CN205156650U - Comprehensive treatment system for flue gas of sintering plant - Google Patents
Comprehensive treatment system for flue gas of sintering plant Download PDFInfo
- Publication number
- CN205156650U CN205156650U CN201521015589.9U CN201521015589U CN205156650U CN 205156650 U CN205156650 U CN 205156650U CN 201521015589 U CN201521015589 U CN 201521015589U CN 205156650 U CN205156650 U CN 205156650U
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- CN
- China
- Prior art keywords
- flue gas
- pipeline
- waste heat
- blower fan
- sintering
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- 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.)
- Withdrawn - After Issue
Links
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 95
- 239000003546 flue gas Substances 0.000 title claims abstract description 94
- 238000005245 sintering Methods 0.000 title claims abstract description 60
- 239000002918 waste heat Substances 0.000 claims abstract description 40
- 239000000428 dust Substances 0.000 claims abstract description 29
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 39
- 239000011593 sulfur Substances 0.000 claims description 38
- 229910052717 sulfur Inorganic materials 0.000 claims description 38
- 239000007789 gas Substances 0.000 claims description 27
- 239000000779 smoke Substances 0.000 claims description 19
- 238000001816 cooling Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 6
- 238000006477 desulfuration reaction Methods 0.000 abstract description 22
- 230000023556 desulfurization Effects 0.000 abstract description 20
- 238000011084 recovery Methods 0.000 abstract description 5
- 238000012545 processing Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 53
- 238000003672 processing method Methods 0.000 description 8
- 239000003517 fume Substances 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 229910052602 gypsum Inorganic materials 0.000 description 4
- 239000010440 gypsum Substances 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000003245 coal Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides a sintering plant flue gas integrated processing system. The system comprises a sintering machine (1), a cooler (2), a denitration device (3), a desulfurization device (4), a first dust removal device (5), a second dust removal device (6), a heat exchanger (7), a first fan (8), a second fan (9), a third fan (10), a fourth fan (11) and a waste heat boiler (12). The utility model provides a system takes flue gas waste heat recovery, flue gas dust removal, flue gas desulfurization, flue gas denitration and hot-blast sintering into general consideration, and when clean flue gas, furthest has retrieved the waste heat and has carried out reasonable distribution to the waste heat and recycle, has improved the thermal efficiency of sintering system, and then has realized energy saving and emission reduction.
Description
Technical field
The utility model relates to a kind of sintering plant smoke gas comprehensive treatment system, belongs to fume treatment technical field.
Background technology
The iron and steel output of China occupies the first in the world for years, but the energy input in steel manufacture process and discharge water are on average far above advanced international standard, and therefore, energy-saving and emission-reduction have a high potential.And iron ore sintering energy consumption in the Production Process for Steel Enterprise of China occupies the second, discharge ranks first place, and therefore it plays decisive role to the energy-saving and emission-reduction of steel and iron industry.The high efficiente callback of waste heat resources in sintering process is one of the Main way and approach that reduce sintering plant revamp with utilizing.So develop a kind of comprehensive fume treatment scheme, make the program under the prerequisite ensureing standard limit of smog release, as far as possible emissions reduction, improve utilization rate of waste heat, significant to the sustainable development of China's sintering industry.
Sintering plant fume treatment technology mainly comprises: desulphurization and denitration, dedusting and waste heat recovery etc.But at present, China's sintering technology research only focuses on one of them aspect mostly, and ignores this few person as the interrelated of sintering system and impact.Any one aspect of independent consideration, all can cause using energy source unreasonable.
Therefore, a kind of smoke gas comprehensive treatment system that the techniques such as desulphurization and denitration, dedusting and waste heat recovery can be combined is developed and method has become the technical problem that this area needs solution badly.
Utility model content
The purpose of this utility model is to provide a kind of sintering plant smoke gas comprehensive treatment system.
For reaching above-mentioned purpose, the utility model provides a kind of sintering plant smoke gas comprehensive treatment system, and this system comprises sintering machine 1, cooler 2, denitrification apparatus 3, desulfurizer 4, first dust arrester 5, second dust arrester 6, heat exchanger 7, first blower fan 8, second blower fan 9, the 3rd blower fan 10, four fan device 11 and waste heat boiler 12;
The high sulfur contained high temoperature exhanst gas outlet of described sintering machine 1 is connected with the first entrance of heat exchanger 7 via denitrification apparatus 3, first dust arrester 5 by pipeline, first outlet of heat exchanger 7 is connected by the entrance of pipeline with desulfurizer 4, the outlet of desulfurizer 4 is connected with the second entrance of heat exchanger 7 by pipeline, and the second outlet of heat exchanger 7 is connected with the first blower fan 8 by pipeline;
The low sulfur-bearing low-temperature flue gas outlet of described sintering machine 1 is connected with the second blower fan 9 via the second dust arrester 6 by pipeline;
The high temperature section exhanst gas outlet of described cooler 2 is connected by the entrance of pipeline with waste heat boiler 12, and the outlet of waste heat boiler 12 is connected with the cooling bed of material entrance of cooler 2 via the 3rd blower fan 10 by pipeline;
The low-temperature zone exhanst gas outlet of described cooler 2 is connected with above the sinter bed of sintering machine 1 via four fan device 11 by pipeline; The low-temperature zone exhanst gas outlet of this cooler 2 is connected with the return air duct entrance of waste heat boiler 12 by pipeline.
According to system described in the utility model, preferably, this system also comprises chimney 13, and described chimney 13 is connected with the first blower fan 8, second blower fan 9 respectively by pipeline.
According to system described in the utility model, preferably, described denitrification apparatus 3 is SCR denitration device.
According to system described in the utility model, above-mentioned sintering machine 1, cooler 2, denitrification apparatus 3, desulfurizer 4, first dust arrester 5, second dust arrester 6, heat exchanger 7, first blower fan 8, second blower fan 9, the 3rd blower fan 10, four fan device 11 and waste heat boiler 12 are the conventional equipment of this area, and the utility model does not improve the said equipment.
System described in the utility model goes for multiple diverse ways and carries out integrated treatment to sintering plant flue gas, in order to be described system of the present utility model further, the utility model additionally provides application system of the present utility model to the method for sintering plant smoke comprehensive process, wherein, said method comprising the steps of:
A, described high sulfur contained high temoperature flue gas is carried out denitration process, dust removal process successively, then the high sulfur contained high temoperature flue gas through denitration process, dust removal process is lowered the temperature, then desulfurization process is carried out to it, finally discharge after heating through the flue gas of desulfurization process;
B, described low sulfur-bearing low-temperature flue gas is carried out dust removal process, then the flue gas after process is discharged;
C, described high temperature section flue gas is cooled in waste heat boiler after, be circulated to cooler cooling the bed of material;
D, part low-temperature zone flue gas is caused above sintering machine sinter bed, for hot gas sintering; Part low-temperature zone flue gas causes the return air duct of waste heat boiler, mends wind for hot blast.
According to method described in the utility model, described sintering plant flue gas comprises sintering device flue gas and cooler flue gas; This sintering device flue gas comprises high sulfur contained high temoperature flue gas and low sulfur-bearing low-temperature flue gas, this high sulfur contained high temoperature flue gas by sintering in large flue, rear portion flue gas forms, this low sulfur-bearing low-temperature flue gas is mixed by the low-temperature flue gas of sintering machine front portion and the high-temperature flue gas of tail; Cooler flue gas comprises high temperature section flue gas and low-temperature zone flue gas;
In described high sulfur contained high temoperature flue gas and low sulfur-bearing low-temperature flue gas, the division of sulfur content can meet national standard (GB28662-2012) and local relevant emission standards for benchmark with low sulfur-containing smoke gas, sulfur content exceedes the flue gas of this national standard (GB28662-2012) and local relevant emission standards, is high sulfur-containing smoke gas.
" high temperature " of described high sulfur contained high temoperature flue gas is the temperature compared to low sulfur-bearing low-temperature flue gas, and usually, the temperature of high sulfur contained high temoperature flue gas is about 230 DEG C, and the temperature of low sulfur-bearing low-temperature flue gas is about 150 DEG C.
" high temperature " of described high temperature section flue gas is the temperature compared to low-temperature zone flue gas, and usually, the temperature of high temperature section flue gas is about 350 DEG C, and the temperature of low-temperature zone flue gas is about 130 DEG C.
According to method described in the utility model, denitration process described in the utility model can adopt the denitration processing method of this area routine, and the denitration described in step a is treated to SCR denitration process.Wherein, SCR denitration process is also the denitration processing method of this area routine, those skilled in the art can according to field operation needs, suitable SCR denitration treatment process parameter is selected to carry out denitration process to high sulfur contained high temoperature flue gas of the present utility model, as long as the object of denitration can be realized, as long as and the concentration of NOx after denitration in flue gas meets the discharge standard of this area (industry).
According to method described in the utility model, the dust removal process described in step a also can adopt the dust removal process method of this area routine, as long as can realize the object of high sulfur contained high temoperature flue gas ash removal.
According to method described in the utility model, in the embodiment that the utility model is concrete, the cooling described in step a is that the temperature of the high sulfur contained high temoperature flue gas through denitration process, dust removal process is down to about 150 DEG C.
According to method described in the utility model, desulfurization process described in the utility model can adopt the desulfuration processing method of this area routine, and the desulfurization described in step a is treated to desulfurization by lime gypsum method process.Wherein, desulfurization by lime gypsum method process is also the desulfuration processing method of this area routine, those skilled in the art can according to field operation needs, suitable desulfurization by lime gypsum method treatment process parameter is selected to carry out desulfurization process to high sulfur contained high temoperature flue gas of the present utility model, as long as the object of desulfurization can be realized, as long as and sulfur content in flue gas after desulfurization meets the discharge standard of this area (industry).
According to method described in the utility model, in the embodiment that the utility model is concrete, described in step a, be heated to be the flue gas after by desulfurization process to about 95 DEG C.Utilize the flue gas after the waste-heat desulfurization of non-desulfurization fume in step a, and its heating temperatures is caused corrosion to prevent sulphur remaining in flue gas after desulfurization to equipment to about 95 DEG C.
According to method described in the utility model, in the embodiment that the utility model is concrete, high temperature section flue gas is cooled to about 140 DEG C by being cooled to described in step c.Now, the steam that waste heat boiler produces can be used for generating.After being cooled in waste heat boiler by high temperature section flue gas in the utility model step c, then be circulated to the cooler cooling bed of material, the discharge of flue gas can also be reduced while realizing flue gas waste heat recovery.
According to method described in the utility model, in steps d, part low-temperature zone flue gas is caused above sintering machine, for hot gas sintering, can coal consumption be reduced; Part low-temperature zone flue gas is caused the return air duct of waste heat boiler, mend wind for hot blast, the temperature of the flue gas entering exhaust-heat boiler inlet can be improved.
In addition, the amount of the utility model to the low-temperature zone flue gas causing above sintering machine sinter bed in steps d and cause waste heat boiler return air duct does not all do requirement, those skilled in the art can regulate and control respectively according to the consumption of the needs of field operation to the two, as long as can realize its object.
The utility model additionally provides the application of above-mentioned sintering plant smoke comprehensive processing method in sintering plant fume treatment.
Compared with existing equipment, the sintering plant smoke gas comprehensive treatment system cost that the utility model provides is lower, and equipment investment is little.
The sintering plant smoke comprehensive processing method that the utility model provides is a kind of Novel integrated fume treatment technology, flue gas waste heat recovery, flue gas ash removal, flue gas desulfurization, denitrating flue gas and hot gas sintering are considered as a whole by this technology, while guarantee smoke evacuation index (desulfurization reaches discharge standard), reduce the concentration of NOx in exhaust smoke level and flue gas, and farthest reclaimed sintering waste heat and sinter cooler waste heat by energy classified utilization and waste heat carried out to rational distribution recycling, improve the thermal efficiency of sintering system, and then achieve energy-saving and emission-reduction.
In addition, high sulfur contained high temoperature waste heat flue gas in sintering device flue gas is introduced denitrification apparatus by the utility model, as compared to traditional handicraft (sinter fume of about 150 DEG C is directly sent into denitrification apparatus, needs additionally to heat flue gas), greatly reduce the heat added needed for heat smoke.
Accompanying drawing explanation
Fig. 1 is sintering plant smoke gas comprehensive treatment system schematic diagram of the present utility model;
Fig. 2 is sintering plant smoke comprehensive processing method process chart of the present utility model.
Main Reference label declaration:
1, sintering machine 2, cooler 3, SCR denitration device 4, desulfurizer 5, first dust arrester
6, the second dust arrester 7, heat exchanger 8, first blower fan 9, second blower fan 10, the 3rd blower fan
11, four fan device 12, waste heat boiler 13, chimney.
Detailed description of the invention
Describe the beneficial effect of implementation process of the present utility model and generation below by way of specific embodiment and Figure of description in detail, be intended to help reader to understand essence of the present utility model and feature better, not as can the restriction of practical range to this case.
Embodiment 1
Present embodiments provide a kind of sintering plant smoke gas comprehensive treatment system, as shown in Figure 1, this system comprises sintering machine 1, cooler 2, SCR denitration device 3, desulfurizer 4, first dust arrester 5, second dust arrester 6, heat exchanger 7, first blower fan 8, second blower fan 9, the 3rd blower fan 10, four fan device 11, waste heat boiler 12 and chimney 13 to its schematic diagram;
The high sulfur contained high temoperature exhanst gas outlet of described sintering machine 1 is connected with the entrance of heat exchanger 7 via SCR denitration device 3, first dust arrester 5 by pipeline, the outlet of heat exchanger 7 is connected by the entrance of pipeline with desulfurizer 4, the outlet of desulfurizer 4 is connected by the entrance of pipeline with heat exchanger 7, and the outlet of heat exchanger 7 is connected with chimney 13 via the first blower fan 8 by pipeline;
The low sulfur-bearing low-temperature flue gas outlet of described sintering machine 1 is connected with chimney 13 via the second dust arrester 6, second blower fan 9 by pipeline;
The high temperature section exhanst gas outlet of described cooler 2 is connected by the entrance of pipeline with waste heat boiler 12, and the outlet of waste heat boiler 12 is connected with the cooling bed of material entrance of cooler 2 via the 3rd blower fan 10 by pipeline;
The low-temperature zone exhanst gas outlet of described cooler 2 is connected via the top of four fan device 11 with sintering machine 1 by pipeline; The low-temperature zone exhanst gas outlet of this cooler 2 is connected with the return air duct entrance of waste heat boiler 12 by pipeline.
Embodiment 2
Present embodiments provide a kind of sintering plant smoke comprehensive processing method, the method is that the system using embodiment 1 to provide realizes, and as shown in Figure 2, the method comprises the following steps its process chart:
Sintering plant flue gas comprises sintering device flue gas and cooler flue gas; Sintering device flue gas is divided into high sulfur contained high temoperature flue gas and low sulfur-bearing low-temperature flue gas, processes respectively.
The temperature of described high sulfur contained high temoperature flue gas is higher, is about 230 DEG C, high sulfur contained high temoperature flue gas is introduced SCR denitration device 3 and carries out SCR denitration process; Flue gas after denitration, after the first dust arrester 5 dust removal process (after denitration process, dust removal process, its temperature is about 220 DEG C to high sulfur contained high temoperature flue gas), enter heat exchanger 7, after temperature is reduced to about 150 DEG C by heat exchanger, enter desulfurizer 4 and carry out desulfurization by lime gypsum method; Flue gas (its temperature is about 50 DEG C) after desulfurization absorbs after thermal temperature rises to about 95 DEG C through heat exchanger 7, by the first blower fan 8, together with low sulfur-bearing low-temperature flue gas, is disposed to air through chimney 13.
The temperature of described low sulfur-bearing low-temperature flue gas is about 150 DEG C, and low sulfur-bearing low-temperature flue gas, after the second dust arrester 6 dedusting, is disposed to air through chimney 13 by the second blower fan 9 together with high sulfur contained high temoperature flue gas.
Described cooler flue gas comprises high temperature section flue gas (about 350 DEG C) and low-temperature zone flue gas (about 130 DEG C), and the processing mode of high temperature section flue gas is: according to different energy level, reclaim respectively.High temperature section flue gas is introduced waste heat boiler 12, after being cooled to about about 140 DEG C, sends into the cooling bed of material of cooler 2 through the 3rd blower fan 10, form circulation, make use of the waste heat of flue gas, and decrease the discharge of flue gas.The steam that waste heat boiler 12 produces, can be used for generating.
The processing mode of low-temperature zone flue gas is: cause above sintering machine 1 by part low-temperature zone flue gas, for hot gas sintering, can reduce coal consumption; Part low-temperature zone flue gas causes the return air duct of waste heat boiler 12, mends wind, to improve the flue-gas temperature entering waste heat boiler for hot blast.
Claims (3)
1. a sintering plant smoke gas comprehensive treatment system, it is characterized in that, this system comprises sintering machine (1), cooler (2), denitrification apparatus (3), desulfurizer (4), the first dust arrester (5), the second dust arrester (6), heat exchanger (7), the first blower fan (8), the second blower fan (9), the 3rd blower fan (10), four fan device (11) and waste heat boiler (12);
The high sulfur contained high temoperature exhanst gas outlet of described sintering machine (1) is connected with the first entrance of heat exchanger (7) via denitrification apparatus (3), the first dust arrester (5) by pipeline, first outlet of heat exchanger (7) is connected by the entrance of pipeline with desulfurizer (4), the outlet of desulfurizer (4) is connected by second entrance of pipeline with heat exchanger (7), and the second outlet of heat exchanger (7) is connected with the first blower fan (8) by pipeline;
The low sulfur-bearing low-temperature flue gas outlet of described sintering machine (1) is connected with the second blower fan (9) via the second dust arrester (6) by pipeline;
The high temperature section exhanst gas outlet of described cooler (2) is connected by the entrance of pipeline with waste heat boiler (12), and the outlet of waste heat boiler (12) is connected with the cooling bed of material entrance of cooler (2) via the 3rd blower fan (10) by pipeline;
The low-temperature zone exhanst gas outlet of described cooler (2) is connected with above the sinter bed of sintering machine (1) via four fan device (11) by pipeline; The low-temperature zone exhanst gas outlet of this cooler (2) is connected by the return air duct entrance of pipeline with waste heat boiler (12).
2. system according to claim 1, is characterized in that, this system also comprises chimney (13), and described chimney (13) is connected with the first blower fan (8), the second blower fan (9) respectively by pipeline.
3. system according to claim 1 and 2, is characterized in that, described denitrification apparatus (3) is SCR denitration device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521015589.9U CN205156650U (en) | 2015-12-09 | 2015-12-09 | Comprehensive treatment system for flue gas of sintering plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521015589.9U CN205156650U (en) | 2015-12-09 | 2015-12-09 | Comprehensive treatment system for flue gas of sintering plant |
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| CN205156650U true CN205156650U (en) | 2016-04-13 |
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| CN201521015589.9U Withdrawn - After Issue CN205156650U (en) | 2015-12-09 | 2015-12-09 | Comprehensive treatment system for flue gas of sintering plant |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105333748A (en) * | 2015-12-09 | 2016-02-17 | 北京京诚科林环保科技有限公司 | Comprehensive treatment system and method for sintering plant flue gas and application |
| CN107166963A (en) * | 2017-05-26 | 2017-09-15 | 上海交通大学 | A kind of agglomeration for iron mine system and method |
| CN107504812A (en) * | 2017-07-21 | 2017-12-22 | 上海交通大学 | A kind of iron ore hot gas sintering system and method |
-
2015
- 2015-12-09 CN CN201521015589.9U patent/CN205156650U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105333748A (en) * | 2015-12-09 | 2016-02-17 | 北京京诚科林环保科技有限公司 | Comprehensive treatment system and method for sintering plant flue gas and application |
| CN107166963A (en) * | 2017-05-26 | 2017-09-15 | 上海交通大学 | A kind of agglomeration for iron mine system and method |
| CN107504812A (en) * | 2017-07-21 | 2017-12-22 | 上海交通大学 | A kind of iron ore hot gas sintering system and method |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160413 Effective date of abandoning: 20171107 |