CN106955562B - A kind of purifying VOCs exhaust gas spiral step fin tower - Google Patents
A kind of purifying VOCs exhaust gas spiral step fin tower Download PDFInfo
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- CN106955562B CN106955562B CN201710268263.4A CN201710268263A CN106955562B CN 106955562 B CN106955562 B CN 106955562B CN 201710268263 A CN201710268263 A CN 201710268263A CN 106955562 B CN106955562 B CN 106955562B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/06—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40084—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by exchanging used adsorbents with fresh adsorbents
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- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
The present invention relates to volatile organic compound from waste gas Treatment process fields, and in particular to a kind of purifying VOCs exhaust gas spiral step fin tower.It is characterized in that: including tower body component, deslagging rotary disc assembly, idler assembly, cushion cap.Helical feed is reacted working principle with tower to be effectively combined, capable of solving under air-proof condition adsorbent very well using helical feed, persistently mobile and tower reactor has that phase border contact area is big, the higher advantage of mass-transfer efficiency, can be realized adsorbent filler constantly keeps phase border to contact with VOCs exhaust gas, and disengage in time when saturated, solve continuing purge VOCs exhaust gas technical problem under the conditions of continuous production.
Description
Technical field
The present invention relates to volatile organic compound from waste gas Treatment process fields, and in particular to a kind of purifying VOCs exhaust gas spiral shell
Revolve ladder fin tower.
Background technique
The gaseous pollutant of industrial discharge is the main source of air environmental pollution object, and wherein volatile organic compounds is useless
Gas (VOCs) is the gaseous pollutant all to environment with serious harm effect, while being also to influence operator in workplace
Health occupational source, it derives from the chemical work such as paint, coating, coating, lubricating oil, rubber extensively
Industry.Since it acts on the considerable damage of human body and natural environment, country has put into effect relevant laws and regulations and it is administered and is discharged
Carry out strict control.The currently used processing method of VOCs treatment technology has combustion method, chemical oxidization method, chemical absorbing
Method, absorption method, bioanalysis etc..Wherein absorption method is a kind of common organic waste-gas purification effective ways, is to utilize various solids
The method that adsorbent (such as active carbon, activated carbon fibre, molecular sieve) carries out adsorption cleaning to the pollutant in discharge exhaust gas.It inhales
Attached method equipment is simple, applied widely, purification efficiency is high, is a kind of traditional waste gas pollution control and treatment technology, and most widely used at present
Treatment process, but adsorbent absorption VOCs saturation after, need replacing adsorbent, then just need stop production to have cooperated
At, and chemical company is generally continuous production, stops very big to the product quality, cost impact that normally produce, needs thus
Purification device needed for can satisfy continuous production.Chinese invention patent (number of patent application 201210077796.1, proprietary term
Referred to as a kind of electrothermal purifying filter element for Wind Volume VOCs waste gas pollution control and treatment) it discloses and a kind of is controlled for Wind Volume VOCs exhaust gas
The electrothermal purifying filter element of reason, including building enclosure and its internal adsorption bed loaded, it is characterised in that: the electrothermal
The box-type shaped polyhedron structure that purifying filter element appearance is air intake surface, outlet air surface is parallel, air intake surface, outlet air surface are the more of one or more layers
Hole sieve plate or sieve, the building enclosure include hermetic unit and above-mentioned air intake surface, outlet air surface；Adsorption bed is by active carbon
Eyelet fabric or porous activated carbon fiber cloth are formed by stacking by plane compression, adsorption bed any two opposing end surface or are connect therewith
Near position is equipped with electrode A and electrode B, and electric current can be passed through to adsorption bed, galvanic couple is equipped in adsorption bed, in electrothermal heating process
The temperature of middle test adsorption bed；Alternatively, the electrothermal purifying filter element appearance be cylindrical body, building enclosure by inner cylinder,
End cap and outer barrel composition, inner cylinder and outer barrel are respectively air intake surface and outlet air surface, and inner cylinder is closed at one end hollow more
Hole cylindrical body, is closely wound active carbon eyelet fabric thereon or porous activated carbon fiber cloth forms adsorption bed, and outer barrel is by one layer
Or multilayer is netted or porous material is made, and electricity is arranged using end cap as electrode or in adsorption bed upper and lower end face or close position
Pole A and electrode B can be passed through electric current to adsorption bed, galvanic couple are arranged in adsorption bed, test adsorbent bed during electrothermal heating
The temperature of layer；The active carbon eyelet fabric shape of a mesh is round, ellipse or polygon, two holes of longitudinal arbitrary neighborhood
Internal diameter be greater than its hole wall, using longitudinally be closely wound or plane compress superposition by the way of form adsorption bed；Or laterally take up an official post
Anticipate two adjacent holes internal diameter be greater than its hole wall, using laterally be closely wound or plane compress superposition by the way of form adsorbent bed
Layer；The porous activated carbon fiber cloth, the shape in hole are round, ellipse or polygon, two holes of longitudinal arbitrary neighborhood
Internal diameter be greater than its pitch of holes, using longitudinally be closely wound or plane compress superposition by the way of form adsorption bed；Or in transverse direction
The internal diameter in two holes of arbitrary neighborhood is greater than its pitch of holes, forms suction in such a way that transverse direction is closely wound or plane compresses superposition
Attached bed；Alternatively, the porous activated carbon fiber cloth, the shape in hole is strip, X-shaped, cross, crescent, arc, L
One of shape is a variety of, and circulation of embarking on journey along longitudinal direction occurs, and the immediate hole in position is in length and breadth in any one hole row adjacent thereto
Projection in both direction has coincidence, using it is vertical or horizontal be closely wound or plane compress superposition by the way of form adsorbent bed
Layer；Or only projection horizontally has coincidence, and the projected length of hole horizontally is greater than between laterally adjacent two hole in the longitudinal direction
Projector distance, or only projection in the longitudinal direction has a coincidence, and the projected length of hole in the longitudinal direction is greater than between longitudinally adjacent two hole
Projector distance horizontally forms adsorbent bed in such a way that vertical and horizontal are alternately closely wound or plane compresses superposition
Layer.(number of patent application 201510779318.9, patent name turn Chinese invention patent for a kind of combined type VOCs Adsorption Concentration
Wheel and its application method) disclose a kind of combined type VOCs Adsorption Concentration runner and its application method, it is characterised in that: it be by
Molecular sieve runner and cellular activated carbon runner be coaxial, with made of diameter docking, the cellular activated carbon runner be located at VOCs into
Mouthful side is laid with adsorption zone, desorption area and cooling zone on each runner, isolation ring, institute is provided at the docking of two runners
Isolation ring is stated for separating the adsorption zone of two runners, desorption area and cooling zone, and cloth wind, reduction windage again；Described point
Son sieve runner is that VOCs adsorbent is attached on cellular web by way of spraying, elution or dipping to obtain.
The prior art one proposes building enclosure for Wind Volume VOCs waste gas pollution control and treatment practical problem and air intake surface, outlet air surface are
The electrothermal purifying filter element technical solution of the adsorption bed of one or more layers porous sieve plate or sieve filling, but inhaling
Electrothermal purifying filter element, which how is replaced, in normal production after attached VOCs exhaust gas saturation does not propose solution；The prior art two
It proposes to adsorb VOCs exhaust gas using molecular sieve runner and cellular activated carbon runner for VOCs waste gas pollution control and treatment practical problem, take off
Attached, concentration, burning technical solution, since VOCs exhaust gas usually carries particulate matter, since particulate matter is that solid cannot lead to
It is detached through air-introduced machine after crossing desorption, concentration and is sent to burner, the more can only collect the more more at adsorbent (active powdered carbon, coating etc.),
Purification device is finally blocked, is given up by the above-mentioned prior art it is found that failing continuing purge VOCs under the conditions of guaranteeing continuous production
Air lift goes out perfect technical solution.
Summary of the invention
In view of the above-mentioned problems, the object of the present invention is to provide a kind of purifying VOCs exhaust gas spiral step fin tower, feature
It is: including tower body component, deslagging rotary disc assembly, idler assembly, cushion cap.
The tower body component includes exhaust tube, plow harrow, adsorbent entrance, tower body, support column, bearing block, the exhaust tube
It is connect with tower body, purified tail gas is discharged into atmosphere from exhaust tube, and the plow harrow is mounted at the top of tower body, from adsorbent
The adsorbent uniform filling booth that entrance enters is multicast on the spiral step fin of rotation, and the support column is connect with tower body, fixed
Tower body is on cushion cap.
The deslagging rotary disc assembly includes spiral step fin, fixed chain, newel, rotary case, cloth wind tower component, support
Frame component, VOCs exhaust gas inlet, dreg scraper knife component, slag-drip opening.Spiral step fin one end is around newel helical stand piecewise
Stepwise installation is fixed, and the other end is consolidated by fixing chain.The center top end is positioned by being mounted on the bearing block at the top of tower body, bottom
End is connect with bracket assembly, and on rotary case, the cloth wind tower component is mounted on rotary case bracket assembly location and installation,
It is connect with VOCs exhaust gas inlet, the dreg scraper knife component is mounted on rotary case, the solid waste for having adsorbed VOCs exhaust gas
It is discharged through slag-drip opening.
The idler assembly is mounted on cushion cap, and support deslagging rotary disc assembly simultaneously rotates it around tower body center line.It is described
Cloth wind tower component includes pedestal and watt grid, and watt grid multilayer is tired folded, and pedestal is mounted on rotary case.
Inventors have found that solve continuing purge VOCs exhaust gas technical problem under the conditions of continuous production, need adsorbent
Filler constantly keeps phase border to contact with VOCs exhaust gas, and disengages in time when saturated, can be helical feed and tower
Reaction working principle is effectively combined, and can solve what adsorbent under air-proof condition persistently moved very well using helical feed
Practical problem and tower reactor have that phase border contact area is big, the higher advantage of mass-transfer efficiency, and design spiral step fin tower is used for
Purifying VOCs exhaust gas.Spiral step fin around newel spiral terrace, fix piecewise by the installation of helical stand stepwise, spiral step fin
Between gap walk flowing from above under for VOCs exhaust gas, and adsorbent is entered the spiral shell that uniformly booth is multicast to rotation by tower body upper end
It revolves on ladder fin, is conveyed downwards in tower body inside spin, it, can be according to the dense of VOCs exhaust gas with the effective contact mass transfer of VOCs exhaust gas
Degree realizes the efficient using useless with continuing purge VOCs of adsorbent by adjusting the revolving speed of newel and the inlet amount of adsorbent
The target of gas.
Inventors have found that spiral step fin has guide functions to VOCs exhaust gas, VOCs exhaust gas enters from tower body lower part,
The spiral under the guidance of spiral step fin essentially adds VOCs exhaust gas residence time in tower body, to increase
Time with adsorbent contact mass transfer, the purification efficiency of adsorbent is improved, also reduces tower body height, the purification dress of saving
The cost set.
Inventors have found that spiral step fin tower is substantially also helix transporting device, it can be absorption VOCs exhaust gas
Solid waste is discharged through deslagging rotary disc assembly, will not block purification device and increase ventilation resistance, reduce ventilation device energy
Consumption.
Inventors have found that VOCs exhaust gas through watt grid gap in cloth wind tower component to tower body even distributing wind, and through between watt grid
Flow velocity is very fast when gap, the absorption VOCs exhaust gas solid waste fallen can be purged along tower inclined-plane to rotary case, it is not easy to stifled
Fill in ventilation hole.
Compared with the existing technology, the present invention, which at least contains, has the advantage that first, and helical feed is reacted working principle with tower
It is effectively combined, can solve that adsorbent persistently moves practical problem under air-proof condition and tower is anti-very well using helical feed
Answering device to have, phase border contact area is big, the higher advantage of mass-transfer efficiency, can be realized adsorbent filler constantly with VOCs exhaust gas
The contact of phase border is kept, and is disengaged in time when saturated, continuing purge VOCs exhaust gas technology is asked under the conditions of solving continuous production
Topic；Second, spiral step fin around newel spiral terrace, fix piecewise by the installation of helical stand stepwise, between spiral step fin
Gap walks flowing under for VOCs exhaust gas from above, and adsorbent is entered the spiral step that uniformly booth is multicast to rotation by tower body upper end
It on fin, conveys downwards in tower body inside spin, with the effective contact mass transfer of VOCs exhaust gas, can be led to according to the concentration of VOCs exhaust gas
The revolving speed of adjustment newel and the inlet amount of adsorbent are crossed, realizes the efficient mesh using with continuing purge VOCs exhaust gas of adsorbent
Mark；Third, spiral step fin tower is substantially also helix transporting device, the solid waste of absorption VOCs exhaust gas can be passed through
The discharge of deslagging rotary disc assembly will not block purification device and increase ventilation resistance, reduce ventilation device energy consumption；4th, spiral
Ladder fin has guide functions to VOCs exhaust gas, and VOCs exhaust gas enters from tower body lower part, under the guidance of spiral step fin
Spiral essentially adds VOCs exhaust gas residence time in tower body, thus increase with adsorbent contact mass transfer when
Between, the purification efficiency of adsorbent is improved, also reduces tower body height, the cost of the purification device of saving；5th, VOCs exhaust gas
Through watt grid gap in cloth wind tower component to tower body even distributing wind, and flow velocity is very fast when warp watt grid gap, can be the suction fallen
Attached VOCs exhaust gas solid waste is purged along tower inclined-plane to rotary case, it is not easy to block ventilation hole；6th, always in closed dress
Middle operation is set, the discharge of pollutant is avoided, and can be realized the storage of solid waste centralized collection, for further effective use
The remaining calorific value of absorption VOCs exhaust gas solid waste is realized resource-effective and reduces pollutant emission and has done excellent basis
Work.
Detailed description of the invention
Fig. 1 is a kind of schematic view of the front view of purifying VOCs exhaust gas spiral step fin tower.
Fig. 2 is a kind of overlooking structure diagram of purifying VOCs exhaust gas spiral step fin tower.
Fig. 3 is a kind of A partial enlargement structural representation of purifying VOCs exhaust gas spiral step fin tower.
Fig. 4 is a kind of B-B the schematic diagram of the section structure of purifying VOCs exhaust gas spiral step fin tower.
Fig. 5 is a kind of C partial enlargement structural representation of purifying VOCs exhaust gas spiral step fin tower.
Fig. 6 is a kind of D partial enlargement structural representation of purifying VOCs exhaust gas spiral step fin tower.
Fig. 7 is a kind of E partial enlargement structural representation of purifying VOCs exhaust gas spiral step fin tower.
1- exhaust tube 2- plow harrow 3- adsorbent entrance 4- spiral step fin 5- fixes chain
6- newel 7- tower body 8- tower body component 9- support column 10- deslagging rotary disc assembly
11- idler assembly 12- cloth wind tower component 13- bracket assembly
14-VOCs exhaust gas inlet 15- rotary case 16- dreg scraper knife component 17- slag-drip opening
20- watts of grid 21- pedestal of 18- bearing block 19- cushion cap.
Specific embodiment
The present invention is described further with specific embodiment with reference to the accompanying drawing.
As shown in Figure 1, Figure 2, shown in Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7, a kind of purifying VOCs exhaust gas spiral step fin tower is special
Sign is: including tower body component 8, deslagging rotary disc assembly 10, idler assembly 11, cushion cap 19.
The tower body component 8 includes exhaust tube 1, plow harrow 2, adsorbent entrance 3, tower body 7, support column 9, bearing block 18, institute
It states exhaust tube 1 to connect with tower body 7, purified tail gas is discharged into atmosphere from exhaust tube 1, and the plow harrow 2 is mounted on the top of tower body 7
Portion, from the spiral step fin 4 that adsorbent uniform filling that adsorbent entrance 3 enters booth is multicast to rotation, the support column 9
It is connect with tower body 7, fixed tower body 7 is on cushion cap 19.
The deslagging rotary disc assembly 10 includes spiral step fin 4, fixed chain 5, newel 6, rotary case 15, cloth wind tower group
Part 12, bracket assembly 13, VOCs exhaust gas inlet 14, dreg scraper knife component 16, slag-drip opening 17.Described 4 one end of spiral step fin
Around newel 6, the installation of helical stand stepwise is fixed piecewise, and the other end is consolidated by fixing chain 5.6 top of newel is by being mounted on tower
The bearing block 18 at 7 top of body positions, and bottom end is connect with bracket assembly 13, and 13 location and installation of bracket assembly is in rotary case 15
On, the cloth wind tower component 12 is mounted on rotary case 15, is connect with VOCs exhaust gas inlet 14, and the dreg scraper knife component 16 is installed
On rotary case 15, the solid waste for having adsorbed VOCs exhaust gas is discharged through slag-drip opening 17.
The idler assembly 11 is mounted on cushion cap 19, and support deslagging rotary disc assembly 10 simultaneously turns it around 7 center line of tower body
It is dynamic.The cloth wind tower component 12 includes pedestal 21 and watt grid 20, and 20 multilayer of watt grid is tired folded, and pedestal 21 is mounted on rotary case 15.
According to the disclosure and teachings of the above specification, those skilled in the art in the invention can also be to above-mentioned embodiment party
Formula is changed and is modified.Therefore, the invention is not limited to the specific embodiments disclosed and described above, to of the invention
Some modifications and changes should also be as falling into the scope of the claims of the present invention.In addition, although being used in this specification
Some specific terms, these terms are merely for convenience of description, does not limit the present invention in any way.
Claims (1)
1. a kind of purifying VOCs exhaust gas spiral step fin tower, it is characterized in that: including tower body component, deslagging rotary disc assembly, carrying roller
Component, cushion cap；Tower body component includes exhaust tube, plow harrow, adsorbent entrance, tower body, support column, bearing block, exhaust tube and tower body
Connection, purified tail gas are discharged into atmosphere from exhaust tube, and plow harrow is mounted at the top of tower body, what is entered from adsorbent entrance
Adsorbent uniform filling booth is multicast on the spiral step fin of rotation, and support column is connect with tower body, and fixed tower body is on cushion cap；Institute
State deslagging rotary disc assembly include spiral step fin, fixed chain, newel, rotary case, cloth wind tower component, bracket assembly,
VOCs exhaust gas inlet, dreg scraper knife component, slag-drip opening；Around newel, the installation of helical stand stepwise is solid piecewise for spiral step fin one end
Fixed, the other end is consolidated by fixing chain；Center top end is positioned by being mounted on the bearing block at the top of tower body, bottom end and bracket assembly
Connection, on rotary case, cloth wind tower component is mounted on rotary case bracket assembly location and installation, is connected with VOCs exhaust gas inlet
It connects, dreg scraper knife component is mounted on rotary case, and the solid waste for having adsorbed VOCs exhaust gas is discharged through slag-drip opening；The carrying roller
Component is mounted on cushion cap, and support deslagging rotary disc assembly simultaneously rotates it around tower body center line；The cloth wind tower component includes base
Seat and watt grid, watt grid multilayer is tired folded, and pedestal is mounted on rotary case.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710268263.4A CN106955562B (en) | 2017-04-22 | 2017-04-22 | A kind of purifying VOCs exhaust gas spiral step fin tower |
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| CN201710268263.4A CN106955562B (en) | 2017-04-22 | 2017-04-22 | A kind of purifying VOCs exhaust gas spiral step fin tower |
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| CN106955562A CN106955562A (en) | 2017-07-18 |
| CN106955562B true CN106955562B (en) | 2019-05-10 |
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| CN110755971A (en) * | 2018-07-25 | 2020-02-07 | 曲靖市首锋矿山配件有限公司 | Steel rolling production tail gas treatment system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201016969Y (en) * | 2007-03-23 | 2008-02-06 | 中南大学 | Moving bed adsorption experimental device |
| CN205288011U (en) * | 2016-01-21 | 2016-06-08 | 江西小淼环保有限公司 | Spiral organic waste gas adsorption tower |
| CN105903314A (en) * | 2016-06-01 | 2016-08-31 | 北京神雾环境能源科技集团股份有限公司 | Fluidized bed gas adsorption-desorption system and treatment method thereof |
| CN205700037U (en) * | 2016-06-01 | 2016-11-23 | 北京神雾环境能源科技集团股份有限公司 | Fluidized bed gas adsorption/desorption system |
-
2017
- 2017-04-22 CN CN201710268263.4A patent/CN106955562B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201016969Y (en) * | 2007-03-23 | 2008-02-06 | 中南大学 | Moving bed adsorption experimental device |
| CN205288011U (en) * | 2016-01-21 | 2016-06-08 | 江西小淼环保有限公司 | Spiral organic waste gas adsorption tower |
| CN105903314A (en) * | 2016-06-01 | 2016-08-31 | 北京神雾环境能源科技集团股份有限公司 | Fluidized bed gas adsorption-desorption system and treatment method thereof |
| CN205700037U (en) * | 2016-06-01 | 2016-11-23 | 北京神雾环境能源科技集团股份有限公司 | Fluidized bed gas adsorption/desorption system |
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Address after: 362000 the 2 floor of 32 new gate Street and 1916 Creative Industrial Park, Licheng District, Quanzhou, Fujian, China, 1916 Applicant after: Yang Song Address before: 362000 No. 135 Cui Hu Road, Hu tou Town, Anxi County, Quanzhou, Fujian Applicant before: Yang Song |
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Effective date of registration: 20190415 Address after: 518101 27 Second Industrial City, Tangtou, Songgang Street, Baoan District, Shenzhen City, Guangdong Province Applicant after: Shenzhen far wing intelligent manufacturing Limited by Share Ltd Address before: 362000 the 2 floor of 32 new gate Street and 1916 Creative Industrial Park, Licheng District, Quanzhou, Fujian, China, 1916 Applicant before: Yang Song |
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