The present invention relates to a reactor for the separation of material included in composite raw material, which reactor comprises at least one reaction chamber and at least one rotor, said reaction chamber comprising at least one housing that is sealed in relation to the surroundings and has at least one inlet opening and at least one outlet opening, and said rotor comprising at least one shaft.
U.S. Pat. No. 6,165,349 discloses a reactor comprising a reaction chamber having a rotation mechanism that consists of a shaft to which vanes are symmetrically attached by means of driving discs. The shaft is carried in bearings in both ends of the reaction chamber. An extensive dismounting work is required to release the vanes for service and possible replacement.
A first object of the present invention is to provide a reactor that, with a minimum of dismounting work, allows access to the rotor including occurring vanes for service and/or replacement. A second object of the present invention is to provide a reactor that, with a minimum of dismounting work, allows access to occurring wear surfaces in the reaction chamber/housing for service and/or replacement. Thus, the invention embraces a reactor for the separation of material included in composite raw material, which reactor comprises at least one reaction chamber and at least one rotor, said reaction chamber comprising at least one housing that is sealed in relation to the surroundings and has at least one inlet opening and at least one outlet opening, and said rotor comprising at least one shaft, wherein at least a first part of said rotor is situated in said housing, and said shaft extends in only one direction from said first part through and out of said housing.
At least one support device may act together on a part of said shaft situated outside said housing, alternatively on an additional shaft joined to this part, said support device entirely supporting the reactor. At least one support device may act together on a part of said shaft situated outside said housing, alternatively on an additional shaft joined to this part, said support device partly supporting the reactor. Said shaft may be carried in bearings in at least two planes that extend primarily perpendicular to a principal direction of extension of said shaft, and where said planes are situated outside said jacket. Said support device may comprise at least one stand. Said support device may comprise at least two bearings for the bearing mounting of said shaft in said planes. Said support device may comprise at least one bearing housing.
Said housing may have a primarily cylindrical shape. Said housing may have at least one dismountable part. Said dismountable part may be attached to a remainder of said housing by screw joints and/or bolt joints. Said dismountable part may be internally provided with wear-resistant material. Said housing may be sealed in such a way that exchange of gas between said reaction chamber and the surroundings is primarily prevented.
The remainder of said housing may be attached to at least one of said at least one bearing housing and be supported entirely by this/these. The remainder of said housing may be attached to at least one of said at least one bearing housing and be supported partly by this/these. The remainder of said housing may be attached to at least one of said at least two bearings and be supported entirely by this/these. The remainder of said housing may be attached to at least one of said at least two bearings and be supported partly by this/these. The remainder of said housing may be attached to at least one of said at least one stand and be supported entirely by this/these. The remainder of said housing may be attached to at least one of said at least one stand and be supported partly by this/these.
Said first part of said rotor may comprise at least one hammer. At least one of said hammers may comprise at least one fixed part and at least one articulated part. Said fixed part may be fixedly attached to said first part of said rotor and said articulated part may be articulately attached to said fixed part. Said articulated part may have a centre of gravity lying on a first radius of said rotor at the same time as an axis of rotation for rotation between said articulated part and said fixed part is lying on a second radius of said rotor, said first radius trailing said second radius upon rotation of said rotor in connection with operation of the reactor. Upon rotation of said rotor in connection with operation of the reactor, for each hammer in the direction of rotation, there may arise a force F2 that is proportional to
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In an analogous way, in a second end, the housing 6 connects to a bearing housing 10, the housing 6 as well as the bearing housing 10 being provided with a mating circumferential flange having a second diameter for a common bolt joint. The first diameter is greater than the second diameter. The bearing housing 10 is in turn supported by a stand 11 and accommodates two bearings 12 for the bearing mounting of the rotor shaft 5 where the same extends outside the reaction chamber 2, i.e., only on one side of the reaction chamber 2, the stand 11 accordingly supporting the entire reactor 1. In the housing 6, there is also a primarily cylindrical insert 13 of a wear-resistant material such as steel or ceramic material, which insert 13 is easily replaceable. In the housing 6, there is also an inner wall (not shown) that allows gas to pass through the centre of said wall into an inner/rear space (not shown) in the reaction chamber 2, from where the gas can continue out of the reactor through one of the mentioned outlet openings 9 and further to a possible distillation unit (not shown), or a condensation unit (not shown), or directly for combustion in an engine (not shown) or a heating system (not shown). The reaction chamber 2 is, apart from occurring inlet openings 8 and outlet openings 9, separated from the surroundings, i.e., the housing 6 with the lid 7 and occurring connection to said bearing housing 10 comprising occurring seal at shaft bushing of the rotor shaft 5 are in other respects to be considered as primarily gas-tight in relation to the surroundings. In this way, the reaction chamber 2 and the reactor 1 differ from usual hammer mills, which are more or less open toward the surroundings. The lid 7 can easily be dismounted when it is desired to check the state of the insert 13 and/or replace it, and/or when it is desired to check the state of the rotor 3 including the hammers 4.
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By the effective length I2 of the hammer, reference is made to a perpendicular distance between the force F2 and said axis of rotation 14. The force F2 attacks in the central point (the centre of mass) of the material accumulated on the hammer and which the force F2 should work against.
Thus, a desired power per hammer can be calculated and set by predetermining the parameters listed above. Occurring torque will hold each hammer in the predetermined place—against a stop for each hammer (not shown)—by the determined force F2, and if it is exceeded because of too much material being fed into the reactor or because of some heavier impurity having entered into the reactor, the articulated part 4b bends rearward and lets the material pass until equilibrium of forces arises again. This function provides a levelling effect during normal operation and protection against breakdown if, for instance, foreign items would accompany the material to be processed.
In use of the reactor, raw material is brought in through one or more of occurring inlet openings 8 into the reaction chamber 2 where it is decomposed by the kinetic energy of the hammers 4 of the rotor, as well as by the kinetic energy of particles that are thrown around by the rotary motion of the rotor, and by the heat energy that is created by friction between the hammers 4 and parts of the raw material. Inorganic material in the form of sand, catalysts, steel, glass, etc., may be used to increase the friction and thereby the temperature. The inorganic particles affect the decomposition process favourable by the fact that they have a large total contact surface that acts as an efficient heat exchanger against the raw material, as well as a catalyst for the breaking of hydrocarbon polymers and greater hydrocarbon molecules. Hydrocarbon compounds, water and other organic material are gasified in the device. The centrifugal forces created by the rotor separate the gas from the heavier inorganic materials, the gas part being brought out of the reactor in the centre thereof and the heavier particles can be tapped at the periphery of the reactor, and in both cases through occurring outlet openings 9.
The invention is not limited to the embodiments shown herein, but may be varied within the scope of the subsequent claims.
Number | Date | Country | Kind |
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0901600-7 | Dec 2009 | SE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/SE10/51452 | 12/21/2010 | WO | 00 | 8/28/2012 |