CAJ | 학술논문

国内某炼厂1.7 Mt/a 煤柴油加氢精制装置包括1.4 Mt/a 柴油加氢精制部分和0.3 Mt/a 煤油加氢精制部分，两部分热量联合，共用一套公用工程系统。对该装置的工程设计与工业标定进行总结，简要介绍了工艺及工程技术特点，并对装置的工业运转标定结果作了简要分析。结果表明，柴油加氢精制催化剂 DN-3630和煤油加氢精制催化剂 FH-40B 效果良好，柴油产品硫含量达到15μg/g，满足国 IV 车用柴油排放标准，煤油产品全面满足 GB6537-2006标准3#喷气燃料要求，装置能耗达到国内先进水平。
국내모련엄1.7 Mt/a 매시유가경정제장치포괄1.4 Mt/a 시유가경정제부분화0.3 Mt/a 매유가경정제부분，량부분열량연합，공용일투공용공정계통。대해장치적공정설계여공업표정진행총결，간요개소료공예급공정기술특점，병대장치적공업운전표정결과작료간요분석。결과표명，시유가경정제최화제 DN-3630화매유가경정제최화제 FH-40B 효과량호，시유산품류함량체도15μg/g，만족국 IV 차용시유배방표준，매유산품전면만족 GB6537-2006표준3#분기연료요구，장치능모체도국내선진수평。
A 1.7 Mt/a kerosene and diesel hydrofining unit is composed of 1.4 Mt/a diesel hydrofining section and 0.3Mt/a kerosene hydrofining section, whose heat is combined and shared by a set of utilities system. In this paper, the engineering design and industry calibration of the unit were summarized, including an introduction of process flow, technology features and a brief analysis of industry calibration. The results indicate that the performances of catalyst DN-3630 and FH-40B are excellent. Diesel product can meet China IV diesel with sulfur content less of 15 μg/g, and kerosene product can meet GB6537-2006 3# jet fuel. The energy consumption of diesel hydrofining section and kerosene hydrofining section both can reach domestic advanced level.