CN100528335C - Composition of baffle for generating vortex liquid state flow or vortex combustive flow - Google Patents

Composition of baffle for generating vortex liquid state flow or vortex combustive flow Download PDF

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Publication number
CN100528335C
CN100528335C CNB2005100905226A CN200510090522A CN100528335C CN 100528335 C CN100528335 C CN 100528335C CN B2005100905226 A CNB2005100905226 A CN B2005100905226A CN 200510090522 A CN200510090522 A CN 200510090522A CN 100528335 C CN100528335 C CN 100528335C
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baffle plate
type baffle
combination
type
combustion
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CN1915484A (en
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张才腾
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Priority to CNB2005100905226A priority Critical patent/CN100528335C/en
Priority to US11/503,086 priority patent/US20070039608A1/en
Priority to JP2006006633U priority patent/JP3134132U/en
Publication of CN1915484A publication Critical patent/CN1915484A/en
Priority to US11/878,008 priority patent/US20070261828A1/en
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23M—CASINGS, LININGS, WALLS OR DOORS SPECIALLY ADAPTED FOR COMBUSTION CHAMBERS, e.g. FIREBRIDGES; DEVICES FOR DEFLECTING AIR, FLAMES OR COMBUSTION PRODUCTS IN COMBUSTION CHAMBERS; SAFETY ARRANGEMENTS SPECIALLY ADAPTED FOR COMBUSTION APPARATUS; DETAILS OF COMBUSTION CHAMBERS, NOT OTHERWISE PROVIDED FOR
    • F23M9/00—Baffles or deflectors for air or combustion products; Flame shields
    • 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
    • B01D50/40—Combinations of devices covered by groups B01D45/00 and B01D47/00
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/003—Arrangements of devices for treating smoke or fumes for supplying chemicals to fumes, e.g. using injection devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23M—CASINGS, LININGS, WALLS OR DOORS SPECIALLY ADAPTED FOR COMBUSTION CHAMBERS, e.g. FIREBRIDGES; DEVICES FOR DEFLECTING AIR, FLAMES OR COMBUSTION PRODUCTS IN COMBUSTION CHAMBERS; SAFETY ARRANGEMENTS SPECIALLY ADAPTED FOR COMBUSTION APPARATUS; DETAILS OF COMBUSTION CHAMBERS, NOT OTHERWISE PROVIDED FOR
    • F23M9/00—Baffles or deflectors for air or combustion products; Flame shields
    • F23M9/06—Baffles or deflectors for air or combustion products; Flame shields in fire-boxes

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Separation Of Particles Using Liquids (AREA)
  • Treating Waste Gases (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Chimneys And Flues (AREA)

Abstract

A combined baffle plate structure for generating vortex liquid flow or vortex combustion flow in the washing tower or combustion tower is disclosed. A guide region is arranged at the gas inlet in tower body for making the incoming gas to generate tangent acceleration. The gas is then flowing in the vortex plate region formed by said combined baffle plate structure to generate vortex flow while the water or oil is sprayed for higher vortex effect.

Description

Produce the baffle combination structure of whirlpool liquid flow or whirlpool combustion flow
Technical field
The present invention relates to a kind of baffle combination structure, particularly relating to special deflector of a kind of mat and baffle plate makes gas produce underbalance effect, stable form water whirlpool or burning whirlpool and be difficult for leaving, can effectively promote dissolving, reaction and filter the generation whirlpool liquid flow of (perhaps Ran Shao efficient) or the baffle combination structure of whirlpool combustion flow, it is used for washing or medicine is washed scrubbing tower or resistant to elevated temperatures combustion tower.
Background technology
The baffle plate of prior art all is used for controlling air-flow, and the control for eddy-currents only sees control gas, in swirling water current or whirlpool liquid flow or whirlpool combustion flow, be the application of baffle plate, the whirlpool scrubbing tower or the whirlpool combustion tower that utilize this special swirling water current or whirlpool liquid flow or whirlpool combustion flow to develop into are not more arranged.
It is quite multiple that tradition is used for the mechanism of dissolved air (or combustion air gas), but all belong to small-sized or traditional filled type washing (or traditional hot tubular type boiler) as Wen's washing mostly, and be set up in the family, as chemistry, dyeing and weaving, the dissolved air filtration (or combustion air oxidation structure) that large-sized workshop such as sprays paint and design, the promptly rare high dissolved efficiency mode of special progress (or high burning efficiency mode) that adopts, because factory building ground is wide, and chemical gas isoconcentration height, air quantity is big, may contain a large amount of poison gas, therefore, traditional washing structure, not only dissolved efficiency is bad, blocks easily, can not be applicable to the factory building of super large air quantity; Perhaps because of traditional combustion structure of the poison gas of the calorific value that contains a large amount, not only efficiency of combustion is bad, blocks easily, and secondary pollution is serious, and it is unclean burn, can't be applicable to the factory building of the super large air quantity that burns.
Generally be applied to the scrubbing tower of large-scale factory, its principle is to utilize earlier to fill material (as the Raschig ring layer) and water spray watering, air and water-soluble separating are reacted on the filling material, if air quantity is big, it is just many to fill the material requirement, it is big that tower body just must become, and filtration need slowly be reacted and be raised the efficiency, and investment goods volume and soil cost are very huge.So adopt tradition filling material mode effect not obvious, about 6 one-tenth of washing dissolved efficiency, when the filling material wanted high temperature resistant, the many costs of quantity were also very high, can't reach economic and practical.
For another example, the combustion tower that is applied to large-scale factory of prior art, its principle is to utilize combustion chamber and sprinkling earlier, air and oil firing are reacted on tubing (waterwall tube), the hot water that burns in the tubing transfers the steam utilization again to, when air quantity is big, the combustion chamber requirement is just many, and it is big that tower body just must become, and burning velocity need slowly be reacted and be raised the efficiency, investment goods volume and soil cost are just very huge, so adopt traditional combustion chamber mode effect not obvious, because about 6 one-tenth of efficiency of combustion, required prevention of secondary pollution equipment burns, burning quantity is many, cost is also very high, can't reach economy.
This shows that the defective that existing scrubbing tower and combustion tower exist is demanded urgently further being improved.Therefore found a kind of structure improved scrubbing tower and combustion tower, just become the current industry utmost point to need improved target.
Because the defective of above-mentioned existing scrubbing tower and combustion tower, the inventor is based on abundant for many years practical experience and professional knowledge, cooperate the utilization of scientific principle, actively studied innovation, in the hope of the generation whirlpool liquid flow of founding a kind of new structure or the baffle combination structure of whirlpool combustion flow.Through constantly research, design, and after studying sample and improvement repeatedly, create the present invention who has practical value finally.
Summary of the invention
The objective of the invention is to, a kind of generation whirlpool liquid flow of new structure or the baffle combination structure of whirlpool combustion flow are provided, technical problem to be solved is to make it produce whirlpool liquid flow or whirlpool combustion flow, thereby is suitable for practicality more.
Another object of the present invention is to, a kind of baffle combination structure that produces whirlpool liquid flow or whirlpool combustion flow is provided, technical problem to be solved is to make it produce whirlpool washing and replacement filling material, perhaps produce the whirlpool burning and replace old combustion chamber, be suitable for practicality more thereby can promote economic benefit, and have the value on the industry.
The object of the invention to solve the technical problems realizes by the following technical solutions.According to a kind of baffle combination structure that produces whirlpool liquid flow or whirlpool combustion flow that the present invention proposes, be used for the tower body of scrubbing tower or combustion tower, this baffle combination structure is by being
Figure C20051009052200051
Type baffle plate and/or be the combination of (comprising and being made as being of oblique angle " _/" type baffle plate) of " ㄇ " type baffle plate is
Figure C20051009052200052
Type baffle plate and being
Figure C20051009052200053
The combination of type baffle plate is "＜_〉" type baffle plate and is the combination of "＜_〉" type baffle plate, is "＜_〉" type baffle plate and/or is the combination of "/_ " type baffle plate, is Type baffle plate and/or be
Figure C20051009052200055
The type baffle plate (is included as being of oblique angle
Figure C20051009052200056
The type baffle plate) combination is " ∧ _ ∧ " type baffle plate and the combination that is " ∧ _ ∧ " type baffle plate, is
Figure C20051009052200057
Type baffle plate and being
Figure C20051009052200058
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be
Figure C20051009052200059
The combining structure with at least one combination in the oblique stepped combination of type baffle plate, and the various baffle plate intersection in each combination embeds arrangement and twists joint, above-mentioned baffle combination structure separates scrubbing tower or combustion tower work one on the zone of tower body central authorities, make a side of tower be provided with air inlet, opposite side sets out gas port, and on the air inlet position of tower inside, be provided with corresponding water conservancy diversion district and deflector, be provided with rinsing bowl or combustion chamber in the bottom of tower.
The object of the invention to solve the technical problems also adopts following technical scheme to realize.According to a kind of baffle combination structure that produces whirlpool liquid flow or whirlpool combustion flow that the present invention proposes, be used for the tower body of scrubbing tower or combustion tower, this baffle combination structure is by being
Figure C200510090522000510
Type baffle plate and/or be the combination of " ㄇ " type baffle plate (being included as being of oblique angle setting " _/" type baffle plate) is
Figure C200510090522000511
Type baffle plate and being
Figure C200510090522000512
The combination of type baffle plate is "＜_〉" type baffle plate and is the combination of "＜_〉" type baffle plate, is "＜_〉" type baffle plate and/or is the combination of "/_ " type baffle plate, is
Figure C200510090522000513
Type baffle plate and/or be
Figure C200510090522000514
The type baffle plate (is included as being of oblique angle
Figure C200510090522000515
The type baffle plate) combination is " ∧ _ ∧ " type baffle plate and the combination that is " ∧ _ ∧ " type baffle plate, is
Figure C200510090522000516
Type baffle plate and being
Figure C200510090522000517
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be The combining structure with at least one combination in the oblique stepped combination of type baffle plate, and the various baffle plate intersection in each combination embeds arrangement and twists joint, this baffle combination structure is provided in a side of old-fashioned use and fills in the scrubbing tower or combustion tower of material/pipe, fill material/pipe in order to replace, this baffle combination structure forms and is made as a structure that is combined as the baffle plate of whole layer, in combustion tower, setting is tiltedly put or kept flat to this baffle combination structure, in scrubbing tower, this baffle combination structure is kept flat setting, replace old-fashioned filling material or combustion chamber with the baffle combination structure that keeps flat or tiltedly put setting, wherein, the baffle plate in the baffle combination structure is made as makes by being
Figure C200510090522000519
Type baffle plate or be "＜_〉" type baffle plate or be
Figure C200510090522000520
Type baffle plate or the gas that is " ∧ _ ∧ " type baffle plate produce eddy current, thus the position that makes the washing/combustion process of the gas in tower body concentrate on eddy current carry out, and produce swirling water current/whirlpool burning, thereby have high dissolving/efficiency of combustion.
The object of the invention to solve the technical problems also can be applied to the following technical measures to achieve further.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow, wherein said being
Figure C200510090522000521
Figure C200510090522000522
Type baffle plate and be the combination of (comprising and being made as being of oblique angle " _/" type baffle plate) of " ㄇ " type baffle plate, be
Figure C200510090522000523
Type baffle plate and being
Figure C200510090522000524
The type baffle plate (comprises and being made as being of oblique angle
Figure C200510090522000525
The type baffle plate) combination and the cross arrangement that is "＜_〉" type baffle plate and is the combination of "/_ " type baffle plate are to be " ㄇ " or to be
Figure C200510090522000526
The opening of type baffle plate is towards the exhausting face, and is
Figure C200510090522000527
The structure of the opening of type baffle plate towards the windward side intersects and embeds the setting of twisting joint; To be "/_ " type baffle openings towards the exhausting face be "＜_〉" type baffle openings structure and intersect and embed the setting of twisting joint towards the windward side.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow, wherein said being
Figure C200510090522000528
Type baffle plate and be the combination of (comprising and being made as being of oblique angle " _/" type baffle plate) of " ㄇ " type baffle plate, be Type baffle plate and being
Figure C20051009052200062
The type baffle plate (comprises and being made as being of oblique angle
Figure C20051009052200063
The type baffle plate) combination and the cross arrangement that is "＜_〉" type baffle plate and is the combination of "/_ " type baffle plate are to be
Figure C20051009052200064
The type baffle openings is towards the exhausting face, and is " ㄇ " type baffle plate or is
Figure C20051009052200065
The structure of type baffle openings towards the windward side intersects and embeds the setting of twisting joint; Being "＜_〉" type baffle openings, and being "/_ " type baffle openings and intersecting to the structure of windward side and embed the setting of twisting joint towards the exhausting face.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow, wherein said being Type baffle plate and be the combination of (comprising and being made as being of oblique angle " _/" type baffle plate) of " ㄇ " type baffle plate, be
Figure C20051009052200067
Type baffle plate and being The type baffle plate (comprises and being made as being of oblique angle
Figure C20051009052200069
The type baffle plate) combination, is
Figure C200510090522000610
Type baffle plate and being
Figure C200510090522000611
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be "/_ " type baffle plate combination, be "＜_〉" type baffle plate and
Figure C200510090522000612
The type baffle plate with oblique stepped combination and be " ∧ _ ∧ " type baffle plate and the windward side side of the combination of " ∧ _ ∧ " type baffle plate is provided with the baffle plate that dams, and this baffle plate that dams is arbitrary in slanting baffle or the angle bar baffle plate.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow, the baffle plate in combustion tower is combined by several water pipe walls or waterwall plate.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow, the windward side side of the baffle plate in combustion tower are provided with the ignition point with gaseous fuel or liquid fuel or solid fuel importing.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow is
Figure C200510090522000613
Type baffle plate and be the combination of (comprising and being made as being of oblique angle " _/" type baffle plate) of " ㄇ " type baffle plate, be
Figure C200510090522000614
Type baffle plate and being
Figure C200510090522000615
The type baffle plate (comprises and being made as being of oblique angle
Figure C200510090522000616
The type baffle plate) combination, is
Figure C200510090522000617
Type baffle plate and being
Figure C200510090522000618
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be "/_ " type baffle plate combination, be "＜_〉" type baffle plate and be
Figure C200510090522000619
The type baffle plate with oblique stepped combination and be " ∧ _ ∧ " type baffle plate and be the baffle combination structure of the combination of " ∧ _ ∧ " type baffle plate, be arranged in the airtight generation whirlpool liquid flow and can work as static mixer, be arranged in the scrubbing tower, the baffle plate of windward side side is provided with at least one hole.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow is
Figure C200510090522000620
Type baffle plate and be the combination of (comprising and being made as being of oblique angle " _/" type baffle plate) of " ㄇ " type baffle plate, be
Figure C200510090522000621
Type baffle plate and being
Figure C200510090522000622
The type baffle plate (comprises and being made as being of oblique angle
Figure C200510090522000623
The type baffle plate) combination, is
Figure C200510090522000624
Type baffle plate and being
Figure C200510090522000625
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be "/_ " type baffle plate combination, be "＜_〉" type baffle plate and be
Figure C200510090522000626
The type baffle plate with oblique stepped combination and be " ∧ _ ∧ " type baffle plate and be the baffle combination structure of the combination of " ∧ _ ∧ " type baffle plate, be arranged in the combustion tower, be cross arrangement and stackedly be provided with flatwise.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow is
Figure C200510090522000627
Type baffle plate and be the combination of (comprising and being made as being of oblique angle " _/" type baffle plate) of " ㄇ " type baffle plate is
Figure C200510090522000628
Type baffle plate and being
Figure C200510090522000629
The combination of type baffle plate is "＜_〉" type baffle plate and is the combination of "＜_〉" type baffle plate, is "＜_〉" type baffle plate and is the combination of "/_ " type baffle plate, is
Figure C200510090522000630
Type baffle plate and being The type baffle plate (is included as being of oblique angle
Figure C200510090522000632
The type baffle plate) combination, the opening that is between the baffle plate of " ∧ _ ∧ " type baffle plate and the combination that is " ∧ _ ∧ " type baffle plate is a relative embedding setting.
The baffle combination structure of aforesaid generation whirlpool liquid flow is arranged in the scrubbing tower, is provided with by most identical or different baffle-panels horizontally sets, and parallel overlapping arrangement or spacing is arranged be arranged in parallel.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow, it is arranged in the combustion tower, when combustion of gaseous, form the burning layer by layer of baffle-panels, ventilation state prolongs burning to make progress, when combustion of liquid or solid, be set to suitablely with the space that liquid or solid placed the second layer or the 3rd interlayer and enlarge this interlayer with what form main chamber, and serve as to be advisable in inferior combustion chamber so that the baffle space that continue to prolong four layers of burnings to the and layer 5 by the vacuum suction state to be set.
The baffle combination structure of aforesaid generation whirlpool liquid flow or whirlpool combustion flow, wherein said being
Figure C20051009052200071
Type baffle plate and be the combination of (comprising and being made as being of oblique angle " _/" type baffle plate) of " ㄇ " type baffle plate is
Figure C20051009052200072
Type baffle plate and being The type baffle plate with oblique stepped combination, be
Figure C20051009052200074
Type baffle plate and being
Figure C20051009052200075
The type baffle plate (comprises and being made as being of oblique angle
Figure C20051009052200076
The type baffle plate) combination is "＜_〉" type baffle plate and is the combination of "＜_〉" type baffle plate, is "＜_〉" type baffle plate and is
Figure C20051009052200077
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be the combination of "/_ " type baffle plate, be Type baffle plate and being
Figure C20051009052200079
The type baffle plate (comprises and being made as being of oblique angle
Figure C200510090522000710
The type baffle plate) combination is Type baffle plate and being The combination of type baffle plate, after the baffle plate that is " ∧ _ ∧ " type baffle plate and is the combination of " ∧ _ ∧ " type baffle plate intersects and twists joint, twist joint baffle-panels for one when keeping flat or tiltedly put, function with many whirlpools control of dust and gs-oil separator more has the function that produces swirling water current or liquid flow or whirlpool combustion flow when keeping flat.
Major technique of the present invention thes contents are as follows:
Baffle combination structure of the present invention is arranged in the scrubbing tower of old-fashioned filling material, if use instead " ㄇ " type or
Figure C200510090522000713
The type baffle plate and
Figure C200510090522000714
The type baffle plate, perhaps
Figure C200510090522000715
The type baffle plate and
Figure C200510090522000716
The type baffle plate relatively intersects to be twisted joint, perhaps "＜_〉" type baffle plate and "/_ " type baffle plate, and perhaps "＜_〉" type baffle plate and "＜_〉" type baffle plate, perhaps
Figure C200510090522000717
The type baffle plate, or " ㄇ " type baffle plate, or " ∧ _ ∧ " type baffle plate keeps flat after twisting joint mutually and replaces tradition to fill material, and gas and air-flow pass through with vertical substantially direction from this piece baffle-panels, and can produce the Scroll-tupe washing, the washing of this improvement or the medicine mode of washing can become high temperature resistant whirlpool scrubbing tower.Replace tradition to fill in the material, when being all the right angle with each angle of " ㄇ " type baffle plate, the eddy current that the gas windward side is produced forms irregular state, so be placed on the exhausting face, the exhausting face is drained very soon because of wind, can not cause sinuous flow, so must not
Figure C200510090522000718
The type baffle plate, with " ㄇ " type baffle plate or Type baffle plate or novel flow-guiding type baffle plate just can, and and
Figure C200510090522000720
The type baffle plate is twisted joint mutually, makes each gas-droplet concentrate on
Figure C200510090522000721
At at the end of type baffle plate filter; Just collocation during "＜_〉" type baffle plate in like manner "/_ " the type baffle plate.Its principle be first utilization " ㄇ " type baffle openings towards be placed on the exhausting face (
Figure C200510090522000722
Or the concave surface of " ㄇ " shape) and
Figure C200510090522000723
The type baffle openings towards be placed on the windward side ( Or the convex surface of ㄇ shape) twist joint mutually, make by
Figure C200510090522000725
The gas of type baffle plate produces eddy current, and the gas washing is concentrated on whirlpool portion, because each angle of " ㄇ " type baffle plate is all the right angle, is placed on the exhausting face, is not easy to form eddy current, makes the gas exhausting smooth and easy, allows
Figure C200510090522000726
The type baffle plate is placed on the eddy current formation rule state that the windward side produces, and can not cause sinuous flow, makes each gas washing concentrate on
Figure C200510090522000727
Within the type baffle plate filter,, can become the scrubbing tower of high dissolved efficiency especially at the trickle aggegation of washing.Only fill filter material than the conventional washing tower and be responsible for washing, and effectively strengthen many times of dissolved efficiencies by one.
A kind of baffle combination produces the whirlpool washing, the washing of improvement or medicine are washed can high temperature resistant scrubbing tower, it is in a scrubbing tower side of sealing air inlet to be set, opposite side sets out gas port, scrubbing tower inside is provided with corresponding water conservancy diversion district in the air inlet position, with producing the straight line tangential acceleration so that enter the gas of scrubbing tower, enter eddy plate and water spray watering and will good eddy effect be arranged with swirling water current, the bottom of scrubbing tower is provided with water leg in addition, the cross arrangement baffle plate that the central appropriate location of scrubbing tower is provided with some steering currents keeps flat, make scrubbing tower work one is separated, the baffle plate that dams has been set up in the baffle plate outside, make air-flow equably by the gap of (windward side) baffle-panels outside less than 90 degree slanting baffles or angle bar baffle plate, speed difference because of, reason produces negative pressure, this gap can be held back and assemble the proportion dirt bigger than gas.The improvement again of the control of dust of whirlpool more than this kind, gs-oil separator, except make gas produce underbalance effect by dam baffle plate and whirlpool baffle plate, raising of washing dissolution rate or medicine are washed strengthened concentrated reaction efficiency, and it all is stranded in the interior water of scrubbing tower, increase whirlpool good stable formation whirlpool by swirling water current in the eddy plate in addition and be difficult for leaving the efficient that effectively to promote dissolving, reaction and filter.
A kind of baffle combination produces swirling water current, this and the gas washing is concentrated on whirlpool portion in the whirlpool flow-guiding structure of whirlpool scrubbing tower
Figure C200510090522000728
The inboard water of assembling a large amount of fluctuations of baffle plate or "＜_〉" type baffle plate are provided with plurality of holes during the reciprocal stream of air and water and are positioned at
Figure C200510090522000729
Within the baffle plate, can pass through at air water
Figure C20051009052200081
Behind the gap in the baffle-panels, increase the stable of draining and be difficult for obstruction by hole.
One air-flow runs into a lot of little shaping whirlpool baffle plates through tangential acceleration, become a lot of little washing vortical flow, original big whirlpool washing pressure is big, and it is little to turn a lot of little whirlpool washing pressure into, as long as little whirlpool washing pressure just can, so the air force crushing reduces relatively.Big whirlpool can dissolve big pollutant, little whirlpool can dissolve more small pollutant and rate of dissolution faster, so the water scrubber of these a lot of little whirlpools is water scrubbers of a kind of lower resistance high-dissolvability two-forty.Another mode that also has the whirlpool liquid flow, the eddy plate traverse is fixed in the closed container, can work as static mixer, different liquid object together flow into eddy plate and mix to stir, mat draw water stream make enter liquid not cracked ends whirlpool liquid flow mix and stir youngster and reach the static agitation purpose.More than other baffle plate in like manner learn.
In addition, the baffle combination structure is arranged in the old-fashioned combustion tower for another example, if use instead
Figure C20051009052200082
The type baffle plate and The type baffle plate, perhaps "＜_〉" type baffle plate and "＜_〉" type baffle plate, perhaps " ㄇ " type baffle plate and
Figure C20051009052200084
The type baffle plate, perhaps
Figure C20051009052200085
The type baffle plate and The type baffle plate, perhaps "＜_〉" type baffle plate and "/_ " type baffle plate, perhaps
Figure C20051009052200087
The type baffle plate, or " ㄇ " type baffle plate, or " ∧ _ ∧ " type baffle plate relatively intersects and keeps flat after twisting joint, and replaces the traditional combustion chamber, and this type shape baffle plate can be managed (waterwall tube) by majority and be formed or the waterwall plate is formed, gas passes through, and can produce the Scroll-tupe burning, the gas combustion of this improvement or material spray burning incendivity be combustion mechanism completely, can become high temperature resistant whirlpool combustion tower, replace the traditional combustion chamber
Figure C20051009052200088
Or "＜_〉" each angle of type baffle plate is all round corner cut, and the eddy current that the gas windward side is produced forms the rule spin states, makes each gas-droplet concentrate on
Figure C20051009052200089
Or at the end of "＜_〉" type baffle plate filter.Its principle is first utilization
Figure C200510090522000810
The cross arrangement of type baffle plate or "＜_〉" type baffle plate well later is in layer to gather into folds mutually, and is same
Figure C200510090522000811
Or "＜_〉" type baffle openings mutually towards relatively or
Figure C200510090522000812
Or "＜_〉" type baffle openings is towards opposite one deck
Figure C200510090522000813
Or "＜_〉" type baffle openings puts relatively together, becomes the full wafer combustion chamber in succession, make by
Figure C200510090522000814
Or the gas of "＜_〉" type baffle plate produces eddy current, and gas combustion is concentrated on whirlpool portion, because each angle of baffle plate is all round corner cut, forms eddy current easily, makes the gas air-supply smooth and easy, allows
Figure C200510090522000815
Or "＜_〉" baffle plate is placed on the eddy current that the windward side produces and forms the rule state, go to another layer of opposite then and can not cause sinuous flow, make each gas combustion concentrate within the baffle plate filter, especially at the trickle aggegation of burning, the whirlwind of straight line incision circumference and cold and hot exchange can be strengthened spinning and whirlwind can enlarge and prolongs burning, can make Mars, ashes to around disperse the enhancing intensity of a fire, through strengthening evenly burning layer by layer, can become the combustion tower of high burning efficiency.Only be responsible for burning than the traditional combustion tower, and effectively strengthen many times of efficiencies of combustion by a combustion chamber.
Therefore provide a kind of baffle combination to produce the whirlpool burning, the gas combustion of improvement or material spray burning incendivity be combustion mechanism completely, can high temperature resistant combustion tower, for the unprecedented new discovery of a kind of combustion tower is many whirlpools combustion tower, it is in a combustion tower side of sealing air inlet to be set, opposite side sets out gas port, combustion tower inside is provided with corresponding water conservancy diversion district in the air inlet position, deflector makes eddy plate become the combustion chamber, and with producing the straight line tangential acceleration so that enter the gas of combustion tower, entering eddy plate and oil spout spills material and eddy plate is had good whirlpool incendiary effect, the inboard burning whirlpools of assembling a large amount of fluctuations of baffle plate.The bottom of combustion tower is provided with air blast in addition, and the central appropriate location of combustion tower is provided with some innovations and complies with the cross arrangement baffle plate of air-flow and keep flat and make combustion tower do one to separate, and aforesaid whirlpool burning is described
Figure C200510090522000816
The cross arrangement well of type baffle plate and " ㄇ " type baffle plate or "＜_〉" type baffle plate and "/_ " type baffle plate is to keep flat in layer to gather into folds mutually later, and is same
Figure C200510090522000817
Or "＜_〉" type baffle openings mutually towards relatively or
Figure C200510090522000818
Or "＜_〉" type baffle openings is put relatively together towards opposite one deck " ㄇ " or "/_ " type baffle openings, become the full wafer combustion chamber in succession, preceding described burning layer by layer, when combustion liquid or solid, liquid state or solid are placed on the second layer mostly or main chamber is worked as in the 3rd interlayer expansion space, and the vacuum suction state is time combustion chamber toward four layers of downward burnings to the and layer 5 to more following one deck then.The baffle plate bogie side frame is provided with ignition point, the combustion tower of whirlpool more than this kind, except make by deflector and baffle plate the gas velocity difference because of, produce underbalance effect, combustion rate is improved or whirlpool is strengthened concentrated combustion efficient, and be stranded in the burning eddy plate and make burning fully, increase the whirlpool good stable by whirlpool burning in the eddy plate in addition and form the whirlpool burning fully and be difficult for leaving, utilizing repeatedly in the whirlpool increases the holdup time again, can effectively promote burning fully, the efficient of reaction and the energy.
One air-flow runs into a lot of little shaping whirlpool baffle plates through tangential acceleration, become a lot of little burning vortical flow, original big whirlpool combustion pressure is big, and it is little to turn a lot of little whirlpool combustion pressures into, as long as little whirlpool combustion pressure just can, so the air force crushing reduces relatively.Can burn more small dirt and burn rate of the big whirlpool big dirt that can burn, little whirlpool is faster, so these a lot of little whirlpool combustion towers are combustion towers of a kind of low hold-up time high combustion degree two-forty.More than other baffle plate in like manner learn.
In addition, " ㄇ " type baffle plate and
Figure C20051009052200091
The type baffle plate or
Figure C20051009052200092
The type baffle plate and
Figure C20051009052200093
Type baffle plate or "＜_〉" type baffle plate and "＜_〉" type baffle plate or "＜_〉" type baffle plate and "/_ " type baffle plate or
Figure C20051009052200094
After type baffle plate or " ∧ _ ∧ " type baffle plate were twisted joint mutually, the function that also can do many whirlpools control of dust, gs-oil separator is directly put or tiltedly put to the monoblock area, and the invention again that this sent keeps flat and then can do whirlpool scrubbing tower or whirlpool combustion tower.More than other baffle plate in like manner learn.
Via as can be known above-mentioned, the invention relates to a kind of baffle combination structure that produces whirlpool liquid flow or whirlpool combustion flow, be used for washing or scrubbing tower or resistant to elevated temperatures combustion tower that medicine is washed, be to be provided with corresponding water conservancy diversion district in the air inlet position of tower body inside, with producing tangential acceleration so that enter the gas of scrubbing tower or whirlpool combustion tower, gas enters the eddy plate of being made up of the baffle combination structure that produces whirlpool then, and make it have good eddy effect through water spray watering, perhaps make whirlpool combustion tower oil spout/gas igniting have good whirlpool incendiary effect.The present invention is to keep flat after the various baffle plate cross arrangement and separates tower body, make gas produce underbalance effect by intercepter plate and baffle plate, raising of washing dissolution rate or medicine are washed strengthened concentrated the reaction in the water that is stranded in the scrubbing tower, other increases vortex stabilization by whirlpool water in the eddy plate/combustion flow and is difficult for leaving, thereby effectively increase dissolving, reaction and the filter efficiency of scrubbing tower and make the combustion tower burning fully, increase reaction and energy efficiency.
By technique scheme, the baffle combination structure that the present invention produces whirlpool liquid flow or whirlpool combustion flow has following advantage at least:
1. fill the scrubbing tower of material with prior art, under identical air quantity, necessary filter area is little, volume can be reduced into the conventional washing tower three to sixth, because of the present invention is applied in the whirlpool scrubbing tower, wind speed can fast 3～10m/s, relative volume has also been dwindled.
2. compare with the scrubbing tower of tradition filling material, baffle combination structure applications of the present invention can make investment goods volume and soil cost very little in scrubbing tower.
3. compare with the scrubbing tower that tradition is filled material, baffle combination structure applications of the present invention is in scrubbing tower, can make 2～3 times of the improved efficiencies of dissolving, reaction and filtration.
4. compare with the scrubbing tower that tradition is filled material, baffle combination structure applications of the present invention is in scrubbing tower, can baffle plate twists joint mutually to replace filling material, can become resistant to elevated temperatures whirlpool washing, under same high temperature, carries out the whirlpool washing, and cost is very cheap.
5. compare with the scrubbing tower of tradition filling material, baffle combination structure applications of the present invention is in scrubbing tower, baffle plate is twisted joint mutually, and plasticity is bigger, can set baffle dimensions size and the spacing of twisting joint mutually to realize required effect by air quantity, gas solubility, wind speed, pressure size, filter area.
6. compare with the scrubbing tower that wind speed that tradition is filled material reaches clean result slowly, baffle combination structure applications of the present invention twists joint baffle plate in scrubbing tower mutually, and wind speed is fast, can reach required effect.
7. compare with the scrubbing tower that tradition is filled material, baffle combination structure applications of the present invention twists joint baffle plate in scrubbing tower mutually, and blast does not need too high, and the scrubbing tower that can fill material with tradition quite or still less.
8. with the combustion tower of traditional combustion chamber, compare under identical air quantity, burning area needs less, volume can dwindle the traditional combustion tower three to sixth, baffle combination structure applications of the present invention is in combustion tower, wind speed is 3m/s soon, relative volume has also been dwindled.
9. the combustion tower of traditional combustion chamber is compared, and baffle combination structure applications of the present invention can make investment goods volume and soil cost very little in combustion tower.
10. the combustion tower of traditional combustion chamber is compared, and baffle combination structure applications of the present invention can make the efficient of burning, reaction promote 2～3 times than in the past in combustion tower, and the burning holdup time is that incendivity is complete than lacking in the past.
11. the combustion tower of traditional combustion chamber is compared, baffle combination structure applications of the present invention is twisted joint baffle plate mutually and is replaced the combustion chamber in combustion tower, can become high temperature resistant whirlpool burning, and under same high temperature, whirlpool combustion tower cost is very cheap.
12. the combustion tower of traditional combustion chamber is compared, baffle combination structure applications of the present invention twists joint baffle plate in combustion tower mutually, and plasticity is bigger, can set the baffle dimensions size and the spacing of twisting joint mutually by air quantity, burning gases caloic, wind speed, pressure size, burning area, to reach required effect.
13. the combustion tower of traditional combustion chamber is compared, baffle combination structure applications of the present invention twists joint baffle plate in combustion tower mutually, and wind speed just can be reached required effect soon, and the traditional combustion chamber wants wind speed just can reach slowly.
14. the combustion tower of traditional combustion chamber is compared, baffle combination structure applications of the present invention twists joint baffle plate in scrubbing tower mutually, and blast does not need too high, and is suitable with the combustion tower of traditional combustion chamber.
15. the combustion tower of traditional combustion chamber is compared, and aspect boiler applications, can replace superheater, compares with traditional combustion chamber combustion tower and can reduce facility, energy savings.
In sum, the generation whirlpool liquid flow of special construction of the present invention or the baffle combination structure of whirlpool combustion flow produce whirlpool liquid flow or whirlpool combustion flow, replace filling material or old combustion chamber.No matter it all has bigger improvement on product structure or function, have large improvement technically, and produced handy and practical effect, and have the extensive value of industry.
Above-mentioned explanation only is the general introduction of technical solution of the present invention, for can clearer understanding technological means of the present invention, and can be implemented according to the content of specification, and for above-mentioned and other purposes, feature and advantage of the present invention can be become apparent, below especially exemplified by preferred embodiment, and conjunction with figs., be described in detail as follows.
Description of drawings
Fig. 1 is a kind of front elevational schematic of old-fashioned filling material scrubbing tower;
Fig. 2 is " ㄇ " type baffle plate for the present invention and is
Figure C20051009052200101
The type baffle plate is twisted joint mutually in the whirlpool scrubbing tower and in the front elevational schematic of exhausting state;
Fig. 3 adds deflector for the present invention and the baffle plate and in the front elevational schematic of exhausting state of damming;
Fig. 4 is for the present invention
Figure C20051009052200102
Type baffle plate and being
Figure C20051009052200103
The type baffle plate is twisted joint mutually in the whirlpool scrubbing tower and in the front elevational schematic of ventilation state;
Fig. 5 is provided with deflector and the baffle plate that dams for baffle combination structure of the present invention, in the front elevational schematic of ventilation state;
Fig. 6 is " ㄇ " type baffle plate for the present invention and is
Figure C20051009052200104
The front elevational schematic that the type baffle plate is twisted joint mutually;
Fig. 7 is for the present invention
Figure C20051009052200105
The type baffle plate be the front elevational schematic that " ㄇ " type baffle plate is twisted joint back welding slanting baffle mutually;
Fig. 8 is the present invention The type baffle plate is twisted joint mutually with " ㄇ " type baffle plate and is afterwards welded the front elevational schematic of angle bar baffle plate;
Fig. 9 is for the present invention is a plurality of The front elevational schematic that the type baffle plate is twisted joint back welding slanting baffle mutually;
Figure 10 is the present invention is a plurality of is "＜_〉" after the type baffle plate is twisted joint mutually the whirlpool scrubbing tower front elevational schematic at ventilation state;
Figure 11 is the present invention is a plurality of is "＜_〉" after the type baffle plate is twisted joint mutually front elevational schematic;
The front elevational schematic that Figure 12 twists joint mutually and welds slanting baffle for the present invention a plurality of "＜_〉" type baffle plate;
Figure 13 is "＜_〉" type baffle plate and is "/_ " the type baffle plate front elevational schematic of back at the exhausting state of twisting joint mutually for the present invention;
Figure 14 is the present invention "＜_〉" type and "/_ " front elevational schematic after the type baffle plate is twisted joint mutually;
Figure 15 is for the present invention
Figure C20051009052200111
The type baffle plate and
Figure C20051009052200112
The front elevational schematic that the type baffle plate is twisted joint mutually;
Figure 16 is for the present invention
Figure C20051009052200113
Type baffle plate and being
Figure C20051009052200114
The type baffle plate is twisted joint mutually in the front elevational schematic of whirlpool combustion tower at ventilation state;
Figure 17 twists joint in the whirlpool combustion tower mutually for the present invention is "＜_〉" type baffle plate and is "＜_〉" type baffle plate, and in the front elevational schematic of ventilation state;
Figure 18 is for the present invention
Figure C20051009052200115
The type baffle plate be " ㄇ " type baffle plate and twist joint mutually in the whirlpool combustion tower, and in the front elevational schematic of exhausting state;
Figure 19 twists joint in the whirlpool combustion tower mutually for the present invention is "＜_〉" type baffle plate and is "/_ " type baffle plate, and in the front elevational schematic of exhausting state;
Figure 20 be a kind of being "＜_〉" type baffle plate be "＜_〉" type baffle plate and twist joint mutually in the front elevational schematic of whirlpool combustion tower (boiler) state;
Figure 21 is the present invention
Figure C20051009052200116
The type baffle plate and The floor map that the type baffle plate is twisted joint mutually;
Figure 22 floor map that to be the present invention " ∧ _ ∧ " type twist joint mutually with " ∧ _ ∧ " type baffle plate;
Figure 23 is the present invention
Figure C20051009052200118
Type and
Figure C20051009052200119
The schematic diagram that the type baffle plate is trapezoidal arrangement and twists joint mutually;
Figure 24 is "＜_〉" type baffle plate for the present invention and is
Figure C200510090522001110
The floor map that type baffle plate (being trapezoidal arrangement) is twisted joint mutually.
9: combustion tower 10: scrubbing tower
11: air inlet 12: gas outlet
13: rinsing bowl 14: deflector
15: slanting baffle 16: the angle bar baffle plate
17: igniting 18: "/_ " the type baffle plate
19: "＜_ " type baffle plate 20: baffle-panels
21: " ㄇ " type baffle plate (or " _/" type) 22:
Figure C200510090522001111
The type baffle plate
24: water pipe wall/waterwall plate 25: fuel gas
26: liquid fuel or solid fuel 27: baffle space
28: main chamber 29: secondary combustion chamber
30: water pump 40: air blast
41: air-supply air blast 42: the air blast of bleeding
43:
Figure C200510090522001112
The type baffle plate (or
Figure C200510090522001113
Type) 44: " ∧ _ ∧ " type baffle plate
45: Type baffle plate 46:
Figure C200510090522001115
The type baffle plate
The specific embodiment
Reach technological means and the effect that predetermined goal of the invention is taked for further setting forth the present invention, below in conjunction with accompanying drawing and preferred embodiment, to describe in detail according to its specific embodiment of baffle combination structure of the present invention, structure, feature and effect thereof as after.Baffle combination structure of the present invention can be arranged in the new-type scrubbing tower, also can be arranged at old-fashioned filling material scrubbing tower, to replace the use of filling material.Various baffle plate is made by metal material.In addition, in the present invention, represent each baffle shapes each "＜_〉", "/_ ",
Figure C200510090522001116
" _/",
Figure C200510090522001117
" ∧ _ ∧ " waits is integrated structure, and concrete shape please refer to shown in the accompanying drawing, with above-mentioned symbol baffle shapes is not limited.
See also Fig. 2 to Fig. 5, Figure 10, shown in Figure 13, and cooperate and to consult Fig. 6 to Fig. 9, Figure 11, Figure 12, Figure 14, shown in Figure 15, thereby be a kind ofly to produce the scrubbing tower that the whirlpool liquid flow is washed by baffle combination structure of the present invention.
This new-type scrubbing tower be for one can wash, medicine is washed, resistant to elevated temperatures case type scrubbing tower, in this new-type scrubbing tower, a side of the scrubbing tower 10 of this sealing is provided with an air inlet 11, opposite side sets out gas port 12.Near the position of the air inlet 11 of scrubbing tower 10 inside, be provided with corresponding control valve and deflector 14, respectively in order to adjust flow and to make the gas that enters scrubbing tower 10 produce the straight line tangential acceleration, gas enters the baffle combination structure that produces whirlpool then, and make itself and swirling water current produce good eddy effect through water spray watering, the bottom of scrubbing tower is provided with rinsing bowl 13 in addition, the central appropriate location of scrubbing tower 10 is provided with the baffle-panels 20 (please cooperate and consult Fig. 2～Fig. 5 and shown in Figure 10) of some cross arrangements, wherein, baffle-panels 20 is faces of the baffle combination structure that forms of the baffle combination by following different shape, in addition, cooperate simultaneously again and consult Fig. 6～Fig. 9 and Figure 11, Figure 12, Figure 14, baffle-panels 20 shown in Figure 15 is to give chamfering at two right angles of one " ㄇ " type baffle plate 21 to form one
Figure C20051009052200121
Type baffle plate 22, and make this
Figure C20051009052200122
Each angle of type baffle plate 22 is all greater than the face of baffle plates of 90 degree; Or a plurality of knuckles form one
Figure C20051009052200123
Type baffle plate 22; Or two tangent and and the tangent line of the circumferential edge of together two circles one being of forming
Figure C20051009052200124
Type baffle plate 22, and the gap of this baffle plate when rabbeting mutually then is the face of 0.45～0.65 times baffle plate of this two circular diameter; Or be the face of the baffle plate 19 of "＜_〉" type.Baffle-panels 20 with horizontally set, is separated scrubbing tower in tower body.When pilot gas enters above-mentioned baffle plate, dash mutually for avoiding air-flow, utilize the baffle plate 21 that is " ㄇ " type to be set to the position of opening, and be to the exhausting face
Figure C20051009052200125
The baffle plate 22 of type is arranged on the position of opening to the windward side, and the embedding that intersects is twisted joint; Perhaps be arranged on the position of opening, and be "＜_〉" type baffle plate 19 and be arranged on the position of opening, intersect to embed and twist joint to the windward side to the exhausting face with the baffle plate 18 that is "/_ " type; Perhaps with above-mentioned baffle plate 22 and baffle plate 22 relative intersect to embed twist joint; Perhaps above-mentioned baffle plate 19 and baffle plate 19 be relative to intersect to embed and twists joint, by said structure, make by
Figure C20051009052200126
The gas of type baffle plate 22 or "＜_〉" type baffle plate 19 produces eddy current, thereby the process that gas is washed is concentrated on whirlpool portion carries out, and then can guide water flow generation vortex effect regularly, improve dissolved efficiency, as Fig. 6～Fig. 9 and Figure 11, Figure 12, Figure 14, shown in Figure 15, be set to polygonal baffle plate the 21,22,18, the 19th, relatively be provided with one by one and be connected into baffle-panels 20, baffle plate 21 and baffle plate 22; Perhaps baffle plate 22 and baffle plate 22; Perhaps baffle plate 18 and baffle plate 19; Perhaps baffle plate 19 is to regulate control with the gap of baffle plate 19, simultaneously, baffle-panels 20 traverses that are connected into is arranged, and becomes the filtering reaction layer, replaces the filling material of conventional washing tower with it.The outside of baffle-panels 20 is provided with several baffle plates that dams, this baffle plate that dams comprises slanting baffle 15 and angle bar baffle plate 16, wherein the angle of slanting baffle is set to the structure less than 90 degree, and this slanting baffle 15 or angle bar baffle plate 16 are welded on the baffle-panels 20, and be positioned at two baffle plates 21 and 21, perhaps baffle plate 22 and 22, perhaps baffle plate 18 and 18, perhaps between the baffle plate 19 and 19, thereby can make the air-flow gap of slanting baffle 15 or the angle bar baffle plate 16 by baffle-panels 20 outsides (being the windward side) equably, and because speed difference, make it produce the negative pressure relation, so the crack can be held back and be assembled the proportion dirt bigger than gas during this time, and this dirt slowly is mixed in the washing thing, in addition, the water that a large amount of fluctuations are arranged is assembled in inboard at baffle plate 22 or baffle plate 19, when air-flow is placed in one, the whirlpool baffle combination causes the whirlpool flow-guiding structure, falling down water above goes in it, the outer water level height of water table ratio whirlpool flow-guiding structure, because the fluctuation of high low water level and water conservancy diversion clearance air turbulent flow cause the gas-liquid effect that mixes, this kind water conservancy diversion has Wen's clean result, thereby produce high dissolved efficiency, this baffle plate 22 or the baffle plate 19 inboard water of assembling a large amount of fluctuations when empty G﹠W adverse current, are located at several holes 23 of baffle plate 22 or baffle plate 19, can after air water be by the gap in the baffle-panels 20, increase the stable of draining and be difficult for obstruction by hole 23.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
In the present invention, various baffle plate be the windward side side with air inlet 11 sides, with gas outlet 12 sides is the exhausting face, because the open side that is arranged on the various baffle plate on the baffle-panels outside is as being located at the windward side side, the eddy current that gas is produced forms erratic flow regime, should be arranged on exhausting face side so be arranged on the open side of the various baffle plate on the baffle-panels outside, and can not cause the generation of sinuous flow phenomenon.Simultaneously, intersect the baffle plate that embeds the combination of twisting joint with above-mentioned opening mutually to the baffle plate of exhausting face side and be made as opening windward side side mutually, utilize tangential acceleration to make air-flow in the baffle plate of windward side side, produce whirlpool at opening, so baffle combination structure of the present invention is to be foundation with above-mentioned principle, be formed with the baffle combination structure of multilayer, and the number of plies of this baffle combination structure is not limited, thereby and all structures with above-mentioned feature generation whirlpool/whirlpool are all the scope of baffle combination structure of the present invention.
As Fig. 2 and cooperate Fig. 3, Fig. 6, Fig. 7, Fig. 8, Figure 13, shown in Figure 14, scrubbing tower 10 inner deflectors are made a water conservancy diversion to gas, force the gas that enters by top air inlet successively via deflector 14, hold back baffle plate 15 or 16, baffle-panels 20, baffle plate 22 or baffle plate 19, carrying out gas-liquid mixes, and the bigger dirt of density will be stranded on baffle plate 22 or 19 gaps, drop again or directly in rinsing bowl 13, the clean air of filtration that at last gas-liquid mixed is discharged via the gas outlet.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
Fig. 4 cooperates Fig. 5 for another example, Fig. 6, Fig. 7, Fig. 8, Fig. 9,10 figure and Figure 11, Figure 12, shown in Figure 15, air is after side-edge air bleeds 11 is introduced, at first, must keep out mutually in following air deflector, when then entering rinsing bowl 13, can produce the contact of first ripple earlier, and with dust, chemistry dirt or matter, the dust of other larger particles is concentrated and is stranded in the rinsing bowl 13, please cooperate shown in Figure 4 again, when air-flow is passed through between the baffle plate 20, will make air-flow produce most compact scrolls of second ripple by angle greater than 90 degree, and when air-flow reaches the position of baffle plate 22 or baffle plate 19, by stopping of fluctuation water, can assist more gas of generation and liquid phase molten, and being detained, the gas that more is difficult for mixing is dissolved in the water.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
In addition, please cooperate and consult Fig. 2～Fig. 5 and Figure 10, shown in Figure 13, for trying to achieve more more washing effect, on the baffle-panels of the present invention after the top of scrubbing tower 10 is with respect to each traverse or have a deflector 14, it makes the gas that enters scrubbing tower 10 produce tangential acceleration, be provided with a rinsing bowl 13 and can arrange in pairs or groups in bottom of the present invention, water pump 30, the water that utilizes water pump 30 to twitch in the rinsing bowl 13 is sprinkled water from last water spray, and with air with water-solublely separate reaction, air blast 40 is twitched gas and is upward flowed from top to bottom or by side, utilize cold and hot air and water exchange principle, make it easilier the gas that mixes is detained be dissolved in the water, more utilize to produce the strength of eddy current traction, thus dissolved gas further.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
Above-mentionedly be the baffle-panels that traverse is arranged, also can be, or the parallel overlapping traverse type that is arranged in spacing ground is arranged by most or different overlapping being arranged in parallel of baffle-panels, make that the gas-liquid effect that mixes is more remarkable.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
In addition, baffle combination structure of the present invention can also be applied to old-fashioned filling material scrubbing tower, wherein, the combination of baffle combination structure of the present invention and shape, function is same as described above, so do not repeat them here, this baffle combination structure is with whole layer traverse and replaces old-fashioned filling material (as the Raschig ring layer), gas and air-flow pass through with vertical substantially direction on this layer baffle-panels, and in the baffle combination structure, produce whirlpool, thereby gas or air-flow are carried out the Scroll-tupe washing, the scrubbing tower with this baffle combination structure is become to wash or resistant to elevated temperatures whirlpool scrubbing tower that medicine is washed.
See also shown in Figure 16 to 20, and please cooperate and consult Figure 21 to shown in Figure 24, a kind of baffle combination structure of the present invention is arranged at the application in the combustion tower that produces the whirlpool combustion flow, wherein, the part that structure, function that is arranged at scrubbing tower with above-mentioned baffle combination structure etc. is identical repeats no more, and the baffle combination structure in application and the scrubbing tower also can be applicable in the combustion tower, and vice versa.
In one the sealing combustion tower 9 wherein a side one air inlet 11 is set, opposite side sets out gas port 12.Combustion tower 9 inside are provided with control valve and deflector 14 near the corresponding zone of air inlet 11 positions, respectively in order to adjust flow and to make the gas that enters combustion tower 9 produce the straight line tangential acceleration, the bottom of combustion tower is provided with air blast 40 in addition, on the central appropriate location of combustion tower 9, be provided with the baffle-panels 20 (please cooperate Figure 16～shown in Figure 20) of the horizontally set that the baffle plate of some cross arrangements forms, in addition just like Fig. 6～Fig. 9, Figure 11, Figure 12, Figure 14, baffle-panels 20 shown in Figure 15, this baffle plate can be made up of a plurality of waterwall tubes or waterwall plate, make and combustion tower is done one separate, it is to give chamfering in two right angles that are " ㄇ " type baffle plate 21 and one being of forming
Figure C20051009052200141
Type baffle plate 22 is this
Figure C20051009052200142
Each angle of type baffle plate 22 is all greater than 90 degree; Or two tangent and and the tangent line of the circumferential edge of together two circles one being of forming
Figure C20051009052200143
Type baffle plate 22; Or be "＜_ " type baffle plate 19.When pilot gas enters baffle plate, dash mutually, be arranged on the position of opening, and be to the exhausting face and utilize to be " ㄇ " type baffle plate 21 or to be "/_ " type baffle plate 18 for avoiding air-flow
Figure C20051009052200144
Type baffle plate 22 or be "＜_〉" type baffle plate 19 and be placed on the position of opening to the windward side intersects relatively and twists joint; Perhaps baffle plate 22 is twisted joint with 19 relative intersections of baffle plate with baffle plate 22, baffle plate 19, thus make by The gas of type baffle plate 22 or "＜_〉" type baffle plate 19 produces eddy current, and the position of gas combustion is concentrated on whirlpool portion, and then make it can guide combustion-gas flow generation vortex effect regularly, as Fig. 6～Fig. 9, Figure 11, Figure 12, Figure 14, shown in Figure 15, be arranged to polygonal baffle plate 21,22 or baffle plate 18, the 19th, be connected into baffle-panels 20 one by one relatively, baffle plate 21 and baffle plate 22, baffle plate 18 and baffle plate 19 or baffle plate 22 and baffle plate 22, baffle plate 19 is to regulate control with the gap of baffle plate 19, simultaneously, the baffle-panels traverse that is connected into is arranged be set to the whirlpool conversion zone, thereby the combustion chamber that replaces traditional combustion tower, baffle-panels 20 windward sides are provided with several igniting 17 thereon, in this 17 places importing of lighting a fire gaseous fuel or liquid fuel or solid fuel are arranged, make the air-flow can be equably by being positioned at baffle plate 21 and baffle plate 21, baffle plate 18 and baffle plate 18, baffle plate 22 and baffle plate 22, the gap of the baffle-panels 20 windward side sides between baffle plate 19 and the baffle plate 19, because of the speed difference relation produces negative pressure, the gathering air-flow can be held back in this gap, make the air-flow rapid mixing in burning, residual after the combustion reaction can also be concentrated on again whirlpool burning in the eddy plate that forms by the baffle combination textural association that produces whirlpool, and utilize the repeatedly whirlpool that produces to increase the holdup time of air-flow, make and evenly finish burning fully.In addition, the combustion wave of assembling a large amount of fluctuations in the inboard of baffle-panels 22 or 19, when combustion-gas flow is placed in one, the whirlpool flow-guiding structure of forming by the whirlpool baffle combination, on the burning that faces down go in it, burning position is higher than the whirlpool flow-guiding structure position of burning outward, because the effect that the fluctuation of height burning position and water conservancy diversion clearance air turbulent flow cause burning to mix, this water conservancy diversion has combustion efficiency thereby produces high burning efficiency, this baffle plate 22 or the baffle plate 19 inboard burnings of assembling a large amount of fluctuations can increase the holdup time when air and burning adverse current.Being made up of most water pipe walls (or waterwall plate) 24 has several to be positioned at gap within baffle plate 22 or the baffle plate 19, and it can increase the stable and difficult obstruction of exhaust by the gap after burning is by the gap in the baffle-panels 20.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
Specific embodiments of the invention as shown in figure 20, this specific embodiment comprises the boiler of a common vertical combustion as shown in the reference numeral 9, it has the baffle-panels 20 of the above-mentioned shape of the overlapping arrangement of a plurality of levels, and can form the fender board space 27 that baffle-panels forms by most water pipe walls or waterwall plate 24 and hold from multiple spot firearm 17 burned flames.Multiple spot firearm 17 is positioned at a porch of fender board space 27, and goes in the air blast 41 of one's intention as revealed in what one says band or forced draught to be advisable to be located on the entry conductor 11 through being connected to boiler 9 one.Multiple spot firearm 17 goes in the fender board space 27 of boiler 9 fuel for burning usefulness.Above-mentioned boiler 9 is a kind of new designs, it includes most water pipe walls (or waterwall plate) 24 and establishes thereon, burning and gas-exhausting up moves along fender board space 27 Scroll-tupes, down turn to angle by 180 degree, the boiler tube (baffle space 27) that moves down then and form by a row baffle space 27, utilize whirlwind hot pressing to promote cold and hot air exchange principle to be applied in most the water pipe walls (or waterwall plate) 24, in this stage, water pipe wall (baffle space 27) carries out heat exchange and gives quenching so that produce pipe at burning and gas-exhausting via boiler, and each jetting type of these boiler tubes is connected between each steam drum of up and down.Burning and gas-exhausting stimulate the menstrual flow subsequently exhaust uptake 12 and chimney and leave this element.Forced drainage equipment 41 provides necessary air so that with desired flow rates burning, and provides static pressure to overcome all resistances in this boiler combustion gas extraction system and discharge burning gases to outside by chimney.The number of a most waterwall plate (or water pipe wall) 24 and diameter thereof, baffle shapes, arrangement mode and interval and material are to use the known fluid of industry to flow and heat transfer relation is selected, thereby obtain that needed water/water vapour side pressure is fallen and needed heat absorption from flue gas, and will reduce to minimum owing to the NOx that combustion process produces.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
Most water pipe walls (or waterwall plate) 24 formation that inside constituted circulation of air baffle tube assembly are made as baffle-panels 20, when air being sent to individual waterwall plate (or water pipe wall) 24 of the majority of last layer or the following above-mentioned formation circulation of air of one deck baffle tube assembly and air pressure ventilation, because of gap string channelling passes in the forced draught air blast 41 mutually, thereby the air that dispenses out that provides is entered in the fender board space 27, put via the restriction combustion heat and release speed and can make
Figure C20051009052200151
Formation reduce to minimum, simultaneously, the fender board space 27 of empty one deck (secondary combustion chamber) is with after-combustion.Any carbon monoxide is burnouted at last fully.The baffle plate of number in the figure 43,44,45,46 does not repeat them here with overhead gage in like manner.
As Figure 16, shown in Figure 17, and cooperation Figure 15, shown in Figure 11, after the air inlet 11 that is communicated with air-supply air blast 41 that air is provided with from downside is introduced, at first, must keep out mutually in air deflector, when deflector enters the main chamber 28 of kerve, can produce first ripple burning contact earlier, thereby material that will heavier particle is concentrated and is stranded in the kerve, be more suitable for the burning of fuel gas 25, please cooperate again and consult Figure 15, shown in Figure 11, when air-flow is passed through between the baffle-panels 20, generation changes greater than the angle of 90 degree (circle corner cut), and will make combustion-gas flow produce most small-sized vortexs of second ripple, and when combustion-gas flow reaches baffle plate 22 or baffle plate 19 positions, by stopping of fluctuation fire, can auxiliary produce more combustion gas fire and mix, and more nonflammable gas is detained burn in wherein.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
Figure 18 for another example, shown in Figure 19, and please cooperate and consult Fig. 6, shown in Figure 14, the deflector of combustion tower 9 inside is made a water conservancy diversion to air, force the gas that enters by top air inlet successively via baffle-panels 20, baffle plate 22, baffle plate 19 carries out the gas fire and mixes, thereby burning liquid fuels or solid fuel 26 are in main chamber 28, wherein, flame is up to rise, and wind is down to blow rapidly, thereby liquidates mutually, has increased the holdup time under inconsistent, and the cold airflow that the current of warm air that rises forms with down being blown rapidly by wind dashes mutually, constituted strong convection current, the flame front expansion is speed more, prolongs burning and heal fast.Which floor continue again down to produce the whirlpools burning and to become inferior combustion chamber 29 in the baffle space of forming by a plurality of baffle-panels 27, wherein, bigger flame will be detained on the space of baffle plate 22, baffle plate 19, at last, the combustion gas fire is mixed and the clean air that burns is discharged via the gas outlet that is connected with the air blast 42 of bleeding 12.Particularly, it is to become the full wafer combustion chamber in succession by the baffle combination structure with multilayer, and the burning layer by layer of formation therein, when combustion liquid or solid, liquid state or solid are the space being enlarged and forms main chamber at the second layer or the 3rd interlayer, then, and under the vacuum suction state, continue to prolong four layers of burnings to the and layer 5, or layer 5 and layer 6 are time combustion chamber.The bogie side frame of baffle plate is provided with igniting, many whirlpools combustion tower of this kind structure, make gas produce speed difference by deflector and baffle plate, so have underbalance effect, make combustion rate raising or whirlpool strengthen concentrated combustion efficient and be stranded in the burning eddy plate one by one, make burning fully, increase vortex by whirlpool burning in the eddy plate in addition, form the whirlpool burning fully and make, and be difficult for leaving, can effectively promote burning fully, the efficient of reaction and the energy.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
In addition, and for example shown in Figure 16, and please cooperate and consult Figure 17 to shown in Figure 19, for trying to achieve more combustion efficiency, the baffle-panels of the present invention after the combustion tower top is with respect to each traverse go up or have a deflector 14, make the gas that enters combustion tower produce tangential acceleration, and can arrange in pairs or groups a kerve is set in bottom of the present invention, and concentrate for material that will heavier particle and to be stranded in the kerve, and utilize petrolift to twitch fuel oil spout on baffle-panels 20 of groove, with air and oil firing reaction, air blast 40 is twitched gas and is upward flowed from top to bottom or by side, utilizes whirlwind hot pressing to promote cold and hot air exchange principle to be applied to most water pipe walls (or waterwall plate) 24, thereby make cold-hot air convection, and easilier burning gases are detained burn in wherein, and utilize the strength that produces the eddy current traction, further even burning gases.The baffle plate of label 43,44,45,46 does not repeat them here with overhead gage in like manner in the accompanying drawing.
The baffle-panels that above-mentioned traverse is arranged can overlappingly be arranged in the traverse type by most baffle-panels are parallel, and becomes the baffle space of being made up of a plurality of baffle-panels 27, makes that the gas-liquid combustion efficiency is more remarkable.Simultaneously, the baffle combination structure also can be as Figure 23 and shown in Figure 24, by being
Figure C20051009052200161
Type baffle plate and being
Figure C20051009052200162
Type retaining or be "＜_〉" type baffle plate and be
Figure C20051009052200163
The type baffle plate intersects mutually in conjunction with being provided with, and is combined to form stair-stepping baffle combination structure, and the function of this baffle combination structure, purposes are identical with other baffle combination structure, all are to be produced eddy combustion or vortex to wash by the combination of various baffle plate.
In addition, being " ㄇ " type baffle plate and being in the baffle combination structure of the present invention
Figure C20051009052200164
The combination of type baffle plate perhaps is
Figure C20051009052200165
Type baffle plate and being
Figure C20051009052200166
The combination of type baffle plate perhaps is "＜_〉" type baffle plate and is the combination of "＜_〉" type baffle plate, perhaps is "＜_〉" type baffle plate and is the combination of "/_ " type baffle plate, perhaps is Combination between the type baffle plate, or be combination between " ㄇ " type baffle plate, or the combination that is between " ∧ _ ∧ " type baffle plate is to intersect relatively to twist joint, then, the monoblock baffle-panels is directly put or is tiltedly put, and can have the function of many vortexs control of dust, gs-oil separator, change the invention again that thus, that is, keep flat the design that then can do the whirlpool scrubbing tower that produces swirling water current or liquid flow or the combustion tower of whirlpool burning etc., all comprise in the present invention.
In sum, baffle combination structure of the present invention makes gas produce the eddy current spin that forms rule easily in being arranged at the baffle plate of windward side, makes each gas-droplet concentrate on this and is
Figure C20051009052200168
Or be the bottom of "＜_〉" type baffle plate.Particularly, the present invention utilizes earlier to be
Figure C20051009052200169
Type baffle plate or be "＜_〉" type baffle plate and intersect to embed and arrange forms one deck baffle combination structure, is successively folded mutually then, is equally
Figure C200510090522001610
Or the opening that is "＜_〉" type baffle plate is oppositely arranged, and perhaps is Or be "＜_〉" type baffle openings and be and being of the baffle combination structure of opposite one deck
Figure C200510090522001612
Or the opening that is "＜_〉" type baffle plate is oppositely arranged, thereby becomes full wafer baffle space 27 in succession, makes by being
Figure C200510090522001613
Or the gas that is "＜_〉" type baffle plate produces eddy current, and gas scrubbing/burning is concentrated on this whirlpool portion, because each angle of baffle plate is all round corner cut, forms eddy current easily, and it is smooth and easy that gas is blown, and makes to be
Figure C200510090522001614
Type or the opening that is "＜_〉" type baffle plate are arranged on the windward side, thereby the eddy current that produces has the rule state, after air communication is crossed this layer baffle plate, can not cause the phenomenon of sinuous flow to take place in one deck baffle combination structure down, make the washing/burning of each gas concentrate within the baffle combination structure, the combinatorial principle of the baffle combination structure of other combining forms of the present invention all is arranged in a crossed manner relatively, and can produces eddy current in the peristome of windward side with above-mentioned identical.In combustion tower, at the trickle aggegation of burning, spin is strengthened in the whirlwind and the cold and hot exchange of straight line incision circumference especially, and whirlwind can enlarge and prolong burning, can make Mars, ashes to around disperse, strengthen the intensity of a fire, through strengthening evenly burning layer by layer, become the combustion tower of high burning efficiency.
Baffle combination structure of the present invention is arranged in the scrubbing tower, improves the disappearance of conventional washing filter, promptly increases the dissolved efficiency that gas-liquid mixes, and more obtains the effect of lower resistance high-dissolvability; In addition, baffle combination structure of the present invention is arranged in the combustion tower, improves the disappearance of conventional burners, promptly increases the efficiency of combustion that the gas-liquid fire fires mutually, more reaches the effect of low hold-up time high combustion degree.
The above, it only is preferred embodiment of the present invention, be not that the present invention is done any pro forma restriction, though the present invention discloses as above with preferred embodiment, yet be not in order to limit the present invention, any those skilled in the art, in not breaking away from the technical solution of the present invention scope, when the technology contents that can utilize above-mentioned announcement is made a little change or is modified to the equivalent embodiment of equivalent variations, in every case be the content that does not break away from technical solution of the present invention, according to technical spirit of the present invention to any simple modification that above embodiment did, equivalent variations and modification all still belong in the scope of technical solution of the present invention.

Claims (11)

1, a kind of baffle combination structure that produces whirlpool liquid flow or whirlpool combustion flow is used for the tower body of scrubbing tower or combustion tower, it is characterized in that this baffle combination structure is by being
Figure C2005100905220002C1
Type baffle plate and be " ㄇ " type baffle plate or be the combination of " _/" type baffle plate is
Figure C2005100905220002C2
Type baffle plate and being
Figure C2005100905220002C3
The combination of type baffle plate is "＜_〉" type baffle plate and is the combination of "＜_〉" type baffle plate, is "＜_〉" type baffle plate and is the combination of "/_ " type baffle plate, is Type baffle plate and being
Figure C2005100905220002C5
Type baffle plate or be the combination of " ￣ _/￣ " type baffle plate is " ∧ _ ∧ " type baffle plate and is the combination of " ∧ _ ∧ " type baffle plate, is
Figure C2005100905220002C6
Type baffle plate and being The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be The combining structure with at least one combination in the oblique stepped combination of type baffle plate, and the various baffle plate intersection in each combination embeds arrangement and twists joint, above-mentioned baffle combination structure separates scrubbing tower or combustion tower work one on the zone of tower body central authorities, make a side of tower be provided with air inlet, opposite side sets out gas port, and on the air inlet position of tower inside, be provided with corresponding water conservancy diversion district, in scrubbing tower, this baffle combination structure is kept flat setting, in combustion tower, setting is tiltedly put or kept flat to this baffle combination structure, be provided with rinsing bowl or combustion chamber in the bottom of tower, the baffle plate in the baffle combination structure is to be made as to make by being
Figure C2005100905220002C9
Type baffle plate or be "＜_〉" type baffle plate or be
Figure C2005100905220002C10
Type baffle plate or the gas that is " ∧ _ ∧ " type baffle plate produce eddy current, thus the position that makes the washing/combustion process of the gas in tower body concentrate on eddy current carry out, and produce swirling water current/whirlpool burning, thereby have high dissolving/efficiency of combustion.
2, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow is characterized in that wherein said being
Figure C2005100905220002C11
The type baffle plate and be " ㄇ " type baffle plate or be " _/" type baffle plate combination, be
Figure C2005100905220002C12
Type baffle plate and being Type baffle plate or be the combination of " ￣ _/￣ " type baffle plate and the cross arrangement that is "＜_〉" type baffle plate and is the combination of "/_ " type baffle plate is to be " ㄇ " or to be
Figure C2005100905220002C14
The opening of type baffle plate is towards the exhausting face, and is
Figure C2005100905220002C15
The structure of the opening of type baffle plate towards the windward side intersects and embeds the setting of twisting joint; To be "/_ " type baffle openings towards the exhausting face be "＜_〉" type baffle openings structure and intersect and embed the setting of twisting joint towards the windward side.
3, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow is characterized in that wherein said being The type baffle plate and be " ㄇ " type baffle plate or be " _/" type baffle plate combination, be
Figure C2005100905220002C17
Type baffle plate and being
Figure C2005100905220002C18
Type baffle plate or be the combination of " ￣ _/￣ " type baffle plate and the cross arrangement that is "＜_〉" type baffle plate and is the combination of "/_ " type baffle plate is to be
Figure C2005100905220002C19
The type baffle openings is towards the exhausting face, and is " ㄇ " type baffle plate or is
Figure C2005100905220002C20
The structure of type baffle openings towards the windward side intersects and embeds the setting of twisting joint; Being "＜_〉" type baffle openings, and being "/_ " type baffle openings structure and intersecting and embed the setting of twisting joint towards the windward side towards the exhausting face.
4, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow is characterized in that described therein being
Figure C2005100905220002C21
The type baffle plate and be " ㄇ " type baffle plate or be " _/" type baffle plate combination, be
Figure C2005100905220002C22
Type baffle plate and being
Figure C2005100905220002C23
The type baffle plate or be " ￣ _/￣ " type baffle plate combination, be
Figure C2005100905220002C24
Type baffle plate and being
Figure C2005100905220002C25
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be "/_ " type baffle plate combination, be "＜_〉" type baffle plate and be The type baffle plate be provided with the baffle plate that dams with oblique stepped combination and the windward side side that is " ∧ _ ∧ " type baffle plate and is the combination of " ∧ _ ∧ " type baffle plate, and this baffle plate that dams is arbitrary in slanting baffle or the angle bar baffle plate.
5, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow is characterized in that the baffle plate in combustion tower is combined by several water pipe walls or waterwall plate.
6, the baffle combination structure of generation whirlpool liquid flow according to claim 5 or whirlpool combustion flow, the windward side side that it is characterized in that the baffle plate in combustion tower are provided with the ignition point that gaseous fuel or liquid fuel or solid fuel are imported.
7, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow is characterized in that being
Figure C2005100905220003C1
The type baffle plate and be " ㄇ " type baffle plate or be " _/" type baffle plate combination, be
Figure C2005100905220003C2
Type baffle plate and being
Figure C2005100905220003C3
The type baffle plate or be " ￣ _/￣ " type baffle plate combination, be
Figure C2005100905220003C4
Type baffle plate and being
Figure C2005100905220003C5
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be "/_ " type baffle plate combination, be "＜_〉" type baffle plate and be
Figure C2005100905220003C6
The type baffle plate with oblique stepped combination and be " ∧ _ ∧ " type baffle plate and be the baffle combination structure of the combination of " ∧ _ ∧ " type baffle plate, being arranged in the airtight generation whirlpool liquid flow is to be static mixer, be arranged in the scrubbing tower, the baffle plate of windward side side is provided with at least one hole.
8, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow is characterized in that being
Figure C2005100905220003C7
The type baffle plate and be " ㄇ " type baffle plate or be " _/" type baffle plate combination, be
Figure C2005100905220003C8
Type baffle plate and being
Figure C2005100905220003C9
The type baffle plate or be " ￣ _/￣ " type baffle plate combination, be
Figure C2005100905220003C10
Type baffle plate and being
Figure C2005100905220003C11
The type baffle plate with oblique stepped combination, be "＜_〉" type baffle plate and be "/_ " type baffle plate combination, be "＜_〉" type baffle plate and be
Figure C2005100905220003C12
The type baffle plate with oblique stepped combination and be " ∧ _ ∧ " type baffle plate and be the baffle combination structure of the combination of " ∧ _ ∧ " type baffle plate, be arranged in the combustion tower, be cross arrangement and stackedly be provided with flatwise.
9, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow is characterized in that being
Figure C2005100905220003C13
Type baffle plate and be " ㄇ " type baffle plate or be the combination of " _/" type baffle plate is
Figure C2005100905220003C14
Type baffle plate and being
Figure C2005100905220003C15
The combination of type baffle plate is "＜_〉" type baffle plate and is the combination of "＜_〉" type baffle plate, is "＜_〉" type baffle plate and is the combination of "/_ " type baffle plate, is
Figure C2005100905220003C16
Type baffle plate and being
Figure C2005100905220003C17
Type baffle plate or be the combination of " ￣ _/￣ " type baffle plate, the opening that is between the baffle plate of " ∧ _ ∧ " type baffle plate and the combination that is " ∧ _ ∧ " type baffle plate is a relative embedding setting.
10, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow, it is characterized in that it is arranged in the scrubbing tower, be provided with by most identical or different baffle-panels horizontally sets, and parallel overlapping arrangement or spacing is arranged be arranged in parallel.
11, the baffle combination structure of generation whirlpool liquid flow according to claim 1 or whirlpool combustion flow, it is characterized in that it is arranged in the combustion tower, when combustion of gaseous, form the burning layer by layer of baffle-panels, ventilation state prolongs burning to make progress, when combustion of liquid or solid, forming the setting of main chamber, and be inferior combustion chamber so that the baffle space that continue to prolong four layers of burnings to the and layer 5 by the vacuum suction state to be set with the space that liquid or solid placed the second layer or the 3rd interlayer and enlarge this interlayer.
CNB2005100905226A 2005-08-17 2005-08-17 Composition of baffle for generating vortex liquid state flow or vortex combustive flow Expired - Fee Related CN100528335C (en)

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CNB2005100905226A CN100528335C (en) 2005-08-17 2005-08-17 Composition of baffle for generating vortex liquid state flow or vortex combustive flow
US11/503,086 US20070039608A1 (en) 2005-08-17 2006-08-14 Baffle assembly structure for producing fluid or flame whirls
JP2006006633U JP3134132U (en) 2005-08-17 2006-08-16 Damper combined structure of swirling liquid flow or swirling combustion flow
US11/878,008 US20070261828A1 (en) 2005-08-17 2007-07-20 Baffle assembly for establishing fluid or flame cyclones

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Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008154046A1 (en) * 2007-06-15 2008-12-18 Auburn University Fluid storage containers with baffles
US9061230B2 (en) * 2012-10-24 2015-06-23 Yaser K. Barakat System to remove contaminants from air stream
US10808953B2 (en) * 2013-06-28 2020-10-20 Illinois Tool Works Inc. Airborne component extractor with baffled debris collection
DE102015212893A1 (en) * 2014-07-10 2016-01-14 Metallbau Eckert GmbH Flue gas heat exchanger and method for operating a flue gas heat exchanger
CN104235872A (en) * 2014-08-20 2014-12-24 胡延节 Energy saving device of fuel oil and gas boiler
CN104501181A (en) * 2014-11-11 2015-04-08 朱家元 Tobacco-stem biomass boiler
US11530826B2 (en) 2015-07-16 2022-12-20 Illinois Tool Works Inc. Extractor with segmented positive pressure airflow system
US11014132B2 (en) 2015-07-16 2021-05-25 Illinois Tool Works Inc. Extractor with end-mounted positive pressure system
CN105999942B (en) * 2016-06-27 2017-12-01 广州敦诚润宇环保工程有限公司 A kind of dust arrester of industrial waste gas before purified treatment
CN110250930A (en) 2017-08-09 2019-09-20 沙克忍者运营有限责任公司 Cooking system
KR102196567B1 (en) * 2019-04-24 2020-12-29 현권혁 Small sized wet scrubber for livestock facilities
CN111229038A (en) * 2020-03-16 2020-06-05 西安西热锅炉环保工程有限公司 A cut apart storehouse formula guide plate structure for exhaust-heat boiler flaring flue
JP2022177578A (en) * 2021-05-18 2022-12-01 富士電機株式会社 Scrubber apparatus for geothermal power generation
CN114307509B (en) * 2022-01-24 2023-05-02 无锡市华天环保科技有限公司 High-efficient scrubbing tower is used in exhaust-gas treatment

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2604150A (en) * 1944-10-17 1952-07-22 Servel Inc Flash tube igniter for burners at different levels
US3616744A (en) * 1969-08-21 1971-11-02 Donald D Jensen Air cleansing system for cooking ranges
US3920424A (en) * 1971-02-16 1975-11-18 Texas Gulf Inc Liquid sulphur gas scrubber apparatus
US3945812A (en) * 1973-01-24 1976-03-23 Doane Dewitt H Method of filtering grease-laden air
FI77163C (en) * 1984-03-09 1989-02-10 Halton Oy Air Purifier
US4827903A (en) * 1985-10-31 1989-05-09 Kim Byung N Barbecue cooker with smoke and collection system
DE4131988C2 (en) * 1991-09-26 1995-05-11 Rentschler Reven Lueftungssyst Separator for liquids from a gas stream, especially for oil mist
ES2090736T3 (en) * 1993-03-02 1996-10-16 Wimbock Besitz Gmbh DEVICE TO SEPARATE PARTICLES, ESPECIALLY OIL OR FAT PARTICLES.
US6216687B1 (en) * 1996-03-22 2001-04-17 The Majestic Products Company Unvented heating appliance having system for reducing undesirable combustion products
US6041774A (en) * 1998-11-13 2000-03-28 Evs, Inc. Overhead ventilation system for use with a cooking appliance
US5983888A (en) * 1999-04-07 1999-11-16 Whirlpool Corporation Low noise cooker hood
US6290742B1 (en) * 1999-12-23 2001-09-18 Durr Industries, Inc. Baffle system for separating liquid from a gas stream

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