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分离罐     
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  separation tank
     Problems and Modification of LowPressure Flash Separation Tank
     低压闪蒸分离罐存在的问题及改造
短句来源
  separation pot
     Model free control for liquid level of low pressure separation pot
     低压分离罐液位的无模型控制
短句来源
     In adaptation to the characteristics of liquid level of low pressure separation pot, model free control system has been designed.
     针对低压分离罐液位的特点,设计了无模型控制系统。
短句来源
  separation drums
     The design and application of high efficient separation drums
     高效分离罐设计与应用
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  “分离罐”译为未确定词的双语例句
     The calculation indicates that,with the pressure in low pressure separator maintained at 13kg/cm~2,increasing the pressure in high pressure separator to 19,25,35,or 60kg/cm~2,the hydrogen purity will be increased by 1.6,2.5,4.0 or 7.0 units respectively.
     计算表明,低压分离罐压力13公斤/厘米~2时,高压分离罐压力如为l9、25、35和60公斤/厘米~2,则氢纯度相应提高1.6、2.5、4.0和7.0个单位.
短句来源
     It was concluded from the analysis of the corrosion of the caustic liquid separator that the large-scale rapid corrosion of the separator was mainly caused by H 2S corrosion and defects in equipment construction.
     对碱液分离罐腐蚀原因进行了分析 ,指出H2 S腐蚀与设备结构缺陷是造成分离罐大面积、快速腐蚀的主要原因。
短句来源
     By re-contacting the recycle hydrogen from the low pressure separator of a catalytic reformer with reformate under high pressure,a new equilibrium is reached and a hydrogen stream with higher purity is obtained.
     在重整流程中采用一种简便易行的办法提高氢纯度,即将低压分离罐的氢气与重整生成油在较高压力下再次接触,气液重新达到平衡,分离出的氢气纯度要比原来高.
短句来源
     Cleaning of the grease separator of offshore oil platform
     海上石油平台油水分离罐的清洗
短句来源
     The composition and formation of oil base sludge, the danger and safety in the sludge removal are introduced. The method and steps of cleaning of HZ26-1 platform are analysed.
     叙述了原油油泥的组成、成因及其清洗过程中的危险性和安全对策,介绍了HZ26-1海上石油平台油水分离罐的清洗方法和清洗步骤
短句来源
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      knockout drum
    The clean syngas exiting the absorber column passes through a knockout drum and demister to remove any entrained solvent.
          
      separation tank
    Moreover, sulfide production did not exceed the permissible exposure limit in the water-oil separation tank studied treated with nitrate.
          
    A predetermined liquid composition was charged into a 200-gal 0.76 m3 storage/separation tank.
          
    Both the hydrasieve and separation tank functioned to remove a percentage of solids from the chill water prior to ozonation.
          
    The column emptied into a six-gallon separation tank, which in turn drained back to the reservoir.
          
    The construction of the oil separation tank does not present serious problems and the dimensions are adequate for the new upgraded flow rates.
          
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    By re-contacting the recycle hydrogen from the low pressure separator of a catalytic reformer with reformate under high pressure,a new equilibrium is reached and a hydrogen stream with higher purity is obtained.The calculation indicates that,with the pressure in low pressure separator maintained at 13kg/cm~2,increasing the pressure in high pressure separator to 19,25,35,or 60kg/cm~2,the hydrogen purity will be increased by 1.6,2.5,4.0 or 7.0 units respectively.If the pressure of re-contacting is equal to the...

    By re-contacting the recycle hydrogen from the low pressure separator of a catalytic reformer with reformate under high pressure,a new equilibrium is reached and a hydrogen stream with higher purity is obtained.The calculation indicates that,with the pressure in low pressure separator maintained at 13kg/cm~2,increasing the pressure in high pressure separator to 19,25,35,or 60kg/cm~2,the hydrogen purity will be increased by 1.6,2.5,4.0 or 7.0 units respectively.If the pressure of re-contacting is equal to the discharge pressure of the recycle gas compressor,the additional investment cost will be reimbursed in about one month.If the pressure is raised to 60kg/cm~2,the pay off time will be about 8 months.

    在重整流程中采用一种简便易行的办法提高氢纯度,即将低压分离罐的氢气与重整生成油在较高压力下再次接触,气液重新达到平衡,分离出的氢气纯度要比原来高.计算表明,低压分离罐压力13公斤/厘米~2时,高压分离罐压力如为l9、25、35和60公斤/厘米~2,则氢纯度相应提高1.6、2.5、4.0和7.0个单位.如提高的压力就是压缩机出口压力,则增加的设备投资1个月即可回收;如压力提高到60公斤/厘米~2,则增加的设备投资8个月即可回收.

    The recovery oil in the wastewater treatment plant mainly comes from the oil tank dewatering.It is an important problem to solve the second de- water of oil tank so as to prevent on the wastewater treatment plant from impact.The refinery has succeeded in new second dewatering technology of oil tank by means of texts and research for years.This method uses joint pipe and different density between oil and water to separate oil from water. The electrode of auto-dewatering instrument is installed in oil tank,thus...

    The recovery oil in the wastewater treatment plant mainly comes from the oil tank dewatering.It is an important problem to solve the second de- water of oil tank so as to prevent on the wastewater treatment plant from impact.The refinery has succeeded in new second dewatering technology of oil tank by means of texts and research for years.This method uses joint pipe and different density between oil and water to separate oil from water. The electrode of auto-dewatering instrument is installed in oil tank,thus it is easy installed,maintained and extensively.

    污水处理场回收污油主要来自油罐脱水,解决油罐二次脱水是防止污水处理场冲击的一个重要问题。我厂经过多年来试验和技术攻关,开创了油罐二次脱水新技术。该技术利用连通管原理和油水比重差进行油水分离效果较好。将油水自动脱水仪表电极安装在油水分离罐内,便于安装、维修和推广应用。

    Fennel oil was isolated by supercritical fluid extraction(SFE) using CO2, and then followed by a two-stage fractional separation. Two products were obtained, the one rich in essential oil, the other rich in fatty oil. Their yields were dependent on the separation pressure in the first separator. The total yield of SFE from fennel seeds was different from those obtained by hydrodistillation and Soxhlet extraction. Chemical analysis revealed that extracts obtained by SFE at various extlaction periods, possessed...

    Fennel oil was isolated by supercritical fluid extraction(SFE) using CO2, and then followed by a two-stage fractional separation. Two products were obtained, the one rich in essential oil, the other rich in fatty oil. Their yields were dependent on the separation pressure in the first separator. The total yield of SFE from fennel seeds was different from those obtained by hydrodistillation and Soxhlet extraction. Chemical analysis revealed that extracts obtained by SFE at various extlaction periods, possessed a widely different percentage composition. The composition of SFE products was also compared with those of essential oil prepared by hydrodistillation and extlact by Soxhlet extraction.

    本文介绍从小茴香子中采用超临界CO2萃取和分级分离富含精油和富含脂油两种产品的工艺可行性,探讨了采用不同规模的超临界苹取装置萃取过程对萃取物组成、风味和CO2消耗量的影响以及第一分离罐的分离压力对两种产品产率的影响.对超临界CO2萃取法、索氏萃取法和水蒸气蒸馏法所制备的茴香精油或萃取物的产率和主要挥发性成分进行了比较和分析。

     
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