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10萬t/a混合C5生產1,4-丁二醇工藝中氧化反應器的模擬與優化

Study on the simulation and optimization of the oxidative reactor in the mixed C5 hydrocarbons to BDO process with a treatment capacity of 100 000 t/a

  • 摘要: 針對10萬t/a順酐法生產1,4-丁二醇工藝受原料影響較大的缺陷👫🏻,結合我國混合C5烴的市場情況,采用C5原料生產1,4-丁二醇,針對該工藝的關鍵設備-正戊烷氧化反應器🤷🏿,采用Aspen Plus軟件對影響順酐和苯酐產率和選擇性的關鍵參數進行了靈敏度分析,優化了反應參數,提高了順酐和苯酐的產率和選擇性✍️。在優化條件下,正戊烷的轉化率以及苯酐和順酐的產量大大提高💳🕖。在單耗不變的情況下🤸🏿,順酐的產率和選擇性由原來的34.1%和6.9%分別增加到45.1%和32.1%,苯酐的產率從15.7%降低到13.5%🏋🏼‍♀️,苯酐的選擇性從3.2%升高到9.6%🌓,而一氧化碳的產率和選擇性由原來的43.1%和8.7%分別降低到32.0%和2.7%👨🏻‍✈️💅🏼。優化後的反應條件提高了順酐的產率和選擇性,有利於正戊烷氧化生成順酐的反應。

     

    Abstract: Combined with the market situation of mixed C5 hydrocarbons in China, using C5 raw materials produced 1,4- butanediol to avoid that a maleic anhydride method for producing 1,4-butanediol (100000 t/a) was greatly affected by raw materials. The sensitivity analysis of reaction parameters of of n-pentane oxidation to maleic anhydride on the output of phthalic anhydride and maleic anhydride was analyzed by Aspen Plus software, and its optimal operating parameters were determined. Also, the conversion of n-pentane and the yield of phthalic anhydride and maleic anhydride are greatly improved. The simulation results showed the conversion of n-pentane and the yield of phthalic anhydride and maleic anhydride were greatly improved. Under the condition of the same unit consumption, The yield and selectivity of maleic anhydride increased from 34.1% and 6.9% to 45.1% and 32.1% respectively. The yield of phthalic anhydride decreased from 15.7 to 13.5%, and the selectivity of phthalic anhydride increased from 3.2 to 9.6%. The yield and selectivity of carbon monoxide decreased from 43.1% and 8.7% to 32.0% and 2.7% respectively.The optimized reaction conditions were conducive to the oxidation of n-pentane to maleic anhydride leading to an increase in the yield and selectivity of maleic anhydride.

     

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