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    • 8. 发明授权
    • Catalytic production of lactide directly from lactic acid
    • 直接从乳酸催化生产丙交酯
    • US5332839A
    • 1994-07-26
    • US584466
    • 1990-09-18
    • Herman P. BeneckeRichard A. MarkleRichard G. Sinclair
    • Herman P. BeneckeRichard A. MarkleRichard G. Sinclair
    • B01J21/04B01J21/08C07B61/00C07D319/12
    • C07D319/12B01J2219/1942
    • The present invention is directed to a method for making lactide from aqueous lactic acid. The invention method comprises converting feed aqueous lactic acid to its vapor phase. The feed vapors then are passed through a reactor maintained at elevated temperature and in which optionally is disposed an alumina catalyst. Withdrawn from the reactor is product lactide, water, and unreacted lactic acid which are subjected to separation for recovery of the lactide product. The separated unreacted lactic acid is eligible for readmission to the process for making additional lactide. This cyclic process embodiment of the present invention comprises the steps of passing make-up aqueous lactic acid feed into a vaporization zone along with unreacted aqueous lactic acid filtrate from another step of the process and therein forming aqueous lactic acid feed vapors. The thus-generated vapors that are passed through a vapor phase reaction zone held at elevated temperature for forming lactide therein. Lactide as a solid is separated from unreacted aqueous lactic acid filtrate; and the filtrate is passed into the vaporization zone in the initial step of the process.
    • 本发明涉及从乳酸水溶液制备丙交酯的方法。 本发明的方法包括将进料水乳酸转化成其气相。 然后将进料蒸气通过保持在升高温度下的反应器,并且其中任选地设置氧化铝催化剂。 从反应器中抽出的是产品丙交酯,水和未反应的乳酸,它们进行分离以回收丙交酯产物。 分离的未反应的乳酸有资格重新进入制备额外的丙交酯的方法。 本发明的循环方法实施方案包括以下步骤:将乳酸含水原料与来自该方法的另一步骤的未反应的乳酸水溶液一起送入蒸发区,并形成含水乳酸进料蒸气。 由此产生的蒸气通过保持在升高的温度下的气相反应区以在其中形成丙交酯。 作为固体的丙交酯与未反应的乳酸水溶液分离; 并且在该过程的初始步骤中将滤液进入蒸发区。
    • 9. 发明授权
    • Lactide production from dehydration of aqueous lactic acid feed
    • 乳酸生产脱水乳酸饲料
    • US5274127A
    • 1993-12-28
    • US584126
    • 1990-09-18
    • Richard G. SinclairRichard A. MarkleRussell K. Smith
    • Richard G. SinclairRichard A. MarkleRussell K. Smith
    • C07D319/12C08J5/18C08L67/04C09D167/04C07D319/00
    • C08J5/18C07D319/12C08L67/04C09D167/04B01J2219/1942C08J2367/04
    • The present invention is directed to a method for making L-lactide from aqueous L-lactic acid. Aqueous lactic acid feed for present purposes comprehends an aqueous mixture of one or more of L.sub.1 A, L.sub.2 A, and L.sub.3 A, optionally with LD being present. L-lactic acid is the preferred feed configuration for making L-lactide, and is to be understood even though the configuration symbol is not used throughout this application. Aqueous lactic acid feed is treated for removal of water therefrom until a degree of polymerization (DP) not substantially above about 2 is reached. The treatment then is ceased to produce a crude LD product. LD then is separated from the crude LD product. A preferred treatment involves heating the feed at elevated temperature to remove water. LD can be separated from the crude LD product by a variety of techniques to produce an LD-depleted product. This LD-depleted product, optionally augmented with additional aqueous lactic acid and/or water then can be readmitted to the process for making additional lactide. This cyclic or recycle process embodiment of the present invention enables very high lactide conversions to be realized.
    • 本发明涉及从L-乳酸水溶液制备L-丙交酯的方法。 用于本发明目的的乳酸乳液饲料包括L1A,L2A和L3A中的一种或多种的任何含水混合物,任选地存在LD。 L-乳酸是用于制备L-丙交酯的优选进料构型,并且即使在本申请中不使用配置符号也将被理解。 处理水性乳酸进料以从中除去水,直到达到基本上不超过约2的聚合度(DP)。 然后处理停止生产粗制LD产品。 然后将LD与粗LD产物分离。 优选的处理包括在升高的温度下加热进料以除去水。 LD可以通过各种技术与粗LD产物分离以产生LD-贫化的产物。 然后,任选地用另外的乳酸和/或水增加的LD-贫化产物可以重新进入用于制备额外的丙交酯的方法。 本发明的这种循环或再循环方法实现了能够实现非常高的丙交酯转化。
    • 10. 发明授权
    • Process for producing an expandable silicone resin
    • 生产可膨胀硅树脂的方法
    • US4467053A
    • 1984-08-21
    • US566276
    • 1983-12-28
    • Richard A. Markle
    • Richard A. Markle
    • C08J9/16C08J9/00C08J9/02C08J9/10
    • C08J9/02C08J9/0066C08J9/10C08J2383/04
    • A process for the production of an expandable silicone resin includes reacting a substantial amount of the silanol (SiOH) groups present in the resin to form siloxane bonds and water, and heating the resin to a temperature above the resin's melting point, at which chemical reaction (condensation) of the silanol groups occur. The reaction increases the molecular weight of the resin and decreases the amount of water that must be removed during a subsequent foaming step, thereby controlling the rate and extent of foaming which can occur. The resin is solidified, pulverized and size-reduced to a powder form. The resin powder is blended with a minor amount of a particulate inert filler which is coated with a silicone resin curing catalyst and also with a minor amount of blowing agent (powder). The dry powder blend is then thermally fused for a closely-controlled, short duration, time at a temperature near the lower end of the blowing agent's gas-generating temperature range. The fused mass is ground to a powdered form to produce an expandable resin.
    • 制造可发性硅树脂的方法包括使大量存在于树脂中的硅烷醇(SiOH)基团与硅氧烷键和水反应,并将树脂加热到高于树脂熔点的温度,在该温度下,化学反应 (缩合)出现硅烷醇基团。 该反应增加了树脂的分子量,并减少了在随后的发泡步骤期间必须除去的水量,从而控制了可能发生的发泡速率和程度。 将树脂固化,粉碎并减小至粉末形式。 将树脂粉末与少量的用有机硅树脂固化催化剂和少量发泡剂(粉末)涂覆的惰性惰性填料混合。 然后将干粉混合物在接近发泡剂产气温度范围下端的温度下进行热熔融以达到紧密控制的短时间。 将熔融物质研磨成粉末形式以产生可发性树脂。