CA3068541A1 - Feed device and feed method for a pyrolysis apparatus - Google Patents

Feed device and feed method for a pyrolysis apparatus Download PDF

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Publication number
CA3068541A1
CA3068541A1 CA3068541A CA3068541A CA3068541A1 CA 3068541 A1 CA3068541 A1 CA 3068541A1 CA 3068541 A CA3068541 A CA 3068541A CA 3068541 A CA3068541 A CA 3068541A CA 3068541 A1 CA3068541 A1 CA 3068541A1
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Prior art keywords
feed
chamber
pyrolysis
processed
feed device
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CA3068541A
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French (fr)
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Tommi Pajala
Juhani Vanttinen
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ECOMATION Oy
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ECOMATION Oy
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B31/00Charging devices
    • C10B31/02Charging devices for charging vertically
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B31/00Charging devices
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/07Destructive 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/02Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10Production 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/20Apparatus; Plants
    • C10J3/30Fuel charging devices
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/50Fuel charging devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/442Waste feed arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00Feeding or distributing other fuel to combustion apparatus
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B7/00Coke ovens with mechanical conveying means for the raw material inside the oven
    • C10B7/06Coke ovens with mechanical conveying means for the raw material inside the oven with endless conveying devices
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1003Waste materials
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/15Details of feeding means
    • C10J2200/154Pushing devices, e.g. pistons
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/0946Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K2203/00Feeding arrangements
    • F23K2203/20Feeding/conveying devices

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 Al, and US2007029184 Al.
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
2 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
3 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.
4 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
5 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.
6 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 11, 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 11, in which case the feed opening 11 is open. In this case, the feed material 12 can be fed through the feed opening 11 into the
7 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 11 as presented in Figure 2.
As presented in Figure 2, the seal 16 of the gate valve in the feed opening 11 seals the gate valve 15 to the walls of the feed opening 11 so that the feed opening 11 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 11, 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
8 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 11, in which case the feed opening 11 is open again as presented in Figure 1. Thus, the feed material 12 can once again be fed through the feed opening 11 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.
9 LIST OF REFERENCE NUMBERS
Feed device 11 Feed opening 5 12 Feed material 14 Closing member Gate valve 16 Gate valve seal 17 Cylinder
10 18 Piston Feed chamber 21 Vacuum pump 22 Pipe 23 Valve 15 24 Sensor Discharge member 31 Push plate 32 Cylinder 33 Piston 20 40 Discharge chamber 41 Discharge opening 50 Emptying member 51 Closing plate 52 Cylinder 25 53 Piston 60 Pyrolysis apparatus 61 Pyrolysis chamber 62 Conveyor 63 Pipe

Claims (9)

10
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 or 2, 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 to 4, 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, c h a r a c t e r i s ed 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, ch ar acter is ed 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 to 6, c h a r a c t er i s e d 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).
CA3068541A 2017-06-28 2018-06-28 Feed device and feed method for a pyrolysis apparatus Abandoned CA3068541A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FI20170097 2017-06-28
FI20170097A FI20170097A (en) 2017-06-28 2017-06-28 Feeder for a pyrolysis apparatus
PCT/FI2018/000016 WO2019002661A1 (en) 2017-06-28 2018-06-28 Feed device of a pyrolysis apparatus and feeding method

Publications (1)

Publication Number Publication Date
CA3068541A1 true CA3068541A1 (en) 2019-01-03

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CA3068541A Abandoned CA3068541A1 (en) 2017-06-28 2018-06-28 Feed device and feed method for a pyrolysis apparatus

Country Status (5)

Country Link
US (1) US20200140760A1 (en)
EP (1) EP3645663A4 (en)
CA (1) CA3068541A1 (en)
FI (1) FI20170097A (en)
WO (1) WO2019002661A1 (en)

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5411714A (en) * 1992-04-06 1995-05-02 Wu; Arthur C. Thermal conversion pyrolysis reactor system
CA2282176A1 (en) * 1998-09-23 2000-03-23 Jose Manuel Lago Lucio Solid waste treatment plant
AU2012359291B2 (en) * 2011-12-20 2014-03-27 Vulcan Pyrotech Limited Continuous pyrolysis apparatus
CN202658130U (en) * 2012-03-31 2013-01-09 赵旭荣 Spiral charge pump for pyrolyzing household garbage and tire waste
AU2013307600B2 (en) * 2012-08-30 2017-12-21 Frank Riedewald Process and system for whole tyres and plastic composites pyrolysis to fuel conversion and compund recovery

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US20200140760A1 (en) 2020-05-07
WO2019002661A1 (en) 2019-01-03
EP3645663A4 (en) 2021-04-28
FI20170097A1 (en) 2018-12-29
EP3645663A1 (en) 2020-05-06
FI20170097A (en) 2018-12-29

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Effective date: 20231228