This is the national stage of International Application PCT/EA2017/000001, filed Jan. 25, 2017.
The invention relates to power generation and the environment and is intended for the thermal processing of solid and free-flowing materials, in particular in processes for the pyrolysis of solid carbon-containing materials, including municipal and domestic waste. The apparatus can also be used for activation of carbon materials, calcination, drying and in other operational procedures associated with heating in a controlled environment.
A method of thermal decomposition of fuels [1] is known in the prior art, in which furnace walls are made of flameless gas burners. Fuel enters the upper part of the furnace and, while descending, is directly exposed to infrared rays, which enables intensification of the process. The disadvantage of the method is that radiant heat cannot be transferred to the entire depth of the product layer.
Another prior art discloses an assembly for thermal decomposition of carbon-containing materials [2]. The assembly comprises a rotating drum with a retort installed axisymmetrically therein; pyrolysis gases are burned in an annular space between the retort and walls of the drum, whereby external radiating/conductive heating of the retort is provided.
The disadvantage of the known invention is the uneven heating of the retort and the drum.
The prior art most closely related to the present invention by its technical nature is an externally heated pyrolysis furnace for carbonization and activation of carbon material [3], comprising a hollow rotating body having an inlet and a discharging side and mounted with a downward tilt towards the discharging side; a housing surrounding the body and defining, together with the body, a plurality of heating chambers; gas burners in each heating chamber, wherein the temperature of each chamber is independently adjustable; annular partitions spaced apart along the rotating body to control the movement of material through the body; means for supplying carbonaceous material to the charging end; a feed pipe for supplying substantially oxygen-free vapour or carbon dioxide into the rotating body.
The pyrolysis furnace is insufficiently reliable and safe due to the use of flame gas burners and the potential for overheating the rotating body at elevated temperature of the gas burner torch, as well as the insufficient intensity of heat exchange and a certain complexity of maintenance.
The object of the present invention is to provide an externally heated drum-type pyrolysis furnace for processing solid carbon-containing materials, which exhibits enhanced reliability, safety, heat transfer efficiency and improved maintainability.
The object is attained in an externally heated pyrolysis furnace for processing solid carbon-containing materials, comprising a base 1; a pyrolysis chamber 2 disposed on said base and being in the shape of a cylinder with end covers 3, which are connected to a charging tube 4 and a discharging tube 5; a heating chamber 6, which surrounds the pyrolysis chamber 2 and includes a thermally-insulated housing 7 having disposed therein heating elements 8 and 9, partitions 10, 11, 12 and a branch pipe 13 for the removal of flue gases, which is situated in the upper part of the heating chamber 6; a feed pipe 14 for supplying an atmosphere of water vapour or carbon dioxide to the pyrolysis chamber 2; and a pipe 15 for the removal of gaseous products from the pyrolysis chamber 2. The heating chamber 6 is assembled from an upper part and a lower part, which can be joined; each of the parts of the heating chamber 6 is provided with two rows of heating elements 8, 9, which are arranged along the length of the housing 7 of the heating chamber 6 symmetrically relative to a vertical plane which passes through the axis of the pyrolysis chamber 2. The heating elements 8, 9 are in the form of units containing at least one flameless gas burner, wherein the heating elements 8 in the upper part of the heating chamber 6 are arranged in a checkerboard fashion relative to the heating elements 9 in the lower part of the heating chamber 6. The partitions 10, 11, 12 comprise: two end annular partitions 10 disposed on the edges of the heating chamber 6; a partition 11 disposed along the lower part of the heating chamber 6; annular partitions 12 defining pairwise separate gas channels 16 for each heating element 8, 9 for exhaust gas streams leaving them. The branch pipe 13 for the removal of flue gases is provided with a heat exchanger 17, to which the feed pipe 14 is connected for supplying an atmosphere of water vapour or carbon dioxide to the pyrolysis chamber 2.
Alternatively to the first embodiment, in the second embodiment the partitions comprise: two end annular partitions 10 disposed on the edges of the heating chamber 6; a partition disposed along the lower part of the heating chamber 6; screening partitions 18 in the upper part of the heating chamber 6 for directing the exhaust gas stream from the heating element 8 upward the heating chamber 6 and restricting the influence of the heating elements 9 of the lower part of the heating chamber 6 on them; and screening partitions 19 in the lower part of the heating chamber 6 for restricting lateral movement of the exhaust gas stream from the heating elements 9 and the mutual influence thereof.
Furthermore, in the preferred second embodiment the screening partitions 18 consist of two side parts made in the form of a ring segment and disposed on both sides of each heating element 8, the side parts being coupled by a splitter directed toward the heating elements 9. The screening partitions 19 also made in the form of a ring segment.
In both embodiments the pyrolysis chamber 2 can be a drum-type or screw-type chamber.
In both embodiments the heat exchanger 17 is preferably coil-shaped, and the pyrolysis chamber 2 is provided with pressure and temperature sensors.
Use of the present invention offers the following technical advantages.
1. The use of flameless gas burners as heating elements eliminates potential overheating of the pyrolysis chamber walls when gas is burned in them owing to the absence of open flame and exposure of the walls to high temperature effects, whereby reliability and safety are enhanced.
2. The arrangement of heating elements in a checkerboard fashion provides even distribution of radiation fluxes and exhaust gas streams from the heating elements over the outer surface of the pyrolysis chamber, and the present options of arrangement of partitions in the heating chamber housing can organize movement of flue gases from operating heating elements such that they would not influence each other and impair their performance, and the high-temperature combustion products (flue gases) would not go beyond the heating chamber through its end surfaces, while evenly flowing around the pyrolysis chamber surface with maximum contact area. Such an optimal combination of radiant heating (by radiation) and convective heating (by contact with flue gases) of the pyrolysis chamber in the present heating chamber design significantly intensifies the heat exchange between the heating chamber and the pyrolysis chamber compared to heating only by flue gases when flame gas burners are used.
3. The assembly of the heating chamber from upper and lower parts, which can be joined, enhances maintainability owing to the fact that maintenance and replacement of the pyrolysis chamber can be organized with the upper part of the heating chamber removed.
The invention is illustrated in the drawings.
An externally heated pyrolysis furnace for processing solid carbon-containing materials (
The invention is presented in two embodiments. According to a first embodiment, the partitions comprise: two end annular partitions 10 (
The second embodiment also comprises two end annular partitions 10 (
In both embodiments the pyrolysis chamber 2 can be a drum-type or screw-type chamber.
If a drum-type pyrolysis chamber 2 is used, the end covers 3 are provided with end seals (not shown) to ensure immobility of the covers 3 when the drum-type pyrolysis chamber 2 is rotating.
The pyrolysis chamber 2 can be provided with pressure and temperature sensors (not shown).
The externally heated pyrolysis furnace according to the invention can use an automation system.
The externally heated pyrolysis furnace according to the first embodiment operates as follows.
Carbon dioxide is fed, via the feed pipe 14, into the pyrolysis chamber 2, and the pyrolysis chamber 2 is purged to displace residual air. Combustion gas is then supplied to the heating elements 9 and they are ignited. The pyrolysis chamber 2 is exposed to thermal radiation from the heating elements 9, and owing to convection the heat of flue gases resulting from operation of the heating elements, which, being pushed away from the partition 11 dividing the internal space of the heating chamber 6 into two symmetrical parts, move upward through the gas channels 16 defined by the annular partitions 12 and outward from the heating chamber 6 through the branch pipe 13, while flowing around the outer surface of the pyrolysis chamber 2 from both sides relative to the vertical plane in which the partition 11 is disposed. Combustion gas is fed to the heating elements 8 and they are ignited. The intensity of heating the pyrolysis chamber 2 increases due to the additional effect of thermal radiation from the heating elements 8 and also due to convective heat transfer from the flue gases resulting from operation of the heating elements; these flue gases are carried away by the exhaust gas streams from the heating elements 9, move upward and outward from the heating chamber 6 via the branch pipe 13; therewith, the uniformity of heating the surface of the pyrolysis chamber 2 is improved due to the checkerboard arrangement of the heating elements 8 and 9. Flue gases resulting from the operation of the heating elements 8 and 9 leave the heating chamber 6 through the branch pipe 13, while flowing around the heat exchanger 17 and heating the same by convention. Water vapour or carbon dioxide, heated in the heat exchanger 17, is supplied through the feed pipe 14 into the pyrolysis chamber 2 to provide protective atmosphere therein. Pre-ground solid carbon-containing material is supplied via the charging tube 4 into the heated pyrolysis chamber 2, where it contacts the inner surface of the pyrolysis chamber 2, having high temperature owing to the heat transfer from the heating elements 8 and 9 and flue gases exhaust from them, and the pyrolysis process takes place. Pyrolysis gas entering the pipe is withdrawn outward from the pyrolysis chamber 2; solid residue resulting from the decomposition of the solid carbon-containing material after release of pyrolysis gas is also withdrawn outward from the pyrolysis chamber 2 through the discharging tube 5.
Operation of the externally heated pyrolysis furnace according to the second embodiment is different from that according to the first embodiment in that the flue gases resulting from operation of the heating elements 9, pushed away from the partition 11, move upward the heating chamber 6, while the screening partitions 19 restrict lateral movement of the exhaust gas streams from adjacent heating elements 9 and mutual influence of the heating elements 9. Then the exhaust gas flows around the outer surface of the pyrolysis chamber 2 from both sides relative to the vertical plane, in which the partition 11 is disposed, flows around outer sides of the screening partitions 18 and leave the heating clamber 6 via the branch pipe 13, while flowing around the heat exchanger 17 and heating the same by convention.
Flue gases resulting from operation of the heating elements 8, pushed away from the screening partitions 18, move upward the heating chamber 6, mix with the exhaust gas stream from the heating elements 9 and leave the heating chamber 6 via the branch pipe 13, while flowing around the heat exchanger 17 and also heating the same by convention. Therewith, the partitions 18 cut the flue gases resulting from operation of the heating elements 9 and rising up to the output branch pipe 13 and do not adversely affect ignition and performance of the heating elements 9.
Number | Date | Country | Kind |
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201600392 | Apr 2016 | EA | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EA2017/000001 | 1/25/2017 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2017/186253 | 11/2/2017 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
8366882 | Rinker | Feb 2013 | B2 |
8470134 | Rinker | Jun 2013 | B2 |
20110136971 | Tucker | Jun 2011 | A1 |
20120161451 | Struble | Jun 2012 | A1 |
20130004409 | Tucker | Jan 2013 | A1 |
Number | Date | Country | |
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20190137181 A1 | May 2019 | US |