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(2-(2-(hexyloxy)ethoxy)ethoxy)benzene | 928346-61-6

中文名称
——
中文别名
——
英文名称
(2-(2-(hexyloxy)ethoxy)ethoxy)benzene
英文别名
2-(2-Hexoxyethoxy)ethoxybenzene
(2-(2-(hexyloxy)ethoxy)ethoxy)benzene化学式
CAS
928346-61-6
化学式
C16H26O3
mdl
——
分子量
266.381
InChiKey
VSNOZZZVTWGUQB-UHFFFAOYSA-N
BEILSTEIN
——
EINECS
——
  • 物化性质
  • 计算性质
  • ADMET
  • 安全信息
  • SDS
  • 制备方法与用途
  • 上下游信息
  • 反应信息
  • 文献信息
  • 表征谱图
  • 同类化合物
  • 相关功能分类
  • 相关结构分类

物化性质

  • 沸点:
    359.9±22.0 °C(Predicted)
  • 密度:
    0.969±0.06 g/cm3(Predicted)

计算性质

  • 辛醇/水分配系数(LogP):
    3.9
  • 重原子数:
    19
  • 可旋转键数:
    12
  • 环数:
    1.0
  • sp3杂化的碳原子比例:
    0.62
  • 拓扑面积:
    27.7
  • 氢给体数:
    0
  • 氢受体数:
    3

反应信息

  • 作为反应物:
    描述:
    (2-(2-(hexyloxy)ethoxy)ethoxy)benzene氯甲烷氯磺酸三氯氧磷 作用下, 以 二氯甲烷异丁酰胺乙腈 为溶剂, 反应 3.0h, 生成
    参考文献:
    名称:
    Lubricant composition, bearing apparatus, sliding member and triazine-ring compound
    摘要:
    揭示了一种新型润滑剂组合物。该组合物包括至少一种化合物,其在压力等于或大于10 MPa时,随着压力的增加,具有最小摩擦系数,并且在40°C时,具有粘度-压力系数等于或小于20 GPa−1,由公式(1)表示。在该公式中,Y和Z分别表示从NRa组成的羟基或二价连接基团,其中Ra是氢原子或C1-30烷基基团,氧,硫,羰基,磺酰基和它们的任何组合中选择的单键;A和B分别表示取代或非取代的烷基基团,烯基基团,炔基基团,芳基或杂环基团;T为—S—R1,—O—R2或—NR3R4;R1,R2,R3和R4分别表示取代或非取代的烷基基团,烯基基团,炔基基团,芳基或杂环基团。
    公开号:
    US20070054814A1
  • 作为产物:
    描述:
    2-(2-Hexoxyethoxy)ethyl methanesulfonate苯酚 在 sodium hydride 作用下, 以 N,N-二甲基甲酰胺 为溶剂, 反应 1.0h, 生成 (2-(2-(hexyloxy)ethoxy)ethoxy)benzene
    参考文献:
    名称:
    Lubricant composition, bearing apparatus, sliding member and triazine-ring compound
    摘要:
    揭示了一种新型润滑剂组合物。该组合物包括至少一种化合物,其在压力等于或大于10 MPa时,随着压力的增加,具有最小摩擦系数,并且在40°C时,具有粘度-压力系数等于或小于20 GPa−1,由公式(1)表示。在该公式中,Y和Z分别表示从NRa组成的羟基或二价连接基团,其中Ra是氢原子或C1-30烷基基团,氧,硫,羰基,磺酰基和它们的任何组合中选择的单键;A和B分别表示取代或非取代的烷基基团,烯基基团,炔基基团,芳基或杂环基团;T为—S—R1,—O—R2或—NR3R4;R1,R2,R3和R4分别表示取代或非取代的烷基基团,烯基基团,炔基基团,芳基或杂环基团。
    公开号:
    US20070054814A1
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文献信息

  • Process for the preparation of cyclic esters and method for purification of the same
    申请人:——
    公开号:US20030191326A1
    公开(公告)日:2003-10-09
    The present invention provides a process for production of a cyclic ester by depolymerization of an aliphatic polyester. In the process, a mixture containing the aliphatic polyester and a specific polyalkylene glycol ether, which has a boiling point of 230-450° C. and a molecular weight of 150-450, is heated under normal or reduced pressure to a temperature at which depolymerization of the aliphatic polyester takes place. Then, a substantially homogeneous solution phase, consisting of the melt phase of the aliphatic polyester and the liquid phase of the polyalkylene glycol ether, is formed. Heating of the solution phase is continued to form the cyclic ester by depolymerization and distil out the cyclic ester together with the polyalkylene glycol ether, and then the cyclic ester is recovered from the distillate. The present invention also provides a process for purification of a crude cyclic ester by use of the specific polyalkylene glycol ether described above.
    本发明提供了一种通过脂肪族聚酯的降解来生产环酯的方法。在该过程中,将含有脂肪族聚酯和具有沸点在230-450°C和分子量在150-450之间的特定聚烷基乙二醇醚的混合物,在常压或减压下加热至脂肪族聚酯发生降解的温度。然后,形成由脂肪族聚酯的熔融相和聚烷基乙二醇醚的液相组成的基本均相溶液相。继续加热溶液相以通过降解形成环酯并与聚烷基乙二醇醚一起蒸馏出环酯,然后从馏出物中回收环酯。本发明还提供了一种利用上述特定聚烷基乙二醇醚对粗环酯进行纯化的方法。
  • LOW VISCOSITY LOW VOLATILITY LUBRICATING OIL BASE STOCKS AND PROCESSES FOR PREPARING SAME
    申请人:ExxonMobil Research and Engineering Company
    公开号:US20170137735A1
    公开(公告)日:2017-05-18
    A composition that includes one or more compounds represented by the formula R 1 —O—R 2 wherein R 1 is a substituted or unsubstituted aryl or polyaryl group having from about 4 to about 40 carbon atoms, and R 2 is the residue of a substituted or unsubstituted glycol ether having from about 4 to about 40 carbon atoms. The composition has a viscosity (Kv 100 ) from about 1 to about 10 cSt at 100° C. as determined by ASTM D-445, a viscosity index (VI) from about −100 to about 300 as determined by ASTM D-2270, and a Noack volatility of no greater than 50 percent as determined by ASTM D-5800. The disclosure also relates to a process for producing the composition, a lubricating oil base stock and lubricating oil containing the composition, and a method for improving one or more of oxidative stability, solubility and dispersancy of polar additives of a lubricating oil by using as the lubricating oil a formulated oil containing the composition.
    一种包括一个或多个化合物的组合物,其表示为R1—O—R2,其中R1是具有大约4到大约40个碳原子的取代或未取代芳基或多芳基基团,而R2是具有大约4到大约40个碳原子的取代或未取代乙二醇醚的残基。该组合物在100°C下通过ASTM D-445确定的粘度(Kv100)约为1到约10厘斯特,通过ASTM D-2270确定的粘度指数(VI)约为-100到约300,通过ASTM D-5800确定的Noack挥发性不大于50%。该公开还涉及生产该组合物的方法,含有该组合物的润滑油基础油和润滑油,以及通过使用含有该组合物的配制油作为润滑油来改善润滑油的氧化稳定性、溶解性和极性添加剂的分散性的方法。
  • [EN] LOW VISCOSITY, LOW VOLATILITY LUBRICATING OIL BASESTOCKS<br/>[FR] HUILES DE BASE POUR HUILE LUBRIFIANTE À FAIBLE VISCOSITÉ ET FAIBLE VOLATILITÉ
    申请人:EXXONMOBIL RES & ENG CO
    公开号:WO2015060985A1
    公开(公告)日:2015-04-30
    This disclosure provides low viscosity, low volatility aryl ether compounds represented by formula (1): and represented by formula (2): wherein R1 is the same or different and is a linear or branched alkyl group having from 1 to 20 carbon atoms; R2 is the same or different and is hydrogen or an alkyl group having from 1 to 4 carbon atoms; and n is the same or different and is a value from 0 to 8. This disclosure also provides processes for producing the aryl ether compounds, lubricating oil basestocks and lubricating oils containing one or more of the aryl ether compounds, and a method for improving one or more of solubility and dispersancy of polar additives and/or sludge in a lubricating oil by using as the lubricating oil a formulated oil containing one or more of the aryl ether compounds.
    本公开提供了由式(1)表示的低黏度、低挥发性芳基醚化合物和由式(2)表示的低黏度、低挥发性芳基醚化合物:其中R1相同或不同,是具有1至20个碳原子的线性或支链烷基基团;R2相同或不同,是氢或具有1至4个碳原子的烷基基团;n相同或不同,是0至8的值。本公开还提供了制备芳基醚化合物的方法、含有一种或多种芳基醚化合物的润滑油基础油和润滑油,以及通过使用含有一种或多种芳基醚化合物的配方油作为润滑油,来改善极性添加剂和/或沉淀物的溶解度和分散性的方法。
  • PROCESS FOR THE PREPARATION OF CYCLIC ESTERS AND METHOD FOR PURIFICATION OF THE SAME
    申请人:KUREHA KAGAKU KOGYO KABUSHIKI KAISHA
    公开号:EP1310496A1
    公开(公告)日:2003-05-14
    The present invention provides a process for production of a cyclic ester by depolymerization of an aliphatic polyester. In the process, a mixture containing the aliphatic polyester and a specific polyalkylene glycol ether, which has a boiling point of 230-450°C and a molecular weight of 150-450, is heated under normal or reduced pressure to a temperature at which depolymerization of the aliphatic polyester takes place. Then, a substantially homogeneous solution phase, consisting of the melt phase of the aliphatic polyester and the liquid phase of the polyalkylene glycol ether, is formed. Heating of the solution phase is continued to form the cyclic ester by depolymerization and distil out the cyclic ester together with the polyalkylene glycol ether, and then the cyclic ester is recovered from the distillate. The present invention also provides a process for purification of a crude cyclic ester by use of the specific polyalkylene glycol ether described above.
    本发明提供了一种通过脂肪族聚酯解聚生产环酯的工艺。在该工艺中,将含有脂肪族聚酯和特定聚亚烷基乙二醇醚(沸点为 230-450°C,分子量为 150-450)的混合物在常压或减压下加热至脂肪族聚酯发生解聚的温度。然后形成基本均匀的溶液相,该溶液相由脂肪族聚酯的熔体相和聚亚烷基二醇醚的液相组成。继续加热溶液相,通过解聚作用形成环酯,并将环酯和聚烷基乙二醇醚一起蒸馏出来,然后从蒸馏物中回收环酯。本发明还提供了一种通过使用上述特定聚亚烷基二醇醚提纯粗环酯的工艺。
  • METHOD FOR PRODUCING GLYCOLIDE
    申请人:Kureha Corporation
    公开号:EP2377858A1
    公开(公告)日:2011-10-19
    The invention provides a production process of glycolide comprising the respective steps of: Step 1 of heating a mixture containing a glycolic acid oligomer and a high boiling polar organic under normal or reduced pressure to reflux the mixture and at that time, conducting a total reflux operation in a reflux time within a range of 0.1 to 20 hours under conditions that substantially the whole amount of a distillate distilled out of a reflux system containing the mixture is refluxed into the reflux system; Step 2 of heating the mixture after the total reflux operation or a mixture obtained by adding the high boiling polar organic solvent to a glycolic acid oligomer component recovered from the mixture after the total reflux operation to conduct depolymerization; and Step 3 of collecting glycolide from a co-distillate.
    本发明提供了一种羟基乙酸的生产工艺,包括以下步骤:步骤 1 在常压或减压下加热含有羟基乙酸低聚物和高沸点极性有机物的混合物,使混合物回流,然后进行全回流操作,回流时间在 0.1至20小时的条件下,从含有该混合物的回流系统中蒸馏出的蒸馏物基本上全部回流到该回流系统中;步骤2加热全回流操作后的混合物或将高沸点极性有机溶剂加入到全回流操作后从该混合物中回收的乙醇酸低聚物组分而得到的混合物,以进行解聚;以及步骤3从共蒸馏物中收集乙二醇醚。
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