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    • 2. 发明授权
    • Mouthpiece with coupler
    • 带耦合器的嘴
    • US06263871B1
    • 2001-07-24
    • US09558181
    • 2000-04-26
    • Richard I. BrownDavid S. Brown
    • Richard I. BrownDavid S. Brown
    • B63C1102
    • B63C11/2227A62B9/06B63C11/186
    • A mouthpiece is provided having a quick connect coupler to facilitate the rapid replacement of mouthpieces for use with breathing devices that may be used by many different individuals, such as in diver training classes and rental operations. In a preferred embodiment, the mouthpiece has a coupler including a pin to engage and lock with a slot in an opening of the regulator housing. The mouthpiece can further include one-way inhalation and exhalation pathways to prevent pathogenic entities in the exhalation and saliva of the diver from contaminated the body of the regulator. An exhaust tee is provided to direct bubbles away from the diver's line of vision. The regulator housing can further include an independent exhaust valve opening. A seal is provided to prevent the regulator body from flooding through the exhaust valve opening when the regulator is used with a mouthpiece having its own exhalation pathway. A flapper valve replaces the exhaust valve opening seal to permit conventional operation when the regulator is used with a conventional mouthpiece after being taken out of service for use by multiple users.
    • 提供了一种具有快速连接联接器的接口,以便于快速更换用于与多个不同人员(例如潜水员训练课程和租赁操作)可能使用的呼吸装置一起使用的吸嘴。 在优选实施例中,接口管具有联接器,该联接器包括销,以在调节器壳体的开口中与槽接合和锁定。 吸嘴还可以包括单向吸入和呼气途径,以防止潜水员的呼出和唾液中的病原体污染调节器的体内。 提供排气三通以引导泡沫远离潜水员的视线。 调节器壳体还可包括独立的排气门开口。 当调节器与具有其自身呼气路径的接口管一起使用时,提供密封件以防止调节器主体通过排气阀开口淹没。 当调节器在停止使用以供多个用户使用之后,当调节器与常规接口管一起使用时,挡板阀替代排气阀打开密封件以允许常规操作。
    • 3. 发明授权
    • Condenser operation with isolated on-line test loop
    • 冷凝器操作与孤立的在线测试回路
    • US5060600A
    • 1991-10-29
    • US566222
    • 1990-08-09
    • David S. BrownW. Cave Baum
    • David S. BrownW. Cave Baum
    • F01K21/06F22D11/00F28B1/02F28B11/00
    • F22D11/006F01K21/06F28B1/02F28B11/00
    • A condenser structure wherein both ends of at least one tube, which is physically located among the other (numerous) tubes of the condenser's tube bundles, is not connected to the inlet water box nor to the outlet water box; instead, this tube is provided with separate inlet and outlet connections. The separate inlet connection is preferably provided with a separately-controlled admixture of water treatment chemicals. Also disclosed is an innovative method of operating a steam condenser. One or more tubes, which are physically located among the other (numerous) tubes of the condenser, are isolated to provide a real-time test loop. The tube thus isolated is chosen to be among the tubes with the highest heat load, so that this tube provides a worst-case proxy for scaling in the other condenser tubes. The isolated tube is frequently inspected for scaling (e.g. at intervals of a week or so), and addition of anti-scaling chemicals to the cooling water is controlled with reference to the scaling (or lack thereof) seen in the isolated tube. Preferably the level of treatment chemicals is held at a lower level in the isolated test loop than in the primary cooling water supply.
    • 冷凝器结构,其中物理上位于冷凝器管束的另一(多个)管中的至少一个管的两端不连接到入口水箱或出水箱; 相反,该管设有独立的入口和出口连接。 单独的入口连接件优选地设置有单独控制的水处理化学品的混合物。 还公开了一种操作蒸汽冷凝器的创新方法。 物理上位于冷凝器的其它(多个)管中的一个或多个管被隔离以提供实时测试回路。 这样隔离的管被选择在具有最高热负荷的管之中,使得该管提供了在另一个冷凝器管中的最佳代理。 经常检查隔离管的结垢(例如以一周左右的间隔),并且参照在隔离的管中看到的结垢(或不存在)来控制向冷却水中加入防垢化学物质。 优选地,处理化学品的水平在隔离的测试环路中比在一级冷却水供应中保持在较低水平。
    • 7. 发明授权
    • Purifying feed for reforming over zeolite catalysts
    • 用于在沸石催化剂上重整的净化进料
    • US5106484A
    • 1992-04-21
    • US629879
    • 1990-12-19
    • Murray NadlerJohn F. WalshDavid S. Brown
    • Murray NadlerJohn F. WalshDavid S. Brown
    • C10G35/06C10G45/04C10G45/06C10G45/12C10G50/00C10G61/06C10G67/06C10G67/14C10G69/08
    • C10G61/06C10G67/06C10G69/08
    • The present invention is directed to a process for treating hydrotreated naphtha which involves treating the naphtha over massive nickel catalyst followed by treating the naphtha over a metal oxide under conditions effective for removing impurities from said naphtha to result in substantially purified naphtha, wherein the metal oxide is selected from the group of metal oxides having a free energy of formation of sulfide which exceeds said free energy of formation of platinum sulfide, such as manganous oxide. In so doing, naphtha in the gas phase in the presence of hydrogen is passed over the manganous oxide at a temperature within the range of about 800.degree. F. and 1100.degree. F., a hydrogen to oil molar ratio between about 1:1 and 6:1, a whsv between about 2 and 8, and pressure between about 50 and 300 psig; and the naphtha in the liquid phase at a temperature between about 300.degree. F. and about 350.degree. F., and whsv less than about 5 is passed over the massive nickel.The naphtha in the liquid phase, at about ambient temperature, and at a whsv between 2 and 10, may also be passed over a Na Y mole sieve prior to treating over massive nickel and manganous oxide. In addition the naphtha be being passed over alumina after treating over massive nickel and prior to treating over manganous oxided in the liquid phase, at a temperature between 300.degree. F. and 350.degree. F., and a whsv between 2 and 10.The naphtha may also be passed over a mole sieve water trap in the liquid phase at ambient temperature and at a whsv between 2 and 10, prior to treating over massive nickel and manganous oxide.
    • 本发明涉及一种处理加氢处理的石脑油的方法,该方法涉及在大量镍催化剂上处理石脑油,然后在有效去除所述石脑油杂质的条件下在金属氧化物上处理石脑油,导致基本上纯化的石脑油,其中金属氧化物 选自具有形成硫化物的自由能的金属氧化物的组,其超过形成硫化铂的所述自由能,例如氧化锰。 在这样做的过程中,氢气存在下的气相中的石脑油在约800°F至1100°F的温度范围内通过二氧化锰,氢与油的摩尔比约为1:1至 6:1,约2至8之间的压力,压力在约50至300psig之间; 并且液相中的石脑油在约300°F至约350°F之间,小于约5°的温度通过块状镍。 液相中的石脑油在约环境温度和2至10秒之间也可以通过Na Y摩尔筛,然后处理大量的镍和氧化锰。 此外,石脑油在处理大量镍之后,在液相中处理过氧化锰之前,在300°F至350°F的温度和2至10°之间的范围内,通过氧化铝。石脑油 也可以在处理大量镍和氧化锰之前在环境温度和2至10℃之间的液相中通过摩尔筛捕集器。