A lignite drying device and method coupled with entrained flow bed and fluidized bed
A drying device and air-flow bed technology, which is applied in the directions of drying gas arrangement, drying solid materials, and heating to dry solid materials, etc., which can solve the problems that it is difficult to achieve sufficient drying of small particle materials, poor system safety performance, and low dehydration rate.
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Embodiment 1
[0038] This embodiment provides an entrained-fluidized-bed coupled lignite drying device 5, which includes: a fluidized-bed reactor and an entrained-bed reactor.
[0039] A first drying heat source inlet is provided at the middle and lower part of the fluidized bed reactor, and a large particle diameter coal discharge port is provided at the bottom;
[0040] The entrained-bed reactor is arranged in communication with the fluidized-bed reactor,
[0041] Located above the fluidized bed reactor and communicated with the fluidized bed reactor, the height ratio of the fluidized bed reactor and the entrained bed reactor is 1:20, and the transverse direction of the entrained bed reactor The sectional area is less than the cross-sectional area of the entrained bed reactor of the fluidized bed reactor and the diameter ratio of the fluidized bed reactor and the entrained bed reactor is 5:1; the upper part of the entrained bed reactor is provided with Wet coal feed port, the top is pr...
Embodiment 2
[0047] This embodiment provides a lignite drying device 5 coupled with an entrained flow bed-fluidized bed, such as figure 1 As shown, the setup includes: a cylindrical fluidized bed reactor and a cylindrical entrained entrained bed reactor.
[0048] A first drying heat source inlet is provided at the middle and lower part of the fluidized bed reactor, and a large particle diameter coal discharge port is provided at the bottom;
[0049] Located above the fluidized bed reactor and communicated with the fluidized bed reactor, the height ratio of the fluidized bed reactor and the entrained bed reactor is 1:10, and the transverse direction of the entrained bed reactor The sectional area is less than the cross-sectional area of the entrained bed reactor of the fluidized bed reactor and the diameter ratio of the fluidized bed reactor and the entrained bed reactor is 3:1; the upper part of the entrained bed reactor is provided with Wet coal inlet, the top is equipped with a small ...
Embodiment 3
[0056] This embodiment provides an entrained-fluidized bed coupled lignite drying device 5, which includes: a cylindrical fluidized bed reactor and a cylindrical entrained entrained bed reactor.
[0057] A first drying heat source inlet is provided at the middle and lower part of the fluidized bed reactor, and a large particle diameter coal discharge port is provided at the bottom;
[0058] Located above the fluidized bed reactor and communicated with the fluidized bed reactor, the height ratio of the fluidized bed reactor and the entrained bed reactor is 1:4, and the transverse direction of the entrained bed reactor The cross-sectional area is equal to the cross-sectional area of the fluidized bed reactor and the diameter ratio of the fluidized bed reactor and the entrained bed reactor is 1:1; the upper part of the entrained bed reactor is provided with a wet coal feed port, The top is equipped with a small particle size coal outlet, and the middle and lower part is equippe...
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