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Fuel Reform Facility and Fuel Reform Procedures

机译:燃油改革设施和燃油改革程序

摘要

A fuel reforming device comprising: an ammonia tank (4),a reformer (5) for the reforming of ammonia and for the production of highly concentrated hydrogen gas with a hydrogen content of at least 99%;a mixing tank (7) for mixing ammonia and hydrogen for temporary storage; and a control (10) to control the respective quantities of ammonia and highly concentrated hydrogen gas supplied to the mixing tank (7). The control medium (10) calculates the combustion rate coefficient C of the blend gas in relation to a reference fuel on the basis of equation (1). Equation (1): So=SHXC+SA(1-C). In equation (1) is Thus the combustion rate of the reference fuel, SH is the combustion rate of hydrogen,SA is the combustion rate of ammonia and C is the combustion rate coefficient of mixed gas. In addition, the control device (10) on the basis of equation (2) determines the volume components of ammonia and hydrogen supplied to the mixing tank. Equation (2): C=1-exp(A xMB). In equation (2), M is the volume part of hydrogen in the blend gas, and A and B are constant.
机译:一种燃料重整装置,包括:氨罐(4),用于改进氨的重整器(5),以及用于生产高浓缩的氢气,其氢含量至少为99%;混合罐(7)混合氨和氢气用于临时储存;和控制(10)以控制供应到混合罐(7)的各自的氨和高度浓缩的氢气。控制介质(10)根据等式(1)计算共混气体的燃烧速率系数C.等式(1):SO = SHXC + SA(1-C)。因此,在等式(1)中,因此参考燃料的燃烧速率,SH是氢气的燃烧速率,SA是氨的燃烧速率,C是混合气体的燃烧速率系数。另外,基于等式(2)的控制装置(10)确定提供给混合罐的氨和氢的体积分量。等式(2):C = 1-EXP(XMB)。在等式(2)中,M是共混气体中氢的体积部分,A和B是恒定的。

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