WO2007066782A1 - 廃プラスチック材の油化処理装置及び油化処理方法 - Google Patents
廃プラスチック材の油化処理装置及び油化処理方法 Download PDFInfo
- Publication number
- WO2007066782A1 WO2007066782A1 PCT/JP2006/324604 JP2006324604W WO2007066782A1 WO 2007066782 A1 WO2007066782 A1 WO 2007066782A1 JP 2006324604 W JP2006324604 W JP 2006324604W WO 2007066782 A1 WO2007066782 A1 WO 2007066782A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- waste plastic
- heating furnace
- oil
- granite
- heating
- Prior art date
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 66
- 229920003023 plastic Polymers 0.000 title claims abstract description 61
- 239000004033 plastic Substances 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 96
- 239000010438 granite Substances 0.000 claims description 54
- 239000000463 material Substances 0.000 claims description 52
- 238000000354 decomposition reaction Methods 0.000 claims description 15
- 239000002994 raw material Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000004575 stone Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 66
- 238000002474 experimental method Methods 0.000 description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 25
- 239000007789 gas Substances 0.000 description 24
- 238000001816 cooling Methods 0.000 description 18
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 14
- 239000003054 catalyst Substances 0.000 description 14
- 239000004568 cement Substances 0.000 description 12
- 239000007788 liquid Substances 0.000 description 12
- 230000002093 peripheral effect Effects 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 8
- 239000003925 fat Substances 0.000 description 8
- 239000010433 feldspar Substances 0.000 description 8
- 239000000498 cooling water Substances 0.000 description 7
- 229910052742 iron Inorganic materials 0.000 description 7
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 6
- 239000000919 ceramic Substances 0.000 description 6
- 239000011734 sodium Substances 0.000 description 6
- 229910052708 sodium Inorganic materials 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000000605 extraction Methods 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000000470 constituent Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000005979 thermal decomposition reaction Methods 0.000 description 3
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical group [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 150000001805 chlorine compounds Chemical class 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- IYDMICQAKLQHLA-UHFFFAOYSA-N 1-phenylnaphthalene Chemical compound C1=CC=CC=C1C1=CC=CC2=CC=CC=C12 IYDMICQAKLQHLA-UHFFFAOYSA-N 0.000 description 1
- 239000005711 Benzoic acid Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 208000033962 Fontaine progeroid syndrome Diseases 0.000 description 1
- 235000010650 Hyssopus officinalis Nutrition 0.000 description 1
- 240000001812 Hyssopus officinalis Species 0.000 description 1
- 241000269799 Perca fluviatilis Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052612 amphibole Inorganic materials 0.000 description 1
- 229910052626 biotite Inorganic materials 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical group 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical compound CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 description 1
- HQWKKEIVHQXCPI-UHFFFAOYSA-L disodium;phthalate Chemical compound [Na+].[Na+].[O-]C(=O)C1=CC=CC=C1C([O-])=O HQWKKEIVHQXCPI-UHFFFAOYSA-L 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000009970 fire resistant effect Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000012254 powdered material Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- RYYKJJJTJZKILX-UHFFFAOYSA-M sodium octadecanoate Chemical compound [Na+].CCCCCCCCCCCCCCCCCC([O-])=O RYYKJJJTJZKILX-UHFFFAOYSA-M 0.000 description 1
- XHFLOLLMZOTPSM-UHFFFAOYSA-M sodium;hydrogen carbonate;hydrate Chemical compound [OH-].[Na+].OC(O)=O XHFLOLLMZOTPSM-UHFFFAOYSA-M 0.000 description 1
- 230000008674 spewing Effects 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
- C08J11/12—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by dry-heat treatment only
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
- C08J11/16—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with inorganic 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
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
- C10B47/44—Other processes in ovens with mechanical conveying means with conveyor-screws
-
- 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
- C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
-
- 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
- C10B7/00—Coke ovens with mechanical conveying means for the raw material inside the oven
- C10B7/10—Coke ovens with mechanical conveying means for the raw material inside the oven with conveyor-screws
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Definitions
- the present invention relates to the plastic material division in which waste plastic material is put into heating and decomposed by heating to be converted into a material that can be reused. 550-800 under conventional circumstances with added plastic materials, and phthalnium stearin soda and other promoters. It is carried out by heating the waste plastic material at a high temperature such as C. Here, as a result of the heat, the polymer of the plastic material is cut, and the converted oil and fat is generated. Then, the fractions can be separated to obtain reusable oils and fats such as naphtha.
- the model is a heater for the peripheral wall.
- the heating unit is equipped with a heater that is covered by the heat insulation of the heater, a feeder that supplies the waste plastic material to the heating, and a vaporized gas that recovers the vaporized gas generated by the thermal decomposition of the supplied plastic material. It consists of recovering by thermal decomposition of the arastic material.
- Method (3) is a method of plastic treatment that includes the step of heating and decomposing a plastic material, and the method is characterized in that the above steps are carried out with the use of granite.
- (4 is a method for producing a component using a plastic material as a raw material, which comprises a step of heating and decomposing a plastic material, wherein the above step is carried out with a granite.
- (5) is a method for producing from a plastic material as a raw material, which comprises a step of heating and decomposing a plastic material, wherein the above step is carried out with granite.
- shadow stone is 65 to 70 if the dioxide is 65, quartz feldspar is the main component, and if there are more than one species, the mother and the flint. ) Is included.
- the plastic material can be decomposed in a shorter time and at a rate, which enables rapid waste disposal and also obtains industrially valuable decomposition (minutes, carbonization) at a rate. When it becomes possible, it plays a fruit.
- the decomposed products for example, when treated with 50 C, a large amount of styrene tylbenzene (such as styrene) and other useful components can be obtained as oil, and carbonization (as However, it is possible to obtain a large amount of a component that does not contain iron, for example, even if it is used as iron making it is a weak iron and can be used as an excellent copper.
- Is a side view of the processing device (the body is viewed from the side in the processing direction (from left to right inside).
- the 2 corresponds to a side view of the processing device (the body is viewed from the side in the processing direction).
- 3 corresponds to the right side view of the processing device (the body is viewed from the side in the processing direction).
- FIG. 4 is a processing device (the body is laid sideways from left to right in the processing direction (view).
- FIG. 5 is a cross-sectional view of the processing device ().
- FIG. 6 is a sectional view of the processing device ().
- FIG. 7 is a physical device (touch type) body.
- 8 is a view showing a partial structure of a processing device (touch type).
- 9 is a view showing a step structure of the present drawing device (touch type).
- Fig. 0 is a diagram showing a child in a physical device (challenge type) until the body is guided to a part when the body is cooled by heating and oxidizes. Good for carrying out Ming
- the treatment device is equipped with a heating granite that heats and decomposes the plastic material. Therefore, in the following, the body structure of the processing device will be first described, and the configuration related to the feature (() will be described below, and then the remaining components will be described.
- heating Walls to which "granite” has been applied e.g., as long as there is a heated granite, for example, granite (where X is the ceramic containing it is heated or in the furnace)
- it may be in the form of being covered with iron plates, or in the form of granite mixed in plastic.
- the processing equipment consists of a cylindrical heating along the processing direction, a fee to feed the waste plastic material into the heating, and a sodium-based contact inside the heating.
- the gas to be supplied 3 and the vaporized gas generated by decomposing the plastic material put into the heating by the heat treatment are emitted, and the vaporized gas 4 and the vaporized gas 4 are introduced to the cooling 5 described later. Cooling 5 that cools the vaporized gas that is generated in 4 and discharge that mainly consists of the elements that are generated in the heating.
- heating which is a characteristic component of Ming
- 0 which is formed in a cylindrical shape along the processing direction, and 0 is a front and back (side wall 1 that extends from the direction.
- a shadow stone m is formed in the part.
- the granite m is not particularly limited as long as it contains granite, and the granite itself is a panel), the granite-containing cerac, and the granite-cemente-water mixed cerac. (Nell), including granite can be exemplified. More specifically, a mode in which a panel made of natural granite stone is attached to the heating wall, and the crushed natural stone is used as cement and water to form a mortar-shaped heating wall. Aspect (, it is possible to cite that it is burned by heating by heating to form a stone, which is a ceramic body.
- the preferred embodiment is the granite, the aspect “R” containing the granite as a crushed piece having a size of pebble.
- the amount of time is much higher than that when the granite is present in (“Test” (“3”), and cracking of the ceramic panel is suppressed.
- an electrothermal heater is wound around the heating 0 (0), and the wound heater is insulated. Is further wound in a multi-layered manner.
- a step is adopted from the viewpoint of easy and reliable control, but It can be in any form (eg, using a combustion system in the implementation) as long as it can be set (or prescribed) each time.
- the feeder 2 is composed of 20 for inputting a plastic material, 22 for connecting 2 of the hopper 20, 22 for a screw-shaped cylinder inside the 22 and a motor M2 for driving the cylinder 23. It In addition, there are 24 connections for heating, which are connected to 5 of the heating (4) and introducing the plastic material. And the plastic material put into the hoo 20 is driven by the motor 2 The movement of the conveyor 23 by means of 22 directs it towards 22 (4). And the plastic material pressed to 22 is introduced into the heating from supply 5 through 24 connected to.
- the rotary valve-shaped reel 25 is provided with the plastic material.
- Per 30 and the medium put in the hot It consists of a fixed amount of a fixed amount 3 and a predetermined amount of induction 32.
- 32 is connected to the intermediate portion of the feeder 2 in the direction of 22.
- the vaporized gas 4 is then placed slightly behind the heating, as shown in 4. Also, as shown in 5, the vaporized gas 4 passes through heating 40, and In addition to being placed in the section, it is placed at an angle of 30 degrees with respect to the upper and lower X passing through the peripheral wall 0. As a result, the vaporized gas accumulated in the heating part, the vaporized gas vapor generated from the plastic material, and the cooling 5 described later are efficiently introduced.
- the cooling 5 stores an airtightly formed cooling box 50, a radiator-shaped heat exchanger 5 arranged in the cooling box 50, and cooling cooled by freezing, which circulates in the heat exchanger 5.
- the exchanger 5 described above is provided with 53, which receives the oil and fat content converted to by cooling, in a reed shape.
- 54 which discharges the contained oil and fat, is connected to 53, and is connected via Le V, and a recovery tank is further connected to that point.
- the steam generated from the water supplied into the heating was condensed from the steam that was introduced into the cooling box 50 through the vaporized gas 4 together with the vaporized gas (the solution of the alcohol and the reaction with the sodium system).
- the C generated in step 53 is also stored in the receiver 53 together with the above-mentioned liquefied oil and fat, and stays in the lower layer apart from that, and the water pipe 55 continued via V2 of 53. Pass it to the tank 2 connected to it, and let the mixture go out without separating it with the device.
- the recovery pin 62 is provided with an outlet 64 for cooling and discharging. Then, at this outlet 64, a yatta 65 that prevents the pin 62 from coming out is also installed at the opening / closing position. Further, when the yatter 65 is opened, a container 66 is provided at the outlet 64 for taking it out to the outside cooled and cooled.
- cut plastic material is put into the hopper 20.
- the plastic material that has been washed with water may be thrown in without being drained.
- feeder 3 contains plastic material.
- Nalium-based materials such as sodium oxide, sodium, etc.
- the degree of heating at which these plastic sodium-based materials are introduced is particularly limited. No (suitably upper limit.
- the degree is set below 500 C, for example, 50 to 400. Set to C.
- the processing device has a substantially rectangular shape 0, a burner 2 for heating the heating, and a burner 2 connected to the burner 2 and passing through the 0 part Heat transfer 03 and heat transfer 103 0 to prevent it from being introduced into the In order to cool and turn off the heat generated by the equipment (this is the cooling tank sent to the water pump, which will be described later, connected to the water pump 06, heating 07 installed under 07, and heating 0 degree control line. 09 and a frame 0 for storing them .. As described above, it may be configured to further include 08 for cooling 07 with a cooling gas.
- heat transfer 03 is arranged in U as expected. At this point, the energy from node 2 is introduced into the transmission 03. And the heat of combustion air is transferred through heat transfer 03.
- cooling stage As a result of being transferred into 0, heating 0 is heated. , By adjusting the baking in the oven 2 by the amount in the heating. Next, the structure of the cooling stage according to the present best mode will be described with reference to 9.
- 9 is a cross-sectional view at 0 minutes of heating. Cooling 2 with cooling pipes embedded inside is attached to the 0th and side surfaces. And, it adopts this 0, 2 double structure.
- the space into which the generated decomposition gas is introduced the space for constructing the gas is installed on the upper and right sides. And for the left and right, it is generated in the heating 0. Slip the introduced gas to the above
- the generated decomposition gas G is guided to the decomposition gas through the introduction stoke, and the decomposition gas G is cooled by contacting with Cooling 2 to be cooled. Then, as indicated by the mark ,, falls due to its own weight and is stored in the above-mentioned 07. , 07 is also the same. For this reason If the decomposed gas is released up to 07 without doing so, the same mechanism will be used in this case as well.
- n is the number of children until the body is led to nn when the body is cooled by heating 0 and is transformed.
- the cut steel material is placed on a steel plate at a predetermined position in heating 0, that is, transmission nR.
- the plastic material that has been washed with water may be put in after it has been drained.
- this plastic material decomposes the elemental compounds that are generated when the resin contained in the plastic material is decomposed.
- the degree of heating for introducing these natrium-based materials such as sodium oxide and natrium
- the introduction of these rustic-nalium-based materials suitable the upper limit is 500.
- the switch type oil treatment device shown in 6 and so on was used.
- the cut plastic material was mounted on an iron plate placed at heat transfer 03.
- a granite plate was mounted on an iron plate
- fire-resistant cement was applied on the iron plate
- a granite was mounted on the iron plate.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Sustainable Development (AREA)
- Polymers & Plastics (AREA)
- Medicinal Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Thermal Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Wood Science & Technology (AREA)
- Combustion & Propulsion (AREA)
- Environmental & Geological Engineering (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Coke Industry (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/085,016 US20080296205A1 (en) | 2005-12-06 | 2006-12-04 | Waste Plastic Liquefaction Plant and Waste Plastic Liquefaction Process |
JP2006554368A JP4519862B2 (ja) | 2005-12-06 | 2006-12-04 | 廃プラスチック材の油化処理装置及び油化処理方法 |
EP20060834359 EP1964876A1 (en) | 2005-12-06 | 2006-12-04 | Waste plastic liquefaction plant and waste plastic liquefaction process |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005-352597 | 2005-12-06 | ||
JP2005352597 | 2005-12-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007066782A1 true WO2007066782A1 (ja) | 2007-06-14 |
Family
ID=38122928
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2006/324604 WO2007066782A1 (ja) | 2005-12-06 | 2006-12-04 | 廃プラスチック材の油化処理装置及び油化処理方法 |
Country Status (7)
Country | Link |
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US (1) | US20080296205A1 (ja) |
EP (1) | EP1964876A1 (ja) |
JP (1) | JP4519862B2 (ja) |
KR (1) | KR20080087797A (ja) |
CN (1) | CN101321815A (ja) |
TW (1) | TW200728444A (ja) |
WO (1) | WO2007066782A1 (ja) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2945294B1 (fr) * | 2009-05-07 | 2012-04-20 | Olivier Lepez | Procede et installation de densification energetique d'un produit sous forme de solides divises, en vue de l'obtention d'huiles pyrolytiques a vocation energetique |
KR101237744B1 (ko) * | 2009-09-21 | 2013-02-28 | 한국화학연구원 | 보조용매를 이용한 스티렌모노머 회수장치 |
EP2766109A1 (fr) * | 2011-10-10 | 2014-08-20 | Lepez Conseils Finance Innovations-LCFI | Procede et installation de pyrolyse d'un produit sous forme de solides divises, en particulier des dechets polymeriques |
US20130327627A1 (en) * | 2012-06-12 | 2013-12-12 | Phillips 66 Company | Catalytic biomass pyrolysis in an auger reactor |
KR101626814B1 (ko) * | 2014-12-17 | 2016-06-03 | 주식회사 포스코 | 성형탄 및 성형탄 제조방법 |
CN105802653B (zh) * | 2014-12-30 | 2018-08-28 | 浙江大道环保科技有限公司 | 带干式氯气回收装置的卧式固定裂解装置 |
KR101664350B1 (ko) * | 2016-01-12 | 2016-10-11 | 박용일 | 폐기물용 유류 정제장치 |
US10814525B1 (en) | 2019-09-04 | 2020-10-27 | Valgroup S.A. | Continuous liquefaction and filtration system for waste plastic treatment |
KR102554309B1 (ko) * | 2020-11-06 | 2023-07-12 | 한국에너지기술연구원 | 열분해장치를 위한 투입장치 |
KR102482675B1 (ko) * | 2020-11-06 | 2023-01-02 | 한국에너지기술연구원 | 보조열원을 갖는 폐플라스틱 열분해 시스템 |
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2006
- 2006-12-04 JP JP2006554368A patent/JP4519862B2/ja not_active Expired - Fee Related
- 2006-12-04 KR KR20087014907A patent/KR20080087797A/ko not_active Application Discontinuation
- 2006-12-04 US US12/085,016 patent/US20080296205A1/en not_active Abandoned
- 2006-12-04 CN CNA2006800457504A patent/CN101321815A/zh active Pending
- 2006-12-04 WO PCT/JP2006/324604 patent/WO2007066782A1/ja active Application Filing
- 2006-12-04 EP EP20060834359 patent/EP1964876A1/en not_active Withdrawn
- 2006-12-04 TW TW095144958A patent/TW200728444A/zh unknown
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JPH09241658A (ja) * | 1996-03-08 | 1997-09-16 | Mitsui Petrochem Ind Ltd | 合成重合体の分解による油状物の製造方法 |
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Also Published As
Publication number | Publication date |
---|---|
KR20080087797A (ko) | 2008-10-01 |
EP1964876A1 (en) | 2008-09-03 |
JP4519862B2 (ja) | 2010-08-04 |
US20080296205A1 (en) | 2008-12-04 |
JPWO2007066782A1 (ja) | 2009-05-21 |
TW200728444A (en) | 2007-08-01 |
CN101321815A (zh) | 2008-12-10 |
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