CN106753484A - A kind of biomass microwave is pyrolyzed modified reactor assembly - Google Patents
A kind of biomass microwave is pyrolyzed modified reactor assembly Download PDFInfo
- Publication number
- CN106753484A CN106753484A CN201710075318.XA CN201710075318A CN106753484A CN 106753484 A CN106753484 A CN 106753484A CN 201710075318 A CN201710075318 A CN 201710075318A CN 106753484 A CN106753484 A CN 106753484A
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- China
- Prior art keywords
- microwave
- conversion zone
- pyrolyzed
- casing
- reactor assembly
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002028 Biomass Substances 0.000 title claims abstract description 30
- 238000006243 chemical reaction Methods 0.000 claims abstract description 68
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000010453 quartz Substances 0.000 claims abstract description 12
- 238000009529 body temperature measurement Methods 0.000 claims abstract description 4
- 239000010425 asbestos Substances 0.000 claims description 5
- 229910052895 riebeckite Inorganic materials 0.000 claims description 5
- 238000007789 sealing Methods 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims description 3
- 230000007246 mechanism Effects 0.000 claims description 2
- 238000000197 pyrolysis Methods 0.000 abstract description 14
- 238000010438 heat treatment Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 3
- 239000000463 material Substances 0.000 description 13
- 239000007789 gas Substances 0.000 description 8
- 239000012075 bio-oil Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 235000019198 oils Nutrition 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000002551 biofuel Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000010431 corundum Substances 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
Classifications
-
- 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
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- 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
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of biomass microwave pyrolysis modified reactor assembly, including open-close type microwave reaction casing, the reactor that is horizontally installed in the microwave reaction casing, the microwave reaction casing is connected between microwave generator by waveguide；Described reactor includes the exhaust section and conversion zone of being disconnected, the conversion zone and exhaust section are horizontally disposed with the air inlet pipe and blast pipe for having and extending to outside microwave reaction casing respectively, the conversion zone middle part is extended some temperature tubes for installing infrared and thermocouple temperature measurement instrument, and being horizontally disposed with the conversion zone has quartz plate.The present invention has the advantages that operation is simple and reliable, pyrolysis effect is good, can be used as microwave-heating biomass reaction vessel, reaches smooth effective implementation of microwave-heating.
Description
Technical field
The present invention relates to microwave-heating biomass equipment, more particularly to a kind of biomass microwave pyrolysis modified reactor dress
Put.
Background technology
Biomass energy is energy solar energy being stored in chemical energy form as carrier with biomass in biomass, is had
It is distributed wide, renewable, low cost and other advantages.Using converting technology, biomass energy can be converted into liquid fuel（Biological bavin
Oil, bio-crude oil, methyl alcohol, ethanol and vegetable oil etc.）, heat, electricity, gaseous fuel（Hydrogen, biological fuel gas and biogas etc.）With it is solid
Fluid fuel（Charcoal or shaped fuel）Just gradually causing the attention of people Deng, its development and utilization, following very likely turning into can
The important component of continuous energy system.
Microwave is that frequency is 300MHZ ~ 300GHZ, and wavelength is the frequency electromagnetic waves of 1mm ~ 1m.Heating using microwave is to utilize material
Under the microwave energy field action of high frequency conversion, the motion of molecule becomes orderly high frequency vibrating by original rambling state
Dynamic, the kinetic energy of molecule is transformed into heat energy, reaches uniform heating.Microwave-heating be on the basis of conventional pyrolytic, with reference to microwave plus
Thermal technology is proposed and grown up, with advantages below with the conventional pyrolysis technology compared with：Microwave directly acts on material molecule
Or atom, firing rate is fast, efficiency high；Homogeneous heating, thermal inertia is small, it is easy to control；Penetrability is good, can directly to large scale thing
Material is pyrolyzed, and saves the pretreatment process of material；All thermal decomposition products can be trapped and utilized, and product property is better than
Conventional pyrolysis.
Existing numerous scholars are studied using the pyrolysis characteristicses that microwave produces bio-fuel to biomass both at home and abroad.It is micro-
Ripple pyrolysis is different from conventional pyrolysis, it is desirable to which reaction vessel, supporter etc. do not absorb or less absorption microwave, and high temperature resistant,
To realize ventilating during experiment in addition, be vented, collecting biological oil, pyrolysis gas and thermometric, so the material that most of experiment is used is anti-
Container is answered to use three mouthfuls of quartz flasks；Breather pipe, blast pipe in microwave reaction system also make by quartz；Three mouthfuls of quartz burn
The stopper of the connecting interface of bottle uses resistant to elevated temperatures silica gel plug, and the supporter of bottom is using heat-preservation cotton, ceramics, corundum cup.But
Three mouthfuls of quartz flasks have some defects：Material picks and places cumbersome, residue cleaning difficulty, and material easily lumps at thermocouple during reaction
And be difficult to quickly complete completely.Therefore, it is necessary to design the modified reactor assembly for being suitable for biomass microwave pyrolysis.
The content of the invention
Shortcoming and defect it is an object of the invention to overcome existing apparatus, there is provided a kind of material picks and places convenience, reaction fully, in fact
Test biomass microwave pyrolysis modified reactor assembly simple to operate.
The present invention is achieved through the following technical solutions：
A kind of biomass microwave is pyrolyzed modified reactor assembly, including open-close type microwave reaction casing, be horizontally installed on institute
The reactor in microwave reaction casing is stated, the microwave reaction casing is connected between microwave generator by waveguide；Described is anti-
Answering device includes the exhaust section and conversion zone of being disconnected, and the conversion zone and exhaust section are horizontally disposed with extend to microwave reaction respectively
Air inlet pipe and blast pipe outside casing, the conversion zone middle part is extended has some installations infrared and thermocouple temperature measurement instrument
Temperature tube, being horizontally disposed with the conversion zone has quartz plate.
Further, exhaust section ground and the conversion zone mill for being separately provided for connection of the exhaust section and conversion zone
Mouthful, diameter of the exhaust section more than conversion zone so that exhaust section is wrapped in conversion zone during connection, it is to avoid the bio oil of generation
It is bonded at both junctions.
Further, the conversion zone and air inlet pipe are integral type structure, and the exhaust section and blast pipe are integral type machine
Structure.
Further, the axis of described air inlet pipe and blast pipe is located in same horizontal line.
Further, it is provided with ground at the mouth of pipe of described temperature tube, air inlet pipe and blast pipe, it is ensured that the gas of device
Close property.
Further, described microwave reaction casing is included by flange and bolt seal connected casing and chamber door, institute
State air inlet pipe and blast pipe extends to the casing left and right sides.
Further, the casing left and right sides is respectively arranged with the air inlet pipe passed through for the air inlet pipe and blast pipe and leads to
Road and exhaust duct passageway, the casing middle part is extended thermometric tube passage, passes through for temperature tube, and the chamber door middle part extends
It is provided with the temperature tube channel seal with thermometric tube passage sealing pressing.
Further, described casing is provided with gasket seal with the junction of chamber door, and the gasket seal inside is soft
Property insulating pad, outside for parcel mesh member.
Further, the flexible heat-insulating pad uses rubbery asbestos gasket, and the parcel mesh member is woven wire.Rubber
Glue asbestos washer, can bear higher temperature, and outer wrap mesh is woven wire, in flange by after bolt presses, casing
Can realize being in close contact between chamber door, play a part of to prevent microwave leakage.
Further, described each temperature tube is respectively positioned in the vertically symmetrical plane of reactor so that at two point for measuring temperature with
Microwave point is apart from identical, it is ensured that the temperature of measurement has comparability.
Pyrolytic reaction of the invention includes as follows：It is laid in the biomass of quartz plate to be heated up under microwave action pyrolysis, produces
Raw high-temperature biological oil gas body is taken away by the nitrogen that two ends are passed through and enters condenser system.
It is of the invention that there is advantages below compared with existing device：
（1）This biomass microwave be pyrolyzed modified reactor assembly by simple experiment it is accurate for the purpose of, by changing vertical direction
Blast pipe is horizontal direction, makes the bio oil gas of generation and need not overcome the influences such as rising gravity, prevents bio oil condensing reflux,
The measure of the biological oil quality of influence；Exhaust pipe length is shortened, stroke of the gas in pipe is reduced, reduced in pipe directly
The time of condensation, is that bio oil fully condenses the condition of creating at condenser pipe；
（2）Reaction casing is upper and lower folding, and compared to conventional casing, operating space is bigger, is easy to pick and place reactor during experiment；
（3）Connected using ground between reactor parts, be easy to the assembly and disassembly before and after experiment, frosted ensures the gas of device at ground
Close property.Blast pipe bore is slightly larger than reaction tube, it is to avoid the bio oil of generation is bonded at ground.Centre is using quartz plate as reaction
Loading end, material is picked and placeed conveniently.Each reactive element is concentrated in reaction chamber body, and compact conformation is easy to operate, using flexible, is fitted
R＆D units are closed to use；
（4）Material is laid on quartz plate, and thermocouple probe does not go deep into inside material, is prevented because microwave is in tip aggregation causes
Between material caking and outer ring material is not sufficiently reactive；Infrared measurement of temperature port is in same perpendicular with thermocouple, and temperature has
Comparability.
In summary, the present invention has the advantages that operation is simple and reliable, pyrolysis effect is good, can be used as microwave-heating biomass
Reaction vessel, reaches and smoothly effectively implements.
Brief description of the drawings
Fig. 1 is the reactor schematic front view of the embodiment of the present invention.
Fig. 2 is the reactor left view schematic diagram of the embodiment of the present invention.
Fig. 3 is the microwave reaction casing dimensional structure diagram of the embodiment of the present invention.
In figure：1- blast pipes；2- exhaust sections；3- exhaust section grounds；4- conversion zone grounds；5- temperature tubes；6- conversion zones；7-
Air inlet pipe；8- chamber doors；9- casings；10- sides temperature tube passage seal；11- sides temperature tube passage；12- gasket seals；13- parcel nets
Orifice；14- air inlet tube passages.
Specific embodiment
The present invention is more specifically described in detail with reference to specific embodiment.
Embodiment
As shown in Figure 1 to Figure 3, a kind of microwave reaction case of biomass microwave pyrolysis modified reactor assembly, including open-close type
Body, the reactor being horizontally installed in the microwave reaction casing, pass through ripple between the microwave reaction casing and microwave generator
Lead connected
As depicted in figs. 1 and 2, described reactor includes the exhaust section 2 and conversion zone 6 of being disconnected, the conversion zone 6 and exhaust
Section 2 is horizontally disposed with the air inlet pipe 7 and blast pipe 1 for having and extending to outside microwave reaction casing, the conversion zone 6 and air inlet pipe 7 respectively
It is integral type structure, the exhaust section 2 and blast pipe 1 are integral type mechanism, meanwhile, described air inlet pipe 7 and the axle of blast pipe 2
Line is located in same horizontal line.The middle part of the conversion zone 6 is extended some surveys for installing infrared and thermocouple temperature measurement instrument
Warm pipe 5, being horizontally disposed with the conversion zone 6 has quartz plate, and in the present embodiment, the internal diameter of conversion zone 6 is 200mm, the He of air inlet pipe 7
The external diameter of blast pipe 1 is 10mm, and length is 110mm, a diameter of 10mm of the temperature tube 5, and length is 90mm.
Described each temperature tube 5 is respectively positioned in the vertically symmetrical plane of reactor so that point for measuring temperature occurs with microwave at two
Place is apart from identical, it is ensured that the temperature of measurement has comparability.
The exhaust section ground 3 and conversion zone ground 4 that are separately provided for connection of the exhaust section 2 and conversion zone 6, row
The width of gas section ground 3 and conversion zone ground 4 is 40mm, diameter of the exhaust section 2 more than conversion zone 6 so that arranged during connection
Gas section 2 is wrapped in conversion zone, it is to avoid the bio oil of generation is bonded at both junctions.
Ground is provided with the mouth of pipe of described temperature tube 5, air inlet pipe 7 and blast pipe 1, ensures the air-tightness of device.
As shown in figure 3, described microwave reaction casing is included by flange and bolt seal connected casing 9 and chamber door 8,
The left and right sides of the casing 9 is respectively arranged with the air inlet tube passage 14 that is passed through for the air inlet pipe 7 and blast pipe 1 and blast pipe is logical
Road, the air inlet pipe 7 and blast pipe 1 extend to the left and right sides of the casing 9, and the middle part of the casing 9 is extended temperature tube
Passage 11, the middle part of the chamber door 8 is extended the temperature tube channel seal 10 having with the thermometric tube passage 11 sealing pressing.
Described casing 9 is provided with gasket seal with the junction of chamber door 8, and the gasket seal inside is flexible gasket
Piece 12, the flexible sealing gasket 12 uses rubbery asbestos gasket, and outside is parcel mesh member 13, and the parcel mesh member 13 is
Woven wire.Rubbery asbestos gasket can bear higher temperature, and outer wrap mesh is woven wire, and bolt pressure is passed through in flange
After tight, can realize being in close contact between casing 9 and chamber door 8, play a part of to prevent microwave leakage.
The course of reaction of the present embodiment is as follows：
Nitrogen being passed through from air inlet pipe 7 and forming oxygen deficient atmospheres, a certain amount of biomass are uniformly laid on horizontal card in reaction before experiment
On quartz plate in device, microwave generator is opened after checking out device air-tightness, biomass heat up under microwave energy effect and are pyrolyzed,
React after the bio oil for producing is taken out of by nitrogen from blast pipe 1 and enter condenser system.
Embodiments of the present invention are simultaneously not restricted to the described embodiments, and other are any without departing from Spirit Essence of the invention
With the change, modification, replacement made under principle, combine, simplify, should be equivalent substitute mode, be included in of the invention
Within protection domain.
Claims (10)
1. a kind of biomass microwave is pyrolyzed modified reactor assembly, it is characterised in that：Microwave reaction casing including open-close type,
The reactor in the microwave reaction casing is horizontally installed on, waveguide phase is passed through between the microwave reaction casing and microwave generator
Even；Described reactor includes the exhaust section (2) and conversion zone (6) of being disconnected, and the conversion zone (6) and exhaust section (2) are respectively
Horizontally disposed to have the air inlet pipe (7) and blast pipe (1) extended to outside microwave reaction casing, conversion zone (6) middle part extension sets
Some temperature tubes (5) for installing infrared and thermocouple temperature measurement instrument are equipped with, being horizontally disposed with the conversion zone (6) has quartz plate.
2. biomass microwave according to claim 1 is pyrolyzed modified reactor assembly, it is characterised in that：The exhaust section
(2) and conversion zone (6) be separately provided for connection exhaust section ground (3) and conversion zone ground (4), the exhaust section
(2) more than the diameter of conversion zone (6).
3. biomass microwave according to claim 1 is pyrolyzed modified reactor assembly, it is characterised in that：The conversion zone
(6) and air inlet pipe (7) is integral type structure, the exhaust section (2) and blast pipe (1) are integral type mechanism.
4. biomass microwave according to claim 1 is pyrolyzed modified reactor assembly, it is characterised in that：Described air inlet
The axis of pipe (7) and blast pipe (2) is located in same horizontal line.
5. biomass microwave according to claim 1 is pyrolyzed modified reactor assembly, it is characterised in that：Described thermometric
Ground is provided with the mouth of pipe of pipe (5), air inlet pipe (7) and blast pipe (1).
6. biomass microwave according to claim 1 is pyrolyzed modified reactor assembly, it is characterised in that：Described microwave
Reaction casing includes the casing (9) and chamber door (8) that are connected by flange and bolt upper-lower seal, the air inlet pipe (7) and exhaust
Pipe (1) extends to the casing (9) left and right sides.
7. biomass microwave according to claim 6 is pyrolyzed modified reactor assembly, it is characterised in that：The casing
(9) left and right sides is respectively arranged with and leads to for the air inlet pipe (7) and the air inlet tube passage (14) that passes through of blast pipe (1) and blast pipe
Road, casing (9) middle part is extended thermometric tube passage (11), and chamber door (8) middle part is extended to be had and the survey
The temperature tube channel seal (10) of warm tube passage (11) sealing pressing.
8. biomass microwave according to claim 6 is pyrolyzed modified reactor assembly, it is characterised in that：Described casing
(9) gasket seal is provided with the junction of chamber door (8), the gasket seal inside is flexible heat-insulating pad (12), and outside is
Parcel mesh member (13).
9. biomass microwave according to claim 8 is pyrolyzed modified reactor assembly, it is characterised in that：The flexible guarantor
Temperature pad (12) piece uses rubbery asbestos gasket, and the parcel mesh member (13) is woven wire.
10. biomass microwave according to claim 1 is pyrolyzed modified reactor assembly, it is characterised in that：Described is each
Temperature tube (5) is respectively positioned in the vertically symmetrical plane of reactor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710075318.XA CN106753484B (en) | 2017-02-13 | 2017-02-13 | Improved reactor device for biomass microwave pyrolysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710075318.XA CN106753484B (en) | 2017-02-13 | 2017-02-13 | Improved reactor device for biomass microwave pyrolysis |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106753484A true CN106753484A (en) | 2017-05-31 |
| CN106753484B CN106753484B (en) | 2023-11-10 |
Family
ID=58955851
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710075318.XA Active CN106753484B (en) | 2017-02-13 | 2017-02-13 | Improved reactor device for biomass microwave pyrolysis |
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| Country | Link |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090064583A1 (en) * | 2005-04-01 | 2009-03-12 | Genova Ltd. | Method And Reactor For Biomass Pyrolytic Conversion |
| GB201013357D0 (en) * | 2009-08-10 | 2010-09-22 | Spectionz Ltd | Improvements in the production of wax products by the pyrolysis of plastics |
| CN102069086A (en) * | 2010-11-17 | 2011-05-25 | 山东大学 | Method for reclaiming and treating electronic waste |
| CN102513032A (en) * | 2011-11-20 | 2012-06-27 | 华中科技大学 | Quartz reactor of horizontal fixed bed |
| CN205687862U (en) * | 2016-05-25 | 2016-11-16 | 北京化工大学 | A kind of interior external heat, indirectly and directly add the moving bed pyrolysis system of thermal |
| CN206562403U (en) * | 2017-02-13 | 2017-10-17 | 华南理工大学 | A kind of biomass microwave is pyrolyzed modified reactor assembly |
-
2017
- 2017-02-13 CN CN201710075318.XA patent/CN106753484B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090064583A1 (en) * | 2005-04-01 | 2009-03-12 | Genova Ltd. | Method And Reactor For Biomass Pyrolytic Conversion |
| GB201013357D0 (en) * | 2009-08-10 | 2010-09-22 | Spectionz Ltd | Improvements in the production of wax products by the pyrolysis of plastics |
| CN102069086A (en) * | 2010-11-17 | 2011-05-25 | 山东大学 | Method for reclaiming and treating electronic waste |
| CN102513032A (en) * | 2011-11-20 | 2012-06-27 | 华中科技大学 | Quartz reactor of horizontal fixed bed |
| CN205687862U (en) * | 2016-05-25 | 2016-11-16 | 北京化工大学 | A kind of interior external heat, indirectly and directly add the moving bed pyrolysis system of thermal |
| CN206562403U (en) * | 2017-02-13 | 2017-10-17 | 华南理工大学 | A kind of biomass microwave is pyrolyzed modified reactor assembly |
Non-Patent Citations (1)
| Title |
|---|
| 黄河洵等: "微波破解污泥的固定床热解实验研究", 《华中科技大学学报（自然科学版）》 * |
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| CN106753484B (en) | 2023-11-10 |
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