Protrusion type partition reactor
A reactor, raised technology, applied in the field of raised partitioned reactors, can solve problems affecting the service life of refractory bricks, refractory material ablation, single-nozzle gasifier capacity limitation, etc.
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Embodiment 1
[0057] Embodiment 1: Convex zone reactor of the present invention
[0058] The implementation mode of this embodiment is as follows:
[0059] The raised zone reactor of the present invention includes a reaction chamber 17 and a cooling chamber 20 . The reaction chamber 17 communicates with the cooling chamber 20 through the slag port 18, and the reaction chamber 17 and the cooling chamber 20 have a common central axis; the inner wall of the reaction chamber 17 is paved with a refractory lining 7 made of high-temperature refractory bricks.
[0060] The reaction chamber 17 is made up of a vertical reaction zone 14 and 2-12 lateral reaction zones 13, and the vertical reaction zone 14 and the side reaction zone 13 are all bell-shaped structures, and are all arranged on their tops for installing nozzles 16 nozzle mounting openings 15, the central axis of the installation nozzle 16 coincides with the corresponding reaction zone central axis; the side reaction zone 13 (i.e. the vert...
Embodiment 2
[0065] Embodiment 2: Raised type partition reactor of the present invention
[0066] The implementation of this embodiment is the same as that of Example 1, except that a lateral reaction zone 13 is arranged at the lower end of the vertical reaction zone 14, and the included angle α between the longitudinal axis of the vertical reaction zone 14 and the longitudinal axis of the lateral reaction zone 13 is 30°. The ratio of the length H1 of the vertical reaction zone 14 to the length H2 of the lateral reaction zone 13 is 1.0. The ratio of the height H1 of the vertical reaction zone 14 at the upper part of the reaction chamber 17 to the height H3 of the cylinder 10 at the lower part of the reaction chamber 17 is 0.2.
Embodiment 3
[0067] Embodiment 3: Raised type partition reactor of the present invention
[0068] The implementation of this embodiment is the same as that of Example 1, except that a lateral reaction zone 13 is arranged at the lower end of the vertical reaction zone 14, and the included angle α between the longitudinal axis of the vertical reaction zone 14 and the longitudinal axis of the lateral reaction zone 13 is 150°. The ratio of the length H1 of the vertical reaction zone 14 to the length H2 of the lateral reaction zone 13 is 2.4. The ratio of the height H1 of the vertical reaction zone 14 at the upper part of the reaction chamber 17 to the height H3 of the cylinder 10 at the lower part of the reaction chamber 17 is 3.0.
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