Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

馏分油临氢和非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相中无机电解质浓度越大，石油酸钠对馏分油的力越强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果酸模中分离鉴定13脂肪酸成分、2甾类成分和1植醇，占色谱总馏分出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介油通过双炉双塔分离精制生产甲基萘和苊油馏分的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述裂解汽油重质馏分产BTX芳烃的技术进展以及与此相关的加氢脱烷基和非芳烃加氢裂解技术。

Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

馏分油临氢和非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相中无机电解质浓度越大，石油酸钠对馏分油的增溶能力越强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果酸模中分了13脂肪酸成分、2甾类成分和1植，谱总馏分出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介绍了洗油通过双炉双塔分精制生产甲基萘和苊油馏分的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述了裂解汽油重质馏分增产BTX芳烃的技术进展以及与此相关的加氢脱烷基和非芳烃加氢裂解技术。

Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

油临氢和非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相中无机电解质浓度越大，石油酸钠油的增溶能力越强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果酸模中离鉴定了13脂肪酸成、2甾类成和1植醇，占色谱总出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介绍了洗油通塔离精制生产甲基萘和苊油的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述了裂解汽油重质增产BTX芳烃的技术进展以及与此相关的加氢脱烷基和非芳烃加氢裂解技术。

Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

馏分油临氢和非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相中无机电解质大，石油酸钠对馏分油的增溶能力强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果酸模中分离鉴定了13脂肪酸成分、2甾类成分和1植醇，占色谱总馏分出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介绍了洗油通过双炉双塔分离精甲基萘和苊油馏分的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述了裂解汽油重质馏分增BTX芳烃的技术进展以及与此相关的加氢脱烷基和非芳烃加氢裂解技术。

Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

馏分临氢和非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相中无机电解质浓度越大，石酸钠对馏分的增溶能力越强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果酸模中分离鉴定了13脂肪酸成分、2甾类成分和1植醇，占色谱总馏分出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介绍了洗通过双炉双塔分离精制生产甲基萘和苊馏分的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述了裂解汽重质馏分增产BTX芳烃的技术及与此相关的加氢脱烷基和非芳烃加氢裂解技术。

Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

油临氢和非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相无机电解质浓度越大，石油钠对油的增溶能力越强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果离鉴定了13脂肪成、2甾类成和1植醇，占色谱出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介绍了洗油通过双炉双塔离精制生产甲基萘和苊油的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述了裂解汽油重质增产BTX芳烃的技术进展以及与此相关的加氢脱烷基和非芳烃加氢裂解技术。

Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

馏油临氢非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相中无机电解质浓度越大，石油钠对馏油的增溶能力越强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果模中离鉴定了13、2甾类1植醇，占色谱总馏出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介绍了洗油通过双炉双塔离精制生产甲基萘苊油馏的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述了裂解汽油重质馏增产BTX芳烃的技术进展以及与此相关的加氢脱烷基非芳烃加氢裂解技术。

Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

馏分油临氢非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相中解质浓度越大，石油酸钠对馏分油的增溶能力越强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果酸模中分离鉴定了13脂肪酸成分、2甾类成分1植醇，占色谱总馏分出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介绍了洗油通过双炉双塔分离精制生产甲基油馏分的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述了裂解汽油重质馏分增产BTX芳烃的技术进展以及与此相关的加氢脱烷基非芳烃加氢裂解技术。

Both hydrodewaxing and dewaxing without hydrogen have been commercialized in China.

馏分油临氢非临氢降凝工艺技术均已工业化。

The increase of concentration of inorganic electrolyte in aqueous phase can also markedly raise the solubilization capacity of sodium naphthenates for oil.

水相中无质浓度越大，石油酸钠对馏分油的增溶能力越强。

13 fatty acids components, 2 sterol and phytol ones were identified from R. dentatua L., amounting to 86.03% of the total constituents.

从齿果酸模中分离鉴定了13脂肪酸成分、2甾类成分1植醇，占色谱总馏分出峰面积的86.03%。

This article introduces the process design of rectification separation of methylnaphthalene and acenaphthylene fraction from Wash Oil with twin furnaces and twin column.

介绍了洗油通过双炉双塔分离精制生产甲苊油馏分的工艺设计。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper.

综述了裂汽油重质馏分增产BTX芳烃的技术进展以及与此相关的加氢脱烷非芳烃加氢裂技术。