CN201572596U - Cross flow type moving bed desulfurizing tower - Google Patents
Cross flow type moving bed desulfurizing tower Download PDFInfo
- Publication number
- CN201572596U CN201572596U CN2009203520591U CN200920352059U CN201572596U CN 201572596 U CN201572596 U CN 201572596U CN 2009203520591 U CN2009203520591 U CN 2009203520591U CN 200920352059 U CN200920352059 U CN 200920352059U CN 201572596 U CN201572596 U CN 201572596U
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- desulfurizing tower
- flue
- main body
- moving bed
- activated coke
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Abstract
The patent discloses a cross flow type moving bed desulfurizing tower, which comprises a desulfurizing tower main body, an air inlet smoke canal and an air outlet smoke canal arranged on the main body, a hopper arranged under the main body; the desulfurizing tower main body comprises an air inlet chamber arranged in the middle part, active coke layers arranged at two side of the air inlet chamber, air outlet chambers respectively arranged at the side surfaces of the active coke layers, wherein, the air inlet smoke canal is connected with air inlet chamber, the air inlet chamber is communicated with the active coke layers, the active coke layers are communicated with the air outlet chambers, the top ends of the air outlet chambers are connected with the air outlet smoke canal by at least one pair of communicating smoke canals. The apparatus has advantages of large smoke throughput, low resistance force, and uniform air flow distribution, and the desulfurizing efficiency can be obviously improved.
Description
Technical field
It is the active coke dry-method desulfuration tower that boiler of power plant, metallurgy and chemical industry waste gas carry out desulfurization that this patent relates to a kind of, relates in particular to a kind of to the various SO of containing
2The useless flue gas of industry carries out desulfurization and can realize the cross-flow type moving bed desulfurizing tower of sulphur resource.
Background technology
Flue gas desulfurization is to control SO at present in the world
2The main means of polluting.Electric power and metallurgy industry adopt limestone-gypsum wet type desulfurizing technology mostly at present, and this method adopts lime stone as desulfurizing agent, and desulfurization product is a gypsum.Yet exist water consumption big in this technical process, desulfurated plaster causes bulk deposition to cause problems such as the secondary pollution and the sulphur wasting of resources because of utilizing, along with going deep into of energy-saving and emission-reduction and circular economy concept, the use of this technology has been subjected to restriction to a certain degree in very most of area.
Active coke dry-method desulfuration process using activated coke is as adsorbent, and under the uniform temperature condition, activated coke is adsorbed SO in the flue gas
2, oxygen and steam, SO under the catalytic action of activated coke surface-active point
2Be oxidized to SO
3, SO
3Generate sulfuric acid with steam reaction, be adsorbed on the surface of activated coke.Activated coke high temperature heating after the absorption is resolved and is generated SO
2, CO
2And H
2O etc., SO in the gas
2Content 20%～40% can be processed as chemical products such as sulfuric acid, elemental sulfur as required, and the activated coke behind the desorption can recycle.This technical process is consume water not substantially, and activated coke can be recycled, the desulfuration efficiency height, and SR is low, and advantages such as recyclable sulphur resource more and more are applied in electric power, metallurgy and chemical industry widely.
The absorption type desulfurizing tower is the nucleus equipment of active coke dry-method desulfuration technology, what commercial Application was more is fixed bed desulfurizing tower and moving bed desulfurizing tower, wherein the intermittent operation mode of fixed bed desulfurizing tower can not adapt to the big exhaust gas volumn situation of handling, and moving bed desulfurizing tower has characteristics such as the smoke treatment amount is big, resistance is low and is widely used.According to flue gas and activated coke way of contact moving bed desulfurizing tower can be divided into again and stream, adverse current and three kinds of forms of cross-flow, cross-flow moving bedly integrate counter-flow moving bed and advantage radial fixed-bed reactor, this type is convenient to the separating treatment of gas-solid phase because gas separates with the stream of solid; Its advantage is that the gas-solid contact area is big, processing is large-minded, pressure drop is little, catalysis adsorption reaction speed is fast, and has created condition for adopting short grained catalyst to improve space velocity, thereby has improved the space time yield of equipment.
Present cross-flow type moving bed desulfurizing tower employing side is advanced side and is gone out intake method, see accompanying drawing 1, air inlet flue 7 is from a side air inlet, enter inlet plenum 6, activated coke layer 2 has mobile activated coke to move from top to down, flue gas passes activated coke layer 2 from inlet plenum 6 and enters into the discharge chamber 3 that is positioned at both sides, after converging then again the flue 1 of giving vent to anger from opposite side discharge.The problem that the cross-flow type moving bed desulfurizing tower of this structure exists is as follows:
1, import and export flue (1,7) and arrange that for both sides overall structure is compact inadequately, floor space is bigger, can't adapt to the conditional situation in place.
2, there is certain defective in intake method of the prior art, on the one hand because air inlet flue 7 no guiding devices are difficult to guarantee the uniformity of air-flow distribution in the inlet plenum 6, and produces eddy current easily in the air inlet flue, thereby increases SR; Fall from top to down owing to activated coke on the other hand, the activated coke adsorption capacity of the superiors is stronger, downward more activated coke adsorption capacity is weak more, but flue gas is to enter from the side, contact with activated coke layer 2, distribute and to be complementary with the adsorption capacity of activated coke on this direction along the flue gas load on activated coke layer 2 short transverse like this, thereby cause being difficult to obtain higher desulfuration efficiency.
The utility model content
The purpose of this utility model provides a kind of cross-flow type moving bed desulfurizing tower, and this device flue gas treating capacity is big, resistance is low, air-flow is evenly distributed, can significantly improve desulfuration efficiency.
In order to achieve the above object, the utility model provides following technical scheme:
A kind of cross-flow type moving bed desulfurizing tower, comprise a desulfurizing tower main body, and be arranged on the air inlet flue and the flue of giving vent to anger on the described main body, be arranged on the discharge bucket of described main body below, described desulfurizing tower main body comprises the inlet plenum in the middle of being arranged on, be arranged on the activated coke layer of described inlet plenum both sides, be separately positioned on the discharge chamber of described activated coke layer side, described air inlet flue is connected with described inlet plenum, described inlet plenum with the conducting of described activated coke layer, described activated coke layer and described discharge chamber conducting, the top of described discharge chamber is connected with the described flue of giving vent to anger by at least one pair of conducting flue.
As the further improvement of the technical program, described air inlet flue is arranged on the bottom of described desulfurizing tower main body, and the described flue of giving vent to anger is arranged on the top of described desulfurizing tower main body.
As the further improvement of the technical program, in the described air inlet flue at least one deflector is set.Adopt three deflectors in this patent.Further, described deflector comprises the straightsided shape section that is used for the segmental arc that air-flow is turned to and is used for the air-flow after turning to is carried out current stabilization.
Further improvement as the technical program, described conducting flue is arranged on the top of described activated coke layer, the described flue of giving vent to anger is arranged on the top of described inlet plenum, and described discharge chamber, described conducting flue, described this three's of flue that gives vent to anger top all is in same horizontal plane, and to make described desulfurizing tower main body top be a plane.
Further, described desulfurizing tower main body is similar cuboid, and described conducting flue is 3 pairs, and described deflector is 3.
Further, described conducting flue and described discharge chamber and described outlet passageway surround 4 activated coke stockpiling areas.
Further, the longitudinal section of described stockpiling area is up-narrow and down-wide trapezoidal shape.
Desulfurizing tower of the present utility model adopts similar cuboid, the square-section, the flue gas area of passage is big, by the activated coke layer being set respectively in the inlet plenum both sides and going out gas-bearing formation, can satisfy the situation of handling big exhaust gas volumn in the industrial process, the often high tens of rice of existing desulfurizing tower, often need field fabrication during construction, install, waste time and energy, each parts all can directly be assembled connection in the whole device of this patent, simple and compact for structure, realize modularization production easily, quick and easy for installation like this, it is also very convenient to keep in repair.
The desulfurizing tower intake method generally has three kinds: the side direction air inlet, give vent to anger in air inlet bottom, top, give vent to anger in the bottom inflow top, these three kinds of intake methods are adopted numerical flow simulation, the result shows and adopts give vent to anger flue gas under the mode of bottom inflow top to cross a flow velocity along the activated coke flow direction behind the bottom inflow and reduce gradually, and activated coke adsorption capacity from top to down just in time by strong and a little less than, can contact the generation adsorption reaction rapidly near the stronger fresh activated coke of higher relatively flue gas of top flow velocity and adsorption capacity like this, near the relatively low flue gas of bottom velocity then with activated coke haptoreaction slowly and fully, thereby realized the flue gas load of reasonable distribution along activated coke layer height direction, mated the activated coke adsorption capacity on the different bed heights, realize the maximization of activated coke adsorption capacity, improved the desulfuration efficiency of system greatly.
Simultaneously in desulfurizing tower bottom inflow flue, deflector is set, come out according to optimizing calculation Design in the shape of deflector and installation site, can guarantee to be evenly distributed, avoid taking place flow field defectives such as air-flow whirlpool and flue gas short circuit along flue gas flow rate in inlet plenum on the tower length direction and the activated coke layer.Conducting flue circulation area behind the discharge chamber is big, and flue gas flow rate is low, and it is little to converge the pressure process loss, causes whole desulfurizing tower overall resistance low.
Desulfurizing tower activated coke layer is removed top windrow section three place's cavitys outward respectively, for making full use of the space, realize the densification of desulfurizing tower structure, this three places cavity is made as the conducting flue, and discharge chamber top, the both sides flue gas of symmetry flows out desulfurizing tower through many after being pooled to the flue of giving vent to anger that is positioned at the inlet plenum top after to parallel gas passes respectively.Conducting flue top, the flue top of giving vent to anger, discharge chamber three top is concordant is a horizontal plane, and desulfurizing tower integral body is similar cuboid, and top plan can be used as inspection platform like this, and compact conformation is regular.
Description of drawings
Fig. 1 is the structural representation of desulfurizing tower in the prior art;
Fig. 2 is the structural representation of this patent desulfurizing tower;
Fig. 3 is the longitudinal section profile of Fig. 2;
Fig. 4 is the A-A profile of Fig. 2;
Fig. 5 is the B-B profile of Fig. 2;
Fig. 6 is the modularization assembling schematic diagram of patent device;
The number in the figure explanation:
The 1-flue 2-activated coke layer 3-discharge chamber 4-conducting flue 5-stockpiling area of giving vent to anger
6-inlet plenum 7-air inlet flue 8-discharge bucket 9-deflector
The specific embodiment
Now with the specific embodiment this patent is described in further details in conjunction with the accompanying drawings:
Embodiment one:
Present embodiment is for using the desulfurizing tower in metallurgy industry set of circumstances cigarette system, and as shown in Figure 2, the desulfurizing tower main body is made up of inlet plenum 6, activated coke layer 2, discharge chamber 3, discharge bucket 8, top conducting flue 4, air inlet flue 7 and the flue 1 of giving vent to anger.Ring collection flue-gas temperature is 60 ℃, directly after arc straight flange deflector 9 guiding, upwards flow into inlet plenum 3 from air inlet flue 7, the shunting rear side is to passing through monosymmetric activated coke layer 2, the activated coke gravitate moves down with certain speed through stockpiling area 5 from charge door, contact with the flue gas formation cross-flow that side direction flows into, adsorption reaction takes place remove wherein most pernicious gas SO
2, flue gas after the desulfurization flows into discharge chamber 3 and converges through both sides conducting flue 4 and enter the flue 7 of giving vent to anger and flow out desulfurizing towers, adsorbs saturated activated coke and flows downward and enter bottom discharge bucket 8.
Consult Fig. 3, polylith arc straight flange deflector 9 is set in the bottom inflow flue 7, the flue gas reasonable direction that air inlet flue 7 is flowed into is eliminated eddy-currents on the one hand; Deflector 9 can play the flue gas load of reasonable distribution along the absorption tower length direction in addition, is implemented in the uniform of flue gas flow field on this direction.
Consult Fig. 4, Fig. 5, can clearly find out the concrete structure of patent device, in conjunction with Fig. 6, as can be seen, in the patent device, activated coke layer 2 top are provided with conducting flue 4, conducting flue 4 surrounds four stockpiling areas 5 respectively with discharge chamber 3, outlet passageway 1, the longitudinal section of stockpiling area 5 or be up-narrow and down-wide trapezoidal shape or be rectangle that being arranged to the cross section is that trapezoidal stockpiling area mainly is a concrete condition of considering windrow in actual the use, makes full use of the windrow space like this.
A distinguishing feature of patent device is a modularization, referring to Fig. 6, in actual the use, the height of desulfurizing tower is generally tens of rice, integral constructing is wasted time and energy, if adopt modularization production, then very convenient and swift, as Fig. 6, whole desulfurizing tower is divided into three groups of upper, middle and lowers, and every group of about 4 meters height are respectively with activated coke layer 2, discharge chamber 3 is assembled on the inlet plenum 6 that is positioned at central authorities, for uppermost this group, the flue 1 of will giving vent to anger is assembled on the inlet plenum 6, conducting flue 4 is assembled into discharge chamber 3 respectively and gives vent to anger between the flue 1, then this group of centre is stacked on following this group, top that group is stacked on middle this group, and binding site can adopt the mode of welding or sealing and fixing.
Result of implementation shows, this desulfurizing tower flow field distributes rationally, and very favourable to adsorption reaction along taper off the from top to bottom smoke distribution form of trend of height of bed direction, system's desulfuration efficiency can improve 2-5% than desulfurizing tower of the prior art.Desulfurizing tower SR decline 50-100Pa, the desulphurization system fan energy consumption significantly descends.
Embodiment two:
Present embodiment is that a sulfuric acid preparation facilities afterbody uses desulfurizing tower of the present utility model to carry out flue gas desulfurization, and the overall structure of desulfurizing tower such as embodiment 1, the flue gas behind the humidifying cooling enter desulfurizing tower and remove SO after activated coke absorption
2, desulfuration efficiency can reach more than 95%, and the desulfuration efficiency of the desulfurizing tower of prior art generally has only about 90%.
Those skilled in the art will recognize that; the above-mentioned specific embodiment is exemplary; be in order to make those skilled in the art can better understand this patent content; should not be construed as is restriction to this patent protection domain; change or modify so long as disclose spiritual any being equal to of being done, all fall into this patent protection domain according to this patent.
Claims (8)
1. cross-flow type moving bed desulfurizing tower, comprise a desulfurizing tower main body, and be arranged on the air inlet flue and the flue of giving vent to anger on the described main body, be arranged on the discharge bucket of described main body below, it is characterized in that: described desulfurizing tower main body comprises the inlet plenum in the middle of being arranged on, be arranged on the activated coke layer of described inlet plenum both sides, be separately positioned on the discharge chamber of described activated coke layer side, described air inlet flue is connected with described inlet plenum, described inlet plenum with the conducting of described activated coke layer, described activated coke layer and described discharge chamber conducting, the top of described discharge chamber is connected with the described flue of giving vent to anger by at least one pair of conducting flue.
2. according to the described cross-flow type moving bed desulfurizing tower of claim 1, it is characterized in that: described air inlet flue is arranged on the bottom of described desulfurizing tower main body, and the described flue of giving vent to anger is arranged on the top of described desulfurizing tower main body.
3. according to the described cross-flow type moving bed desulfurizing tower of claim 2, it is characterized in that: in the described air inlet flue at least one deflector is set.
4. according to the described cross-flow type moving bed desulfurizing tower of claim 3, it is characterized in that: described deflector comprises the straightsided shape section that is used for the segmental arc that air-flow is turned to and is used for the air-flow after turning to is carried out current stabilization.
5. according to the described cross-flow type moving bed desulfurizing tower of the arbitrary claim of claim 1 to 4, it is characterized in that: described conducting flue is arranged on the top of described activated coke layer, the described flue of giving vent to anger is arranged on the top of described inlet plenum, and described discharge chamber, described conducting flue, described this three's of flue that gives vent to anger top all is in same horizontal plane, and to make described desulfurizing tower main body top be a plane.
6. according to the described cross-flow type moving bed desulfurizing tower of claim 5, it is characterized in that: described desulfurizing tower main body is similar cuboid, and described conducting flue is 3 pairs, and described deflector is 3.
7. according to the described cross-flow type moving bed desulfurizing tower of claim 6, it is characterized in that: described conducting flue and described discharge chamber and described outlet passageway surround 4 activated coke stockpiling areas.
8. according to the described cross-flow type moving bed desulfurizing tower of claim 7, it is characterized in that: the longitudinal section of described stockpiling area is up-narrow and down-wide trapezoidal shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203520591U CN201572596U (en) | 2009-12-24 | 2009-12-24 | Cross flow type moving bed desulfurizing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203520591U CN201572596U (en) | 2009-12-24 | 2009-12-24 | Cross flow type moving bed desulfurizing tower |
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| Publication Number | Publication Date |
|---|---|
| CN201572596U true CN201572596U (en) | 2010-09-08 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009203520591U Expired - Lifetime CN201572596U (en) | 2009-12-24 | 2009-12-24 | Cross flow type moving bed desulfurizing tower |
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| Country | Link |
|---|---|
| CN (1) | CN201572596U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106823488A (en) * | 2017-02-14 | 2017-06-13 | 北京博汇特环保科技股份有限公司 | Sedimentation basin and the sewage disposal system with it |
| CN107661681A (en) * | 2017-11-08 | 2018-02-06 | 中国科学院过程工程研究所 | A kind of flue gas pollutant purifying column |
-
2009
- 2009-12-24 CN CN2009203520591U patent/CN201572596U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106823488A (en) * | 2017-02-14 | 2017-06-13 | 北京博汇特环保科技股份有限公司 | Sedimentation basin and the sewage disposal system with it |
| CN107661681A (en) * | 2017-11-08 | 2018-02-06 | 中国科学院过程工程研究所 | A kind of flue gas pollutant purifying column |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20100908 Effective date of abandoning: 20091224 |