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樓主: Taylor
21#
發(fā)表于 2025-3-25 03:28:52 | 只看該作者
,Die Steuermannskunst der Universit?t,hydrogen liquefaction and regasification processes. Therefore, these processes are simulated using Aspen Plus V11. process simulator, in order to estimate their capital and operating expenditures from the obtained material and energy balances.
22#
發(fā)表于 2025-3-25 08:34:50 | 只看該作者
23#
發(fā)表于 2025-3-25 11:41:33 | 只看該作者
24#
發(fā)表于 2025-3-25 17:12:16 | 只看該作者
25#
發(fā)表于 2025-3-25 22:52:35 | 只看該作者
26#
發(fā)表于 2025-3-26 00:11:38 | 只看該作者
Dibenzyltoluene/Perhydro-Dibenzyltoluene as Green H2 Carrier, this chapter details the dibenzyltoluene value chain. Hydrogenation and dehydrogenation sections have been analysed in detail thanks to the Aspen Plus V11. process simulation. Considering the process simulation results, the economic assessment of each stage of the value chain is provided.
27#
發(fā)表于 2025-3-26 04:28:07 | 只看該作者
https://doi.org/10.37307/b.978-3-503-20616-2tures and suitability for different transport modes and applications. These carriers undergo continuous innovation and development to enhance their efficiency, safety, and economic viability. To help understanding their applicability, opportunities and drawbacks of each of them are pointed out in this section.
28#
發(fā)表于 2025-3-26 10:44:00 | 只看該作者
29#
發(fā)表于 2025-3-26 14:53:34 | 只看該作者
30#
發(fā)表于 2025-3-26 20:10:57 | 只看該作者
Toluene/methylcyclohexane as Green H2 Carrier,t alternatives. This chapter details the toluene hydrogenation and methylcyclohexane dehydrogenation sections and, considering the process simulation results, provide the economic assessment of each stage of the value chain.
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