CN105542830A - Double-spiral continuous cracking furnace - Google Patents
Double-spiral continuous cracking furnace Download PDFInfo
- Publication number
- CN105542830A CN105542830A CN201610063887.8A CN201610063887A CN105542830A CN 105542830 A CN105542830 A CN 105542830A CN 201610063887 A CN201610063887 A CN 201610063887A CN 105542830 A CN105542830 A CN 105542830A
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- China
- Prior art keywords
- heater
- tubular body
- stir shaft
- propelling
- pushing spiral
- Prior art date
- 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.)
- Pending
Links
- 238000005336 cracking Methods 0.000 title claims abstract description 38
- 238000003756 stirring Methods 0.000 claims abstract description 70
- 239000000463 material Substances 0.000 claims abstract description 53
- 238000010438 heat treatment Methods 0.000 claims abstract description 24
- 239000011229 interlayer Substances 0.000 claims description 7
- 230000003287 optical effect Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 15
- 230000008569 process Effects 0.000 abstract description 8
- 230000006872 improvement Effects 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 9
- 238000007599 discharging Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000009089 cytolysis Effects 0.000 description 2
- 238000013467 fragmentation Methods 0.000 description 2
- 238000006062 fragmentation reaction Methods 0.000 description 2
- 238000003780 insertion Methods 0.000 description 2
- 230000037431 insertion Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000013585 weight reducing agent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a double-spiral continuous cracking furnace, which comprises a tubular furnace body and two propelling stirring shafts, wherein the two propelling stirring shafts are in parallel arrangement; material pushing spiral blades are fixedly arranged on the propelling stirring shafts; the material pushing spiral blade of one propelling stirring shaft is inserted into a gap of the material pushing spiral blade of the other propelling stirring shaft; the material pushing spiral blades of the two propelling stirring shafts have opposite spiral directions; a plurality of stirring teeth are fixedly arranged on the material pushing surfaces of the material pushing spiral blades; a furnace body heating device is arranged outside the tubular furnace body. The material pushing spiral blades respectively push materials in respective propelling cavities to realize the mutual stirring moving; shorter and smaller materials are stirred by stirring teeth during the advancing; longer and larger materials are mutually torn and crushed by the stirring teeth; the materials are continuously stirred, torn and pushed when being heated in the tubular furnace body; the physical and chemical forms of the materials are continuously changed; the material cracking process is continuous, stable and thorough; the double-spiral continuous cracking furnace belongs to the breakthrough improvement on cracking equipment.
Description
Technical field
The present invention relates to a kind of cracking apparatus, particularly relate to a kind of can the stove of continuous cracking.
Background technology
In the treating processes of rubbish, a large amount of solid-state castoffs such as plastic waste, damaged tire etc. can be obtained, these wastes be treated as a large technical barrier, and normally used way carries out cracking, to produce splitting gas and cracking crude oil, realize the recycling of resource; The cracking apparatus of prior art, major part can not continuous seepage, needs blow-on, cools, slags tap, pan feeding, pass stove, heating pyrolyze, above-mentioned steps is repeated again after completing, this cracking process all needs cooling at every turn, and waste mass energy, lysis efficiency is extremely low.The continuous cracking equipment also had, its shortcoming is that material stirring is uneven, cracking is easily wrapped up by charcoal ash, and cracking is thorough, and lysis efficiency is not high equally.
Summary of the invention
Technical problem to be solved by this invention be to provide a kind of can continuously feeding discharging, material stirring fully, the duplex continuous cracking stove of continuous cracking in the traveling process of material.
For solving the problems of the technologies described above, technical scheme of the present invention is: duplex continuous cracking stove, comprises the tubular body of heater of arranged transversely, is provided with opening for feed above the front end of described tubular body of heater, be provided with discharge port below the tail end of described tubular body of heater, the top of described tubular body of heater is provided with air outlet; The inner chamber of described tubular body of heater is provided with two propelling stir shafts be arranged in parallel, described propelling stir shaft is fixed with pushing spiral blade, the described pushing spiral blade of stir shaft is advanced to be inserted in the gap of the described pushing spiral blade advancing stir shaft described in another described in one of them, advance the described pushing spiral blade rotation direction of stir shaft contrary described in two, described in two, advance the pusher of the described pushing spiral blade of stir shaft facing to described discharge port direction; The pusher face of described pushing spiral blade is fixed with multiple stirrer gear; Body of heater heating unit is provided with outside described tubular body of heater; Advance one end of stir shaft stretch out the outside of described tubular body of heater and be connected with drive unit described in two, described in two, advance the rotation direction of stir shaft contrary; The free end of stir shaft is advanced to be rotatably installed in the tail end of described tubular body of heater described in two.
As preferred technical scheme, the bottom of the cross section of the inner chamber of described tubular body of heater becomes " ω " shape, and the inner chamber top of described tubular body of heater is provided with air collecting chamber, and the top of described air collecting chamber is provided with described air outlet.
As the improvement to technique scheme, the chamber wall of " ω " shape inner chamber of described tubular body of heater is provided with the guide bar hindering material to rotate along the axial restraint of described propelling stir shaft.
As preferred technical scheme, the described propelling stir shaft being positioned at described discharge outlet is optical axis, and the described propelling stir shaft between the tail end of described tubular body of heater and described discharge port is provided with and is pushed into the counter of described discharge outlet pushes away screw-blade by counter for the material of the tail end of described tubular body of heater.
As preferred technical scheme, described air outlet is positioned at above the middle part of described tubular body of heater.
As preferred technical scheme, described drive unit comprises electric motor, and described electric motor is connected with wheel box, advances stir shaft described in described gearbox dynamic connection two.
As the improvement to technique scheme, described body of heater heating unit comprises the conduction oil interlayer being arranged on described tubular body of heater outside surface, and described conduction oil interlayer is connected with thermal oil circular heating furnace.
As the improvement to technique scheme, described body of heater heating unit comprises the electric heater unit being arranged on described tubular body of heater outside surface.
As the improvement to technique scheme, described body of heater heating unit comprises boiler, and described tubular body of heater is through the burner hearth of described boiler, and the two ends of described tubular body of heater are positioned at outside described boiler.
Owing to have employed technique scheme, duplex continuous cracking stove, comprises the tubular body of heater of arranged transversely, is provided with opening for feed above the front end of described tubular body of heater, is provided with discharge port below the tail end of described tubular body of heater, and the top of described tubular body of heater is provided with air outlet, the inner chamber of described tubular body of heater is provided with two propelling stir shafts be arranged in parallel, described propelling stir shaft is fixed with pushing spiral blade, the described pushing spiral blade of stir shaft is advanced to be inserted in the gap of the described pushing spiral blade advancing stir shaft described in another described in one of them, advance the described pushing spiral blade rotation direction of stir shaft contrary described in two, described in two, advance the pusher of the described pushing spiral blade of stir shaft facing to described discharge port direction, the pusher face of described pushing spiral blade is fixed with multiple stirrer gear, body of heater heating unit is provided with outside described tubular body of heater, advance one end of stir shaft stretch out the outside of described tubular body of heater and be connected with drive unit described in two, described in two, advance the rotation direction of stir shaft contrary, the free end of stir shaft is advanced to be rotatably installed in the tail end of described tubular body of heater described in two, during work, cracking material is treated from opening for feed feeding by sealed feeder unit, open described body of heater heating unit to heat described tubular body of heater, opening described drive unit and driving described in two advances stir shaft to rotate, material advances along described tubular body of heater inner chamber under the promotion of described pushing spiral blade, in the advance process of material, because pushing spiral blade described in two has mutual insertion portion and rotation direction is contrary, the material in each self-propelled chamber of pushing spiral blade is enable mutually to stir play, simultaneously due to stirrer gear that the pusher face of described pushing spiral blade is provided with, shorter less material is stirred by described stirrer gear while advance, longer larger material is torn fragmentation mutually by described stirrer gear, such material is constantly stirred while heating in described tubular body of heater, tear, advance, the physics and chemistry form of material constantly changes, until cracking is thorough, and on material progress path in described tubular body of heater, the physicochemical change that adjacent material carries out is comparatively close, the cracking process of material is continuous, steadily, thoroughly, it is the breakthrough improvement to cracking apparatus, there is great application value.
Accompanying drawing explanation
The following drawings is only intended to schematically illustrate the present invention and explain, not delimit the scope of the invention.Wherein:
Fig. 1 is the front view of the embodiment of the present invention;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is the structure principle chart of the embodiment of the present invention;
Fig. 4 is the partial enlarged drawing of Fig. 3 left end;
Fig. 5 is the cross-sectional view of this Fig. 1;
In figure: 1-tubular body of heater; 11-opening for feed; 12-discharge port; 13-air outlet; 14-air collecting chamber; 15-guide bar; 16-is counter pushes away screw-blade; 2-advances stir shaft; 21-pushing spiral blade; 22-stirrer gear; 3-electric motor; 31-wheel box; 4-conduction oil interlayer.
Embodiment
Describe in detail with reference to the accompanying drawings according to exemplary embodiment of the present invention.Here it is to be noted that it in the accompanying drawings, by identical Reference numeral imparting mechanism and the substantially identical integral part of function, and in order to make specification sheets more simple and clear, the redundancy eliminated about substantially the same integral part describes.
As shown in Figure 1, Figure 2 and Figure 3, duplex continuous cracking stove, comprises the tubular body of heater 1 of arranged transversely, opening for feed 11 is provided with above the front end of described tubular body of heater 1, during work, opening for feed 11 is connected with sealed feeder unit, and the structure formation of sealed feeder unit is varied, does not repeat them here; Be provided with discharge port 12 below the tail end of described tubular body of heater 1, during work, discharge port 12 is connected with sealed discharging device, and the structure formation of sealed discharging device is also varied, does not repeat them here; The top of described tubular body of heater 1 is provided with air outlet 13, and air outlet 13 connects condensing works, and for the separation to splitting gas, the isolation technique of cracked gas is prior art, also not within protection scope of the present invention, therefore no longer describes in detail; The inner chamber of described tubular body of heater 1 is provided with two propelling stir shafts 2 be arranged in parallel, described propelling stir shaft 2 is fixed with pushing spiral blade 21, the described pushing spiral blade 21 of stir shaft 2 is advanced to be inserted in the gap of the described pushing spiral blade 21 advancing stir shaft 2 described in another described in one of them, advance described pushing spiral blade 21 rotation direction of stir shaft 2 contrary described in two, described in two, advance the pusher of the described pushing spiral blade 21 of stir shaft 2 facing to described discharge port 12 direction; The pusher face of described pushing spiral blade 21 is fixed with multiple stirrer gear 22, and in the present embodiment, described stirrer gear 22 arranges in the shape of a spiral according to the spiral helicine pusher face of described pushing spiral blade 21, to improve the homogeneity and consistence that stir and tear; Body of heater heating unit is provided with outside described tubular body of heater 1; Advance one end of stir shaft 2 stretch out the outside of described tubular body of heater 1 and be connected with drive unit described in two, described in two, advance the rotation direction of stir shaft 2 contrary; The free end of stir shaft 2 is advanced to be rotatably installed in the tail end of described tubular body of heater 1 described in two.
As shown in Figure 5, the bottom of the cross section of the inner chamber of described tubular body of heater 1 becomes " ω " shape, and the inner chamber top of described tubular body of heater 1 is provided with air collecting chamber 14, and the top of described air collecting chamber 14 is provided with described air outlet 13.The chamber wall of " ω " shape inner chamber of described tubular body of heater 1 is provided with the guide bar 15 hindering material to rotate along the axial restraint of described propelling stir shaft 2.The setting of described guide bar 15, adds the frictional force of the surface of internal cavity of material and described tubular body of heater 1, decreases the rotation of material around described propelling stir shaft 2, is conducive to the advance of material.
As shown in Figure 4, be positioned at the described propelling stir shaft 2 at described discharge port 12 place for optical axis, the described propelling stir shaft 2 between the tail end of described tubular body of heater 1 and described discharge port 12 is provided with and is pushed into described the counter of discharge port 12 place pushes away screw-blade 16 by counter for the material of the tail end of described tubular body of heater 1.Material after cracking is pushed to described discharge port 12 place by the described pushing spiral blade 21 on described propelling stir shaft 2 and falls from described discharge port 12, partial material enters the tail end of described tubular body of heater 1, if do not taked technique means, very easily cause the inefficacy sealed between the free end of described propelling stir shaft 2 and described tubular body of heater 1, the described anti-setting pushing away screw-blade 16, push the material that part enters described tubular body of heater 1 tail end to described discharge port 12, then solve this technical barrier at all.
As shown in Figure 5, described air outlet 13 is positioned at above the middle part of described tubular body of heater 1.Fig. 1, Fig. 2 and Fig. 3 in the present embodiment, because comparatively long materials adopts omissive representation, therefore air outlet 13 described in figure not shown, Fig. 5 shows described air outlet 13.At described tubular body of heater 1 inner chamber, scission reaction is mainly carried out at middle part, and front end is the heat drying to material, and rear end forms the lime-ash such as carbon black, and therefore described air outlet 13 is arranged on above the middle part of described tubular body of heater 1, is more conducive to the collection of cracked gas.
Described drive unit comprises electric motor 3, and described electric motor 3 is connected with wheel box 31, advances stir shaft 2 described in described wheel box 31 power connection two.For saving material, weight reduction, the described propelling stir shaft 2 of the present embodiment is tubular shaft, and two ends are welded with solid spindle nose.Certainly, except electric motor, also other power form can be adopted, such as oil motor.
Described body of heater heating unit comprises the conduction oil interlayer being arranged on described tubular body of heater 1 outside surface, and described conduction oil interlayer is connected with thermal oil circular heating furnace.Thermal oil circular heating furnace is known technology, not shown, is also no longer described in detail at this.In prior art, the form of heating unit is varied, such as: described body of heater heating unit comprises the electric heater unit being arranged on described tubular body of heater 1 outside surface; Or described body of heater heating unit comprises boiler, described tubular body of heater 1 is through the burner hearth of described boiler, and the two ends of described tubular body of heater 1 are positioned at outside described boiler, and these two kinds of technical schemes are also within protection scope of the present invention.
During work, cracking material is treated from described opening for feed 11 feeding by sealed feeder unit, open described body of heater heating unit to heat described tubular body of heater 1, opening described drive unit and driving described in two advances stir shaft 2 to rotate backward, material advances along described tubular body of heater 1 inner chamber under the promotion of described pushing spiral blade 21, in the advance process of material, because pushing spiral blade 21 described in two has mutual insertion portion and rotation direction is contrary, the material in each self-propelled chamber of pushing spiral blade 21 is enable mutually to stir play, simultaneously due to stirrer gear 22 that the pusher face of described pushing spiral blade 21 is provided with, shorter less material is stirred by described stirrer gear 22 while advance, longer larger material is torn fragmentation mutually by described stirrer gear 22, such material is constantly stirred while heating in described tubular body of heater 1, tear, advance, the physics and chemistry form of material constantly changes, until cracking is thorough, and on material progress path in described tubular body of heater 1, the physicochemical change that adjacent material carries out is comparatively close, the cracking process of material is continuous, steadily, thoroughly, it is the breakthrough improvement to cracking apparatus, there is great application value.
As mentioned above, specifically describing embodiments of the invention, but the present invention is not limited thereto.It should be appreciated by those skilled in the art, various amendment, combination, sub-portfolio or replacement can be carried out according to design requirements or other factors, and they are in the scope of claims and equivalent thereof.
Claims (9)
1. duplex continuous cracking stove, is characterized in that: the tubular body of heater comprising arranged transversely, is provided with opening for feed above the front end of described tubular body of heater, is provided with discharge port below the tail end of described tubular body of heater, and the top of described tubular body of heater is provided with air outlet; The inner chamber of described tubular body of heater is provided with two propelling stir shafts be arranged in parallel, described propelling stir shaft is fixed with pushing spiral blade, the described pushing spiral blade of stir shaft is advanced to be inserted in the gap of the described pushing spiral blade advancing stir shaft described in another described in one of them, advance the described pushing spiral blade rotation direction of stir shaft contrary described in two, described in two, advance the pusher of the described pushing spiral blade of stir shaft facing to described discharge port direction; The pusher face of described pushing spiral blade is fixed with multiple stirrer gear; Body of heater heating unit is provided with outside described tubular body of heater; Advance one end of stir shaft stretch out the outside of described tubular body of heater and be connected with drive unit described in two, described in two, advance the rotation direction of stir shaft contrary; The free end of stir shaft is advanced to be rotatably installed in the tail end of described tubular body of heater described in two.
2. duplex continuous cracking stove as claimed in claim 1, is characterized in that: the bottom of the cross section of the inner chamber of described tubular body of heater becomes " ω " shape, and the inner chamber top of described tubular body of heater is provided with air collecting chamber, and the top of described air collecting chamber is provided with described air outlet.
3. duplex continuous cracking stove as claimed in claim 2, is characterized in that: the chamber wall of " ω " shape inner chamber of described tubular body of heater is provided with the guide bar hindering material to rotate along the axial restraint of described propelling stir shaft.
4. duplex continuous cracking stove as claimed in claim 1, it is characterized in that: the described propelling stir shaft being positioned at described discharge outlet is optical axis, the described propelling stir shaft between the tail end of described tubular body of heater and described discharge port is provided with and is pushed into the counter of described discharge outlet pushes away screw-blade by counter for the material of the tail end of described tubular body of heater.
5. duplex continuous cracking stove as claimed in claim 1, is characterized in that: described air outlet is positioned at above the middle part of described tubular body of heater.
6. duplex continuous cracking stove as claimed in claim 1, it is characterized in that: described drive unit comprises electric motor, described electric motor is connected with wheel box, advances stir shaft described in described gearbox dynamic connection two.
7. the duplex continuous cracking stove as described in claim as arbitrary in claim 1 to 6, is characterized in that: described body of heater heating unit comprises the conduction oil interlayer being arranged on described tubular body of heater outside surface, and described conduction oil interlayer is connected with thermal oil circular heating furnace.
8. the duplex continuous cracking stove as described in claim as arbitrary in claim 1 to 6, is characterized in that: described body of heater heating unit comprises the electric heater unit being arranged on described tubular body of heater outside surface.
9. the duplex continuous cracking stove as described in claim as arbitrary in claim 1 to 6, is characterized in that: described body of heater heating unit comprises boiler, and described tubular body of heater is through the burner hearth of described boiler, and the two ends of described tubular body of heater are positioned at outside described boiler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610063887.8A CN105542830A (en) | 2016-01-29 | 2016-01-29 | Double-spiral continuous cracking furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610063887.8A CN105542830A (en) | 2016-01-29 | 2016-01-29 | Double-spiral continuous cracking furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105542830A true CN105542830A (en) | 2016-05-04 |
Family
ID=55822401
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610063887.8A Pending CN105542830A (en) | 2016-01-29 | 2016-01-29 | Double-spiral continuous cracking furnace |
Country Status (1)
| Country | Link |
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| CN (1) | CN105542830A (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106623363A (en) * | 2016-12-24 | 2017-05-10 | 无锡明珠增压器制造有限公司 | Mixing device used for waste plastic |
| CN107033932A (en) * | 2017-05-25 | 2017-08-11 | 常熟市伟国环保成套设备有限公司 | A kind of multi-functional successively biaxial fluidized bed cracking stove for being used to handle urban waste |
| WO2017221180A1 (en) * | 2016-06-21 | 2017-12-28 | Golden Renewable Energy, LLC | Char separator and method |
| CN109185888A (en) * | 2018-06-26 | 2019-01-11 | 东营兴盛环保科技股份有限公司 | A kind of consumer waste incineration processing method preventing dioxin |
| US10233393B2 (en) | 2016-07-08 | 2019-03-19 | Golden Renewable Energy, LLC | Heated airlock feeder unit |
| CN109661452A (en) * | 2016-06-21 | 2019-04-19 | 戈登可再生能源有限公司 | Charcoal separator and method |
| CN109772562A (en) * | 2019-03-26 | 2019-05-21 | 广州至简通用设备制造有限公司 | A kind of feeding system |
| US10345048B2 (en) | 2016-05-12 | 2019-07-09 | Golden Renewable Energy, LLC | Cyclonic condensing and cooling system |
| US10436525B2 (en) | 2016-05-12 | 2019-10-08 | Golden Renewable Energy, LLC | Cyclonic cooling system |
| US10731082B2 (en) | 2016-07-05 | 2020-08-04 | Braven Environmental, Llc | System and process for converting waste plastic into fuel |
| US10961062B2 (en) | 2016-06-21 | 2021-03-30 | Golden Renewable Energy, LLC | Bag press feeder assembly |
| CN112662415A (en) * | 2019-10-15 | 2021-04-16 | 百亚巨能(厦门)环保科技有限公司 | Carbonization and tar recovery equipment |
| CN112662416A (en) * | 2019-10-15 | 2021-04-16 | 百亚巨能(厦门)环保科技有限公司 | Carbonization and tar recovery equipment |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080149471A1 (en) * | 2006-12-26 | 2008-06-26 | Nucor Corporation | Pyrolyzer furnace apparatus and method for operation thereof |
| CN201485276U (en) * | 2009-07-21 | 2010-05-26 | 徐浩 | Biomass carbon manufacturing device |
| CN104531227A (en) * | 2014-12-23 | 2015-04-22 | 华中科技大学 | Biomass double-shaft screw pyrolysis device |
-
2016
- 2016-01-29 CN CN201610063887.8A patent/CN105542830A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080149471A1 (en) * | 2006-12-26 | 2008-06-26 | Nucor Corporation | Pyrolyzer furnace apparatus and method for operation thereof |
| CN201485276U (en) * | 2009-07-21 | 2010-05-26 | 徐浩 | Biomass carbon manufacturing device |
| CN104531227A (en) * | 2014-12-23 | 2015-04-22 | 华中科技大学 | Biomass double-shaft screw pyrolysis device |
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10345048B2 (en) | 2016-05-12 | 2019-07-09 | Golden Renewable Energy, LLC | Cyclonic condensing and cooling system |
| US10436525B2 (en) | 2016-05-12 | 2019-10-08 | Golden Renewable Energy, LLC | Cyclonic cooling system |
| US10961062B2 (en) | 2016-06-21 | 2021-03-30 | Golden Renewable Energy, LLC | Bag press feeder assembly |
| CN109661452B (en) * | 2016-06-21 | 2021-05-11 | 戈登可再生能源有限公司 | Carbon separator and method |
| CN109661452A (en) * | 2016-06-21 | 2019-04-19 | 戈登可再生能源有限公司 | Charcoal separator and method |
| WO2017221180A1 (en) * | 2016-06-21 | 2017-12-28 | Golden Renewable Energy, LLC | Char separator and method |
| US11542434B2 (en) | 2016-06-21 | 2023-01-03 | Golden Renewable Energy, LLC | Char separator and method |
| US10544367B2 (en) | 2016-06-21 | 2020-01-28 | Golden Renewable Energy, LLC | Char separator and method |
| US10633595B2 (en) | 2016-06-21 | 2020-04-28 | Golden Renewable Energy, LLC | Char separator |
| US11773330B2 (en) | 2016-07-05 | 2023-10-03 | Braven Environmental, Llc | System and process for converting waste plastic into fuel |
| US10731082B2 (en) | 2016-07-05 | 2020-08-04 | Braven Environmental, Llc | System and process for converting waste plastic into fuel |
| US10233393B2 (en) | 2016-07-08 | 2019-03-19 | Golden Renewable Energy, LLC | Heated airlock feeder unit |
| CN106623363A (en) * | 2016-12-24 | 2017-05-10 | 无锡明珠增压器制造有限公司 | Mixing device used for waste plastic |
| CN107033932A (en) * | 2017-05-25 | 2017-08-11 | 常熟市伟国环保成套设备有限公司 | A kind of multi-functional successively biaxial fluidized bed cracking stove for being used to handle urban waste |
| CN109185888A (en) * | 2018-06-26 | 2019-01-11 | 东营兴盛环保科技股份有限公司 | A kind of consumer waste incineration processing method preventing dioxin |
| CN109772562A (en) * | 2019-03-26 | 2019-05-21 | 广州至简通用设备制造有限公司 | A kind of feeding system |
| CN112662415A (en) * | 2019-10-15 | 2021-04-16 | 百亚巨能(厦门)环保科技有限公司 | Carbonization and tar recovery equipment |
| CN112662416A (en) * | 2019-10-15 | 2021-04-16 | 百亚巨能(厦门)环保科技有限公司 | Carbonization and tar recovery equipment |
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Effective date of registration: 20171130 Address after: No. 71, Yangjia village, quyi street, Changyi, Shandong Applicant after: Liu Zhenliang Address before: 261300 Changyi City, Weifang Province, the United States and the United States and the streets of the office of Tatsu Tatsu Tatsu wire Applicant before: WEIFANG JINSIDA NEW ENERGY TECHNOLOGY CO., LTD. |
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Application publication date: 20160504 |