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    • 111. 发明授权
    • Monomethyl paraffin adsorptive separation process
    • 单甲基石蜡吸附分离过程
    • US06222088B1
    • 2001-04-24
    • US09406430
    • 1999-09-27
    • Santi Kulprathipanja
    • Santi Kulprathipanja
    • C07C712
    • C11D11/04C07C2/76C07C7/13C07C15/00C11D1/14C11D1/29C07C9/00
    • Monomethyl branched C10-C15 paraffins or olefins are recovered from a mixture comprising other nonnormal hydrocarbons such as di-isoparaffins, di-isoolefins, naphthenes and aromatics by adsorptive separation in a process which includes a prepulse step. In the prepulse step nonnormal hydrocarbons which are readily separated from the product is passed into the adsorbent bed immediately before or with the feed stream. This increases the selectivity of the system and allows for easier separation of the desired hydrocarbons. The recovered monomethyl hydrocarbons may then be used to form a monomethyl branched alkylaromatic hydrocarbon useful as a detergent precursor.
    • 在包括预脉冲步骤的过程中,通过吸附分离从包含其它非正常烃如二异链烷烃,二异戊烯,环烷烃和芳族化合物的混合物中回收单甲基支链C10-C15烷烃或烯烃。 在预脉冲步骤中,容易与产物分离的非常规烃在紧邻进料流之前或之后进入吸附剂床。 这增加了系统的选择性,并且允许更容易地分离所需的烃。 然后可以使用回收的单甲基烃形成可用作洗涤剂前体的单甲基支链烷基芳族烃。
    • 119. 发明授权
    • Separation of 1,3-butadiene
    • 1,3-丁二烯的分离
    • US4567309A
    • 1986-01-28
    • US614935
    • 1984-05-29
    • Santi Kulprathipanja
    • Santi Kulprathipanja
    • C07C7/13C07C7/12
    • C07C7/13
    • A process for separating 1,3-butadiene from a feed mixture comprising 1,3-butadiene and at least one other C.sub.4 hydrocarbon. The process comprises contacting the feed, in liquid phase at adsorption conditions, with an adsorbent comprising activated or molecular sieve carbon which selectively adsorbs the 1,3-butadiene. The feed is then removed from the adsorbent and the 1,3-butadiene recovered by desorption at desorption conditions with a desorbent material comprising a hydrocarbon. The feed mixture and desorbent material have boiling points of at least 5.degree. C. difference.
    • 从包含1,3-丁二烯和至少一种其它C 4烃的进料混合物中分离1,3-丁二烯的方法。 该方法包括在吸附条件下液相中的进料与包含选择性吸附1,3-丁二烯的活性或分子筛碳的吸附剂接触。 然后将该进料从吸附剂中除去,并且通过在解吸条件下用包含烃的解吸剂材料解吸回收的1,3-丁二烯。 进料混合物和解吸剂材料的沸点至少为5℃。