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guolianshun

铜虫 (著名写手)

[求助] 请帮我翻译一段文摘谢谢,自己翻译了几遍,老板很不满意。谢谢。

A monolithic cocurrent downflow contactor (CDC) reactor was used for the palladium catalysed liquid phase hydro-genation of 2-butyne-1,4-diol (B) tocis-2-butene-1,4-diol (C) in the temperature range 293–333 K and in the pressure
range 102–304 kPa. Its performance was compared with a slurry CDC reactor and a stirred tank reactor (STR). Appar-ent energy of activation (46–54.5 kJ/mol) and transport calculations indicated the reaction was surface rate controlled. A
Langmuir–Hinshelwood mechanism was used to model the reaction. A good agreement was found between the rates from
the model and the experimental rates. Selectivity to the product C was significantly greater for the monolith and slurry CDC
(0.980–0.993) compared with the STR (0.90–0.95) at conversions of B approaching 100%. It was concluded that the monolith
CDC possesses a performance comparable with the slurry CDC particularly in the selective production of C, but has the added
advantage of allowing easy catalyst separation.

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hookhans

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Farmer

你拿出你的翻译,大家可以帮你润色和修改。
where-there-is-a-will-there-is-a-way.
2楼2013-03-25 10:58:07
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guolianshun

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引用回帖:
2楼: Originally posted by hookhans at 2013-03-25 10:58:07
你拿出你的翻译,大家可以帮你润色和修改。

你好好润色你的吧,
3楼2013-03-25 12:08:32
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