CN202336335U - Rotational flow dual-supergravity machine - Google Patents
Rotational flow dual-supergravity machine Download PDFInfo
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- CN202336335U CN202336335U CN2011204297555U CN201120429755U CN202336335U CN 202336335 U CN202336335 U CN 202336335U CN 2011204297555 U CN2011204297555 U CN 2011204297555U CN 201120429755 U CN201120429755 U CN 201120429755U CN 202336335 U CN202336335 U CN 202336335U
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- Prior art keywords
- eddy flow
- impeller
- gravity
- liquid
- centrifugal
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- 239000007789 gases Substances 0.000 claims abstract description 41
- 239000007788 liquids Substances 0.000 claims abstract description 36
- 238000000889 atomisation Methods 0.000 claims abstract description 19
- 239000003480 eluents Substances 0.000 claims abstract description 16
- 239000011257 shell materials Substances 0.000 claims abstract description 10
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- 230000000694 effects Effects 0.000 abstract description 13
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- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound 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O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxides Inorganic materials 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
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- 239000003546 flue gases Substances 0.000 description 1
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- 238000000034 methods Methods 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N naphthalene Chemical compound 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C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 239000011049 pearl Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001172 regenerating Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002594 sorbents Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N sulphide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 238000003786 synthesis reactions Methods 0.000 description 1
- 230000002194 synthesizing Effects 0.000 description 1
- 238000006276 transfer reactions Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000011901 water Substances 0.000 description 1
Abstract
Description
Technical field
The utility model relates to a kind of hypergravity equipment, is specifically related to the two hypergravity machines of a kind of eddy flow.
Background technology
Hypergravity machine is the common equipment in the chemical field, is commonly used to gas is carried out the wash-out removing impurities, for example: remove foreign gases such as hydrogen sulfide in the gas, sulfur dioxide, carbon dioxide, hydrogen cyanide.In concrete the use, under the high pressure more than the 2.0MPa, the gas travels through packed bed, under the effect of high speed centrifugation power, solution passes through packed bed, realizes gas-liquid reverse absorbing contacting in filler, and this technology is applicable under clean gas and the high pressure and operates.When carrying out coke oven gas purification, solution is from the packed bed of rotation or inboard spray, under centrifugal action; Be easy to pass through packed bed,, belong to low pressure power because coke gas cleaning system pressure is lower than 0.05Mpa; Coke gas is difficult to reverse filler and the solution formation adverse current of passing through; Can only pass through packed bed along the centrifugal force direction with solution and stream, this low pressure and stream absorb to be compared with the high pressure counter-current absorption, and mass transfer effect differs greatly.Can not satisfy user demand.
Summary of the invention
Goal of the invention: to the deficiency that exists in the prior art; The purpose of the utility model provides the two hypergravity machines of a kind of eddy flow; So that coal gas washs the gravity mixing desulfurization that absorbs desulfurization and centrifugal force field through swirling flow atomizing liquid in the two hypergravity machines of eddy flow, overcome the washing that gas-liquid is simple and stream contacts and absorb shortcoming; Reach the effect of atomized liquid and coal gas premixed desulfurization, improve desulfurized effect under the normal pressure.
Technical scheme: in order to realize the foregoing invention purpose, the technical scheme that the utility model adopts is:
The two hypergravity machines of a kind of eddy flow comprise housing, in housing, are provided with the eddy flow gravity sections of atomization and the centrifugal gravity field section that communicate; In described eddy flow gravity sections of atomization, be provided with deflector, on described deflector, be provided with liquid-leaking nozzle; Below deflector, be provided with by atomizing net, the fixing cylindrical shape eddy flow gravity atomizer formed of impeller, eddy flow impeller and base plate, described fixedly impeller and eddy flow impeller are wrapped in atomizing and net interior formation, and base plate is located at the eddy flow wheel bottom; Be provided with eluent import and gas feed at the top of housing, form cavity behind the top seal of described deflector through seal circle and housing, the eluent import communicates with this cavity, and gas feed is passed cavity through the pipeline connection and communicated with cylindrical shell; Section is provided with the centrifugal gravity device in described centrifugal gravity field, above the centrifugal gravity device, is provided with toroidal membrane, in the middle of toroidal membrane, leaves the vapour-liquid through hole, on toroidal membrane, leaves sieve aperture; In housing, be provided with axis, described axis all links to each other with the centrifugal gravity device with the eddy flow impeller blade.
Described fixedly impeller and eddy flow impeller are formed by several impeller blades, and fixedly the impeller blade quantity of impeller and eddy flow impeller is identical or different.
Around the vapour-liquid through hole of said toroidal membrane, be provided with and block the liquid weir.
The eddy flow gravity sections of atomization of the utility model can be arranged on the section of centrifugal gravity field, also can be provided with separately, if gas pressure is too low, then need add the blower fan pressurization.
The centrifugal gravity device is made up of keel frame and packed bed, and packing layer is set on packed bed.
Beneficial effect: compare with hypergravity machine of the prior art, the outstanding advantage that the two hypergravity machines of the eddy flow of the utility model have comprises: simple in structure, design ingenious; Operation combination rule according to coke-stove gas characteristics and process for purifying system; Make coal gas in the two hypergravity machines of eddy flow, washing absorbs the gravity mixing desulfurization of desulfurization and centrifugal force field through swirling flow atomizing liquid, overcomes gas-liquid washing simple and the stream contact and absorbs shortcoming; Reach the effect of atomized liquid and coal gas premixed desulfurization; Improve desulfurized effect under the normal pressure, have good practicability, can produce good economic benefits and social benefit.
In addition, the two hypergravity machines of this eddy flow under multiple pressure condition, are handled through taking off slag, detar, taking off coal gas or other gas behind the naphthalene.Also being applicable to balances each other absorbs and chemical absorbing, and main application direction is sour gas such as gas removal hydrogen sulfide, hydrogen cyanide, sulfur dioxide, and it is synthetic etc. also to can be applicable to water deoxygenation, devolatilization, rectifying, extraction, wastewater treatment, flue gas desulfurization and dedusting, chemical industry.
Description of drawings
Fig. 1 is the structural representation of the two hypergravity machines of eddy flow;
Fig. 2 is the structural representation of eddy flow gravity atomizer.
The specific embodiment
Below in conjunction with concrete accompanying drawing the utility model is done further explanation.
As depicted in figs. 1 and 2, the two hypergravity machines of eddy flow comprise cylindrical shell 1, are provided with eluent import 8 and gas feed 11 at the top of housing 1, and side is provided with subsequent use mouthful 12, and sides is provided with gas liquid outlet 9.Bottom at housing 1 is provided with support.Constitute by the two parts that communicate up and down on the internal structure of housing 1, i.e. eddy flow gravity sections of atomization and eddy flow gravity sections of atomization, eddy flow gravity sections of atomization can be located on the eddy flow gravity sections of atomization or under, preferably be located on the eddy flow gravity sections of atomization.Following emphasis is introduced with preferred scheme.
Eddy flow gravity sections of atomization integral body is a circular cylinder body, and top is provided with deflector 2, on deflector 2, is provided with liquid-leaking nozzle; Have eddy flow gravity atomizer at deflector 2, what eddy flow gravity atomizer was served as reasons atomizing net 3 parcels sets gradually fixedly impeller 4, eddy flow impeller 5 and base plate 18 from top to bottom, and fixedly impeller 4 is fixed, and eddy flow impeller 5 can rotate, axis 7 drivings.Fixedly impeller 4 is formed by several impeller blades with eddy flow impeller 5, and fixedly the impeller blade quantity of impeller 4 and eddy flow impeller 5 is identical or different, and is preferred different.Deflector 2 forms cavity with housing 1 top through seal circle 14 sealing backs, and eluent import 8 communicates with this cavity.
Centrifugal gravity field section, diameter is identical with eddy flow gravity sections of atomization, in establish a centrifugal gravity device 6, its structure is made up of keel frame and packed bed, and packing layer is set on packed bed, centrifugal gravity device 6 is driven by axis 7.
For preventing the gas-liquid short circuit, between eddy flow gravity sections of atomization bottom and centrifugal gravity field section, toroidal membrane 13 is set, toroidal membrane 13 central authorities are provided with vapour-liquid through hole 17, and are provided with a ring baffle as blocking liquid weir 16 along vapour-liquid through hole 17 circumference.On toroidal membrane 13, be provided with sieve aperture 15, sieve aperture 15 makes solution evenly flow into packing layer over against packed bed.Atomization gas and gas get into centrifugal force fields by vapour-liquid through hole 17, in packed bed and the descending solution haptoreaction of meeting.
On Drive Structure, axis 7 passes vapour-liquid through hole 17 and links to each other with eddy flow gravity sections of atomization eddy flow plate 4, drives 4 rotations of eddy flow plate.In housing 1; Magnetic drives and Sealing Technology are adopted in body sealing between axis 7 and the power-equipment; Adopt the sealing of glue spare between gas and the lubricating fluid and be provided with the certain lubricating fluid and the height of refluxing opening, gas can not be revealed by refluxing opening, guarantee normally operation.Adopt liquid hydrostatic bearing or dynamic oil film bearing at the running part box house; Supply with lubricating system by the outside; Guarantee that it is lubricated and transport the heat that is produced that its outer lubricating system of supplying with is provided with operating pressure, pressure current that can hydrostatic bearing; Also dynamic oil film bearing lubrication be can supply with, and the safety valve setting and the warning device of pressure, isobaris surface system are provided with.
During work, eluent B is sprayed downwards by liquid-leaking nozzle on the deflector 2, and gas A is fed in the cylindrical shell by gas feed 11; Eluent B is nebulized by the eddy flow impeller that rotates 5 bumps and mixes with gas A, and under the effect of revolving force, fixedly the eluent B on impeller 4 and the rotary blade 5 produces eddy flow, tears; Under action of centrifugal force, to sputter all around, atomize, A combines with gas; To gas A wash-out, the gas-liquid of sputter passes atomizing net 3, after carrying out once more mechanical atomization and accomplishing for the second time wash-out; Bump to housing 1 inwall, under the effect of gravity, fall, get into centrifugal gravity field section.The center, centrifugal gravity field that gas A and liquid pearl mixture are rotated sucks; And under the gravitational field effect, be pressed into packed bed by central authorities; And tangentially rotate through packing layer; Be thrown into housing 1 inwall at last, collect in centrifugal gravity device 6 bottoms and the gas liquid outlet 9 airbleed liquid mixture C of tangential direction from the side.Knockout through being provided with is in addition isolated circulation fluid, and gas-liquid is accomplished mass transfer operation and separated.
In addition, during work, eluent B and gas A also can reversely carry out, and promptly eluent B is sprayed downwards by liquid-leaking nozzle on the deflector 2; Gas A is fed in the cylindrical shell by gas vent 9, and eluent B is nebulized by the eddy flow impeller that rotates 5 bumps and mixes with gas A, under the effect of revolving force; Fixedly the eluent B on impeller 4 and the rotary blade 5 produces eddy flow, tears, and under action of centrifugal force, to sputter all around, atomizes; A combines with gas, to gas A wash-out, at this moment; Straight sheet when impeller blade is preferably walked abreast by gas-liquid changes curved tabs into, makes gas A in rotation, produce an eddy flow power that makes progress, and makes clean gas discharge from import 11.Wherein, curved tabs can or have the tabs of certain angle for arc-like sheet.
The dual performance of compatible spray reaction section of the two hypergravity eddy flow machines of the eddy flow of the utility model and filler conversion zone.It is the rotation that relies on hydraulic cyclone to produce that spraying absorbs, clash into, cut apart, atomizing, and it is long-pending to make absorption liquid fully disperse to increase sorbent surface, and contact surface is brought in constant renewal in.Eddy flow is by fixedly impeller 4 and rotary blade 5 produce eddy flow under interacting; Under action of centrifugal force; Impact is blade down, isolates regenerating 2 times spiral eddy flows under the active force of lower blade and under the effect of eddy flow impeller 5, rushing at atomizing net 3, and operation outgases; The continuous new eluent of supply passing through and hitting the housing 1 inwall mass transfer reaction that atomizes again behind the atomizing net 3.Separate with toroidal membrane 13 via the reacted gas-liquid mixture of gravity swirling flow atomizing; Atomized liquid is not gathered toroidal membrane 13 sprinkles and is gone into packing layer; And atomized liquid and gas are mixed into centrifugal gravity machine central authorities, and under centrifugal action, pass through the solution cross-flow absorbing contacting sulfide of packed bed and vertical sprinkle.
Therefore the two hypergravity machines of the eddy flow of the utility model can be applicable to that high pressure gas liquid reaction technology also is applicable to low pressure or synthesis under normal pressure technology according to the import and export position of the operating pressure condition adjustment gas-liquid of handling gas.
Claims (9)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204297555U CN202336335U (en) | 2011-11-03 | 2011-11-03 | Rotational flow dual-supergravity machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204297555U CN202336335U (en) | 2011-11-03 | 2011-11-03 | Rotational flow dual-supergravity machine |
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| Publication Number | Publication Date |
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| CN202336335U true CN202336335U (en) | 2012-07-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011204297555U CN202336335U (en) | 2011-11-03 | 2011-11-03 | Rotational flow dual-supergravity machine |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102441323A (en) * | 2011-11-03 | 2012-05-09 | 袁长胜 | Swirl double hypergravity machine |
| CN102872788A (en) * | 2012-09-03 | 2013-01-16 | 神华集团有限责任公司 | Ultra-gravity multifunctional reactor |
-
2011
- 2011-11-03 CN CN2011204297555U patent/CN202336335U/en not_active IP Right Cessation
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102441323A (en) * | 2011-11-03 | 2012-05-09 | 袁长胜 | Swirl double hypergravity machine |
| CN102441323B (en) * | 2011-11-03 | 2013-10-30 | 袁长胜 | Swirl double hypergravity machine |
| CN102872788A (en) * | 2012-09-03 | 2013-01-16 | 神华集团有限责任公司 | Ultra-gravity multifunctional reactor |
| CN102872788B (en) * | 2012-09-03 | 2015-01-07 | 神华集团有限责任公司 | Ultra-gravity multifunctional reactor |
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Granted publication date: 20120718 Termination date: 20141103 |