CN107754585A - A kind of exhuast gas desulfurization denitration filtration equipment for clarifying and filter method for power plant - Google Patents
A kind of exhuast gas desulfurization denitration filtration equipment for clarifying and filter method for power plant Download PDFInfo
- Publication number
- CN107754585A CN107754585A CN201710951987.9A CN201710951987A CN107754585A CN 107754585 A CN107754585 A CN 107754585A CN 201710951987 A CN201710951987 A CN 201710951987A CN 107754585 A CN107754585 A CN 107754585A
- Authority
- CN
- China
- Prior art keywords
- tobacco juice
- clarifying
- blower fan
- filtration equipment
- filter
- 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.)
- Pending
Links
- 238000001914 filtration Methods 0.000 title claims description 41
- 238000006477 desulfuration reaction Methods 0.000 title claims description 24
- 230000023556 desulfurization Effects 0.000 title claims description 24
- 238000000034 method Methods 0.000 title claims description 10
- 241000208125 Nicotiana Species 0.000 claims abstract description 66
- 235000002637 Nicotiana tabacum Nutrition 0.000 claims abstract description 66
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims abstract description 66
- 238000001816 cooling Methods 0.000 claims abstract description 41
- 238000002156 mixing Methods 0.000 claims abstract description 32
- 239000000779 smoke Substances 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000003517 fume Substances 0.000 claims abstract description 20
- 238000004332 deodorization Methods 0.000 claims abstract description 17
- 239000007789 gas Substances 0.000 claims description 34
- 239000007788 liquid Substances 0.000 claims description 25
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 24
- 239000003546 flue gas Substances 0.000 claims description 24
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims description 16
- 238000012546 transfer Methods 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 6
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 4
- 230000005540 biological transmission Effects 0.000 claims description 3
- 235000019504 cigarettes Nutrition 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical group [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims 1
- 239000003292 glue Substances 0.000 claims 1
- 229910052710 silicon Inorganic materials 0.000 claims 1
- 239000010703 silicon Substances 0.000 claims 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 12
- 239000000428 dust Substances 0.000 description 6
- 238000013461 design Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 238000003915 air pollution Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000004176 ammonification Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000000741 silica gel Substances 0.000 description 2
- 229910002027 silica gel Inorganic materials 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 201000004792 malaria Diseases 0.000 description 1
- 230000004630 mental health Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000005619 thermoelectricity Effects 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/60—Simultaneously removing sulfur oxides and nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/90—Odorous compounds not provided for in groups B01D2257/00 - B01D2257/708
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
Abstract
The present invention includes smoke inlet,Filter,Disposal box,Cooling device,Cooling tube,Blower fan,Lead smoke pipe,Support base,Micro bubble apparatus,Tobacco juice blending bin,Drain pipe,Tobacco juice separator box,Water pump,Catheter,Inlet,Supporting plate,Fume extractor,Chimney,Deodorization screen pack and humidifier,Smoke inlet is connected with filter,Filter is arranged on disposal box,Humidifier is arranged in disposal box,Cooling device is connected with filter,One end of cooling tube is arranged in cooling device,The other end of cooling tube is connected with blower fan,Blower fan is connected by leading smoke pipe with micro bubble apparatus,The end of micro bubble apparatus is located in tobacco juice blending bin,Tobacco juice blending bin is connected by drain pipe with tobacco juice separator box,Water pump is arranged in tobacco juice separator box,Water pump is connected by catheter with inlet,Supporting plate is arranged on the top of tobacco juice separator box,Fume extractor is installed on the supporting plate,Chimney is arranged on the side of fume extractor,Deodorization screen pack is arranged in chimney.
Description
Technical field
The present invention relates to a kind of exhuast gas desulfurization denitration filtration equipment for clarifying and filter method for power plant, belong to desulfurization and take off
Nitre filter technical field.
Background technology
With the continuous progress of science and technology, increasing high-tech product is developed, but the progress of science and technology is often
Along with the destruction of ecology, in recent years getting worse the problem of air pollution so that people in trip, it is necessary to wear mouth mask,
Air pollution main source is nitrogen oxides, sulfur dioxide and suspended particulate substance, and nitrogen oxides and sulfur dioxide are most important next
Source is that air pollution can cause very big injury to our body, in order under us caused by coal power generation is burnt in thermal power plant
A generation can continue to live in the earth that we depend on for existence this, and while generating electricity, we are it should also be noted that nitrogen oxides
With the discharge of sulfur dioxide, accomplish to discharge after burning flue-gas filtration, purification.But existing desulphurization denitration filtration equipment for clarifying
Efficiency comparison is low, it is impossible to meets the production requirement of thermal power plant, this make it that the production capacity of thermal power plant is limited, and causes thermoelectricity
Factory's generated energy declines.
In view of this, waste gas purification apparatus is disclosed in the patent document that notification number is CN204582856U, including entered
Tracheae, the deduster being arranged in air inlet pipe, and the nanometer gas-liquid two-phase film device being connected with air inlet pipe, sedimentation basin, it is covered with
Filter, catalyst configured slot, circulate liquid bath, oil-circulating ammonia water tank, the nanometer gas-liquid two-phase film device from top to bottom include according to
The temperature drop depth dust removal component of secondary connection, desulfurization part, desulfurization oxidation part, denitration ammonification part and gas collecting component, drop
Warm depth dust removal component is connected with sedimentation basin by the first pipeline, desulfurization part by second pipe successively be covered with filter and
Catalyst configured slot is connected, and desulfurization aoxidizes part and is connected with circulation liquid bath by the 3rd pipeline, denitration ammonification part and circulation ammonia
Tank is connected by the 4th pipeline.The shortcomings of efficiency that above-mentioned contrast patent has filtering is low, and environmental pollution is serious.
The content of the invention
It is an object of the invention to overcome above shortcomings in the prior art, and provide a kind of reasonable in design
Exhuast gas desulfurization denitration filtration equipment for clarifying and filter method for power plant.
Technical scheme is used by the present invention solves the above problems：This is used for the exhuast gas desulfurization denitration purification filtering of power plant
Device, its design feature are：Including smoke inlet, filter, disposal box, cooling device, cooling tube, blower fan, lead smoke pipe, branch
Support base, micro bubble apparatus, tobacco juice blending bin, drain pipe, tobacco juice separator box, water pump, catheter, inlet, supporting plate, smoke evacuation
Device, chimney, deodorization screen pack and humidifier, the smoke inlet are connected with filter, and the filter is arranged on dust
On case, the humidifier is arranged in disposal box, and the cooling device is connected with filter, one end installation of the cooling tube
In cooling device, the other end of the cooling tube is connected with blower fan, and the blower fan is connected by leading smoke pipe with micro bubble apparatus,
The micro bubble apparatus is arranged in support base, and the end of the micro bubble apparatus is located in tobacco juice blending bin, the feed liquor
Mouth is arranged on the top of tobacco juice blending bin, and the tobacco juice blending bin is connected by drain pipe with tobacco juice separator box, the water pump peace
In tobacco juice separator box, the water pump is connected by catheter with inlet, and the supporting plate is arranged on tobacco juice separator box
Top, the fume extractor and chimney are respectively mounted on the supporting plate, and the chimney is arranged on the side of fume extractor, the deodorization
Screen pack is arranged in chimney.
Further, the micro bubble apparatus includes the first motor, appendix, connecting hole, scattered gas impeller and gas transmission
Hole, one end of the appendix are connected with the first motor, and the connecting hole is arranged on gas transmission pipe outer wall, the appendix
The other end is connected with scattered gas impeller, and the transfer port is arranged on the other end of appendix, the scattered gas impeller and the equal position of transfer port
In in tobacco juice blending bin.
Further, the inside of the appendix is cavity structure, and the connecting hole is connected by leading smoke pipe with blower fan.
Further, the tobacco juice blending bin is internally provided with inclined bottom surface.
Further, the fume extractor includes the second motor, cam, circular groove, connecting tube and the second motor
Axle, the circular groove are arranged on the front side of the second motor, the cam and the second motor axis connection, the cam and
Two drive motor shafts are respectively positioned in circular groove, and the connecting tube is ridden upon on cam, and connecting tube is located at the inwall of cam and circular groove
Between, the both ends of the connecting tube expose to circular groove.
Further, one end of the connecting tube is connected with tobacco juice separator box, and the other end and the chimney of the connecting tube connect
Connect, the material of the connecting tube is silica gel material.
Further, for power plant exhuast gas desulfurization denitration filtration equipment for clarifying filter method, its feature is：It is described
Filter method is as follows：
The first step：Connect the power switch of the filtration equipment for clarifying, now cooling device, blower fan, water pump, the first motor and
Second motor is started working；
Second step：By blower fan, the flue gas of non-purified filtering is entered in the filtration equipment for clarifying from smoke inlet；
3rd step：The flue gas of non-purified filtering enters back into cooling device after smoke inlet enters filter filtering；
4th step：Particle after filtering is fallen into disposal box, and the humid air that humidified device sprays sticks；
5th step：Flue gas into cooling device is cooled down in cooling tube, and the flue gas after cooling enters blower fan；
6th step：Into blower fan flue gas in the presence of micro bubble apparatus, be inhaled into tobacco juice blending bin, and mixed with tobacco juice
Desulphurization denitration liquid in case is mixed；
7th step：Mixed liquid by drain pipe flow into tobacco juice separator box in, then by tobacco juice separator box liquid qi leel from；
8th step：The flue gas of not nitrogen-containing oxide and sulfur dioxide is separated, is entered by fume extractor in chimney, most passed through afterwards
Deodorization screen pack deodorization is crossed, is discharged further onto in air；
9th step：The liquid separated by tobacco juice separator box, tobacco juice is again flowed into by water pump, catheter and inlet and mixed
In case.
Compared with prior art, the present invention has advantages below：This is used for the exhuast gas desulfurization denitration filtration equipment for clarifying of power plant
Using the design of humidifier, micro bubble apparatus, water pump, fume extractor and deodorization screen pack, humidifier can increase in disposal box
Humidity, be advantageous to malaria absorption dust particles, avoid staff extract out disposal box processing dust particles
When, dust particles disorderly fly, and are advantageous to the physical and mental health of staff, by the first motor, appendix, connecting hole, scattered gas
The micro bubble apparatus that impeller and transfer port are formed, can stir the liquid of tobacco juice blending bin, and can increase flue gas and be mixed with tobacco juice
It the contact area of liquid in mould assembling, can be mixed liquid of the flue gas quickly with tobacco juice blending bin, being advantageous to increase should
The speed of filtration equipment for clarifying desulphurization denitration, the design of water pump, it can make to be back to tobacco juice by the liquid that tobacco juice separator box separates
In blending bin, continue to carry out purification filtering to the follow-up flue gas into tobacco juice blending bin, be advantageous to desulfurization in tobacco juice blending bin
The recycling of denitration liquid, the fume extractor being made up of the second motor, cam, circular groove and connecting tube, can speed up tobacco juice
The not mass rate of emission of the flue gas of nitrogen-containing oxide and sulfur dioxide in separator box, the design of deodorization screen pack, can absorb and be free of
Stink in nitrogen oxides and sulfur dioxide flue gas, is advantageous to environment purification.
Brief description of the drawings
Fig. 1 is the structural representation of the exhuast gas desulfurization denitration filtration equipment for clarifying for power plant of the embodiment of the present invention.
Fig. 2 is the structural representation of the micro bubble apparatus of the embodiment of the present invention.
Fig. 3 is the structural representation inside the disposal box of the embodiment of the present invention.
Fig. 4 is the structural representation of the fume extractor of the embodiment of the present invention.
Label declaration：1- smoke inlets, 2- filters, 3- disposal boxes, 4- cooling devices, 5- cooling tubes, 6- blower fans, 7- are led
Smoke pipe, 8- support bases, 9- micro bubble apparatus, the blending bin of 10- tobacco juices, 11- drain pipes, 12- tobacco juices separator box, 13- water pumps,
14- catheters, 15- inlets, 16- supporting plates, 17- fume extractors, 18- chimneys, 19- deodorizations screen pack, 20- humidifiers,
The motors of 901- first, 902- appendixs, 903- connecting holes, 904- dissipate gas impeller, 905- transfer ports, 1701- second and driven
Motor, 1702- cams, 1703- circular grooves, 1704- connecting tubes.
Embodiment
Below in conjunction with the accompanying drawings and the present invention is described in further detail by embodiment, and following examples are to this hair
Bright explanation and the invention is not limited in following examples.
Embodiment.
Referring to shown in Fig. 1 to Fig. 4, it should however be clear that structure, ratio, size depicted in this specification institute accompanying drawings etc., only use
To coordinate the content disclosed in specification, so that those skilled in the art understands and reads, being not limited to the present invention can
The qualifications of implementation, therefore do not have technical essential meaning, the tune of the modification of any structure, the change of proportionate relationship or size
It is whole, in the case where not influenceing the effect of present invention can be generated and the purpose that can reach, all should still fall in disclosed skill
In the range of art content can cover.Meanwhile if in this specification with quote as " on ", " under ", "left", "right", " centre " and
The term of " one " etc., understanding for narration is merely convenient to, and is not used to limit the enforceable scope of the present invention, its relativeness
It is altered or modified, in the case where changing technology contents without essence, when being also considered as the enforceable category of the present invention.
The exhuast gas desulfurization denitration filtration equipment for clarifying for power plant in the present embodiment include smoke inlet 1, filter 2,
Disposal box 3, cooling device 4, cooling tube 5, blower fan 6, lead smoke pipe 7, support base 8, micro bubble apparatus 9, tobacco juice blending bin 10, go out
Liquid pipe 11, tobacco juice separator box 12, water pump 13, catheter 14, inlet 15, supporting plate 16, fume extractor 17, chimney 18, deodorization
Screen pack 19 and humidifier 20, smoke inlet 1 are connected with filter 2, and filter 2 is arranged on disposal box 3, and humidifier 20 is pacified
In disposal box 3, cooling device 4 is connected with filter 2, and one end of cooling tube 5 is arranged in cooling device 4, cooling tube 5
The other end be connected with blower fan 6, blower fan 6 is connected by leading smoke pipe 7 with micro bubble apparatus 9, micro bubble apparatus 9 be arranged on support bottom
On seat 8, the end of micro bubble apparatus 9 is located in tobacco juice blending bin 10, and inlet 15 is arranged on the top of tobacco juice blending bin 10, cigarette
Liquid blending bin 10 is connected by drain pipe 11 with tobacco juice separator box 12, and water pump 13 is arranged in tobacco juice separator box 12, and water pump 13 is logical
Cross catheter 14 to be connected with inlet 15, supporting plate 16 is arranged on the top of tobacco juice separator box 12, fume extractor 17 and chimney 18
It is installed in supporting plate 16, chimney 18 is arranged on the side of fume extractor 17, and deodorization screen pack 19 is arranged in chimney 18.
Micro bubble apparatus 9 in the present embodiment includes the first motor 901, appendix 902, connecting hole 903, scattered gas leaf
Wheel 904 and transfer port 905, one end of appendix 902 are connected with the first motor 901, and connecting hole 903 is arranged on appendix
902 outer walls, the other end of appendix 902 are connected with scattered gas impeller 904, and transfer port 905 is arranged on the other end of appendix 902,
Dissipate gas impeller 904 and transfer port 905 is respectively positioned in tobacco juice blending bin 10；The inside of appendix 902 is cavity structure, connecting hole
903 are connected by leading smoke pipe 7 with blower fan 6；Tobacco juice blending bin 10 is internally provided with inclined bottom surface；Fume extractor includes second and driven
Dynamic motor 1701, cam 1702, circular groove 1703, the drive motor shaft 1705 of connecting tube 1704 and second, circular groove 1703 are arranged on the
The front side of two motors 1701, cam 1702 are connected with the second drive motor shaft 1705, the motor of cam 1702 and second
Axle 1705 is respectively positioned in circular groove 1703, and connecting tube 1704 is ridden upon on cam 1702, and connecting tube 1704 be located at cam 1702 with
Between the inwall of circular groove 1703, the both ends of connecting tube 1704 expose to circular groove 1703；One end of connecting tube 1704 and tobacco juice point
Connected from case 12, the other end of connecting tube 1704 is connected with chimney 18, and the material of connecting tube 1704 is silica gel material.
All orientation description in the present embodiment is defined by Fig. 1.
The filter method of the exhuast gas desulfurization denitration filtration equipment for clarifying for power plant in the present embodiment is as follows：
The first step：The power switch of the filtration equipment for clarifying is connected, now cooling device 4, blower fan 6, the driving electricity of water pump 13, first
The motor 1701 of machine 901 and second is started working；
Second step：By blower fan 6, the flue gas of non-purified filtering is entered in the filtration equipment for clarifying from smoke inlet 1；
3rd step：The flue gas of non-purified filtering enters back into cooling device 4 after smoke inlet 1 enters the filtering of filter 2；
4th step：Particle after filtering is fallen into disposal box 3, and the humid air that humidified device 20 sprays sticks；
5th step：Flue gas into cooling device 4 is cooled down in cooling tube 5, and the flue gas after cooling enters blower fan 6；
6th step：Into blower fan 6 flue gas in the presence of micro bubble apparatus 9, be inhaled into tobacco juice blending bin 10, and and tobacco juice
Desulphurization denitration liquid in blending bin 10 is mixed；
7th step：Mixed liquid is flowed into tobacco juice separator box 12 by drain pipe 11, then by the liquid gas of tobacco juice separator box 12
Separation；
8th step：The flue gas of not nitrogen-containing oxide and sulfur dioxide is separated, is entered by fume extractor 17 in chimney 18, most
Afterwards by the deodorization of deodorization screen pack 19, it is discharged further onto in air；
9th step：The liquid separated by tobacco juice separator box 12, again flowed into by water pump 13, catheter 14 and inlet 15
In tobacco juice blending bin 10.
It is above the filter method of the exhuast gas desulfurization denitration filtration equipment for clarifying for being used for power plant.
Furthermore, it is necessary to illustrate, the specific embodiment described in this specification, the shape of its parts and components, it is named
Title etc. can be different, and the above content described in this specification is only to structure example explanation of the present invention.It is all according to
The equivalence changes or simple change done according to the construction described in inventional idea of the present invention, feature and principle, are included in this hair
In the protection domain of bright patent.Those skilled in the art can do various to described specific embodiment
The modification of various kinds or supplement are substituted using similar mode, without departing from structure of the invention or surmount present claims
Scope defined in book, protection scope of the present invention all should be belonged to.
Claims (7)
- A kind of 1. exhuast gas desulfurization denitration filtration equipment for clarifying for power plant, it is characterised in that：Including smoke inlet, filter, Disposal box, cooling device, cooling tube, blower fan, lead smoke pipe, support base, micro bubble apparatus, tobacco juice blending bin, drain pipe, tobacco juice Separator box, water pump, catheter, inlet, supporting plate, fume extractor, chimney, deodorization screen pack and humidifier, the smoke inlet It is connected with filter, the filter is arranged on disposal box, and the humidifier is arranged in disposal box, the cooling dress Put and be connected with filter, one end of the cooling tube is arranged in cooling device, and the other end and the blower fan of the cooling tube connect Connect, the blower fan is connected by leading smoke pipe with micro bubble apparatus, and the micro bubble apparatus is arranged in support base, micro- gas The end of bulb apparatus is located in tobacco juice blending bin, and the inlet is arranged on the top of tobacco juice blending bin, the tobacco juice blending bin It is connected by drain pipe with tobacco juice separator box, the water pump is arranged in tobacco juice separator box, and the water pump is by catheter with entering Liquid mouth is connected, and the supporting plate is arranged on the top of tobacco juice separator box, and the fume extractor and chimney are respectively mounted on the supporting plate, The chimney is arranged on the side of fume extractor, and the deodorization screen pack is arranged in chimney.
- 2. the exhuast gas desulfurization denitration filtration equipment for clarifying according to claim 1 for power plant, it is characterised in that：It is described micro- Air bubble apparatus includes the first motor, appendix, connecting hole, dissipates gas impeller and transfer port, one end of the appendix and the One motor connects, and the connecting hole is arranged on gas transmission pipe outer wall, and the other end of the appendix is connected with scattered gas impeller, institute The other end that transfer port is arranged on appendix is stated, the scattered gas impeller and transfer port are respectively positioned in tobacco juice blending bin.
- 3. the exhuast gas desulfurization denitration filtration equipment for clarifying according to claim 1 for power plant, it is characterised in that：It is described defeated The inside of tracheae is cavity structure, and the connecting hole is connected by leading smoke pipe with blower fan.
- 4. the exhuast gas desulfurization denitration filtration equipment for clarifying according to claim 1 for power plant, it is characterised in that：The cigarette Liquid blending bin is internally provided with inclined bottom surface.
- 5. the exhuast gas desulfurization denitration filtration equipment for clarifying according to claim 1 for power plant, it is characterised in that：The row Cigarette device includes the second motor, cam, circular groove, connecting tube and the second drive motor shaft, and the circular groove is arranged on the second drive The front side of dynamic motor, the cam and the second motor axis connection, the cam and the second drive motor shaft are respectively positioned on circular groove Interior, the connecting tube is ridden upon on cam, and connecting tube, between cam and the inwall of circular groove, the both ends of the connecting tube are equal Expose to circular groove.
- 6. the exhuast gas desulfurization denitration filtration equipment for clarifying according to claim 1 for power plant, it is characterised in that：The company One end of adapter is connected with tobacco juice separator box, and the other end of the connecting tube is connected with chimney, and the material of the connecting tube is silicon Glue material matter.
- A kind of 7. exhuast gas desulfurization denitration filtration equipment for clarifying for power plant in 1-6 such as claim as described in any claim Filter method, it is characterised in that：The filter method is as follows：The first step：Connect the power switch of the filtration equipment for clarifying, now cooling device, blower fan, water pump, the first motor and Second motor is started working；Second step：By blower fan, the flue gas of non-purified filtering is entered in the filtration equipment for clarifying from smoke inlet；3rd step：The flue gas of non-purified filtering enters back into cooling device after smoke inlet enters filter filtering；4th step：Particle after filtering is fallen into disposal box, and the humid air that humidified device sprays sticks；5th step：Flue gas into cooling device is cooled down in cooling tube, and the flue gas after cooling enters blower fan；6th step：Into blower fan flue gas in the presence of micro bubble apparatus, be inhaled into tobacco juice blending bin, and mixed with tobacco juice Desulphurization denitration liquid in case is mixed；7th step：Mixed liquid by drain pipe flow into tobacco juice separator box in, then by tobacco juice separator box liquid qi leel from；8th step：The flue gas of not nitrogen-containing oxide and sulfur dioxide is separated, is entered by fume extractor in chimney, most passed through afterwards Deodorization screen pack deodorization is crossed, is discharged further onto in air；9th step：The liquid separated by tobacco juice separator box, tobacco juice is again flowed into by water pump, catheter and inlet and mixed In case.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710951987.9A CN107754585A (en) | 2017-10-13 | 2017-10-13 | A kind of exhuast gas desulfurization denitration filtration equipment for clarifying and filter method for power plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710951987.9A CN107754585A (en) | 2017-10-13 | 2017-10-13 | A kind of exhuast gas desulfurization denitration filtration equipment for clarifying and filter method for power plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107754585A true CN107754585A (en) | 2018-03-06 |
Family
ID=61268221
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710951987.9A Pending CN107754585A (en) | 2017-10-13 | 2017-10-13 | A kind of exhuast gas desulfurization denitration filtration equipment for clarifying and filter method for power plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107754585A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108894079A (en) * | 2018-06-29 | 2018-11-27 | 深圳市安思科电子科技有限公司 | A kind of bitumen regeneration equipment of favorable regeneration effect |
| CN109652610A (en) * | 2019-01-09 | 2019-04-19 | 杨帅 | A kind of exhaust-gas efficient processing converter |
| CN111721111A (en) * | 2020-06-30 | 2020-09-29 | 龙南县中利再生资源开发有限公司 | Phosphor waste material bakes burning furnace over a slow fire |
| CN112403260A (en) * | 2020-11-17 | 2021-02-26 | 江苏绿都环境工程有限公司 | Desulfurization and denitrification integrated discharge system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1131580A (en) * | 1994-11-08 | 1996-09-25 | 三菱重工业株式会社 | Gas-liquid contactor and wet flue-gas desulfurization system |
| CN103212292A (en) * | 2013-04-12 | 2013-07-24 | 陕西华祥能源科技集团有限公司 | Integrated flue gas dust removal desulfurization and denitrification device |
| CN205435389U (en) * | 2015-12-31 | 2016-08-10 | 浙江机电职业技术学院 | Integral type sea water desulfurization denitrogenation tail gas processing apparatus |
| CN205516924U (en) * | 2016-04-07 | 2016-08-31 | 尹怡思 | A environment -friendly purification device for room air |
| WO2017096692A1 (en) * | 2015-12-09 | 2017-06-15 | 深圳广昌达环境科学有限公司 | Fuel gas denitration and desulfurization washing system and denitration and desulfurization method |
| CN207641270U (en) * | 2017-10-13 | 2018-07-24 | 华电电力科学研究院 | A kind of exhuast gas desulfurization denitration filtration equipment for clarifying for power plant |
-
2017
- 2017-10-13 CN CN201710951987.9A patent/CN107754585A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1131580A (en) * | 1994-11-08 | 1996-09-25 | 三菱重工业株式会社 | Gas-liquid contactor and wet flue-gas desulfurization system |
| CN103212292A (en) * | 2013-04-12 | 2013-07-24 | 陕西华祥能源科技集团有限公司 | Integrated flue gas dust removal desulfurization and denitrification device |
| WO2017096692A1 (en) * | 2015-12-09 | 2017-06-15 | 深圳广昌达环境科学有限公司 | Fuel gas denitration and desulfurization washing system and denitration and desulfurization method |
| CN205435389U (en) * | 2015-12-31 | 2016-08-10 | 浙江机电职业技术学院 | Integral type sea water desulfurization denitrogenation tail gas processing apparatus |
| CN205516924U (en) * | 2016-04-07 | 2016-08-31 | 尹怡思 | A environment -friendly purification device for room air |
| CN207641270U (en) * | 2017-10-13 | 2018-07-24 | 华电电力科学研究院 | A kind of exhuast gas desulfurization denitration filtration equipment for clarifying for power plant |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108894079A (en) * | 2018-06-29 | 2018-11-27 | 深圳市安思科电子科技有限公司 | A kind of bitumen regeneration equipment of favorable regeneration effect |
| CN109652610A (en) * | 2019-01-09 | 2019-04-19 | 杨帅 | A kind of exhaust-gas efficient processing converter |
| CN111721111A (en) * | 2020-06-30 | 2020-09-29 | 龙南县中利再生资源开发有限公司 | Phosphor waste material bakes burning furnace over a slow fire |
| CN112403260A (en) * | 2020-11-17 | 2021-02-26 | 江苏绿都环境工程有限公司 | Desulfurization and denitrification integrated discharge system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107754585A (en) | A kind of exhuast gas desulfurization denitration filtration equipment for clarifying and filter method for power plant | |
| CN107614892B (en) | Turbine type blower with waterproof and moistureproof | |
| CN108554158A (en) | A kind of high temperature and humidity flue gas cool-down desulfurizing and purifying system | |
| JP2010279937A (en) | Oil mist collector | |
| CN202538580U (en) | Hydraulic push type desulfurization dust remover | |
| CN207203660U (en) | A kind of vertical demister | |
| CN201912859U (en) | Spiral guide plate type desulfurization equipment | |
| CN206793275U (en) | A kind of damp strips dust arrester | |
| CN207641270U (en) | A kind of exhuast gas desulfurization denitration filtration equipment for clarifying for power plant | |
| CN107174905A (en) | Water-fog type centrifugal dust collection device | |
| CN107051098B (en) | Gas-liquid separator | |
| CN106918089A (en) | A kind of air purifier being convenient to clean | |
| CN205760166U (en) | A kind of demister with dual defrosting function for wet desulphurization | |
| CN108837602A (en) | Efficient turbine cigarette vapour clarification system | |
| CN205886495U (en) | Gas -liquid separating device | |
| CN211487041U (en) | Oil smoke separating and purifying device | |
| CN205913951U (en) | Simple and easy rapid defogging device | |
| CN207605532U (en) | A kind of Wet process flue gas purifier | |
| CN107335329A (en) | Snail type spiral vortex denitrating flue gas desulfurization and dedusting one clarifier | |
| CN205914001U (en) | Rapid defogging device | |
| CN109011855B (en) | Device for removing fine particles in gas by virtue of supergravity | |
| CN105536416A (en) | Desulfurization and denitrification dust removal device | |
| CN206229131U (en) | One kind utilizes water wind dedusting equipment integrating | |
| CN209188471U (en) | A kind of out of stock integrated treatment unit of dust-removal and desulfurizing | |
| CN208757184U (en) | A kind of novel energy-conserving air purifier |
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 | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180306 |