METHOD FOR SYNTHESIZING LACTIDE BY MEANS OF CATALYSIS OF LACTID ACID

    公开(公告)号:US20190047976A1

    公开(公告)日:2019-02-14

    申请号:US16078674

    申请日:2016-03-01

    CPC classification number: C07D319/12 B01J23/06 B01J35/0013 B01J35/10

    Abstract: The present invention relates to a method for the catalytic synthesis of lactide from lactic acid. The method relates to the synthesis of lactide from lactic acid under the catalysis of a zinc oxide nanoparticle aqueous dispersion as a catalyst. The present invention has four technical characteristics: I. the zinc oxide nanoparticle aqueous dispersion catalyst has a sufficient surface area, and the size of nanoparticles is merely 30-40 nm, providing a sufficient contact area between the substrate (lactic acid) and the catalyst; II. the new catalyst has a milder catalytic effect on polymerization, allowing the molecular weight distribution of a prepolymer within a range of 400-1500 g/mol, which is advantageous for depolymerization to proceed; III. the new catalyst is stable, thus avoiding oxidation or carbonization in a high temperature reaction; and IV. the new catalyst has a low toxicity and a small threat to human health.

    HYDROTREATING CATALYST FOR HYDROCARBON OIL, PROCESS FOR PRODUCING SAME, AND HYDROTREATING METHOD

    公开(公告)号:US20180104676A1

    公开(公告)日:2018-04-19

    申请号:US15572278

    申请日:2016-04-07

    Abstract: Provided herein is a hydrotreating catalyst for hydrocarbon oil having high desulfurization activity, and high abrasion strength and high compressive strength. A process for producing the hydrotreating catalyst is also provided. The hydrotreating catalyst uses an alumina-phosphorus support. The support contains 0.5 to 2.0 mass % of phosphorus in terms of an oxide. The support loads a metal in Group 6A of the periodic table, and a metal in Group 8 of the periodic table. The hydrotreating catalyst has a specific surface area of 150 m2/g or more. The hydrotreating catalyst has a total pore volume of 0.40 to 0.75 ml/g as measured by a mercury intrusion method. The hydrotreating catalyst has two maximal peaks in a pore diameter range of 6 nm to 13 nm in a log differential pore volume distribution measured by a mercury intrusion method. The hydrotreating catalyst has an abrasion strength of 0.5% or less. The hydrotreating catalyst has a compressive strength of 15 N/mm or more. The support is produced from, for example, a hydrate obtained by adding phosphorus to an alumina hydrate obtained by using two mixtures of an acidic aqueous aluminum salt solution and a basic aqueous aluminum salt solution.

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