Reforming hydrogen production reactor, reforming hydrogen production reformer and reforming hydrogen production reaction method
A reforming hydrogen production and reactor technology, applied in chemical instruments and methods, hydrogen, inorganic chemistry, etc., can solve the problems of increasing the energy consumption of raw gas compressors, increasing the number of active centers of catalysts, and easily deactivating catalysts due to carbon deposition , to achieve the effects of total reduction, long service life, and not easy to deactivate due to carbon deposition
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Embodiment 1
[0083] like figure 1 , figure 2 As shown, the reforming hydrogen production reactor used in this embodiment includes a pressure-bearing shell 12 with a first straight pipe 11 at the upper end and a second straight pipe 14 at the lower end, and four sleeves 15 are arranged inside the shell. (not all shown in the figure) and a radial catalytic reaction zone formed by a central cylinder 13, the upper part of the first straight pipe 11 is provided with an air inlet 1, and the lower part of the second straight pipe 14 is provided with an air outlet 2. The catalytic reaction zone is composed of a flat micro-catalytic reaction plate 10, the angle between the micro-catalytic reaction plate 10 and the horizontal direction is 90°, and the micro-catalytic reaction plates 10 are radially and evenly distributed around the central tube or the central tube respectively, the central tube 6, the central tube 13 , the sleeve 15 and the housing 12 are coaxially arranged; the micro-catalysis re...
Embodiment 2
[0094] like figure 1 , image 3 , Figure 9 As shown, the reforming hydrogen production reactor and the reforming furnace of the present embodiment are the same as the reactor size of Example 1, the distance between two adjacent micro-catalysis reaction plates, the distance between the ring gaps, the matrix material and the active group per unit area of the micro-catalysis reaction plates The NiO loading parameters are the same. The difference from Example 1 is that the micro-catalytic reaction plate in this example is a toothed micro-reaction plate, and the wave direction is along the axial direction of the reactor. For the toothed plate, the distance between the crest and the trough is 4mm, and the distance between two adjacent crests or adjacent troughs of the same microplate is 6.5mm. The reforming hydrogen production reactor and reformer of this embodiment are applied to the hydrogen production reaction by steam reforming of natural gas. The hydrogen production proc...
Embodiment 3
[0099] like figure 1 , Figure 4 , Figure 11 As shown, the reforming hydrogen production reactor and the reforming furnace of the present embodiment are the same as the reactor size of Example 1, the distance between two adjacent micro-catalysis reaction plates, the distance between the ring gaps, the matrix material and the active group per unit area of the micro-catalysis reaction plates The NiO loading parameters are the same. The difference from Example 1 is that the micro-catalytic reaction plate in this example is a corrugated micro-reaction plate, and the wave direction is along the axial direction of the reactor. For the corrugated plate, the distance between the crest and the trough is 4mm, and the distance between two adjacent crests or adjacent troughs of the same micro-catalytic reaction plate is 6.5mm.
[0100] The reforming hydrogen production reactor and reformer of this embodiment are applied to the hydrogen production reaction by steam reforming of natur...
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