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公开(公告)号:US4198865A
公开(公告)日:1980-04-22
申请号:US927712
申请日:1978-07-24
Applicant: William B. Tarpley, Jr. , Donald R. Culp
Inventor: William B. Tarpley, Jr. , Donald R. Culp
CPC classification number: G01N3/32 , G01N2203/0244 , G01N2203/0623 , G01N2291/02827
Abstract: The integrity of attachment of bolts in a substrate such as a wall of a mine is tested by introducing vibratory energy into an exposed end portion of the bolt and ascertaining the vibratory energy absorbed by the bolt and its attachment.
Abstract translation: 通过将振动能量引入螺栓的暴露端部并确定由螺栓及其附件吸收的振动能量来测试螺钉在诸如矿井壁的衬底中的连接的完整性。
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公开(公告)号:US08845863B2
公开(公告)日:2014-09-30
申请号:US12460752
申请日:2009-07-24
Applicant: Clarence P. Stadlwieser , Bernie B. Osborne , John P. Dever , Harvey E. Andresen , Michael L. Hutchison , Steven R. Osborne , Liping L. Zhang , Michael Habenschuss , Andrew Addie , Donald R. Culp
Inventor: Clarence P. Stadlwieser , Bernie B. Osborne , John P. Dever , Harvey E. Andresen , Michael L. Hutchison , Gary L. Culp , Steven R. Osborne , Liping L. Zhang , Michael Habenschuss , Andrew Addie
IPC: B01D3/00 , B01D3/14 , C07D301/32 , C07D303/00 , C07C43/00 , C07C31/18
CPC classification number: C07D301/32
Abstract: Processes and systems for purifying ethylene oxide, including introducing a feed stream including ethylene oxide to a heat exchanger to heat the feed stream, feeding the heated feed stream to a distillation apparatus base below a first stage, removing from the distillation apparatus an impurity fraction as a top exit stream from the distillation apparatus located at a top take-off on the distillation apparatus, removing from the distillation apparatus an ethylene oxide stream of 99.7 weight percent purity, based on the total weight of the ethylene oxide stream, from the distillation apparatus, and removing from the distillation apparatus an aldehyde enriched fraction as a bottom stream from the distillation apparatus, where the aldehyde enriched fraction is fed directly to a glycol reactor.
Abstract translation: 用于纯化环氧乙烷的方法和系统,包括将包含环氧乙烷的进料流引入热交换器以加热进料流,将加热的进料流输送到第一阶段以下的蒸馏装置底部,从蒸馏装置中除去杂质馏分如 来自位于蒸馏装置的顶部排出口的蒸馏装置的顶部出口物流,从蒸馏装置除去基于环氧乙烷料流的总重量为99.7重量%的纯度的环氧乙烷物流,来自蒸馏装置 ,并从蒸馏装置中将来自蒸馏装置的作为底部物流的富含醛的馏分除去,其中富含醛的馏分直接进料到二醇反应器中。
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