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lco

  • 网络催化裂化柴油;液态一氧化碳;几丁质酯寡糖;美铝公司
lcolco
  1. Technical measures for increasing LCO production in a heavy oil catalytic cracking unit

    燕化2Mt/a重油催化裂化装置增产柴油的技术措施

  2. Commercial application of rich technology for improving LCO cetane number

    提高柴油十六烷值RICH工艺技术的工业应用

  3. Advanced process control and plant implementation for FCC LCO quality based on state feedback model predictive control

    状态反馈预测控制在催化裂化柴油产品质量先进控制中的应用

  4. Development of a residual oil cracking catalyst for LCO

    多产中间馏分油的渣油裂化催化剂MLC-500的开发

  5. Study on Refining FCC LCO with FCC Catalyst Adsorption Method

    催化裂化柴油用FCC催化剂吸附精制的研究

  6. Development and commercial application of inferior LCO hydro-upgrading Technology

    劣质催化裂化柴油加氢改质技术的开发及工业应用

  7. Improving Stability of LCO by Double - Solvent Extraction

    双剂抽提法提高FCC柴油氧化安定性

  8. Development and application of MGD Technology for producing more LPG and LCO

    催化裂化多产液化气和柴油工艺技术的开发与应用

  9. The advanced process control system design and plant implementation for LCO quality in FCCU main fractionator were studied .

    对催化裂化装置主分馏塔柴油产品质量先进控制系统进行了设计与工程实施。

  10. Study on kinetic models for deep hydrodesulfurization of LCO

    催化裂化柴油深度加氢脱硫反应动力学模型的研究

  11. Effect of acidic components in FCC LCO on stability of diesels

    催化柴油中酸性组分对柴油安定性的影响

  12. Study on processing conditions of a new generation hydro-upgrading catalyst for FCC LCO and its commercial application

    新一代催化裂化柴油加氢改质催化剂的工艺条件及工业应用

  13. MLC series catalysts for enhancing LCO production in catalytic cracking

    MLC系列催化裂化多产柴油催化剂的研究开发

  14. In this paper , the oxidation and extraction method was systematically studied with the FCC LCO as feed .

    本论文以锦州石化公司催化裂化柴油为原料对氧化抽提方法进行了系统的研究。

  15. There may or may not be actual executables as part of an LCO briefing .

    也许有或也许没有实际的可执行程序作为LCO简报的一部分。

  16. Improving stability of LCO BY ADSORPTION

    吸附精制提高催化裂化柴油的安定性

  17. Study on desulfurization of FCC LCO by oxidative extraction DESULFURIZATION OF CATALYTIC CRACKING DIESEL BY AIR OXIDATION

    催化裂化柴油空气氧化脱硫工艺研究

  18. Improving LCO cetane number by solvent extraction

    溶剂萃取法提高催化裂化柴油十六烷值的研究

  19. A new generation hydro-upgrading catalyst FC-4512 was developed for processing FCC LCO .

    就改善催化裂化柴油新一代加氢改质催化剂FC-4512应用的工艺条件在实验室进行了考察,并在600kt/a柴油加氢工业装置上进行了应用试验。

  20. The ratio of LCO and naphtha is somewhat increased with dry gas as fluid gas instead of steam .

    干气代替蒸汽作流化气,在某种程度上提高了产品的柴汽比。

  21. Refining LCO by adsorption of organic clay

    有机粘土吸附精制催化裂化柴油

  22. And the LCO yield increased from 30 . 59 % to 31 . 34 % .

    柴油产率从30.59%增加到31.34%。

  23. Finally the cropped-delta-wing LCO is computed , and the calculation precision is obviously better than the existing results .

    最后应用该方法研究了切尖三角翼的LCO现象,其计算精度明显优于已有结果。

  24. Feasibility and cost are the important factors in the LCO meeting , and the tester can certainly contribute important data to this decision .

    可行性和成本是LCO会议上的重要因素,并且测试人员无疑可以为该决策贡献重要的数据。

  25. MCI technology for upgrading FCC LCO was applied in the hydroprocessing unit of Dagang Petrochemical Company .

    大港石化公司加氢装置应用MCI技术对催化裂化柴油进行加氢改质。

  26. The result showed that the said technology improved the LCO cetane number effectively , and reduced the existent gum of the product .

    实践证明,该技术能够有效地提高催化裂化柴油的十六烷值,并能降低产品的胶质。

  27. The low aromatics content diesel oil and high octane number gasoline were produced from the LCO by Medium Hydrotreatment upgrading process .

    中压加氢改质技术能够在降低硫、氮含量的同时,降低芳烃含量,并产少量高辛烷值汽油。

  28. The flutter and the LCO of the cropped delta wing are calculated and the results are compared with existing experimental measurements .

    依据所建模型分析切尖三角翼的颤振和LCO,并与试验值进行比较。

  29. Presents the routes and technical measures for producing more LCO and LPG by using optimized operation and MGD technology based on available FCC unit .

    介绍了利用现有的催化裂化装置,通过优化操作及运用MGD技术提高柴油和液化气收率的方法和技术措施。

  30. The stabilization of GX - 105 diesel fuel stabilizator based on oxidation sediments and the color of LCO was studied .

    研究了GX-105柴油稳定剂对催化柴油的氧化沉渣和色度的稳定作用。