CN106975314A - A kind of modularization dynamic gas purifying column - Google Patents
A kind of modularization dynamic gas purifying column Download PDFInfo
- Publication number
- CN106975314A CN106975314A CN201710345374.0A CN201710345374A CN106975314A CN 106975314 A CN106975314 A CN 106975314A CN 201710345374 A CN201710345374 A CN 201710345374A CN 106975314 A CN106975314 A CN 106975314A
- Authority
- CN
- China
- Prior art keywords
- reactors
- reactor
- tube
- airway tube
- purifying column
- 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
Classifications
-
- 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
- B01D53/02—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
-
- 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
- B01D53/75—Multi-step processes
-
- 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
- B01D53/80—Semi-solid phase processes, i.e. by using slurries
-
- 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
- B01D53/86—Catalytic processes
- B01D53/8603—Removing sulfur compounds
-
- 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
- B01D53/86—Catalytic processes
- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8628—Processes characterised by a specific catalyst
-
- 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
- B01D53/86—Catalytic processes
- B01D53/8668—Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/12—Methods and means for introducing reactants
- B01D2259/126—Semi-solid reactants, e.g. slurries
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a kind of modularization dynamic gas purifying column, including collection slag bath, base, one or more horizontal reactors put are provided with the base, realize that gas circuit is connected by airway tube between the multiple reactor, the reactor includes reactor housing, stuffing box, sealing ring, rotary shaft, bearing block, discharging tube, drive, batching hole, drug-feeding tube and dumping pit, modularization dynamic gas purifying column of the present invention can be according to the purification processes demand of specific gas type from the assembling quantity of reactor and the type of packing material, use very flexible, it is adapted to the purification processes of variety classes gas, reactor is by the way of horizontal put, can be along axis rotation, change the built-in filler of conventional tower equipment can only stacking motionless Ta Neiwensi state, so that filler can free movement inside reactor, collision, from without hardened, bias current, liquid flooding, the defect of crystallization.
Description
Technical field
The present invention relates to the technical field applied to industrial multicomponent gas, dust-laden high-temperature gas purification processes device, tool
Body is a kind of modularization dynamic gas purifying column.
Background technology
In works such as the whole world all power plant, coke-oven plant, calcining petroleum coke kiln, silicic acid saltworks, the smelteries of coal and oil
In ore deposit enterprise, desulphurization and denitration in fume treatment, dedirt cooling are one the problem of do not allow disposable.Due to giving up for these factories
It is large-minded how very big, be ten tens of thousands of, hundreds of thousands m3/h at the drop of a hat, many used on small tolerance desulphurization denitration the heart should
The technology of hand, the operating cost that just seems in the atm number of these factories is high must to be difficult to bear (such as ammonia process, ammonia-catalyzed
Method, zinc oxide method, anthraquinone disulphonate method, cobalt molybdenum hydroconversion process etc.).Then, most of factories still have selected economically
Limestone-gypsum method, two alkaline process or their deriving method that can be born.
Meanwhile, the drawbacks of also having to bear the method --- nearly ubiquitous gypsum, calcium carbonate knot in technical process
Crystalline substance, the problem of removal effect is undesirable, maintenance capacity is big, and crystallize the plenty of time paid, human and material resources, wealth to exclude
Power, environment, carry out production strictly in line with rules and regulations in terms of cost.
The desulphurization plant problem of limestone-gypsum method and the method and its equipment of denitration are the very corns of a subject.Although chemical industry
The traditional classical equipment of gas-liquid gas-solid, which is saved your breath also, in the world three, 40 kind, be difficult really to find a kind of entirely appropriate power plant's air
Measure the ideal equipment of desulphurization denitration.
Hollow-spraying-tower desulfurization resistance is small, maintenance is easy, but gas-liquid contact time is short, efficiency is low, hardly possible is up to standard, and denitration effect is not
It is good；
Tubulent contact tower and rotating stream tray scrubber desulfuration efficiency are high, good absorbing, but resistance is big, operating flexibility is small, atm number and variability
Tolerance bad adaptability, same denitration effect is not good；
Packed tower efficiency high, good absorbing, resistance are low, operating flexibility is big, but gas velocity is strictly limited, once crystallization will make resistance
Power is quick-fried to rise, and liquid is unable to come down, and gas does not increase, and liquid flooding is caused disaster, and causes to stop production, also denitration is undesirable；
Bubble column, plate column, foaming tower, atomisation tower are also to be difficult to be competent at.
" a workman must first sharpen his tools if he is to do his work well ", the tower tower class for have anything to take into account desulphurization and denitration, dedusting, cooling can be fitted
The desulphurization and denitration of conjunction limestone-gypsum method, dedirt, cooling feature, this is that countless scholars and engineer dream of.
Lime-gypsum method is successful low-cost processes sulfur-bearing, the technology containing nitre, the high temperature atmosphere amount waste gas of dust-laden, but
Serious crystallization allows user to be in the scale removal being without end, dredge, change pipe and change among pump etc. repairs；Packed tower is in processing gas-liquid
It is very outstanding in terms of mass transfer, but is used at this occasion no one ventured crystallized everywhere；Activated coke is the good material of desulphurization denitration, but adopts
It is easy to form calcium dioxide crystallization in equipment with the technique of lime-gypsum method, activated coke to masking, just can not be played
The effectiveness of activated coke.
The content of the invention
It is an object of the invention to provide a kind of modularization dynamic gas purifying column, to solve to propose in above-mentioned background technology
The problem of.
To achieve the above object, the present invention provides following technical scheme：A kind of modularization dynamic gas purifying column, including collection
It is provided with slag bath, base, the base between one or more horizontal reactors put, the multiple reactor by leading
Tracheae realize gas circuit connect, the reactor include reactor housing, stuffing box, sealing ring, rotary shaft, bearing block, discharging tube,
Drive, batching hole, drug-feeding tube and dumping pit, the rotary shaft run through the axle center of stuffing box, are fixedly connected with stuffing box, described
Stuffing box is arranged on reactor enclosure interior and rotated by rotary shaft two ends with being arranged on the bearing block at reactor housing two ends
Connection, the rotary shaft is provided with sealing ring with reactor housing junction, and described rotary shaft one end is provided with drive, described anti-
Still shell body upper end is answered to be provided with batching hole and drug-feeding tube, the reactor housing lower end is provided with dumping pit and discharging tube.
It is preferred that, the reactor quantity sets five, including reactor, No. two reactors, No. three reactors, four
Number reactor and No. five reactors；A number reactor, No. two reactors are set in parallel on base, special-shaped airway tube one end
Connected with a reactor housing, the other end is connected with No. two reactor housings, a reactor and No. two reactors pass through different
Shape airway tube realizes that gas circuit is connected；No. three reactors are arranged on above a reactor and No. two reactors, airway tube one
End is connected with No. two reactor housings, and the other end is connected with No. three reactor housings, and No. two reactors and No. three reactors pass through
Airway tube realizes that gas circuit is connected；No. four reactors are arranged on above No. three reactors, airway tube one end and No. three reactors
Batching hole connection, the other end connects with the discharging tube of No. four reactors, and No. three reactors and No. four reactors pass through airway tube
Realize that gas circuit is connected；No. five reactors are arranged on above No. four reactors, and airway tube one end feeds intake with No. four reactors
Hole is connected, and the other end is connected with the discharging tube of No. five reactors, and No. four reactors and No. five reactors realize gas by airway tube
Road is connected.
It is preferred that, the reactor housing side is provided with air inlet.
It is preferred that, provided with supporting blind pipe, the special-shaped airway tube lower end between a reactor and No. three reactors
Provided with discharging tube, between No. three reactors and No. four reactors be provided with intermediate support, No. four reactors with No. five instead
Answer and intermediate support is provided between kettle, No. five reactor upper ends are provided with exhaust outlet.
It is preferred that, the drive on a reactor and No. two reactors is connected to motor, and No. one is anti-
Answer between kettle and No. three reactors, between No. three reactors and No. four reactors, between No. four reactors and No. five reactors
Drive is connected by chain two-by-two, and is carried out by the drive being arranged on a reactor for power source
Transmission.
It is preferred that, corresponding filler is filled with inside the stuffing box according to actual needs.
Compared with prior art, the beneficial effects of the invention are as follows：This modularization dynamic gas purifying column can be according to specific
The purification processes demand of gas type is used very clever from the assembling quantity of reactor and the type of packing material
It is living, it is adapted to the purification processes of variety classes gas；
Having overturned tower equipment can only be using erectting the method that put installed, and the method put using Horizontal type；
Overturned Common fluids in tower equipment can only axial counter-current flow method, employ radially inverse in horizontal tower
The method of flowing；
The method that tower equipment can only be erect to discharge side by side during multitower series connection has been overturned, many towers have been employed horizontal folded
The method put is placed, including horizontal direction is placed placed with vertically stacked side by side；
Overturned the built-in filler of conventional tower equipment can only stacking motionless Ta Neiwensi state, being altered to filler can
In reactor intrinsic displacement, collision, rolling, slump etc.；
The situation that tower equipment flow area and designed capacity are restricted by tower internal diameter single factors completely has been overturned, has been altered to
The size of flow area can be changed by changing reactor length and height coefficient, flow area is significantly extended；
Earthfill rockfill concrete riprap RCC tower equipment has been overturned to abstain from very much hardened filler, crystallization, gas-liquid bias current, especially the feelings of liquid flooding occur
Condition, be altered to allow filler inside reactor can free movement, collision, from without hardened, bias current, liquid flooding, crystallization
Defect；
Overturned the actionless pattern of part inside and outside earthfill rockfill concrete riprap RCC tower equipment, by reactor it is horizontally-arranged after be divided into it is fixed not
Dynamic housing and it is supported on housing two ends and is dallied in shell internal frame dynamic stuffing box；
Earthfill rockfill concrete riprap RCC tower equipment is overturned there was only one, two kind of process function, a kind of deficiency of filler can only be loaded, has become
It can according to the actual requirements be divided among in differential responses kettle and install variety classes filler additional, once complete setting for multiple different process
It is standby.
Brief description of the drawings
Fig. 1 is overall structure diagram of the invention；
Fig. 2 is overall structure left view of the invention；
Fig. 3 is overall structure top view of the invention；
Fig. 4 is the present invention one, two, No. three reactor cross-sectional views；
Fig. 5 is reactor structural representation of the present invention；
Fig. 6 is reactor cross-sectional view of the present invention.
In figure：1- collection slag baths；2- bases；3- reactors；Number reactor of 31-；311- air inlets；No. bis- reactors of 32-；
No. tri- reactors of 33-；No. tetra- reactors of 34-；No. five reactors of 35-；4- reactor housings；5- stuffing boxes；6- sealing rings；7- turns
Moving axis；8- bearing blocks；9- fillers；10- discharging tubes；11- drives；12- batching holes；13- drug-feeding tubes；14- dumping pits；15- is led
Tracheae；151- abnormity airway tubes；152- supports blind pipe；16- intermediate supports；17- exhaust outlets；18- motors；19- chains.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Refer in Fig. 1-6, the embodiment of the present invention, a kind of modularization dynamic gas purifying column, including collection slag bath (1), bottom
Five horizontal reactors (3) put, including reactor (31), No. two reactions are provided with seat (2), the base (2)
Kettle (32), No. three reactors (33), No. four reactors (34) and No. five reactors (35)；The reactor (3) includes reactor
Housing (4), stuffing box (5), sealing ring (6), rotary shaft (7), bearing block (8), discharging tube (10), drive (11), batching hole
(12), drug-feeding tube (13) and dumping pit (14), the rotary shaft (7) run through the axle center of stuffing box (5), fixed with stuffing box (5)
Connection, the stuffing box (5) is arranged on reactor housing (4) inside and by rotary shaft (7) two ends with being arranged on reaction still shell
The bearing block (8) at body (4) two ends rotates connection, and the rotary shaft (7) is provided with sealing ring (6) with reactor housing (4) junction,
Described rotary shaft (7) one end is provided with drive (11), and reactor housing (4) upper end is provided with batching hole (12) and enters medicine
Manage (13), reactor housing (4) lower end is provided with dumping pit (14) and discharging tube (10)；A number reactor (31),
No. two reactors (32) are set in parallel on base (2), and a reactor (31) the housing side is provided with air inlet (311),
Provided with supporting blind pipe (152) between a number reactor (31) and No. three reactors (33), supporting blind pipe (152) one end and one
Number reactor (31) housing connection, the other end is fixedly connected with No. three reactor (33) housings, is played assistance airway tube (15) and is propped up
The effect of No. three reactors (33) is held, supporting blind pipe (152) one side is connected with special-shaped airway tube (151) one end, special-shaped air guide
Pipe (151) other end is connected with No. two reactor (32) housings, and special-shaped airway tube (151) lower end is provided with discharging tube (10), convenient
The slag liquid discharge in pipe is deposited in, a reactor (31) and No. two reactors (32) realize gas by special-shaped airway tube (151)
Road is connected；No. three reactors (33) are arranged on above a reactor (31) and No. two reactors (32), airway tube (15)
One end is connected with No. two reactor (32) housings, and the other end is connected with No. three reactor (33) housings, No. two reactors (32) and
No. three reactors (33) realize that gas circuit is connected by airway tube (15)；No. four reactors (21) are arranged on No. three reactors
(16) top, airway tube (15) one end is connected with the batching hole (12) of No. three reactors (33), the other end and No. four reactors
(34) discharging tube (10) connection, No. three reactors (33) and No. four reactors (34) realize that gas circuit connects by airway tube (15)
It is logical；Intermediate support (16) is provided between No. three reactors (33) and No. four reactors (34), intermediate support (16) plays solid
The effect of fixed No. three reactors (33) and No. four reactors (34), it is same to enter to play a part of having supported No. four reactors (34)；Institute
State No. five reactors (35) to be arranged on above No. four reactors (34), airway tube (15) one end feeds intake with No. four reactor (34)
Hole (12) is connected, and the other end is connected with the discharging tube (10) of No. five reactors (35), No. four reactors (34) and No. five reactors
(35) realize that gas circuit is connected by airway tube (15)；Provided with centre between No. four reactors (34) and No. five reactors (35)
Support (16), intermediate support (16) plays a part of fixing No. four reactors (34) and No. five reactors (35), same to enter to play branch
Hold and play No. five reactors (35)；No. five reactors (35) upper end is provided with exhaust outlet (17), exhaust outlet (17) and five
Batching hole (12) connection above number reactor (35), exhaust outlet (17) for gas after purification outlet；A number reactor
(31) and the drive (11) on No. two reactors (32) is connected to motor (18), a reactor (31) with No. three
Between reactor (33), between No. three reactors (33) and No. four reactors (34), No. four reactors (34) and No. five reactors
(35) drive (11) between is connected by chain (19) two-by-two, and by being arranged on a reactor (31)
Drive (11) be driven for power source, the stuffing box (5) inside the effect of transmission, each reactor housing (4)
Can be axle center start to rotate with rotary shaft (7), so as to drive the internal filler (9) of stuffing box (5) and reactor (3) internal
Gas to be purified carries out rotation displacement；Corresponding filler (9) is filled with according to actual needs inside the stuffing box (5).
Such as with the sulfur-bearing from boiler, calcining petroleum coke kiln, roasting furnace or reverberatory furnace, the high temperature containing nitre, dust-laden
Illustrate the equipment course of work exemplified by gas purification, high-temperature gas enters one from the air inlet (311) of a reactor (31)
Number reactor (31) is internal, and the stuffing box (5) in a reactor (31) is equipped with aluminum alloy filler (9), and high-temperature gas is through dynamic
Stuffing box (5) is drilled among the space of aluminum alloy filler (9), and water-main is entered by one in the surface of aluminum alloy filler (9)
The water that drug-feeding tube (13) in number reactor (31) batching hole (12) is sprayed with multiple valves is moistened, and walks gas therein
The dust of body entrained with is adhered in water one after another in unnumbered collision, into the discharging tube of reactor (31) lower end
(10) system is flowed downward out with water, gas then completes dedusting and the process suitably cooled, packing layer is passed upward, it is blind along supporting
Pipe (152) enters special-shaped tracheae (151)；
Gas enters No. two reactors along special-shaped tracheae (151), then from No. two reactor (32) bottoms through stainless (steel) wire
(32) the huge activated coke filler (9) of the specific surface area of granularity 20~50, gas, are filled in the stuffing box (5) of No. two reactors (32)
Body is collided and walked tortuously between activated coke, and absorption, catalysis, the decomposition of activated coke are always carved in this process
Ground is carried out, and contained sulfide, nitrogen oxides, hydrophobicity organic matter, superfine dust are decomposed or adsorbed one after another, leave activity
During burnt packing layer, most of pollutant has been decomposed or intercepted, and leaves the gas of packing layer, by airway tube (15) from
No. three reactor (33) bottoms are internal into No. three reactors (33), and it is more to fill PPR in the stuffing box (5) of No. three reactors (33)
Face body filler (9), gas complications in the space of filler (9) are walked, with getting off to fall in filler from drug-feeding tube (13) sprinkle above
Lime slurry collision on surface, the filler surface impact several times contact through moistening, containing filth amount is more and more lower, then from surface
Multiple batching holes (12) enter airway tube (15), enter No. four reactors (34) through airway tube (15), and so far gas is completed three
Absorption process in number reactor (33).
Gas is in the internal purification process of No. four reactors (34), No. five reactors (35) and in No. three reactors (33)
It is identical.
Last gas is from exhaust outlet (17) discharge of No. five reactor (35) upper ends, and now gas is by an above dedusting
Cool kettle, activated coke adsoption catalysis decomposing pot, three dynamic filler lime slurry absorption kettles totally five reactor gas absorptions
Absorb, sulfur-bearing originally, the high-temperature gas containing nitre, dust-laden, which are processed to have reached, can discharge national standard；The final outlet of gas
It is to be sent out by air exhauster from exhaust outlet, the blade of blower fan rotates the negative pressure to form following each room, the power flowed as gas.
More than, it is only the present invention preferably embodiment, but protection scope of the present invention is not limited thereto, and it is any
Those familiar with the art the invention discloses technical scope in, technique according to the invention scheme and its invention
Design is subject to equivalent substitution or change, should all be included within the scope of the present invention.
Claims (6)
1. a kind of modularization dynamic gas purifying column, including collection slag bath (1), base (2), it is characterised in that：On the base (2)
It is provided between one or more horizontal reactors (3) put, the multiple reactor (3) and gas is realized by airway tube (15)
Road is connected, and the reactor (3) includes reactor housing (4), stuffing box (5), sealing ring (6), rotary shaft (7), bearing block
(8), discharging tube (10), drive (11), batching hole (12), drug-feeding tube (13) and dumping pit (14), the rotary shaft (7) are run through
The axle center of stuffing box (5), is fixedly connected with stuffing box (5), and it is internal and logical that the stuffing box (5) is arranged on reactor housing (4)
Cross rotary shaft (7) two ends be arranged on reactor housing (4) two ends bearing block (8) rotate be connected, the rotary shaft (7) with instead
Still shell body (4) junction is answered to be provided with sealing ring (6), described rotary shaft (7) one end is provided with drive (11), the reaction still shell
Body (4) upper end is provided with batching hole (12) and drug-feeding tube (13), reactor housing (4) lower end be provided with dumping pit (14) and
Discharging tube (10).
2. a kind of modularization dynamic gas purifying column according to claim 1, it is characterised in that：Reactor (3) number
Amount set five, including a reactor (31), No. two reactors (32), No. three reactors (33), No. four reactors (34) and
No. five reactors (35)；A number reactor (31), No. two reactors (32) are set in parallel on base (2), special-shaped air guide
Pipe (151) one end is connected with reactor (31) housing, and the other end is connected with No. two reactor (32) housings, a reactor
(31) realize that gas circuit is connected by special-shaped airway tube (151) with No. two reactors (32)；No. three reactors (33) are arranged on
Above a number reactor (31) and No. two reactors (32), airway tube (15) one end is connected with No. two reactor (32) housings, separately
One end is connected with No. three reactor (33) housings, and No. two reactors (32) and No. three reactors (33) are realized by airway tube (15)
Gas circuit is connected；No. four reactors (21) are arranged on above No. three reactors (16), airway tube (15) one end and No. three reactions
Batching hole (12) connection of kettle (33), the other end is connected with the discharging tube (10) of No. four reactors (34), No. three reactors (33)
Realize that gas circuit is connected by airway tube (15) with No. four reactors (34)；No. five reactors (35) are arranged on No. four reactors
(34) top, airway tube (15) one end is connected with the batching hole (12) of No. four reactors (34), the other end and No. five reactors
(35) discharging tube (10) connection, No. four reactors (34) and No. five reactors (35) realize that gas circuit connects by airway tube (15)
It is logical.
3. a kind of modularization dynamic gas purifying column according to claim 1,2, it is characterised in that：A number reactor
(31) housing side is provided with air inlet (311).
4. a kind of modularization dynamic gas purifying column according to claim 2, it is characterised in that：A number reactor
(31) provided with supporting blind pipe (152) between No. three reactors (33), special-shaped airway tube (151) lower end is provided with discharging tube
(10) intermediate support (16), No. four reactors, are provided between No. three reactors (33) and No. four reactors (34)
(34) intermediate support (16) is provided between No. five reactors (35), No. five reactors (35) upper end is provided with exhaust outlet
(17)。
5. a kind of modularization dynamic gas purifying column according to claim 2, it is characterised in that：A number reactor
(31) and the drive (11) on No. two reactors (32) is connected to motor (18), a reactor (31) with No. three
Between reactor (33), between No. three reactors (33) and No. four reactors (34), No. four reactors (34) and No. five reactors
(35) drive (11) between is connected by chain (19) two-by-two, and by being arranged on a reactor (31)
Drive (11) be driven for power source.
6. a kind of modularization dynamic gas purifying column according to claim 1, it is characterised in that：In the stuffing box (5)
Portion is filled with corresponding filler (9) according to actual needs.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710345374.0A CN106975314A (en) | 2017-05-15 | 2017-05-15 | A kind of modularization dynamic gas purifying column |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710345374.0A CN106975314A (en) | 2017-05-15 | 2017-05-15 | A kind of modularization dynamic gas purifying column |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106975314A true CN106975314A (en) | 2017-07-25 |
Family
ID=59342119
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710345374.0A Pending CN106975314A (en) | 2017-05-15 | 2017-05-15 | A kind of modularization dynamic gas purifying column |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106975314A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109157942A (en) * | 2018-07-09 | 2019-01-08 | 钢研晟华科技股份有限公司 | Material conveying device of desorption tower |
Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10146513A (en) * | 1996-11-19 | 1998-06-02 | Nec Yamagata Ltd | Filled tower type dust collecting apparatus |
| CN1322587A (en) * | 2000-05-09 | 2001-11-21 | 泸天化（集团）有限责任公司 | Rotary packed tower |
| TW506850B (en) * | 2000-11-21 | 2002-10-21 | Desiccant Technology Corp | Regeneration method of turning-wheel absorption concentration system |
| CN1429654A (en) * | 2001-12-25 | 2003-07-16 | 佳能株式会社 | Wet gas processing method and wet gas processing device |
| CN201701849U (en) * | 2010-06-17 | 2011-01-12 | 上海梅思泰克生态科技有限公司 | Vertical current multistage chemical scrubber |
| CN202078821U (en) * | 2010-12-30 | 2011-12-21 | 中盐制盐工程技术研究院 | Flue gas scrubber tower |
| CN202666628U (en) * | 2012-05-16 | 2013-01-16 | 杭州纽创工业设计有限公司 | Rotating device for horizontal water-film cyclone |
| CN103120877A (en) * | 2013-02-20 | 2013-05-29 | 山东天力干燥股份有限公司 | Dust containing tail gas insulating and washing and water recovery process |
| CN103785343A (en) * | 2012-11-03 | 2014-05-14 | 中国石油化工股份有限公司 | A rotary bed and an adsorption method of hydrocarbon-containing exhaust gas |
| CN103933855A (en) * | 2014-04-26 | 2014-07-23 | 南京宇行环保科技有限公司 | Double-tower serially-connected device and method for removing SO2 and NOx from smoke by using biological method |
| CN203750367U (en) * | 2014-03-31 | 2014-08-06 | 宁波市镇海新东方精细化工有限公司 | Waste gas treating and recycling device |
| CN203955024U (en) * | 2014-07-04 | 2014-11-26 | 金广恒环保技术（南京）有限公司 | Square horizontal washing tower |
| CN104474996A (en) * | 2014-11-22 | 2015-04-01 | 中北大学 | Multistage cross-flow rotation packed bed mass transfer and reaction equipment |
| CN104984651A (en) * | 2015-07-08 | 2015-10-21 | 广州市浩立生物科技有限公司 | Supergravity multi-effect flue gas recovery and purification method and device |
| CN205435290U (en) * | 2016-04-08 | 2016-08-10 | 山东金孚环境工程有限公司 | Industry tail gas wet -type purifier |
-
2017
- 2017-05-15 CN CN201710345374.0A patent/CN106975314A/en active Pending
Patent Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10146513A (en) * | 1996-11-19 | 1998-06-02 | Nec Yamagata Ltd | Filled tower type dust collecting apparatus |
| CN1322587A (en) * | 2000-05-09 | 2001-11-21 | 泸天化（集团）有限责任公司 | Rotary packed tower |
| TW506850B (en) * | 2000-11-21 | 2002-10-21 | Desiccant Technology Corp | Regeneration method of turning-wheel absorption concentration system |
| CN1429654A (en) * | 2001-12-25 | 2003-07-16 | 佳能株式会社 | Wet gas processing method and wet gas processing device |
| CN201701849U (en) * | 2010-06-17 | 2011-01-12 | 上海梅思泰克生态科技有限公司 | Vertical current multistage chemical scrubber |
| CN202078821U (en) * | 2010-12-30 | 2011-12-21 | 中盐制盐工程技术研究院 | Flue gas scrubber tower |
| CN202666628U (en) * | 2012-05-16 | 2013-01-16 | 杭州纽创工业设计有限公司 | Rotating device for horizontal water-film cyclone |
| CN103785343A (en) * | 2012-11-03 | 2014-05-14 | 中国石油化工股份有限公司 | A rotary bed and an adsorption method of hydrocarbon-containing exhaust gas |
| CN103120877A (en) * | 2013-02-20 | 2013-05-29 | 山东天力干燥股份有限公司 | Dust containing tail gas insulating and washing and water recovery process |
| CN203750367U (en) * | 2014-03-31 | 2014-08-06 | 宁波市镇海新东方精细化工有限公司 | Waste gas treating and recycling device |
| CN103933855A (en) * | 2014-04-26 | 2014-07-23 | 南京宇行环保科技有限公司 | Double-tower serially-connected device and method for removing SO2 and NOx from smoke by using biological method |
| CN203955024U (en) * | 2014-07-04 | 2014-11-26 | 金广恒环保技术（南京）有限公司 | Square horizontal washing tower |
| CN104474996A (en) * | 2014-11-22 | 2015-04-01 | 中北大学 | Multistage cross-flow rotation packed bed mass transfer and reaction equipment |
| CN104984651A (en) * | 2015-07-08 | 2015-10-21 | 广州市浩立生物科技有限公司 | Supergravity multi-effect flue gas recovery and purification method and device |
| CN205435290U (en) * | 2016-04-08 | 2016-08-10 | 山东金孚环境工程有限公司 | Industry tail gas wet -type purifier |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109157942A (en) * | 2018-07-09 | 2019-01-08 | 钢研晟华科技股份有限公司 | Material conveying device of desorption tower |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100525885C (en) | Turbine type pressure charging acceleration fuel gas desulfurization gas wash tower | |
| CN201815236U (en) | Gas-liquid cross-flow contact device | |
| CN102836631B (en) | Method and device for selectively removing hydrogen sulfide from gas by utilizing amine droplets | |
| CN103785275A (en) | Desulfurization, dedusting and denitration integrated flue-gas purifier | |
| CN108554151A (en) | A kind of flue gas high-efficiency desulfurization dust separation device | |
| CN106582272A (en) | Desulfuration purification process for acidic waste water steam stripping ammonia gas | |
| CN106925097A (en) | It is a kind of based on liquid phase oxidation to the combined column and its technique of flue gas desulfurization and denitrification | |
| CN110732228A (en) | Flue gas desulfurization method and apparatus | |
| CN201735331U (en) | Waste gas desulfurization device | |
| CN201949809U (en) | Multifunctional dynamic wave comprehensive washer | |
| CN106975314A (en) | A kind of modularization dynamic gas purifying column | |
| CN109126815B (en) | Low-temperature denitration catalyst and application | |
| CN206535412U (en) | A kind of desulfuring and denitrifying apparatus | |
| CN203777911U (en) | Desulfuration, dedusting and denitration integrated flue gas cleaner | |
| CN206730794U (en) | Activated coke integrated purifying desulfurizer | |
| CN202161916U (en) | Flue gas desulfurization spraying equipment | |
| CN201592055U (en) | High-efficiency cyclone purifier for disposing exhaust gas | |
| CN101632894B (en) | Semi-dry type flue gas desulfurization method and device | |
| CN202199262U (en) | Flue gas purifying equipment for small and medium-sized coal-fired boilers | |
| CN202700342U (en) | Two-stage adsorption washing tower for desulfuration, denitration, demercuration and removal of particulate matter (PM) 2.5 | |
| CN104061580B (en) | Process ammonia desulfuration equipment and the technique thereof of flue gas desulfurization band liquid | |
| CN105688527B (en) | Device and method for removing sulphur dioxide and dioxin from sintering flue gas | |
| CN1792417A (en) | Tech. for desulphuni zation of flue-gas by using integrated internal circulation and two-speed fluidized bed | |
| CN1221307C (en) | Integrative desulfurizing and dedusting tower of ammonia process | |
| CN206688484U (en) | A kind of combined column based on liquid phase oxidation to flue gas desulfurization and denitrification |
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 |
Application publication date: 20170725 |
|
| RJ01 | Rejection of invention patent application after publication |