon slurry production apparatus and activated carbon slurry production method | |
| CN207890675U (en) | Powder storing bin equipped with auxiliary drawing mechanism | |
| CN207891403U (en) | A kind of leaching tanks easy to clean with Liquid level | |
| CN208771365U (en) | Fluidize powder body material throwing device | |
| CN218189481U (en) | Material mixing device | |
| CN109355832A (en) | A kind of dip dyeing case convenient for expecting clearly | |
| CN218821587U (en) | Rotary kiln is used in production of environmental protection ceramic pigment | |
| CN107376765A (en) | A kind of charcoal element shaping kneading pot multiple spot spray filling pitch system | |
| CN216879168U (en) | Flocculating agent preparation system | |
| CN219647195U (en) | Non-contact powder solvent mixing equipment | |
| CN217626356U (en) | Pneumatic feeding phenolic resin production device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190625 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |