分析化学の翻訳サンプル

Figure 2 shows an SEM image of the Pt/mordenite zeolite catalyst. The image indicates the catalyst has a homogeneous morphology. The surface area is key in the catalyst activity. Higher surface area improves the reactant adsorption. The catalysts surface area was measured by BET. The surface area of Pt/mordneite zeolites were 296.69 m2/gm. The XRDs pattern of Pt/mordenite zeolite (Figure 3) exhibits the most intense diffraction at 2θ = 6 - 30o, and it thus confirmed structure of zeolite as the MOR as well as its crystalline nature being good.
The hydroisomerization of pure n-pentane and n-pentane in a binary mixture of pentane isomers was performed by the Pt/mordenite catalyst for wide ranges of experimental conditions. The hydrological conversion products comprise of both isomerization and cracking products. Hence the following subsections discuss reaction parameters effects with the catalytic performance of pure n-pentane as feed are demonstrated by catalytic activity and isomerization selectivity. After this, the isomerization of n-pentane in the bi mixture is discussed.
Figure 4 shows the conversion of npentane as a function of reaction temperature. The tests were performed in an H2 environment at temperatures ranging from 150 - 350 °C at atmosphere pressures. It clearly shows that the catalyst showed a high catalysing activity for the isomerization of npentane, particularly in the temperature ranging in 220-350 ° C. Because of the low activity of the catalyst and the low reactivity of n-pentane, the conversion of n-pentane is negligible from temperatures below 180 °C. By increasing the temperature at 180 to 220 °C, the conversion of n-pentane rose greatly; however, a further increase in temperature slowly rises conversion. This can be caused by an increasing the number of sites which can be activated for the reaction when the temperatures increases in the range from 180 - 220 °C; but, the rate of conversion decreases because of thermodynamic restriction at bigger temperature. In other words, an increasing temperature always means increasing reaction rate. Thus at low temperatures the actual conversion will be far below the equilibrium conversion because of low reaction rate. On the contrary at higher temperatures the equilibrium conversion will be more easy due to a high reaction rate.

A scanning electron microscopy image of the Pt/mordenite zeolite catalyst is shown in Figure 2 which indicates that the catalyst morphology is homogeneous .High surface area improves the reactant adsorption, thus playing a key role in the catalytic activity . The surface area of the Pt/mordenite zeolite catalyst measured by Brunauer–Emmett–Teller surface analysis.was 296.69 m2/g. The X-ray powder diffraction pattern of Pt/mordenite zeolite (Figure 3) exhibits the most intense diffraction peaks at 2θ = 6°–30°, thus confirming the MOR structure of zeolite as well as its good crystalline nature .
Pure n-pentane and n-pentane in a binary mixture of pentane isomers was hydroisomerized using the Pt/mordenite catalyst under a wide range of experimental conditions. The hydro-conversion process yielded both isomerization and cracking products. In the following subsections, the effects of reaction parameters on the catalytic performance of pure n-pentane as the feed are demonstrated based on catalytic activity and isomerization selectivity. Then, the isomerization of n-pentane in the binary mixture is discussed in the last part of this section.
Figure 4 shows the conversion of n-pentane as a function of reaction temperature. The reactions were performed in an H2 environment at temperatures ranging from 150 °C to 350 °C at at atmospheric pressure. The catalyst is seen to strongly catalyze the isomerization of n-pentane, particularly in the temperature range of 220 °C–350 °C. Because of the low activity of the catalyst and the low reactivity of n-pentane, the conversion of n-pentane is negligible at temperatures below 180 °C. By increasing the temperature from 180 °C to 220 °C, the conversion of n-pentane increased significantly; however, increasing the temperature further results in a slow conversion. This can be attributed to an increase in the number of sites that can be activated for the reaction when the temperatures increases in the range from 180 - 220 °C; however, the r conversion rate begins to decrease as the temperature increases because of thermodynamic restrictions at higher temperatures. In other words, increasing the temperature results in a faster reaction rate. At low temperatures, the low reaction rates cause the actual conversion to be far below the equilibrium conversion rate. In contrast at higher temperatures the equilibrium conversion is easily achieved due to the high reaction rate.

Figure 2shows anAn SEMA scanning electron microscopy1 image of thePt/mordenite zeolite catalyst. The image  is shown in Figure 2and which indicatesthat thecatalyst has a homogeneous morphology. The surface area plays a key role in the catalyticactivity.  is homogeneousHigher.Highsurface area improves the reactant adsorption, of reactants. thus playing a key role in the catalytic activity2. The catalysts surfacearea ofthe Pt/mordenitezeolite3 catalyst was4 measured by BET.Brunauer–Emmett–Teller surface analysis5. Thesurface area of Pt/mordneitemordenite zeoliteswerewas 296.69 m²/gm6.The XRDX-raypowder diffraction pattern of Pt/mordenite zeolite (Figure 3)exhibits the most intense diffraction peaks at 2θ = 6 - 30^o,and it thus confirmed 6°–30^o7, thus confirming the MOR structure ofzeolite asthe MOR as well as and its good crystallinenature beinggood. are thus confirmed.8

Thehydroisomerization of pure Pure n-pentane andn-pentane in a binary mixture of pentane isomers was performed byhydroisomerized usingthe Pt/mordenite catalyst forunder a wide rangesrangeof experimental conditions. The hydrological hydro-conversion9 products comprise ofprocessyielded both isomerization and cracking products. Hence theThe In the followingsubsections, discuss cover howthe effects of reaction parameters effects with10affect on thecatalytic performance of pure n-pentane as the feed are which is demonstratedbybased oncatalytic activity and isomerization selectivity. 11After thisThen,the isomerization of n-pentane in the bibinarymixture is discussed in the last part of this section.12

Figure 4 showsthe conversion of npentane n-pentane13 as a function ofreaction temperature. The testsreactions14 wereperformed in an H₂ environment at temperatures ranging from 150 °C to 350 °C at atmospherepressures. It clearly shows that theatmospheric pressure. The catalyst showeda high catalysing activity for the isseen to strongly catalyze the isomerization of npentanen-pentane, particularlyin the temperature ranging inrange of 220 °C-350 °C. Because of the low activity of thecatalyst and the low reactivity of n-pentane, the conversion of n-pentane isnegligible from at temperatures below 180 °C. By increasing thetemperature at from180 °C to 220 °C, theconversion of n-pentane roseincreased greatlysignificantly;however, a further increase in increasingthe temperature slowly risesfurther results in a slowconversion.15 This can be caused by anincreasingattributed to an increase inthe number of sites which that can be activated for the reaction when thetemperatures increases in the range from 180 °C- 220 °C; buthowever,the rate ofconversion decreases ratebegins to decrease as the temperature increases because ofthermodynamic restrictions at bigger higher temperatures. In other words, an increasing the temperaturealways means increasingresults in ahigherfaster reaction rate. ThusatAt low temperatures,the low reaction rates cause the actualconversion will to be far below the equilibrium conversion because of low reaction rate. On the contraryIncontrast at higher temperatures theequilibrium conversion will be more easyis easily achieved due to a the highreaction rate.