CN108815928A - The device and its working method of tar separation in a kind of pair of pyrolytic gasification gaseous mixture - Google Patents
The device and its working method of tar separation in a kind of pair of pyrolytic gasification gaseous mixture Download PDFInfo
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- CN108815928A CN108815928A CN201811006310.9A CN201811006310A CN108815928A CN 108815928 A CN108815928 A CN 108815928A CN 201811006310 A CN201811006310 A CN 201811006310A CN 108815928 A CN108815928 A CN 108815928A
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- central tube
- tar
- gas
- ontology
- air inlet
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- 238000002309 gasification Methods 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims abstract description 19
- 239000008246 gaseous mixture Substances 0.000 title claims abstract description 17
- 238000000926 separation method Methods 0.000 title claims abstract description 16
- 230000001133 acceleration Effects 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 230000002349 favourable effect Effects 0.000 claims abstract description 5
- 241000589902 Leptospira Species 0.000 claims abstract description 4
- 239000011269 tar Substances 0.000 claims description 49
- 230000033001 locomotion Effects 0.000 claims description 9
- 230000005540 biological transmission Effects 0.000 claims description 7
- 241000883990 Flabellum Species 0.000 claims description 4
- 230000001174 ascending effect Effects 0.000 claims description 4
- 238000010276 construction Methods 0.000 claims description 4
- 239000011286 gas tar Substances 0.000 claims description 3
- 230000000630 rising effect Effects 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 44
- 239000000567 combustion gas Substances 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 238000012423 maintenance Methods 0.000 abstract description 5
- 238000005336 cracking Methods 0.000 abstract description 4
- 238000000197 pyrolysis Methods 0.000 description 5
- 239000002737 fuel gas Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 230000005653 Brownian motion process Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 238000005537 brownian motion Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/14—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/18—Modifying the properties of the distillation gases in the oven
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Cyclones (AREA)
Abstract
The device and its working method of tar separation in a kind of pair of pyrolytic gasification gaseous mixture belong to the technical field of gas separation and tar gasification cracking.The device includes ontology, air inlet acceleration mechanism and central tube.Ontology successively uses inferior pyramidal body, lower cylinder, epicone body to be fixedly connected integrally with upper cylinder.The bottom plate of inferior pyramidal body is equipped with air inlet acceleration mechanism and drain valve, and the side of upper cylinder is equipped with a leptospira structure tangentially connected with discharge pipe.Central tube is located at the medium position of ontology, the lower part cone of central tube reaches always in the corresponding position of lower cylinder intake pipe, the tangential port of favorable current is equipped on the central tube below upper cylinder top plate, tangential port is evenly arranged on central tube using axial multiple rows of circumferential direction.The apparatus structure is simple, easy to use, both can produce more preferably high heating value combustion gas, while also reducing later period many equipment investments as brought by processing tar and water containing tar and the trouble in maintenance.
Description
Technical field
The present invention relates to the devices and its working method of tar separation in a kind of pair of pyrolytic gasification gaseous mixture, belong to gas point
From the technical field with tar gasification cracking.
Background technique
Currently, useless in house refuse, kitchen garbage, medical dangerous waste rubbish, farm crop straw organism matter and other organic matters
In terms of the processing of gurry, all tend to the method using pyrolytic gasification.This method not only thorough reduction, but also by its recycling
Using and can complete harmless discharge, thus develop miscellaneous gasification and pyrolysis device.However, in its pyrolytic gasification
It is generally existing tired in the processing such as washing water containing tar in a large amount of tar and tar water that generate in the process, combustion gas washing process
Difficult and urgent problem to be solved.Currently, all substantially using the following method both at home and abroad：Physical method（Absorption method, WATER-WASHING METHOD,
Electric fishing method）It not only needs to put into other ancillary equipments such as a large amount of scrubbing tower, dehumidifying tower, air bearing settling tank, but also needs additional
Increase electric power and more maintenance costs, thermochemical method（Pyrolysis method, catalystic pyrolysis）A set of high warm must in addition be installed additional
Source and independent cracker carry out heat scission reaction after then again passing through the gas containing a large amount of tar.
Catalystic pyrolysis
While generating fuel gas during house refuse, medical waste, farm crop straw organism matter etc. are in pyrolytic gasification,
Also a large amount of tar and tar vapor are generated.How it is easy fuel gas is separated with tar, containing tar vapor, then general
Tar and containing tar vapor carry out cracking be gasificated into fuel gas, be industry personnel's general concern the problem of.This problem
Solution both can produce more preferably high heating value combustion gas, while decrease the later period by processing tar and the band of water containing tar
The trouble on many equipment investments and maintenance come.
Summary of the invention
In order to overcome problems of the prior art, the present invention provides tar separation in a kind of pair of pyrolytic gasification gaseous mixture
Device and its working method, which answers structure simple, easy to use, both can produce more preferably high heating value combustion gas,
Later period many equipment investments as brought by processing tar and water containing tar and the trouble in maintenance are also reduced simultaneously.
The technical solution adopted by the present invention is that：The device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture, it includes ontology,
It is characterized in：It further includes air inlet acceleration mechanism and a central tube, the ontology successively use inferior pyramidal body, lower cylinder,
Epicone body is fixedly connected integrally with upper cylinder, and air inlet pipe is tangentially fixedly connected with lower cylinder, inferior pyramidal body
Bottom plate is equipped with air inlet acceleration mechanism and drain valve, and the side of upper cylinder is equipped with a spiral tangentially connected with discharge pipe
Body structure；The central tube is located at the medium position of ontology, and the top of central tube is fixedly connected with the top plate of upper cylinder, under
The cone in portion reaches always the center pipe end in the corresponding position of lower cylinder intake pipe, above upper cylinder top plate
Portion's closing, laterally attached escape pipe are equipped with the tangential port of favorable current, tangentially on the central tube below upper cylinder top plate
Port is evenly arranged on central tube using axial multiple rows of circumferential direction.
The air inlet acceleration mechanism is fixed on motor the plate outer side of inferior pyramidal body, and the transmission shaft of motor protrudes into inferior pyramidal
Driving flabellum rotation in vivo, transmission shaft is by the support seat supports that are fixed on the inside of inferior pyramidal body bottom plate.
The upper intracorporal central tube of cylinder is equipped with the circumferential uniformly distributed tangential port of 4-6 row, in the upper of epicone body
The corresponding central tube in portion is equipped with the circumferential uniformly distributed tangential port of 1-2 row.
The working method of the device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture, when mixed gas is from air inlet
When pipe flows into ontology, since body construction and air inlet acceleration mechanism force air-flow to do circle rotation movement, mixed gas carries out rich
Collection and suspension, do circumference and ascending motion, the gas that the big gas of quality can be small by quality along the outer wall and central tube of ontology
It drives and presses to central tube, the big gas of quality can be distributed in the periphery of the small gas of quality, and constantly assemble and be concentrated；Work as gas
When being risen in epicone body by enrichment suspension, mixed gas is further speeded up, the environment that mixed gas rises in rotation
It is lower to enter upper cylinder, the biggish tar of quality is drawn by the tangential direction of gas rotating by discharge pipe and tar water water steams
Gas draws the lesser gas of quality by the central tube of tangential port by escape pipe, thus tar and tar in mixed gas
Vapor is separated.
The beneficial effects of the invention are as follows：This device to tar separation in pyrolytic gasification gaseous mixture includes ontology, air inlet
Acceleration mechanism and central tube.Ontology successively uses inferior pyramidal body, lower cylinder, epicone body to be fixedly connected with upper cylinder
Integrally.The bottom plate of inferior pyramidal body is equipped with air inlet acceleration mechanism and drain valve, and the side of upper cylinder is equipped with one and row
The tangentially connected leptospira structure of outlet pipe.Central tube is located at the medium position of ontology, and the lower part cone of central tube reaches always
The corresponding position of lower cylinder intake pipe is equipped with the tangential gas of favorable current on the central tube below upper cylinder top plate
Mouthful, tangential port is evenly arranged on central tube using axial multiple rows of circumferential direction.The apparatus structure is simple, easy to use, both can produce
More preferably high heating value combustion gas, while also reducing later period many equipment investments as brought by processing tar and water containing tar
With the trouble in maintenance.
Detailed description of the invention
Fig. 1 is the structural front view of the device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture.
Fig. 2 is the structure top view of the device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture.
Fig. 3 is the A-A view in Fig. 1.
Fig. 4 is the B-B view in Fig. 1.
In figure：1, inferior pyramidal body, 2, lower cylinder, 2a, air inlet pipe, 3, epicone body, 4, upper cylinder, 4a, spiral shell
Rotation body structure, 4b, discharge pipe, 5, central tube, 5a, cone, 5b, tangential port, 5c, escape pipe, 6, motor, 6a, support base,
6b, transmission shaft, 6c, flabellum, 7, drain valve.
Specific embodiment
Completely illustrate the present invention by way of example and in conjunction with the accompanying drawings to become apparent from.
Fig. 1,2,3,4 show the structure chart of tar separator in a kind of pair of pyrolytic gasification gaseous mixture.It is this right in figure
The device of tar separation includes ontology, air inlet acceleration mechanism and a central tube 5 in pyrolytic gasification gaseous mixture.Ontology successively uses
Inferior pyramidal body 1, lower cylinder 2, epicone body 3 and upper cylinder 4 are fixedly connected integrally, air inlet pipe 2a and lower cylinder
Body 2 is tangentially fixedly connected, and the bottom plate of inferior pyramidal body 1 is equipped with air inlet acceleration mechanism and drain valve 7, the side of upper cylinder 4
Equipped with a leptospira structure 4a tangentially connected with discharge pipe 4b.Central tube 5 is located at the medium position of ontology, central tube 5
Top is fixedly connected with the top plate of upper cylinder 4, and the cone 5a of lower part is reached always lower 2 intake pipe 2a's of cylinder
Corresponding position, 5 end-enclosed of central tube above upper 4 top plate of cylinder, laterally attached escape pipe 5c, in upper cylinder
Central tube 5 below 4 top plates is equipped with the tangential port 5b of favorable current, during tangential port 5b is evenly arranged on using axial multiple rows of circumferential direction
On heart pipe 5.
Air inlet acceleration mechanism is fixed on motor 6 plate outer side of inferior pyramidal body 1, and the transmission shaft 6c of motor 6 protrudes into lower cone
Driving flabellum 6c rotation in body 1, transmission shaft 6b are supported by being fixed on the support base 6a on the inside of 1 bottom plate of inferior pyramidal body.
Central tube 5 in upper cylinder 4 is equipped with the uniformly distributed tangential port 5b of 4 row's circumferential directions, on the top of epicone body 3
Corresponding central tube 5 is equipped with the uniformly distributed tangential port 5b of 1 row's circumferential direction.
This working method to the device of tar separation in pyrolytic gasification gaseous mixture, when mixed gas is flowed from air inlet pipe 2a
When entering ontology, since body construction and air inlet acceleration mechanism force air-flow to do circle rotation movement, mixed gas carry out enrichment and
It suspends, does circumference and ascending motion along the outer wall and central tube 5 of ontology, the big gas of quality can be by the small gas of quality in
Heart pipe 5 drives pressure, and the big gas of quality can be distributed in the periphery of the small gas of quality, and constantly assembles and be concentrated；When gas quilt
When enrichment suspension is risen in epicone body 3, mixed gas is further speeded up, and mixed gas is in the environment of rotating rising
Into upper cylinder 4, the biggish tar of quality is drawn by the tangential direction of gas rotating by discharge pipe 4b and tar water water steams
Gas, by escape pipe 5c by tangential port 5b central tube 5 draw the lesser gas of quality, thus in mixed gas tar and
Tar vapor is separated.
Using above-mentioned technical solution, when mixed gas is entered with certain air velocity, due to body construction and into
The effect of gas acceleration mechanism causes air-flow forced to do circle rotation movement.Effect of each mixed gas in centrifugal force and centripetal force
Under, it is effectively enriched with and is suspended according to the regularity of distribution of molecular brownian motion.Under the promotion of thermodynamics kinetic energy, gas meeting
Circumference and ascending motion are done along the outer wall and central tube of ontology.It is analyzed according to Blang's molecular motion Distribution Principle：Limited
In space, the small gas of quality can be driven to central area and be pressed by the big gas of quality；And according to Newton's second law and centrifugal force
With the action principle of centripetal force：The big gas of quality can be distributed in the periphery of the small gas of quality, and constantly assemble and be concentrated；
And the small gas of quality drives pressure at it and also assembles constantly around central tube.It is risen to centainly when gas is suspended by enrichment
When degree, it is introduced into the epicone body of small diameter, accelerates mixed gas faster.Mixed gas rises in rotation
In the environment of enter upper cylinder, draw the biggish tar of quality and tar water by the tangential direction of gas rotating by discharge pipe
Vapor, by escape pipe by tangential port central tube draw the lesser gas of quality, thus in mixed gas tar and
Tar vapor is separated.
The method that tar and tar vapor regasify cracking is as follows：The tar and tar vapor drawn from discharge pipe,
In the environment of keeping the temperature 200-240C °, pyrolysis gasification furnace stone or metal plate for standing a stove on as a precaution against fire bottom is input by pipeline, is directly entered its redox
Layer in, carried out without catalyst weight thermal cracking gasification, generate with CH4 gas be advocate peace a small amount of CO, H2 substance high heating value combustion
Gas.
Claims (4)
1. the device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture, it includes ontology, it is characterized in that：It further includes that air inlet adds
Fast mechanism and a central tube（5）, the ontology successively uses inferior pyramidal body（1）, lower cylinder（2）, epicone body（3）With
Upper cylinder（4）It is fixedly connected with integral, air inlet pipe（2a）With lower cylinder（2）It is tangentially fixedly connected, inferior pyramidal body（1）
Bottom plate be equipped with air inlet acceleration mechanism and drain valve（7）, upper cylinder（4）Side be equipped with one and discharge pipe（4b）It cuts
To the leptospira structure of connection（4a）；The central tube（5）Positioned at the medium position of ontology, central tube（5）Top and upper circle
Cylindrical body（4）Top plate be fixedly connected, the cone of lower part（5a）It reaches always in lower cylinder（2）Intake pipe（2a）Phase
Position is answered, in upper cylinder（4）Central tube above top plate（5）End-enclosed, laterally attached escape pipe（5c）, in upper cylinder
Body（4）Central tube below top plate（5）It is equipped with the tangential port of favorable current（5b）, tangential port（5b）Using axial multiple rows of
Circumferential direction is evenly arranged on central tube（5）On.
2. the device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture according to claim 1, it is characterized in that：It is described into
Gas acceleration mechanism is motor（6）It is fixed on inferior pyramidal body（1）Plate outer side, motor（6）Transmission shaft（6c）Protrude into inferior pyramidal
Body（1）Interior driving flabellum（6c）Rotation, transmission shaft（6b）By being fixed on inferior pyramidal body（1）Support base on the inside of bottom plate（6a）Branch
Support.
3. the device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture according to claim 1, it is characterized in that：On described
Cylinder（4）Interior central tube（5）It is equipped with the circumferential uniformly distributed tangential port of 4-6 row（5b）, in epicone body（3）Top
Corresponding central tube（5）It is equipped with the circumferential uniformly distributed tangential port of 1-2 row（5b）.
4. the working method of tar separator, feature in a kind of pair of pyrolytic gasification gaseous mixture according to claim 1
It is：When mixed gas is from air inlet pipe（2a）When flowing into ontology, since body construction and air inlet acceleration mechanism force air-flow to do circumference
Rotary motion, mixed gas are enriched with and are suspended, along the outer wall and central tube of ontology（5）Do circumference and ascending motion, matter
Measuring big gas can be by the small gas of quality to central tube（5）Pressure is driven, the big gas of quality can be distributed in the small gas of quality
Periphery, and constantly assemble and be concentrated；Epicone body is risen to when gas is suspended by enrichment（3）When middle, mixed gas obtain into
One step accelerates, and mixed gas enters upper cylinder in the environment of rotating and rising（4）, by discharge pipe（4b）By gas rotating
Tangential direction draws the biggish tar of quality and tar water vapor, by escape pipe（5c）By tangential port（5b）Central tube
（5）Draw the lesser gas of quality, thus in mixed gas tar and tar vapor separate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811006310.9A CN108815928A (en) | 2018-08-30 | 2018-08-30 | The device and its working method of tar separation in a kind of pair of pyrolytic gasification gaseous mixture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811006310.9A CN108815928A (en) | 2018-08-30 | 2018-08-30 | The device and its working method of tar separation in a kind of pair of pyrolytic gasification gaseous mixture |
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| Publication Number | Publication Date |
|---|---|
| CN108815928A true CN108815928A (en) | 2018-11-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811006310.9A Pending CN108815928A (en) | 2018-08-30 | 2018-08-30 | The device and its working method of tar separation in a kind of pair of pyrolytic gasification gaseous mixture |
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Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1983000100A1 (en) * | 1981-06-29 | 1983-01-20 | Richard Chalupa | Enrichment cyclon of a gas mixture |
| US4371382A (en) * | 1980-08-06 | 1983-02-01 | Caribbean Properties Limited | Process and apparatus for the contact and separation of immiscible fluids |
| DE4234172A1 (en) * | 1992-10-12 | 1994-04-14 | Bert Steffens | Centrifugal separation of particles from a fluid stream - e.g. from air in a pneumatic conveying system |
| JPH10328647A (en) * | 1997-06-03 | 1998-12-15 | Chiyoda Manufacturing Co Ltd | Apparatus for removing fine particle from steam generator for producing pure steam and distilled water |
| WO2003055575A1 (en) * | 2001-12-31 | 2003-07-10 | Shell Internationale Research Maatschappij B.V. | Multistage fluid separation assembly and method |
| US20050211093A1 (en) * | 2004-03-23 | 2005-09-29 | Pratt & Whitney Canada Corp. | Air/oil separation system and method |
| CN101757836A (en) * | 2010-02-11 | 2010-06-30 | 常熟理工学院 | Scale type helical-flow air concentrating and separating device |
| US20100251692A1 (en) * | 2006-10-27 | 2010-10-07 | Kinde Sr Ronald August | Methods of combining a series of more efficient aircraft engines into a unit, or modular units |
| JP2012050929A (en) * | 2010-09-01 | 2012-03-15 | Gijutsu Kaihatsu Sogo Kenkyusho:Kk | Defoaming device |
| CN202237687U (en) * | 2011-09-23 | 2012-05-30 | 北京三川世纪技术有限公司 | Single tornadotron and filter element combined detachable separator |
| CN103041936A (en) * | 2011-10-15 | 2013-04-17 | 高苏茂 | Vortex acceleration dust collector |
| CN203355896U (en) * | 2013-04-27 | 2013-12-25 | 史明生 | Coal mine gas centrifugal separation purifying machine |
| CN205516904U (en) * | 2016-03-15 | 2016-08-31 | 中国石油天然气股份有限公司 | Spiral accelerating oil-gas separator |
| CN107737492A (en) * | 2017-11-25 | 2018-02-27 | 邹德学 | A kind of waste gas complex dust collector |
| CN209254321U (en) * | 2018-08-30 | 2019-08-16 | 大连惠川环保科技有限公司 | The device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture |
-
2018
- 2018-08-30 CN CN201811006310.9A patent/CN108815928A/en active Pending
Patent Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4371382A (en) * | 1980-08-06 | 1983-02-01 | Caribbean Properties Limited | Process and apparatus for the contact and separation of immiscible fluids |
| WO1983000100A1 (en) * | 1981-06-29 | 1983-01-20 | Richard Chalupa | Enrichment cyclon of a gas mixture |
| DE4234172A1 (en) * | 1992-10-12 | 1994-04-14 | Bert Steffens | Centrifugal separation of particles from a fluid stream - e.g. from air in a pneumatic conveying system |
| JPH10328647A (en) * | 1997-06-03 | 1998-12-15 | Chiyoda Manufacturing Co Ltd | Apparatus for removing fine particle from steam generator for producing pure steam and distilled water |
| WO2003055575A1 (en) * | 2001-12-31 | 2003-07-10 | Shell Internationale Research Maatschappij B.V. | Multistage fluid separation assembly and method |
| US20050211093A1 (en) * | 2004-03-23 | 2005-09-29 | Pratt & Whitney Canada Corp. | Air/oil separation system and method |
| US20100251692A1 (en) * | 2006-10-27 | 2010-10-07 | Kinde Sr Ronald August | Methods of combining a series of more efficient aircraft engines into a unit, or modular units |
| CN101757836A (en) * | 2010-02-11 | 2010-06-30 | 常熟理工学院 | Scale type helical-flow air concentrating and separating device |
| JP2012050929A (en) * | 2010-09-01 | 2012-03-15 | Gijutsu Kaihatsu Sogo Kenkyusho:Kk | Defoaming device |
| CN202237687U (en) * | 2011-09-23 | 2012-05-30 | 北京三川世纪技术有限公司 | Single tornadotron and filter element combined detachable separator |
| CN103041936A (en) * | 2011-10-15 | 2013-04-17 | 高苏茂 | Vortex acceleration dust collector |
| CN203355896U (en) * | 2013-04-27 | 2013-12-25 | 史明生 | Coal mine gas centrifugal separation purifying machine |
| CN205516904U (en) * | 2016-03-15 | 2016-08-31 | 中国石油天然气股份有限公司 | Spiral accelerating oil-gas separator |
| CN107737492A (en) * | 2017-11-25 | 2018-02-27 | 邹德学 | A kind of waste gas complex dust collector |
| CN209254321U (en) * | 2018-08-30 | 2019-08-16 | 大连惠川环保科技有限公司 | The device of tar separation in a kind of pair of pyrolytic gasification gaseous mixture |
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Application publication date: 20181116 |