說的也是，這有點困難，但如果您願意的話和我交換的話，我們還是可以跨國互

說的也是，這有點困難，但如果您願意的話和我交換的話，我們還是可以跨國互相寄送

結果 (日文) 1:

私が言ったように、それは少し難しいですが、あなたが私と交換したいのであれば、私たちはまだ国を越えてお互いを送ることができます

結果 (日文) 2:

The deactivation of the Ni/La2O3–aAl2O3 catalyst in the SRE process
is a consequence of the coke formation rate and its nature,
which depend on the concentration of reaction medium components.
Moreover, coke evolution causes a change in Ni morphology,
which contributes to modifying catalyst activity. To understand the
deactivation, three stages have been identified, whose duration
depends on the operating conditions: (i) almost steady performance,
followed by (ii) a severe drop in ethanol conversion and
finally (iii) a steady and slow decrease in ethanol conversion until
total deactivation of the catalyst. The different deactivation rate at each step is explained by the formation of coke with different natures
(filamentous and nonfilamentous) and the different role of
these cokes in the blockage of Ni active sites.
The combination of diverse techniques for coke analysis has
allowed determining that progressive growth of filamentous and
nonfilamentous coke takes place in these stages. In the first reaction
stage the highest filamentous coke yield is reached. This coke
drags Ni particles during its growth, which are located at the end of
the fibers and separated from Ni crystallites, thus causing the
decrease in Ni particle size, but without blocking the sites, and
therefore without causing significant effect on deactivation. In
the second stage, both the dragging and the decrease in the size
of Ni particles continue. However, the change in the coke formation
mechanism, and therefore the change in its nature, plays an essential
role in the deactivation. In this second stage the yield of filamentous
coke decreases, whose structure becomes progressively
more condensed and graphitic, while the formation of nonfilamentous
coke becomes significant, which is the primary cause of deactivation
under these conditions by Ni sites blockage. In the third
stage, corresponding to a highly deactivated catalyst and a high
ethanol concentration in the medium, the formation of coke is very
slow and is mainly of a nonfilamentous nature, whose structure
evolves toward a high graphitization degree, while the progressive
blocking of Ni sites continues.
The coke formation rate and the nature of coke depend on the
concentration of reaction medium components. Thus, operating
conditions with low ethanol concentration (high conversion and
high concentration of CO and CH4) lead to a high formation rate
of coke with a filamentous nature. Operating with high ethanol
concentrations leads to a low coke formation rate, but the coke
formed under these conditions is nonfilamentous.

結果 (日文) 3:

そうです。これはちょっと難しいですが、もしよろしければ、私と交換していただければ、多国籍でお互いに送ることができます。