CN108144414A - A kind of burnt double-circulating fluid bed desulphurization system of powder activity and method - Google Patents
A kind of burnt double-circulating fluid bed desulphurization system of powder activity and method Download PDFInfo
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- CN108144414A CN108144414A CN201810110894.8A CN201810110894A CN108144414A CN 108144414 A CN108144414 A CN 108144414A CN 201810110894 A CN201810110894 A CN 201810110894A CN 108144414 A CN108144414 A CN 108144414A
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- 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
- B01D53/02—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 adsorption, e.g. preparative gas chromatography
- B01D53/06—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 adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
- B01D53/10—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 adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds with dispersed adsorbents
- B01D53/12—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 adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds with dispersed adsorbents according to the "fluidised technique"
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/302—Sulfur oxides
Abstract
The present invention relates to flue gas pollutant sulfur dioxide removal fields, the more particularly to a kind of burnt double-circulating fluid bed desulphurization system of powder activity and method, the system is using powdered activated coke as desulfuration adsorbent, the two-part desulfurizing tower of activated carbon Sulfur capacity effective rate of utilization can be effectively improved simultaneously, by effectively controlling distribution of three kinds of cokes in circulating fluidization adsorption process, and it is acted on using the second adsorption of bag filter surface-active coke filtering layer, cycle coke is subjected to classification processing, to improve the effective rate of utilization of active coke desulphurizing process, and then improve effective Sulfur capacity of weary coke.
Description
Technical field
The present invention relates to flue gas pollutant sulfur dioxide removal field, more particularly to a kind of powder activity coke Two-way Cycle fluidisation
Bed desulphurization system and method.
Background technology
Active coke desulphurizing is a kind of flue gas desulfurization technique of resourcebility, while to pollutants such as the heavy metals in flue gas
There is apparent cooperation-removal to act on.Active coke desulphurizing technology currently on the market is mainly using moving bed absorption-heating regeneration work
Skill route, moving bed absorbing process use the amorphous pellets activated coke of higher mechanical strength, and shape is generally Φ 5-9mm diameters
Column, column activated coke inside diffusional resistance cause greatly utilization rate of inner surface low；The broken abrasion of transmission process causes mechanical damage
Losing increases operating cost；Column complex forming technology increases activated coke cost.Powder activity coke fluidised bed adsorption desulfurization is one
Kind novel active coke sulfur removal technology route, process avoids the mechanical loss that column-shaped active carbon abrasion generates, Powdered Activated Carbons
Cost is relatively low while surface utilisation opposed cylinder activated carbon improves.Powder activity coke fluid-bed sweetening technology is normally based on often
The circulating fluidized bed dry sulfur removal technology reactor types of rule, using activated coke as the sulfur removal technology of desulfurizing agent.It is recycled in activated coke
During fluid-bed sweetening, function according to the property of activated coke and in systems can be divided into fresh activity coke, cycle it is burnt and
Weary coke, wherein fresh activity coke refer to fresh preparation or by activated coke of the regeneration with fresh adsorption capacity；The burnt fingering of cycle
Enter system, at least undergo in a tower and adsorb, be captured and separate into deduster, to send desulfurizing tower back to and continue to adsorb
Activated coke；Weary coke, which refers at least to undergo in a tower, to be adsorbed, and transmitting system is wanted to carry out regenerated activated coke.Regular circulation fluidizes
In bed adsorption form, there are problems that cycle is burnt and weary coke can not be efficiently separated.As a kind of fluidization of patent of invention is lived
Property charcoal combined desulfurization and denitrification process, application number 201010189427.2, disclose fresh activity coke and cycle coke send to desulfurization
Tower bottom is carried along into deduster by rising flue gas, and the activated coke detached through deduster, a part, which sends back to continue cycling through in tower, to be made
With a part of discharge system is regenerated as weary coke.Under this form, it is weary it is burnt be that mix can not with cycle coke
Separation, there is the activated coke not being utilized effectively in weary coke, reduce the effective Sulfur capacity of entirety of activated coke.
Invention content
The above problem of moving bed process and fluidized-bed process in desulfurization technology is adsorbed for existing activated coke, the present invention carries
For a kind of burnt double-circulating fluid bed desulphurization system of powder activity and method, which adsorbed using powdered activated coke as desulfurization
Agent, while the two-part desulfurizing tower of activated coke effective rate of utilization can be effectively improved, by effectively controlling three kinds of cokes circulating fluidized
Change the distribution in adsorption process, and acted on using the second adsorption of bag filter surface-active coke filtering layer, cycle coke is carried out
Classification is handled, to improve the effective rate of utilization of active coke desulphurizing process, and then improve effective Sulfur capacity of weary coke.
In order to solve problem above, the technical scheme is that：
The burnt double-circulating fluid bed desulphurization system of a kind of powder activity, including desulfurizing tower, fresh coke bin, the burnt inertial separation of cycle
Device and cloth bag separator, wherein,
The desulfurizing tower includes epimere and hypomere, is connected between epimere and hypomere by inner member, and inner member is used to prevent
Activated coke in epimere is fallen into hypomere；The bottom of hypomere is provided with gas inlet and weary burnt discharge structure；
The fresh coke bin is connect with epimere, for adding fresh activity coke into epimere；The top of epimere is burnt with cycle
The import connection of inertia separator, the epimere of solid outlet and desulfurizing tower for recycling burnt inertia separator connect, and recycle burnt inertia
The gas vent of separator is connect with cloth bag separator, and the solid outlet of cloth bag separator and the hypomere of desulfurizing tower connect.
For fresh coke bin for storing fresh activity coke, fresh activity coke adsorption capacity is stronger, and fresh activity coke is directly sent
Enter the epimere of desulfurizing tower, made up using the burnt stronger adsorption capacity of fresh activity because the pollutant concentration in the flue gas of top reduces
Caused by adsorption rate reduce situation.And weary burnt outlet is not provided in epimere, it can be burnt too early to avoid fresh activity
Be exhausted from system.
The burnt inertia separator of cycle is burnt for detaching cycle, and passes through primary cycle coke feed component and follow the level-one of capture
Ring coke sends the epimere of desulfurizing tower back to, recycles part cycle coke, cycle coke is avoided to be discharged too early, be conducive to improve cycle
Burnt utilization rate；The separative efficiency of the burnt inertia separator of cycle is designed according to Desulfurization generally according to not higher than 90%.
Bag filter is for detaching the activated coke that the burnt inertia separator of cycle is not kept completely separate, and by the activated coke of separation
Send the hypomere of desulfurizing tower back to.Bag filter dust removal process can persistently form in filter material surface and update activated coke filtering layer, the filter
Layer and flue gas continuous contact, play flue gas certain desulfurization effect, on the one hand improve the desulfuration efficiency of flue gas, the opposing party
Face can improve the effective rate of utilization of activated coke.The activated coke that bag filter separates is drained into the hypomere of desulfurizing tower, with
The smoke contacts being passed through carry out first grade desulfurizing to flue gas.Due to be passed through desulfurizing tower hypomere sulfur dioxide in flue gas content compared with
It is more, even if the adsorption capacity of activated coke is declined, still there is preferable once desulfurization effect to flue gas.Moreover, it is discharged into hypomere
In activated coke adsorb a large amount of sulfur dioxide after, most of activated coke has had changed into weary coke, by this part it is weary it is burnt discharge, can be with
It avoids, by the burnt discharge, and the activated coke in the desulfurizing tower that timely updated too early of fresh burnt or cycle, being conducive to improve activated coke
Sulfur capacity and desulfuration efficiency.
Preferably, it is connected between the inner member and the epimere of desulfurizing tower by divergent segment, the fresh coke bin and desulfurization
Being located above divergent segment for the epimere of tower connects at 1-2 meters.Be conducive to supplement fresh activity coke into desulfurizing tower epimere, and effectively
Prevent excessive fresh activity coke from carrying out desulfurizing tower by flue gas.
Preferably, the bottom of the epimere of the solid outlet and desulfurizing tower of the burnt inertia separator of the cycle connects.For inciting somebody to action
The cycle of capture is burnt to be added in the bottom of desulfurizing tower epimere, make cycle coke first with the smoke contacts from hypomere, this part cigarette
The concentration of sulfur dioxide in gas is higher, and the rate of adsorption of the burnt sulfur dioxide higher to concentration of cycle is very fast.By the burnt suction of cycle
The concentration of attached sulfur dioxide in flue gas further reduces, easily preferably fresh by adsorption capacity when passing through fresh coke
Coke absorption, effectively increases the utilization rate of activated coke and the desulfuration efficiency of flue gas.
Preferably, the bottom of the hypomere of the desulfurizing tower sets the second divergent segment, the solid outlet of the bag filter
With top 1-2 meters of the second divergent segment at connect, and pass through the central axle portion that activated coke is sent to the hypomere of desulfurizing tower by conduit
Position.
Activated coke is sent to the central shaft position of the hypomere of desulfurizing tower, flue gas is flowed up from the bottom of desulfurizing tower, is held
Activated coke is easily blown, the contact area of flue gas and activated coke is improved, improves the desulfurization effect to flue gas.
Preferably, the weary burnt discharge structure includes tower body, collection flitch component and flue gas injection tube, and collection flitch component includes
Several collection flitch, several collection flitch may be contained within inside tower body, and be symmetrical arranged on the section of tower body；Flue gas injection tube
It is set on the axis of tower body；
Tower body inner wall, collection flitch component and flue gas injection tube surround several funnel-shaped structures, each funnel-form knot jointly
The weary burnt outlet of bottommost setting of structure.
Flue gas is entered by smoke inlet in desulfurizing tower, and the activated coke in desulfurizing tower hypomere is blown afloat, and amount of activated coke exists
Under the barrier effect of desulfurization inner wall of tower, along desulfurization inner wall of tower slide downward, fall into funnel-shaped structure, when in funnel-shaped structure
When activated coke runs up to certain altitude, weary coke can be discharged by weary burnt outlet, realize timely updating for activated coke.
Preferably, the shape for integrating flitch is tablet or arc.
It is further preferred that collection flitch and the angle of horizontal direction be not less than 60 °, preferably 60-85 °, further preferably
It is 65 ° -75 °.
Preferably, the quantity for integrating flitch is even number.
Preferably, the weary burnt outlet is provided with slide valve.
It is further preferred that lock gas batcher is connect under the slide valve.Locking gas batcher can will be in bucket-shaped structure
Activated coke discharges desulfurizing tower, while ensures not having on gas to go here and there, and two stand lock gas batchers, which can be connected, depending on concrete condition makes
To ensure air-tightness.
Preferably, the upper end of the flue gas injection tube is higher by the lowermost end 1-3m of tower body.
It is further preferred that the 1/3-1/2 of a diameter of tower body diameter of flue gas injection tube.
It is further preferred that the top of the funnel-shaped structure and the upper end of flue gas injection tube are substantially flush.
Preferably, the tower body updip oblique cutting enters to tilt feed pipe, tilts the upper end of feed pipe and is connected to tower body outlet
Cyclone separator solid outlet connection, the lower end for tilting feed pipe extends to the upper end of flue gas injection tube.Convenient for by whirlwind
The powder activity coke of separator separation is sent to the upper end of flue gas injection tube, is recycled.
Preferably, the height of the tower body is 15-30m.
Using the sulfur method of the burnt double-circulating fluid bed desulphurization system of the powder activity, include the following steps：
Flue gas after dedusting is from the cycle coke contact desulfuriation in the hypomere that the lower part of desulfurizing tower is flowed up with desulfurizing tower, so
After continue up flowing, flow in the epimere of desulfurizing tower, contacted successively with the cycle coke in desulfurizing tower epimere and fresh coke, take off
Sulphur；
The activated coke carried during flue gas outflow desulfurizing tower epimere flows through the burnt inertia separator of cycle and is partially separated, and detaches
Obtained cycle coke is added into the epimere of desulfurizing tower；
Flue gas after the burnt inertia separator separation of cycle flows through bag filter, and the cycle coke in flue gas is in bag-type dust
The filter material surface of device forms the activated coke filtering layer constantly updated, and flue gas is contacted with activated coke filtering layer, realizes the secondary desulfuration of flue gas,
Activated coke after secondary desulfuration is collected by bag filter, and is added to the hypomere of desulfurizing tower.
Preferably, it is 70-90% to recycle the burnt inertia separator separative efficiency burnt to the cycle in flue gas.
Beneficial effects of the present invention are：
For fresh coke bin for storing fresh activity coke, fresh activity coke adsorption capacity is stronger, and fresh activity coke is directly sent
Enter the epimere of desulfurizing tower, made up using the burnt stronger adsorption capacity of fresh activity because the pollutant concentration in the flue gas of top reduces
Caused by adsorption rate reduce situation.And weary burnt outlet is not provided in epimere, it can be burnt too early to avoid fresh activity
Be exhausted from system.
The burnt inertia separator of cycle is burnt for detaching cycle, and passes through primary cycle coke feed component and follow the level-one of capture
Ring coke sends the epimere of desulfurizing tower back to, recycles part cycle coke, cycle coke is avoided to be discharged too early, be conducive to improve cycle
Burnt utilization rate；The separative efficiency of the burnt inertia separator of cycle is designed according to Desulfurization generally according to 70%-90%.
Bag filter is for detaching the activated coke that the burnt inertia separator of cycle is not kept completely separate, and by the activated coke of separation
Send the hypomere of desulfurizing tower back to.Bag filter dust removal process can persistently form in filter material surface and update activated coke filtering layer, the filter
Layer and flue gas continuous contact, play flue gas certain desulfurization effect, on the one hand improve the desulfuration efficiency of flue gas, the opposing party
Face can improve the effective rate of utilization of activated coke.The activated coke that bag filter separates is drained into the hypomere of desulfurizing tower, with
The smoke contacts being passed through carry out first grade desulfurizing to flue gas.Due to be passed through desulfurizing tower hypomere sulfur dioxide in flue gas content compared with
It is more, even if the adsorption capacity of activated coke is declined, still there is preferable once desulfurization effect to flue gas.Moreover, it is discharged into hypomere
In activated coke adsorb a large amount of sulfur dioxide after, most of activated coke has had changed into weary coke, by this part it is weary it is burnt discharge, can be with
It avoids, by the burnt discharge, and the activated coke in the desulfurizing tower that timely updated too early of fresh burnt or cycle, being conducive to improve activated coke
Sulfur capacity and desulfuration efficiency.
Description of the drawings
The accompanying drawings which form a part of this application are used for providing further understanding of the present application, and the application's shows
Meaning property embodiment and its explanation do not form the improper restriction to the application for explaining the application.
Fig. 1 is the structural diagram of the present invention；
Fig. 2 is the side view figure structure schematic representation of the weary burnt discharge structure of the present invention.
Wherein, 1, fresh coke bin, 2, fresh burnt feed component, 3, the epimere of desulfurizing tower, 4, inner member, 5, under desulfurizing tower
Section, 6, weary burnt discharge structure, 7, the burnt inertia separator of cycle, 8, bag filter, 9, primary cycle coke feed component, 10, two
The burnt feed component of grade cycle.
Specific embodiment
It is noted that following detailed description is all illustrative, it is intended to provide further instruction to the application.It is unless another
It indicates, all technical and scientific terms used herein has usual with the application person of an ordinary skill in the technical field
The identical meanings of understanding.
It should be noted that term used herein above is merely to describe specific embodiment, and be not intended to restricted root
According to the illustrative embodiments of the application.As used herein, unless the context clearly indicates otherwise, otherwise singulative
It is also intended to include plural form, additionally, it should be understood that, when in the present specification using term "comprising" and/or " packet
Include " when, indicate existing characteristics, step, operation, device, component and/or combination thereof.
As shown in Figure 1, a kind of burnt double-circulating fluid bed desulphurization system of powder activity, equipped with fresh coke bin 1, fresh burnt feed
Component 2, the epimere 3 of desulfurizing tower, desulfurizing tower middle part inner member 4, the hypomere 5 of desulfurizing tower, weary burnt discharge feed component 6, cycle coke
Inertia separator 7, bag filter 8, primary cycle coke feed component 9, secondary cycle coke feed component 10.
Fresh coke bin 1 is connected by the fresh burnt component 2 that is fed with the epimere 3 of desulfurizing tower；Epimere 3, the desulfurizing tower of desulfurizing tower
The hypomere 5 of middle part inner member 4 and desulfurizing tower collectively constitutes desulfurizing tower；The hypomere 5 of desulfurizing tower is connected with weary burnt discharge structure 6, takes off
The epimere 3 of sulphur tower is connected with the burnt inertia separator 7 of cycle, recycle burnt inertia separator 7 by primary cycle coke be fed component 9 and
The epimere 3 of desulfurizing tower is connected, and bag filter 8 is connected with the burnt inertia separator 7 of cycle, and passes through secondary cycle coke feed component
10 are connected with the hypomere 5 of desulfurizing tower.As shown in Fig. 2, weary coke discharge structure 6 includes at least two collection flitch, collect flitch and desulfurization
Inner wall of tower and flue gas injection tube surround funnel-shaped structure, the weary burnt outlet of bottommost setting of funnel-shaped structure, smoke inlet jointly
It is set on the central shaft of desulfurizing tower；Collection flitch is symmetrical arranged around smoke inlet.Weary burnt outlet is provided with slide valve, slide valve
Lower termination lock gas batcher, the upper end of flue gas injection tube is higher by the lowermost end 1-3m of tower body, a diameter of tower body of flue gas injection tube
The 1/3-1/2 of diameter, the top and the upper end of flue gas injection tube of funnel-shaped structure are substantially flush.Tower body updip oblique cutting enter inclination to
Expects pipe, the solid outlet for tilting cyclone separator of the upper end of feed pipe with being connected to tower body outlet are connect, and tilt feed pipe
Lower end extends to the upper end of flue gas injection tube.Powder activity coke convenient for cyclone separator is detached is sent to flue gas injection tube
Upper end is recycled.
Fresh coke bin 1 is used to store freshly prepared activated coke and completes desulfurization and have fresh desulphurizing ability after regenerating
Activated coke.The grain size of fresh activity coke is less than 1mm.Activated coke is through the fresh burnt epimere 3 for being fed component 2 and being sent into desulfurizing tower.Desulfurization
Activated coke completes the absorption to sulfur dioxide in flue gas in the form of fast bed in the epimere 3 of tower, and activated coke enters cycle with flue gas
Burnt inertia separator 7, activated coke is captured down, and sends the epimere 3 of desulfurizing tower back to through primary cycle coke feed component 9.Cycle is burnt
The activated coke that inertia separator 7 is not kept completely separate is detached through 8 depth of bag filter, and the activated coke separated is through secondary cycle
Coke feed component 10 is sent into the hypomere 5 of desulfurizing tower, and the activated coke in the hypomere 5 of desulfurizing tower adsorbs desulfurization in the form of fast bed,
Amount of activated burnt through weary burnt discharge component 6 discharge desulfurizing tower, amount of activated coke enters desulfurizing tower by inner member 4 in the middle part of desulfurizing tower
Epimere 3, the cycle fed with the fresh burnt and primary cycle coke feed component 9 that fresh burnt feed component 2 is fed is burnt jointly complete
Into the deep purifying of sulfur dioxide in flue gas.
The foregoing is merely the preferred embodiments of the application, are not limited to the application, for the skill of this field
For art personnel, the application can have various modifications and variations.It is all within spirit herein and principle, made any repair
Change, equivalent replacement, improvement etc., should be included within the protection domain of the application.
Claims (10)
1. a kind of burnt double-circulating fluid bed desulphurization system of powder activity, it is characterised in that：Including desulfurizing tower, fresh coke bin, cycle
Burnt inertia separator and cloth bag separator, wherein,
The desulfurizing tower includes epimere and hypomere, is connected between epimere and hypomere by inner member, and inner member is used to prevent epimere
In activated coke fall into hypomere；The bottom of hypomere is provided with gas inlet and weary burnt discharge structure；
The fresh coke bin is connect with epimere, for adding fresh activity coke into epimere；The top of epimere and the burnt inertia of cycle
The import connection of separator, the epimere of solid outlet and desulfurizing tower for recycling burnt inertia separator connect, and recycle burnt inertial separation
The gas vent of device is connect with cloth bag separator, and the solid outlet of cloth bag separator and the hypomere of desulfurizing tower connect.
2. the burnt double-circulating fluid bed desulphurization system of powder activity according to claim 1, it is characterised in that：The inner member
It is connect between the epimere of desulfurizing tower by divergent segment, the epimere of the fresh coke bin and desulfurizing tower is located at 1- above divergent segment
It is connected at 2 meters.
3. the burnt double-circulating fluid bed desulphurization system of powder activity according to claim 1, it is characterised in that：The cycle is burnt
The bottom of the solid outlet of inertia separator and the epimere of desulfurizing tower connects.
4. the burnt double-circulating fluid bed desulphurization system of powder activity according to claim 1, it is characterised in that：The desulfurizing tower
The bottom of hypomere the second divergent segment is set, at top 1-2 meters of the solid outlet of the bag filter and the second divergent segment
Connection, and pass through the central shaft position that activated coke is sent to the hypomere of desulfurizing tower by conduit.
5. the burnt double-circulating fluid bed desulphurization system of powder activity according to claim 1, it is characterised in that：The weary burnt row
Go out structure and include tower body, collection flitch component and flue gas injection tube, collection flitch component includes several collection flitch, several collection flitch
It may be contained within inside tower body, and be symmetrical arranged on the section of tower body；Flue gas injection tube is set on the axis of tower body；
Tower body inner wall, collection flitch component and flue gas injection tube surround several funnel-shaped structures jointly, each funnel-shaped structure
The weary burnt outlet of bottommost setting.
6. the burnt double-circulating fluid bed desulphurization system of powder activity according to claim 5, it is characterised in that：Collect flitch and water
Square to angle be not less than 60 °.
7. the burnt double-circulating fluid bed desulphurization system of powder activity according to claim 5, it is characterised in that：The weary coke goes out
Mouth is provided with slide valve, and lock gas batcher is connect under slide valve.
8. the burnt double-circulating fluid bed desulphurization system of powder activity according to claim 7, it is characterised in that：The flue gas spray
The upper end of blowpipe is higher by the lowermost end 1-3m of tower body, the 1/3-1/2 of a diameter of tower body diameter of flue gas injection tube, the funnel-form
The top of structure and the upper end of flue gas injection tube are substantially flush.
9. using the sulfur method of the burnt double-circulating fluid bed desulphurization system of any powder activities of claim 1-8, feature
It is：Include the following steps：
Flue gas after dedusting is from the cycle coke contact desulfuriation in the hypomere that the lower part of desulfurizing tower is flowed up with desulfurizing tower, Ran Houxiang
On continue to flow, flow in the epimere of desulfurizing tower, contacted successively with the cycle coke in desulfurizing tower epimere and fresh coke, desulfurization；
The activated coke carried during flue gas outflow desulfurizing tower epimere flows through the burnt inertia separator of cycle and is partially separated, isolated
Cycle coke add into the epimere of desulfurizing tower；
Flue gas after the burnt inertia separator separation of cycle flows through bag filter, and the cycle coke in flue gas is in bag filter
Filter material surface forms the activated coke filtering layer constantly updated, and flue gas is contacted with activated coke filtering layer, realizes the secondary desulfuration of flue gas, secondary
Activated coke after desulfurization is collected by bag filter, and is added to the hypomere of desulfurizing tower.
10. sulfur method according to claim 9, it is characterised in that：The burnt inertia separator of cycle is to the cycle in flue gas
Burnt separative efficiency is 70-90%.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108722114A (en) * | 2018-08-08 | 2018-11-02 | 国家能源投资集团有限责任公司 | Powdered activated coke adsorpting desulfurization device and the method that absorption desulfurization is carried out to flue gas using it |
| CN110075662A (en) * | 2019-05-31 | 2019-08-02 | 中石化炼化工程（集团）股份有限公司 | The device and method of SOx and NOx pollutant in a kind of removing regeneration fume from catalytic cracking |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108722114A (en) * | 2018-08-08 | 2018-11-02 | 国家能源投资集团有限责任公司 | Powdered activated coke adsorpting desulfurization device and the method that absorption desulfurization is carried out to flue gas using it |
| CN110075662A (en) * | 2019-05-31 | 2019-08-02 | 中石化炼化工程（集团）股份有限公司 | The device and method of SOx and NOx pollutant in a kind of removing regeneration fume from catalytic cracking |
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