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    • 2. 发明授权
    • Process for producing ethylene glycol
    • 生产乙二醇的方法
    • US4412084A
    • 1983-10-25
    • US352919
    • 1982-02-26
    • John Kollar
    • John Kollar
    • C07C31/00C07C29/32C07C29/38C07C31/20C07C29/00
    • C07C29/32C07C29/38C07C31/20
    • In the preparation of ethylene glycol by reacting methanol, formaldehyde and an organic peroxide, improved yields of ethylene glycol are achieved by the reaction of portions of the total amounts of formaldehyde and peroxide to be reacted with methanol. Formaldehyde and peroxide are incrementally added to a liquid medium containing methanol in controlled amounts during the reaction to permit conversion of each portion of said formaldehyde and peroxide reactants prior to the next addition. The portions are added such that the concentration of glycol in the reaction medium to which a later portion is added is greater than that to which an earlier portion is added. The reaction is continued until all the formaldehyde and peroxide has been incrementally added to the reaction medium and subjected to reaction conditions for a suitable period of time.
    • 在通过使甲醇,甲醛和有机过氧化物反应制备乙二醇时,通过甲醛和过氧化物的总量的一部分与甲醇反应来实现乙二醇的提高。 甲醛和过氧化物在反应过程中以受控量逐渐加入到含有甲醇的液体培养基中,以允许在下次加入之前转化所述甲醛和过氧化物反应物的每一部分。 加入部分,使得添加了较后部分的反应介质中的二醇浓度大于加入较早部分的二醇浓度。 继续反应直到所有甲醛和过氧化物已经逐渐加入到反应介质中并经受适当时间的反应条件。
    • 6. 发明授权
    • Preparation of dialkyl peroxides
    • 二烷基过氧化物的制备
    • US07034189B1
    • 2006-04-25
    • US08567564
    • 1995-12-05
    • John Kollar
    • John Kollar
    • C07C409/00
    • C07C409/16C07C407/00
    • A process is disclosed for the preparation of a dialkyl peroxide comprising reacting one or more members selected from the group consisting of an alkylating alcohol of the formula ROH, and an olefin of the formula (R2)(R2a)C═C(R3)(R3a), wherein R is C1–C10 allyl, and R2, R2a, R3, and R3a are independently selected from hydrogen and C1–C10 alkyl; with a hydroperoxide of the formula R1OOH, wherein R1 is C1–C10 allyl; in the presence of an effective amount of a substantially solid, insoluble, heterogenous acidic catalyst; followed by separation of the reaction mixture from said catalyst; wherein said catalyst has readily available acidity for organic reactions and exists in the solid phase in the processes of the invention, while the reactants in those processes, by contrast, exist in the liquid and/or gaseous phase, whence the catalyst is referred to as heterogeneous.
    • 公开了一种制备二烷基过氧化物的方法,包括使一种或多种选自式ROH的烷基化醇和式(R 2)的烯烃(R 2) CC(R 3)(R 3a)其中R是C 1 -C 3烷基, 10个烯丙基,R 2,R 2,R 3,R 3和R 3a独立地为 选自氢和C 1 -C 10烷基; 与式R 1 OOH的氢过氧化物反应,其中R 1是C 1 -C 10烯丙基; 在有效量的基本上固体的,不溶的,异质的酸性催化剂的存在下; 然后将反应混合物从所述催化剂中分离出来; 其中所述催化剂对于有机反应具有容易获得的酸性并且存在于本发明方法的固相中,而相反,这些方法中的反应物存在于液体和/或气相中,因为催化剂被称为 异质。
    • 7. 发明授权
    • Process for treatment of waste gas from a cyclohexane oxidation reactor
    • 用于处理来自环己烷氧化反应器的废气的方法
    • US5505920A
    • 1996-04-09
    • US318010
    • 1994-10-04
    • John KollarGotz-Gerald BorgerMatthias Stenger
    • John KollarGotz-Gerald BorgerMatthias Stenger
    • B01D53/14C01B31/20C10K1/10
    • B01D53/1487
    • The present invention relates to a process for the treatment of waste gas discharged from a cyclohexane oxidation reactor used in the manufacture of adipic acid, said waste gas containing mainly nitrogen, oxygen, carbon monoxide, carbon dioxide, acetic acid, and up to 10% by weight cyclohexane, as well as other gases or vapors, by (a) scrubbing the waste gas from the cyclohexane oxidation reactor with acetic acid in a first absorption step to reduce the amount of cyclohexane to a residual content of less than about 1% by weight, (b) scrubbing the waste gas from the first absorption step with water in a second absorption step to reduce the amount of acetic acid to a residual content of less than about 1% by weight, and (c) subjecting the scrubbed waste gas from the second absorption step to an oxidation step to oxidize carbon monoxide and other oxidizable components of the waste gas to carbon dioxide and water.
    • 本发明涉及一种处理从用于制造己二酸的环己烷氧化反应器排出的废气的处理方法,所述废气主要包含氮气,氧气,一氧化碳,二氧化碳,乙酸,以及高达10% (a)在第一吸收步骤中用乙酸洗涤来自环己烷氧化反应器的废气,将环己烷的量减少到小于约1%的残留含量,通过 (b)在第二吸收步骤中用水洗涤来自第一吸收步骤的废气以将乙酸的量减少至小于约1重量%的残留含量,和(c)对经洗涤的废气 从第二吸收步骤到氧化步骤,将废气中的一氧化碳和其它可氧化组分氧化成二氧化碳和水。