Hydrogen production method by multi-step copper-chlorine thermochemical cycle
一种热化学、氯化氢的技术,应用在化学仪器和方法、氢/合成气生产、氢的生产等方向
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Embodiment 1-5
[0127] According to the above disclosure of the present invention, the following experiments were carried out in a quartz microreactor. The reaction was carried out as a fixed bed reactor type. The dry hydrogen chloride gas required for the reaction was supplied into the reactor through a mass flow controller through a quartz tube extending to the bottom of the reactor. The reaction is carried out under atmospheric pressure. Dry hydrogen chloride gas is introduced into the reactor at the desired flow rate. The results are shown in Table 1. The reaction is carried out under the following operating conditions:
[0128] Copper (Cu): 0.015 mol (1 gram)
[0129] Molar ratio of HCl / Cu: 5:1
[0130] Copper (Cu) size: 3-5μm
[0131] N 2 Flow rate: 15cm 3 / minute
[0132] Table 1
[0133] Example number
Embodiment 6-8
[0135] According to the above disclosure of the present invention, the following experiments were carried out in a quartz microreactor. The reaction was carried out as a fixed bed reactor type. The dry hydrogen chloride gas required for the reaction was supplied into the reactor through a mass flow controller through a quartz tube extending to the bottom of the reactor. The reaction is carried out under atmospheric pressure. Dry hydrogen chloride gas is introduced into the reactor at the desired flow rate. The results are shown in Table 2. The reaction is carried out under the following operating conditions:
[0136] Copper (Cu): 0.015 mol (1 gram)
[0137] Molar ratio of HCl / Cu: 1:1
[0138] Copper (Cu) size: 3-5μm
[0139] Temperature: 450°C
[0140] Table 2
[0141] Example number
Embodiment 9-11
[0143] According to the above disclosure of the present invention, the following experiments were carried out in a quartz microreactor. The reaction was carried out as a fixed bed reactor type. The dry hydrogen chloride gas required for the reaction was supplied into the reactor through a mass flow controller through a quartz tube extending to the bottom of the reactor. The reaction is carried out under atmospheric pressure. Dry hydrogen chloride gas is introduced into the reactor at the desired flow rate. The results are shown in Table 3. The reaction is carried out under the following operating conditions:
[0144] Copper (Cu): 0.015 mol (1 gram)
[0145] Copper (Cu) size: 3-5μm
[0146] Temperature: 450°C
[0147] N 2 Flow rate: 50cm 3 / minute
[0148] table 3
[0149] Example number
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