WO2019002661A1 - Feed device of a pyrolysis apparatus and feeding method - Google Patents
Feed device of a pyrolysis apparatus and feeding method Download PDFInfo
- Publication number
- WO2019002661A1 WO2019002661A1 PCT/FI2018/000016 FI2018000016W WO2019002661A1 WO 2019002661 A1 WO2019002661 A1 WO 2019002661A1 FI 2018000016 W FI2018000016 W FI 2018000016W WO 2019002661 A1 WO2019002661 A1 WO 2019002661A1
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- feed
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- pyrolysis
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- feed device
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- 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
- C10B31/00—Charging devices
- C10B31/02—Charging devices for charging vertically
-
- 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
- C10B31/00—Charging devices
-
- 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
-
- 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
- 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
- C10G1/02—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
-
- 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
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/30—Fuel charging devices
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/50—Fuel charging devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
-
- 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
- C10B7/06—Coke ovens with mechanical conveying means for the raw material inside the oven with endless conveying devices
-
- 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
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
- C10J2200/154—Pushing devices, e.g. pistons
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2203/00—Feeding arrangements
- F23K2203/20—Feeding/conveying devices
Definitions
- the object of the invention is a pyrolysis apparatus feed device and pyrolysis apparatus feed method according to the preamble to claim 1 .
- a pyrolysis apparatus is used for processing shredded waste material, such as plastic and/or rubber waste using pyrolysis.
- Pyrolysis i.e. dry distillation, is a chemical reaction wherein organic solids are decomposed by heating without allowing oxygen to influence the process.
- Pyrolysis usually uses either a vacuum, as is the case in vacuum pyrolysis, or an inert atmosphere, such as nitrogen, to supplant atmospheric oxygen.
- industrial pyrolysis reactions take place at temperatures of 300 to 700 °C.
- Known pyrolysis apparatuses have been presented in the publications DE102013003319 A1 , US2033730 and US2007029184 A1 .
- waste that contains hydrocarbons for example plastic and/or rubber waste
- plastic and/or rubber waste is shredded and the shredded material is placed in a pyrolysis chamber.
- the chamber is locked to make it air-tight with an air trap which is usually also the closing device for the feed opening for the material to be processed.
- This allows the feed material to be first fed into the feed chamber, which is equipped with closing members such as hatches or valves.
- closing members such as hatches or valves.
- Pyrolysis apparatuses In known pyrolysis apparatuses, however, air entering the closed chamber enters the reactor chamber along with the material fed into it, wherein the oxygen it contains can disrupt the reactor's production process. It is important in pyrolysis reactions that oxygen does not enter the reactor to induce combustion in the reactor because the carbon dioxide resulting from the combustion reduces the quality of the end product. Pyrolysis apparatuses also use feed devices which have a scraper conveyor or a screw conveyor in an inclined position, whose bottom part is placed in a liquid, such as oil, contained in a liquid basin. Thereby the liquid forms an air trap to prevent air from entering into the reactor. The material to be fed into the pyrolysis apparatus is conveyed into a bin which simultaneously forms a liquid basin.
- the scraper conveyor placed in an inclined position lifts the material out of the liquid contained in the bin. From the top end of the scraper conveyor, the material falls into the pyrolysis reactor.
- the problem with an oil-filled screw conveyor is, however, that the oil in the feed device is conveyed into the pyrolysis apparatus together with the feed material.
- the transfer of oil can be reduced using the grooves in the inclined surface of the scraper conveyor, along which oil can flow back into the liquid basin.
- a common problem in known feed devices is also that the particles fed into the pyrolysis apparatus must be crushed into small enough pieces.
- the size of the feed particles in commonly used feed devices must usually be less than 9 mm. If overly large particles accidentally remain among the feed particles, they can cause problems. First of all, large particles can block the feed device.
- An even greater disadvantage is, however, that the pores of the large particles retain air which contains oxygen that disrupts the production process of the pyrolysis reactor when it enters the reactor chamber.
- the purpose of this invention is to create a new pyrolysis feed device that overcomes the above-mentioned drawbacks.
- the pyrolysis apparatus feed device according to the invention is characterised in what has been presented in the characterising section of claim 1 .
- the pyrolysis apparatus feed device includes a feed chamber equipped with closing members, through which the crushed material such as plastic and/or rubber waste is conveyed into the pyrolysis chamber.
- a vacuum pump is also located in conjunction with the pyrolysis apparatus's feed chamber, through which a vacuum or sufficiently large underpressure can be achieved in the feed chamber. Using the vacuum pump, air and the oxygen it contains, which is harmful to the pyrolysis process, can be removed from the feed chamber. At the same time as a vacuum or sufficient underpressure is achieved in the feed chamber, also the air and the oxygen it contains can be sucked out of the pores of the particles fed into the feed chamber.
- the feed device's feed chamber and the size of its closing members can be dimensioned such that the size of the feed material does not cause any problems.
- the channel or conveyor leading from the feed chamber to the pyrolysis reactor can be dimensioned so that larger pieces than normal can be fed through them and the material moves without any problems to the pyrolysis device's pyrolysis chamber.
- the energy-consuming crushing phase can be entirely omitted in the pyrolysis apparatus according to the invention.
- the feed device according to the invention can be attached to any pyrolysis apparatus, in which case the efficient feed device makes the pyrolysis apparatus even more efficient.
- the feed device according to the invention can be located above the pyrolysis reactor, in which case the feed material falls directly from the feed device into the pyrolysis apparatus's pyrolysis chamber.
- the feed device can, however, also be below the pyrolysis reactor or at its side. In this case, the advantage is that the hot pyrolysis chamber does not heat the feed device. In a solution such as this, there is a gas-tight conveyor between the feed device and the pyrolysis reactor, which transfers the feed material from the feed device to the pyrolysis reactor.
- the hot steam from the pyrolysis chamber cannot rise into the feed device either.
- the material to be processed in the pyrolysis apparatus such as plastic and/or rubber waste, is fed into the pyrolysis apparatus's pyrolysis chamber using a feed device that has a feed opening for the material to be processed, a feed chamber, closing members in conjunction with the feed chamber, a vacuum pump for achieving a vacuum in the feed chamber and a discharge opening through which the material to be processed can be conveyed into the pyrolysis apparatus.
- a vacuum pump for achieving a vacuum or sufficient underpressure in the pyrolysis chamber.
- the feed device according to the invention can be made air-tight such that the feed chamber closing member in conjunction with the feed device's feed opening has a gate valve equipped with a seal.
- the second closing member may also include a closing plate that can be pressed tightly against the end of the feed chamber. In this case, when the closing plate of the feed device closing member is open, the feed chamber is connected to the feed device's discharge chamber.
- the feed device of the pyrolysis apparatus can be located above the pyrolysis apparatus's pyrolysis chamber, in which case the material to be processed can be dropped through the discharge opening into the pyrolysis chamber.
- a gas-tight conveyor has been attached to the feed device for transferring the feed material from the feed device to the pyrolysis chamber.
- the pyrolysis apparatus has a feed device with which the material to be processed in the pyrolysis apparatus, such as plastic and/or rubber waste, can be fed into the pyrolysis apparatus, in which feed device there is, for the material to be processed, a feed opening, a feed chamber, closing members in conjunction with the feed chamber and a discharge opening through which the material to be processed can be conveyed into the pyrolysis apparatus's pyrolysis chamber.
- feed device there is, for the material to be processed, a feed opening, a feed chamber, closing members in conjunction with the feed chamber and a discharge opening through which the material to be processed can be conveyed into the pyrolysis apparatus's pyrolysis chamber.
- a vacuum pump has been adjoined in conjunction with the feed device's feed chamber to achieve a vacuum or sufficient underpressure in the feed chamber after the material to be processed has been fed into the feed chamber and the feed chamber closing members 14, 50) have been closed.
- the vacuum pump is attached to the feed chamber with a pipe which has a valve and that a vacuum of sufficient underpressure is achieved in the feed chamber by starting up the vacuum pump and opening the valve.
- a sensor or a meter has been attached in conjunction with the feed chamber in order to measure the value of the vacuum or underpressure achieved by the vacuum pump in the feed chamber.
- the feed chamber's closing member in conjunction with the feed device's feed opening comprises a gate valve equipped with a seal and the second closing member of the feed chamber contains a closing plate that can be pressed tightly against the end of the feed chamber and that when the material to be processed has been fed into the feed chamber and both the gate valve and the closing plate are closed, a vacuum or sufficient underpressure can be achieved in the feed chamber using the vacuum pump.
- the feed chamber containing the material to be processed which has a vacuum or sufficient underpressure can be opened by opening the closing plate of the feed device's closing member, in which case the feed chamber connects with the feed device's discharge chamber and further with the pyrolysis apparatus's pyrolysis chamber.
- a discharge member is in conjunction with the feed device's feed chamber for transferring material from the feed chamber to the feed device's discharge chamber, from which the material is conveyed through the discharge chamber's discharge opening into the pyrolysis apparatus's pyrolysis chamber.
- the feed device of the pyrolysis apparatus is located above the pyrolysis apparatus's pyrolysis chamber, in which case the material to be processed can be dropped through the discharge opening into the pyrolysis chamber.
- the pyrolysis apparatus's feed device is located below the pyrolysis apparatus's pyrolysis chamber or at the side of the pyrolysis chamber, wherein a gas-tight conveyor has been attached to the feed device for transferring the feed material from the feed device to the pyrolysis chamber.
- the pyrolysis apparatus feed method is a method in which the material to be processed in the pyrolysis apparatus, such as plastic and/or rubber, is fed into the pyrolysis apparatus's feed device and onward into the pyrolysis chamber. According to the method, the material to be processed is first fed into the feed device's feed chamber, through the feed opening, after which the feed opening's closing member is closed, in which case both closing members of the feed chamber are closed. Thereafter, the closing member of the feed chamber's discharge opening is opened and the material to be processed is conveyed into the pyrolysis chamber.
- a vacuum or sufficient underpressure is created using the vacuum pump in the feed chamber into which the material to be processed has been fed and both of whose closing members are closed, such that air and the oxygen it contains, which is harmful to the pyrolysis process, are removed from the feed chamber and the material to be processed.
- the closing member of the feed chamber's discharge opening has been opened, the material to be processed, from which the oxygen harmful to the pyrolysis process has been removed, is conveyed into the pyrolysis chamber.
- Fig. 1 shows a pyrolysis apparatus feed device according to the invention in a
- Fig. 2 shows the feed device with the feed chamber closed.
- Fig. 3 shows the feed device with the emptying member opened.
- Fig. 4 shows the feed device in a material discharge situation.
- Fig. 5 shows the feed device according to the invention installed in a pyrolysis
- Fig. 6 shows the feed device installed in a pyrolysis apparatus under the pyrolysis chamber.
- FIG 1 shows a pyrolysis apparatus's feed device 10 according to the invention, which comprises a feed opening 1 1 , closing member 14, feed chamber 20, discharge member 30, discharge chamber 40, emptying member 50 and discharge opening 41 .
- the piston 18 of the closing member's 14 cylinder 17 has pulled the gate valve 15 to the right in Figure 1 , away from the feed opening 1 1 , in which case the feed opening 1 1 is open.
- the feed material 12 can be fed through the feed opening 1 1 into the feed device 10 in which the feed material 12 falls to the bottom of the feed chamber 20.
- the piston 18 of the closing member's 14 cylinder 17 pushes the gate valve 15 to the left in Figure 1 , whereby the gate valve 15 closes the feed opening 1 1 as presented in Figure 2.
- the seal 16 of the gate valve in the feed opening 1 1 seals the gate valve 15 to the walls of the feed opening 1 1 so that the feed opening 1 1 leading to the feed chamber 20 is closed tightly.
- the feed chamber 20 is in that case fully closed because, in addition to the feed opening 1 1 , also the left end of the feed chamber 20 is closed tightly with the emptying member's 50 closing plate 51 , which is pressed against the end of the feed chamber 20.
- the closing plate 51 can be equipped with a seal.
- the valve 23 of the pipe 22 leading to the vacuum pump 21 is opened in which case the vacuum pump 21 begins to suck.
- the creation of a vacuum in the feed chamber 20 is monitored using a sensor 24 or meter attached to the feed chamber 20.
- the creation of a vacuum can also be monitored using an automatic device.
- the feed chamber 20 is opened so that the piston 53 of the emptying member's 50 cylinder 52 pulls the closing plate 51 away from the end of the feed chamber 20.
- this pressure differential can impede the opening of the closing plate 51 . If a pressure differential such as this exists, the pressure differential can also be equalised such that, at the same time as the closing plate 51 is opened, the piston 33 of the discharge member's 30 cylinder 32 pushes the push plate 31 to the left in Figure 2.
- the feed chamber 20 can be opened entirely so that the closing plate 51 is moved to the position shown in Figure 3 to the left edge of the discharge chamber 40.
- the route from the feed chamber 20 to the discharge chamber 40 is open and the feed chamber 20 and discharge chamber 40 are connected to each other.
- the discharge chamber 40 is thus also connected to the pyrolysis apparatus's pyrolysis chamber.
- the piston 33 of the discharge member's 30 cylinder 32 pushes the push plate 31 in the manner shown in Figure 4 to the left, in which case the material 12 fed into the feed chamber 20 falls into the discharge opening 41 located in the discharge chamber 40. From the discharge opening 41 , the material is dropped into the pyrolysis apparatus's pyrolysis chamber if it is located under the discharge opening 41 . If it is not possible to drop the material into the pyrolysis chamber, at least one conveyor can be located between the feed device and pyrolysis chamber.
- FIG. 5 shows the feed device 10 according to the invention installed into the pyrolysis apparatus 60.
- the feed device 10 is above the pyrolysis apparatus 60 such that the feed material falls through the feed device's 10 discharge opening 41 into the pyrolysis chamber 61 of the pyrolysis apparatus 60.
- the pyrolysis apparatus 60 is not described in more detail because the feed device 10 according to the invention can be attached to all types of pyrolysis apparatuses 60.
- FIG. 6 shows the feed device 10 according to the invention installed in the pyrolysis apparatus 60 so that it is below the pyrolysis chamber 61 .
- a gas-tight conveyor 62 has been placed between the feed device 10 and pyrolysis chamber 61 .
- the conveyor 62 lifts the material dropped onto the conveyor through the feed device's 10 discharge opening 41 above the pyrolysis chamber 61 , from where the material falls into the pyrolysis chamber 61 through the pipe 63.
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- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
A feed device (10) of a pyrolysis apparatus (60) and a feed method through which material (12) processed in the pyrolysis apparatus, such as plastic and/or rubber waste, can be fed into the pyrolysis apparatus. In the feed device (10) there is a feed opening (1 1 ) for the material (12) to be processed, a feed chamber (20), closing members (14, 50) in conjunction with the feed chamber and a discharge opening (41 ), through which the material to be processed can be conveyed to the pyrolysis apparatus's pyrolysis chamber (61 ). A vacuum pump (21 ) has been adjoined in conjunction with the feed device's (10) feed chamber (20) to achieve a vacuum or sufficient underpressure in the feed chamber after the material (12) to be processed has been fed into the feed chamber (20) and the feed chamber's closing members (14, 50) have been closed. After the closing member (50) of the feed chamber's (20) discharge opening (41) has been opened, the material (12) to be processed, from which the oxygen harmful to the pyrolysis process has been removed, is conveyed into the pyrolysis chamber (61).
Description
FEED DEVICE AND FEED METHOD FOR A PYROLYSIS APPARATUS
The object of the invention is a pyrolysis apparatus feed device and pyrolysis apparatus feed method according to the preamble to claim 1 .
A pyrolysis apparatus is used for processing shredded waste material, such as plastic and/or rubber waste using pyrolysis. Pyrolysis, i.e. dry distillation, is a chemical reaction wherein organic solids are decomposed by heating without allowing oxygen to influence the process. Pyrolysis usually uses either a vacuum, as is the case in vacuum pyrolysis, or an inert atmosphere, such as nitrogen, to supplant atmospheric oxygen. As a general rule, industrial pyrolysis reactions take place at temperatures of 300 to 700 °C. Known pyrolysis apparatuses have been presented in the publications DE102013003319 A1 , US2033730 and US2007029184 A1 . In the pyrolysis apparatus, waste that contains hydrocarbons, for example plastic and/or rubber waste, is processed such that the process mainly produces oil, carbon and gas. According to a known method, plastic and/or rubber waste is shredded and the shredded material is placed in a pyrolysis chamber. The chamber is locked to make it air-tight with an air trap which is usually also the closing device for the feed opening for the material to be processed. This allows the feed material to be first fed into the feed chamber, which is equipped with closing members such as hatches or valves. When the material has been fed into the closed chamber, the feed hatch is closed. Then the hatch or valve leading to the reactor chamber is opened. This prevents outside air from freely entering the reactor chamber. In known pyrolysis apparatuses, however, air entering the closed chamber enters the reactor chamber along with the material fed into it, wherein the oxygen it contains can disrupt the reactor's production process. It is important in pyrolysis reactions that oxygen does not enter the reactor to induce combustion in the reactor because the carbon dioxide resulting from the combustion reduces the quality of the end product. Pyrolysis apparatuses also use feed devices which have a scraper conveyor or a screw conveyor in an inclined position, whose bottom part is placed in a liquid, such as oil, contained in a liquid basin. Thereby the liquid forms an air trap to prevent air from entering into the reactor. The material to be fed into the pyrolysis apparatus is conveyed into a bin which simultaneously forms a liquid basin. The scraper conveyor placed in an inclined position lifts the material out of the liquid contained in the bin. From the top end of the scraper conveyor, the material falls into the pyrolysis reactor. The problem with an oil-filled screw conveyor is, however, that the oil in the feed device is conveyed into the pyrolysis
apparatus together with the feed material. The transfer of oil can be reduced using the grooves in the inclined surface of the scraper conveyor, along which oil can flow back into the liquid basin. There can also be, attached to the scraper conveyor of the feed device, a timer which sequentially consecutively starts and stops the forward movement of the conveyor, such that the changes in the movement cause at least part of the liquid transported with the material to fall into the groove of the conveyor and flow back into the liquid contained in the feed bin.
A common problem in known feed devices is also that the particles fed into the pyrolysis apparatus must be crushed into small enough pieces. The size of the feed particles in commonly used feed devices must usually be less than 9 mm. If overly large particles accidentally remain among the feed particles, they can cause problems. First of all, large particles can block the feed device. An even greater disadvantage is, however, that the pores of the large particles retain air which contains oxygen that disrupts the production process of the pyrolysis reactor when it enters the reactor chamber.
In order to remove the air trapped in the particles' pores, attempts have been made to compress the particles. Normally, the particles are crushed as small as possible, however. Crushing the particles into small pieces can, however, be difficult, especially when the material in question is rubber. In any case, crushing consumes plenty of energy, which reduces the efficiency of the whole process.
The purpose of this invention is to create a new pyrolysis feed device that overcomes the above-mentioned drawbacks. The pyrolysis apparatus feed device according to the invention is characterised in what has been presented in the characterising section of claim 1 .
According to the invention, the pyrolysis apparatus feed device includes a feed chamber equipped with closing members, through which the crushed material such as plastic and/or rubber waste is conveyed into the pyrolysis chamber. According to the invention, a vacuum pump is also located in conjunction with the pyrolysis apparatus's feed chamber, through which a vacuum or sufficiently large underpressure can be achieved in the feed chamber. Using the vacuum pump, air and the oxygen it contains, which is harmful to the pyrolysis process, can be removed from the feed chamber. At the same time as a vacuum or sufficient underpressure is achieved in the feed chamber, also the air and the oxygen it contains can be sucked out of the pores of the particles fed into the feed chamber. Due to the vacuum or sufficiently large underpressure, there is no longer oxygen in the feed
chamber or the particles inside it, or at least there is so little oxygen that it does not have any significance for the pyrolysis reaction. After this, the feed chamber's closing member leading to the pyrolysis reactor is opened and the particles in the feed chamber are transferred to the pyrolysis reactor. Oxygen does not enter the pyrolysis reactor in connection with the transfer as there is none in the feed chamber or in the pores of the particles being transferred.
Because, as presented above, large particles of more than 9 mm can be fed into the pyrolysis reactor according to the invention, the feed device's feed chamber and the size of its closing members can be dimensioned such that the size of the feed material does not cause any problems. Thus, also the channel or conveyor leading from the feed chamber to the pyrolysis reactor can be dimensioned so that larger pieces than normal can be fed through them and the material moves without any problems to the pyrolysis device's pyrolysis chamber. As the feed particles do not need to be crushed as small as in known feed devices, i.e. no more than 9 mm in size, the energy-consuming crushing phase can be entirely omitted in the pyrolysis apparatus according to the invention.
As a vacuum or sufficient underpressure is achieved in the feed chamber according to the invention, also material that cannot be fed into known feed devices can be fed through the feed chamber into the pyrolysis reactor according to the invention. Materials such as this are floating and porous materials. These materials cannot be fed into the feed devices of known pyrolysis apparatuses but in a feed chamber according to the invention, the air and oxygen located in the pores of porous materials can be removed before the material is fed into the pyrolysis chamber.
The feed device according to the invention can be attached to any pyrolysis apparatus, in which case the efficient feed device makes the pyrolysis apparatus even more efficient. The feed device according to the invention can be located above the pyrolysis reactor, in which case the feed material falls directly from the feed device into the pyrolysis apparatus's pyrolysis chamber. The feed device can, however, also be below the pyrolysis reactor or at its side. In this case, the advantage is that the hot pyrolysis chamber does not heat the feed device. In a solution such as this, there is a gas-tight conveyor between the feed device and the pyrolysis reactor, which transfers the feed material from the feed device to the pyrolysis reactor. When the feed device is under the pyrolysis reactor, the hot steam from the pyrolysis chamber cannot rise into the feed device either.
According to the invention, the material to be processed in the pyrolysis apparatus, such as plastic and/or rubber waste, is fed into the pyrolysis apparatus's pyrolysis chamber using a feed device that has a feed opening for the material to be processed, a feed chamber, closing members in conjunction with the feed chamber, a vacuum pump for achieving a vacuum in the feed chamber and a discharge opening through which the material to be processed can be conveyed into the pyrolysis apparatus. There can also be, in conjunction with the pyrolysis apparatus's pyrolysis chamber, a vacuum pump for achieving a vacuum or sufficient underpressure in the pyrolysis chamber. The feed device according to the invention can be made air-tight such that the feed chamber closing member in conjunction with the feed device's feed opening has a gate valve equipped with a seal. The second closing member may also include a closing plate that can be pressed tightly against the end of the feed chamber. In this case, when the closing plate of the feed device closing member is open, the feed chamber is connected to the feed device's discharge chamber. According to the invention, there can be a discharge member in conjunction with the feed device's feed chamber for transferring material from the feed chamber to the feed device's discharge chamber, from which the material is conveyed through the discharge chamber's discharge opening into the pyrolysis apparatus's pyrolysis chamber.
The feed device of the pyrolysis apparatus can be located above the pyrolysis apparatus's pyrolysis chamber, in which case the material to be processed can be dropped through the discharge opening into the pyrolysis chamber. When the pyrolysis apparatus's feed device is located below the pyrolysis apparatus's pyrolysis chamber or at the side of the pyrolysis chamber, a gas-tight conveyor has been attached to the feed device for transferring the feed material from the feed device to the pyrolysis chamber.
According to the invention, the pyrolysis apparatus has a feed device with which the material to be processed in the pyrolysis apparatus, such as plastic and/or rubber waste, can be fed into the pyrolysis apparatus, in which feed device there is, for the material to be processed, a feed opening, a feed chamber, closing members in conjunction with the feed chamber and a discharge opening through which the material to be processed can be conveyed into the pyrolysis apparatus's pyrolysis chamber. A vacuum pump has been adjoined in conjunction with the feed device's feed chamber to achieve a vacuum or sufficient underpressure in the feed chamber after the material to be
processed has been fed into the feed chamber and the feed chamber closing members 14, 50) have been closed.
The vacuum pump is attached to the feed chamber with a pipe which has a valve and that a vacuum of sufficient underpressure is achieved in the feed chamber by starting up the vacuum pump and opening the valve.
A sensor or a meter has been attached in conjunction with the feed chamber in order to measure the value of the vacuum or underpressure achieved by the vacuum pump in the feed chamber.
The feed chamber's closing member in conjunction with the feed device's feed opening comprises a gate valve equipped with a seal and the second closing member of the feed chamber contains a closing plate that can be pressed tightly against the end of the feed chamber and that when the material to be processed has been fed into the feed chamber and both the gate valve and the closing plate are closed, a vacuum or sufficient underpressure can be achieved in the feed chamber using the vacuum pump.
The feed chamber containing the material to be processed which has a vacuum or sufficient underpressure can be opened by opening the closing plate of the feed device's closing member, in which case the feed chamber connects with the feed device's discharge chamber and further with the pyrolysis apparatus's pyrolysis chamber.
A discharge member is in conjunction with the feed device's feed chamber for transferring material from the feed chamber to the feed device's discharge chamber, from which the material is conveyed through the discharge chamber's discharge opening into the pyrolysis apparatus's pyrolysis chamber.
The feed device of the pyrolysis apparatus is located above the pyrolysis apparatus's pyrolysis chamber, in which case the material to be processed can be dropped through the discharge opening into the pyrolysis chamber.
The pyrolysis apparatus's feed device is located below the pyrolysis apparatus's pyrolysis chamber or at the side of the pyrolysis chamber, wherein a gas-tight conveyor has been attached to the feed device for transferring the feed material from the feed device to the pyrolysis chamber.
The pyrolysis apparatus feed method is a method in which the material to be processed in the pyrolysis apparatus, such as plastic and/or rubber, is fed into the pyrolysis apparatus's feed device and onward into the pyrolysis chamber. According to the method, the material to be processed is first fed into the feed device's feed chamber, through the feed opening, after which the feed opening's closing member is closed, in which case both closing members of the feed chamber are closed. Thereafter, the closing member of the feed chamber's discharge opening is opened and the material to be processed is conveyed into the pyrolysis chamber.
In the pyrolysis apparatus feed method, a vacuum or sufficient underpressure is created using the vacuum pump in the feed chamber into which the material to be processed has been fed and both of whose closing members are closed, such that air and the oxygen it contains, which is harmful to the pyrolysis process, are removed from the feed chamber and the material to be processed. After the closing member of the feed chamber's discharge opening has been opened, the material to be processed, from which the oxygen harmful to the pyrolysis process has been removed, is conveyed into the pyrolysis chamber.
In the following, the invention is described using examples with reference to the appended drawings, in which
Fig. 1 shows a pyrolysis apparatus feed device according to the invention in a
material feed situation.
Fig. 2 shows the feed device with the feed chamber closed.
Fig. 3 shows the feed device with the emptying member opened.
Fig. 4 shows the feed device in a material discharge situation.
Fig. 5 shows the feed device according to the invention installed in a pyrolysis
apparatus above the pyrolysis chamber.
Fig. 6 shows the feed device installed in a pyrolysis apparatus under the pyrolysis chamber.
Figure 1 shows a pyrolysis apparatus's feed device 10 according to the invention, which comprises a feed opening 1 1 , closing member 14, feed chamber 20, discharge member 30, discharge chamber 40, emptying member 50 and discharge opening 41 . In Figure 1 , the piston 18 of the closing member's 14 cylinder 17 has pulled the gate valve 15 to the right in Figure 1 , away from the feed opening 1 1 , in which case the feed opening 1 1 is open. In this case, the feed material 12 can be fed through the feed opening 1 1 into the
feed device 10 in which the feed material 12 falls to the bottom of the feed chamber 20. After this, the piston 18 of the closing member's 14 cylinder 17 pushes the gate valve 15 to the left in Figure 1 , whereby the gate valve 15 closes the feed opening 1 1 as presented in Figure 2.
As presented in Figure 2, the seal 16 of the gate valve in the feed opening 1 1 seals the gate valve 15 to the walls of the feed opening 1 1 so that the feed opening 1 1 leading to the feed chamber 20 is closed tightly. In Figure 2, the feed chamber 20 is in that case fully closed because, in addition to the feed opening 1 1 , also the left end of the feed chamber 20 is closed tightly with the emptying member's 50 closing plate 51 , which is pressed against the end of the feed chamber 20. To ensure tightness, the closing plate 51 can be equipped with a seal.
According to the method according to the invention, when the feed chamber 20 is closed, the valve 23 of the pipe 22 leading to the vacuum pump 21 is opened in which case the vacuum pump 21 begins to suck. The creation of a vacuum in the feed chamber 20 is monitored using a sensor 24 or meter attached to the feed chamber 20. The creation of a vacuum can also be monitored using an automatic device. When in the situation presented in Figure 2, the vacuum or underpressure in the feed chamber 20 has reached the required value, the feed chamber 20 is opened so that the piston 53 of the emptying member's 50 cylinder 52 pulls the closing plate 51 away from the end of the feed chamber 20. As before the opening of the closing plate 51 there is a vacuum or underpressure in the feed chamber 20 and there can be a different type of pressure in the discharge chamber 41 in conjunction with the pyrolysis chamber, this pressure differential can impede the opening of the closing plate 51 . If a pressure differential such as this exists, the pressure differential can also be equalised such that, at the same time as the closing plate 51 is opened, the piston 33 of the discharge member's 30 cylinder 32 pushes the push plate 31 to the left in Figure 2.
After this, the feed chamber 20 can be opened entirely so that the closing plate 51 is moved to the position shown in Figure 3 to the left edge of the discharge chamber 40. In this case, the route from the feed chamber 20 to the discharge chamber 40 is open and the feed chamber 20 and discharge chamber 40 are connected to each other. The
discharge chamber 40 is thus also connected to the pyrolysis apparatus's pyrolysis chamber.
After this, the piston 33 of the discharge member's 30 cylinder 32 pushes the push plate 31 in the manner shown in Figure 4 to the left, in which case the material 12 fed into the feed chamber 20 falls into the discharge opening 41 located in the discharge chamber 40. From the discharge opening 41 , the material is dropped into the pyrolysis apparatus's pyrolysis chamber if it is located under the discharge opening 41 . If it is not possible to drop the material into the pyrolysis chamber, at least one conveyor can be located between the feed device and pyrolysis chamber.
When the material 12 fed into the pyrolysis apparatus's feed device 10 has been transferred as presented above into the pyrolysis apparatus's pyrolysis chamber, the piston 33 of the discharge member's 30 cylinder 32 pulls the push plate 31 back to the right in Figure 4. Similarly, also the piston 53 of the emptying member's 50 cylinder 52 pushes the closing plate 51 against the end of the feed chamber 20, thus sealing the feed chamber 20. After this, the piston 18 of the closing member's 14 cylinder 17 pulls the gate valve 15 away from the feed opening 1 1 , in which case the feed opening 1 1 is open again as presented in Figure 1 . Thus, the feed material 12 can once again be fed through the feed opening 1 1 to the feed chamber 20 and the process described above begins again.
Figure 5 shows the feed device 10 according to the invention installed into the pyrolysis apparatus 60. In this case, the feed device 10 is above the pyrolysis apparatus 60 such that the feed material falls through the feed device's 10 discharge opening 41 into the pyrolysis chamber 61 of the pyrolysis apparatus 60. In Figure 5, the pyrolysis apparatus 60 is not described in more detail because the feed device 10 according to the invention can be attached to all types of pyrolysis apparatuses 60.
Figure 6 shows the feed device 10 according to the invention installed in the pyrolysis apparatus 60 so that it is below the pyrolysis chamber 61 . As the material to be fed into the pyrolysis apparatus 60 cannot be directly dropped into the pyrolysis chamber 61 in this solution, a gas-tight conveyor 62 has been placed between the feed device 10 and pyrolysis chamber 61 . The conveyor 62 lifts the material dropped onto the conveyor through the feed device's 10 discharge opening 41 above the pyrolysis chamber 61 , from where the material falls into the pyrolysis chamber 61 through the pipe 63.
LIST OF REFERENCE NUMBERS
10 Feed device
1 1 Feed opening
12 Feed material
14 Closing member
15 Gate valve
16 Gate valve seal
17 Cylinder
18 Piston
20 Feed chamber
21 Vacuum pump
22 Pipe
23 Valve
24 Sensor
30 Discharge member
31 Push plate
32 Cylinder
33 Piston
40 Discharge chamber
41 Discharge opening
50 Emptying member
51 Closing plate
52 Cylinder
53 Piston
60 Pyrolysis apparatus
61 Pyrolysis chamber
62 Conveyor
63 Pipe
Claims
1. A feed device (10) of a pyrolysis apparatus (60), through which material (12) to be processed in the pyrolysis apparatus, such as plastic and/or rubber waste, can be fed into the pyrolysis apparatus, in which feed device (10) there is a feed opening (11 ) for the material (12) to be processed, a feed chamber (20), closing members (14, 50) in conjunction with the feed chamber and a discharge opening (41), through which the material to be processed can be conveyed to the pyrolysis apparatus's pyrolysis chamber (61 ), characterised in that a vacuum pump (21 ) has been attached in conjunction with the feed device's (10) feed chamber (20) in order to achieve a vacuum or sufficient underpressure in the feed chamber after the material (12) to be processed has been fed into the feed chamber (20) and the feed chamber's closing members (14, 50) have been closed.
2. The feed chamber (10) according to claim 1, characterised in that the vacuum pump (21 ) is attached to the feed chamber (20) with a pipe (22) which has a valve (23) and that a vacuum or sufficient underpressure is achieved in the feed chamber (20) by starting up the vacuum pump (21) and opening the valve (23).
3. The feed chamber (10) according to claim 1 or2, characterised in that a sensor (24) or meter has been attached in conjunction with the feed chamber (20) in order to measure the value of the vacuum or underpressure that the vacuum pump (21 ) has created in the feed chamber (20).
4. The feed chamber (10) according to claim 1,2 or 3, characterised in that the feed chamber's (20) closing member (14) in conjunction with the feed device's (10) feed opening (11) comprises a gate valve (15) equipped with a seal (16) and the second closing member (50) of the feed chamber (20) contains a closing plate (51 ) that can be pressed tightly against the end of the feed chamber and that when the material (12) to be processed has been fed into the feed chamber (20) and both the gate valve (15) and the closing plate (51) are closed, a vacuum or sufficient underpressure can be achieved in the feed chamber (20) using the vacuum pump (21).
5. A feed device (10) according to any one of claims 1 to4, characterised in that the feed chamber (20) containing the material (12) to be processed which has a vacuum or sufficient underpressure can be opened by opening the closing plate (51) of the feed device's (10) closing member (50), in which case the feed chamber (20) is connected with
the feed device's discharge chamber (40) and further with the pyrolysis apparatus's pyrolysis chamber (61).
6. A feed device (10) according to any one of claims 1 to 5, characterised in that there is a discharge member (30) in conjunction with the feed device's (10) feed chamber (20) for the transfer of material (12) from the feed chamber to the discharge chamber (40) of the feed device, from where the material is conveyed through the discharge chamber's discharge opening (41) into the pyrolysis chamber (61) of the pyrolysis apparatus (60).
7. A feed device (10) according to any one of claims 1 to 6, characterised in that the pyrolysis apparatus's (60) feed device (10) is located above the pyrolysis apparatus's pyrolysis chamber (61) in which case the material (12) to be processed can be dropped through the discharge opening (41) into the pyrolysis chamber (61).
8. A feed device (10) according to any one of claims 1 to6, characterised in that the pyrolysis apparatus's (60) feed device (10) is located under the pyrolysis apparatus's pyrolysis chamber (61 ) or at the side of the pyrolysis chamber, in which case a gas-tight conveyor (62) has also been attached to the feed device for transporting the feed material (12) from the feed device to the pyrolysis chamber.
9. A feed method for feeding material (12) to be processed in a pyrolysis apparatus (60), such as plastic and/or rubber waste, into the pyrolysis apparatus's feed device (10) and onward into the pyrolysis chamber (61), according to which method
the material to be processed is first fed into the feed device's (10) feed chamber (20), through a feed opening (11)
the feed opening's (11) closing member (14) is closed in which case both closing members (14 and 50) of the feed chamber (20) are closed,
the closing member (50) of the feed chamber's (20) discharge opening (41 ) is opened and the material (12) to be processed is conveyed into the pyrolysis chamber (61), characterised in that
a vacuum or sufficient underpressure is achieved using the vacuum pump (21) in the feed chamber (20) into which the material (12) to be processed has been fed and both of whose closing members (14 and 50) are closed, such that air and the oxygen it contains, which is harmful to the pyrolysis process, are removed from the feed chamber (20) and the material (12) to be processed,
after which, when the closing member (50) of the feed chamber's (20) discharge opening (41) has been opened, the material (12) to be processed, from which the
oxygen harmful to the pyrolysis process has been removed, is conveyed into the pyrolysis chamber (61 ).
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP18823514.7A EP3645663A4 (en) | 2017-06-28 | 2018-06-28 | Feed device of a pyrolysis apparatus and feeding method |
CA3068541A CA3068541A1 (en) | 2017-06-28 | 2018-06-28 | Feed device and feed method for a pyrolysis apparatus |
US16/626,993 US20200140760A1 (en) | 2017-06-28 | 2018-06-28 | Feed device and feed method for a pyrolysis apparatus |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20170097A FI20170097A1 (en) | 2017-06-28 | 2017-06-28 | Feeder for a pyrolysis apparatus |
FI20170097 | 2017-06-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2019002661A1 true WO2019002661A1 (en) | 2019-01-03 |
Family
ID=64740431
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FI2018/000016 WO2019002661A1 (en) | 2017-06-28 | 2018-06-28 | Feed device of a pyrolysis apparatus and feeding method |
Country Status (5)
Country | Link |
---|---|
US (1) | US20200140760A1 (en) |
EP (1) | EP3645663A4 (en) |
CA (1) | CA3068541A1 (en) |
FI (1) | FI20170097A1 (en) |
WO (1) | WO2019002661A1 (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0992567A2 (en) * | 1998-09-23 | 2000-04-12 | Friu, S.A. | Solid waste treatment plant |
CN202658130U (en) * | 2012-03-31 | 2013-01-09 | 赵旭荣 | Spiral charge pump for pyrolyzing household garbage and tire waste |
WO2014032843A1 (en) * | 2012-08-30 | 2014-03-06 | Frank Riedewald | Process and system for whole tyres and plastic composites pyrolysis to fuel conversion and compund recovery |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5411714A (en) * | 1992-04-06 | 1995-05-02 | Wu; Arthur C. | Thermal conversion pyrolysis reactor system |
WO2013095163A1 (en) * | 2011-12-20 | 2013-06-27 | Vulcan Pyrotech Limited | Continuous pyrolysis apparatus |
-
2017
- 2017-06-28 FI FI20170097A patent/FI20170097A1/en not_active Application Discontinuation
-
2018
- 2018-06-28 CA CA3068541A patent/CA3068541A1/en not_active Abandoned
- 2018-06-28 WO PCT/FI2018/000016 patent/WO2019002661A1/en unknown
- 2018-06-28 US US16/626,993 patent/US20200140760A1/en not_active Abandoned
- 2018-06-28 EP EP18823514.7A patent/EP3645663A4/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0992567A2 (en) * | 1998-09-23 | 2000-04-12 | Friu, S.A. | Solid waste treatment plant |
CN202658130U (en) * | 2012-03-31 | 2013-01-09 | 赵旭荣 | Spiral charge pump for pyrolyzing household garbage and tire waste |
WO2014032843A1 (en) * | 2012-08-30 | 2014-03-06 | Frank Riedewald | Process and system for whole tyres and plastic composites pyrolysis to fuel conversion and compund recovery |
Non-Patent Citations (1)
Title |
---|
See also references of EP3645663A4 * |
Also Published As
Publication number | Publication date |
---|---|
US20200140760A1 (en) | 2020-05-07 |
CA3068541A1 (en) | 2019-01-03 |
FI20170097A (en) | 2018-12-29 |
EP3645663A1 (en) | 2020-05-06 |
FI20170097A1 (en) | 2018-12-29 |
EP3645663A4 (en) | 2021-04-28 |
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