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    • 1. 发明授权
    • Enhanced utilization of power over ethernet
    • 提高以太网供电能力
    • US08930729B1
    • 2015-01-06
    • US12345629
    • 2008-12-29
    • David FifieldDennis Wu
    • David FifieldDennis Wu
    • G06F1/26G06F1/18H04L12/24
    • G06F1/26G06F1/18H04L12/10Y02D50/00
    • An embodiment of the invention includes a circuit to determine the power lost between a network device and a network power supply. Using this determination, an embodiment of the network device may increase its power consumption by an amount equal to the difference between the actual cable power loss and the worst-case cable power loss. This allows the network device to draw more power than allowed by network power standards without triggering the power-limiting circuitry of the network power source or overloading the network power device. The network device can determine an operating configuration that utilizes this additional power consumption to improve performance. The network device may also determine the existence of network power device or cable fault conditions, and adjust its operating configuration as necessary. Operating configurations can include enabling additional or more powerful wired or wireless network interfaces.
    • 本发明的实施例包括确定网络设备和网络电源之间的功率损耗的电路。 使用该确定,网络设备的实施例可以将其功率消耗增加等于实际电缆功率损耗和最坏情况的电缆功率损耗之间的差值。 这允许网络设备比网络电源标准允许的功率更多,而不会触发网络电源的功率限制电路或者超载网络电源设备。 网络设备可以确定利用该额外功耗的操作配置来提高性能。 网络设备还可以确定网络功率设备或电缆故障状况的存在,并根据需要调整其操作配置。 操作配置可以包括启用附加或更强大的有线或无线网络接口。
    • 2. 发明授权
    • Process for forming cyclopentane from dicyclopentadiene
    • 从二环戊二烯形成环戊烷的方法
    • US5998683A
    • 1999-12-07
    • US899544
    • 1997-07-24
    • James R. LattnerC. Harry McMullenLeonel E. SanchezSteven E. SilverbergTronze-I Dennis Wu
    • James R. LattnerC. Harry McMullenLeonel E. SanchezSteven E. SilverbergTronze-I Dennis Wu
    • C07B61/00C07C5/03C07C13/10C07C4/02C07C4/22
    • C07C13/10C07C5/03C07C2101/08C07C2521/04C07C2523/44C07C2523/755C07C2523/882C07C2523/883C08G2101/0025C08G2101/005
    • A method for producing a cyclopentane product which comprises the following steps: (a) cracking dicyclopentadiene to form a cyclopentadiene-rich stream and a higher boiling liquids stream; (b) separating the cyclopentadiene-rich stream from the higher boiling liquids stream; (c) diluting the cyclopentadiene-rich stream with recycled saturates such that the cyclopentadiene content is limited to between about 5-50%; (d) conducting a first hydrogenation of the cyclopentadiene-rich stream in the presence of hydrogen and a first catalyst, and at a temperature (i.e., preferably between about 26 to 94.degree. C., more preferably in the range between about 37 to 66.degree. C.) which is capable of avoiding the repolymerization of cyclopentadiene to dicyclopentadiene, thereby forming a cyclopentadiene-depleted stream; (e) conducting a second hydrogenation of the cyclopentadiene-depleted stream in the presence of a second catalyst wherein any residual olefins and/or cyclopentadiene contained within the cyclopentadiene-depleted stream are saturated, thereby forming a crude cyclopentane product; and (f) flash stripping the crude cyclopentane product to form the cyclopentane product comprising about 95% pure cyclopentane.
    • 一种生产环戊烷产物的方法,包括以下步骤:(a)裂解二环戊二烯以形成富含环戊二烯的料流和较高沸点的液体料流; (b)从较高沸点的液体物流中分离富含环戊二烯的物流; (c)用循环的饱和物稀释富含环戊二烯的流,使得环戊二烯含量限制在约5-50%之间; (d)在氢和第一催化剂的存在下,在一个温度(即,优选在约26至94℃之间,更优选约37至66℃的范围内)对富环戊二烯物流进行第一次氢化 DEG),其能够避免环戊二烯重新聚合成二环戊二烯,由此形成环戊二烯贫化的流; (e)在第二催化剂存在下进行环戊二烯贫化物流的第二次氢化,其中包含在环戊二烯贫化物流内的任何残留烯烃和/或环戊二烯都是饱和的,从而形成粗环戊烷产物; 和(f)快速汽提粗环戊烷产物以形成包含约95%纯环戊烷的环戊烷产物。