A method for determining the process execution sequence in hydrogen network hydrogen saving
A technique for executing the sequence and determining the process, applied in the field of hydrogen network, can solve the problem of not being able to give the target of hydrogen consumption, and achieve the effect of simple design steps, small amount of calculation, and simple method
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[0126] The above example is designed according to the fixed concentration model after purification (HR=95%, Creg=(0.03, 0.25, 0.72) mol%) and the given impurity removal rate model (HR=95%, R=95%).
example 1
[0127] Example 1, it is known that the hydrogen recovery rate HR=95%, and the impurity removal rate IR=95%.
[0128] After determining the execution sequence of the process, each process is also satisfied, that is, the first iteration is completed. Because the amount of the unused source stream in the first iteration is 209.37 mol·s-1, the purified source stream is 175.38 mol·s-1. The consumption of the source stream after purification is 182.40 mol·s-1. Because 175.38<182.40, 175.38 is used as the initial value of the next iteration, and the final design is obtained after four iterations. The results of each iteration are shown in Table 3.
[0129] Table 3. Iterative Design Results of Example 1
[0130]
[0131] see final design Figure 4 , the amount of the external source stream designed is 41.53mol·s-1, the amount of the source stream after purification is 172.89mol·s-1, the amount of the source stream before purification is 206.55mol·s-1, and the impurity concentrat...
example 2
[0132] Example 2, the impurity concentration of the purified source stream is Creg=(0.03, 0.25, 0.72) mol%, and the hydrogen recovery rate is HR=95%.
[0133] The proposed method is used in the following design.
[0134] The method of satisfying the process from the source stream and the method of judging the execution sequence of the process are the same as above, and the design steps are similar to the above. Because the amount of the source stream that was not reused in the first iteration was 192.60 mol·s-1, the amount of the source stream after purification was 160.91 mol·s-1. The consumption amount of the source stream after purification is 200.47mol·s-1. Because 160.91<200.47, the amount of 160.91mol·s-1 of the source stream after purification obtained from the purification of the source stream before purification with an amount of 192.60mol·s-1 is not enough, and it is used as the initial value of the next iteration, The final design was obtained after six iterations...
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