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    • 21. 发明申请
    • System and method of updating data in a contactless flash memory device
    • 更新非接触式闪存设备中的数据的系统和方法
    • US20070283078A1
    • 2007-12-06
    • US11444922
    • 2006-06-01
    • Jun LiRiddhiman GhoshKave EshghiThomas Rathbone
    • Jun LiRiddhiman GhoshKave EshghiThomas Rathbone
    • G06F12/00
    • G06F12/0866G06F8/65G06F2212/2022
    • A flash memory device is powered via an RF field generated by a host unit. A contactless communication channel is established between the flash memory device and the host unit. A first version of a data file, including a first plurality of data chunks, is downloaded from the flash memory device to the host unit. A second version of the data file, including a second plurality of data chunks, is generated at the host unit. Data chunk modifications to the first plurality of data chunks necessary to generate the second plurality of data chunks are identified at the host unit. The contactless communication channel is reestablished. The identified data chunk modifications to the first plurality of data chunks are performed thereby updating the first version of the data file stored on the flash memory device to the second version of the data file.
    • 闪存器件由主机单元产生的RF场供电。 在闪存设备和主机单元之间建立非接触通信信道。 将包括第一多个数据块的数据文件的第一版本从闪存设备下载到主机单元。 在主机单元处生成包括第二多个数据块的数据文件的第二版本。 在主机单元处识别生成第二多个数据块所必需的第一多个数据块的数据块修改。 非接触式通信通道重新建立。 执行对第一多个数据块的所识别的数据块修改,由此将存储在闪存设备上的数据文件的第一版本更新为数据文件的第二版本。
    • 23. 发明授权
    • Air separation
    • 空气分离
    • US5715706A
    • 1998-02-10
    • US697756
    • 1996-08-29
    • Thomas Rathbone
    • Thomas Rathbone
    • F25J3/04
    • F25J3/04466F25J3/04296F25J3/04412F25J3/04448F25J2200/06F25J2200/08F25J2200/20F25J2200/50F25J2200/54F25J2200/90F25J2205/02F25J2235/50F25J2250/42F25J2250/52Y10S62/90
    • Cooled and purified air is introduced into a higher pressure rectification column and separated into oxygen-enriched liquid and nitrogen vapour. A stream of the oxygen-enriched liquid is flashed through a pressure reducing valve to form a mixture of liquid further enriched in oxygen and vapour depleted of oxygen. The liquid is reboiled by reboiler. A stream of the further enriched liquid is reboiled in condenser and is introduced into a lower pressure rectification column for separation into oxygen and nitrogen products. Reflux for the columns and is formed by condensing in condenser nitrogen vapour separated in the higher pressure rectification column. A reboiler provides an upward flow of vapour through the column. The condenser and reboiler take the form of a single heat exchanger. The reboiler is located in a phase separator, the reboiler is located in a rectification column containing liquid-vapour contact devices above the level at which fluid issuing from the valve is introduced. Oxygen-depleted vapour is condensed in the condenser by heat exchange with the further enriched liquid and at least some of the resulting condensate introduced into the lower pressure rectification column.
    • 将冷却纯化的空气引入高压精馏塔中,分离成富氧液体和氮气蒸气。 富氧液体流通过减压阀闪蒸,形成进一步富含氧和蒸气的氧气的液体混合物。 液体通过再沸器再沸腾。 将进一步富集的液体的物流在冷凝器中再沸腾并引入低压精馏塔中以分离成氧气和氮气产物。 通过冷凝在高压精馏塔中分离的冷凝器中形成冷凝塔。 再沸器通过塔提供向上的蒸汽流。 冷凝器和再沸器采取单个热交换器的形式。 再沸器位于相分离器中,再沸器位于精馏塔中,该精馏塔含有液体 - 蒸汽接触装置,高于从阀引发流体的液位。 通过与另外的富集液体的热交换和被引入低压精馏塔的至少一些所得的冷凝物在冷凝器中冷凝贫氧蒸汽。
    • 24. 发明授权
    • Air separation
    • 空气分离
    • US5582035A
    • 1996-12-10
    • US533199
    • 1995-09-25
    • Thomas RathboneJohn T. LavinDavid Stuart
    • Thomas RathboneJohn T. LavinDavid Stuart
    • F25J3/04
    • F25J3/04466F25J3/04296F25J3/04412F25J3/04448F25J2200/08F25J2200/20F25J2205/02Y10S62/90Y10S62/94
    • Cooled and purified air is introduced into a higher pressure rectification column and separated into oxygen-enriched liquid and nitrogen vapor. A stream of the oxygen-enriched liquid is flashed through a pressure reducing valve to form a mixture of liquid further enriched in oxygen and vapor depleted of oxygen. The liquid is reboiled by reboiler. A stream of the further enriched liquid is reboiled in condenser and is introduced into a lower pressure rectification column for separation into oxygen and nitrogen products. Reflux for the columns and is formed by condensing in condenser nitrogen vapor separated in the higher pressure rectification column. A reboiler provides an upward flow of vapor through the column. The condenser and reboiler take the form of a single heat exchanger. The reboiler is located in a phase separator, the reboiler is located in a rectification column containing liquid-vapor contact devices above the level at which fluid issuing from the valve is introduced. Oxygen-depleted vapor is condensed in the condenser by heat exchange with the further enriched liquid and at least some of the resulting condensate introduced into the lower pressure rectification column.
    • 将冷却纯化的空气引入高压精馏塔中,分离成富氧液体和氮气蒸气。 富氧液体流通过减压阀闪蒸,形成进一步富含氧和蒸气的氧气的液体混合物。 液体通过再沸器再沸腾。 将进一步富集的液体的物流在冷凝器中再沸腾并引入低压精馏塔中以分离成氧气和氮气产物。 通过冷凝在高压精馏塔中分离的冷凝器中形成冷凝塔。 再沸器通过塔提供向上的蒸汽流。 冷凝器和再沸器采取单个热交换器的形式。 再沸器位于相分离器中,再沸器位于精馏塔中,该精馏塔含有液体 - 蒸汽接触装置,高于从阀引发流体的液位。 通过与另外的富集液体的热交换和被引入低压精馏塔的至少一些所得的冷凝物在冷凝器中冷凝贫氧蒸汽。
    • 25. 发明授权
    • Air separation
    • 空气分离
    • US5572874A
    • 1996-11-12
    • US488920
    • 1995-06-09
    • Thomas Rathbone
    • Thomas Rathbone
    • F25J3/04
    • F25J3/04715F25J3/0409F25J3/042F25J3/04296F25J3/04303F25J3/04393F25J2200/08F25J2200/10F25J2200/50F25J2215/50F25J2235/50F25J2235/58F25J2240/40Y10S62/924
    • Air is introduced through an inlet into a higher pressure rectification column. A stream of oxygen-enriched liquid is withdrawn through an outlet from the higher pressure rectification column. A part of this stream is introduced into a low pressure rectification column through an inlet. The stream is separated in the column low pressure rectification into oxygen and nitrogen. In addition, an argon-enriched vapor stream is withdrawn from the low pressure rectification column through an outlet, and is at least partially condensed in a reboiler-condenser which reboils oxygen separated in an argon column. One part of the resulting at least partially condensed argon-enriched oxygen stream is reduced in pressure by passage through a valve and is introduced through an inlet into an intermediate mass exchange region of the argon column in which it is separated into argon and oxygen. Another part of the at least partially condensed argon-enriched oxygen stream is returned by a pump to the low pressure rectification column.
    • 空气通过入口引入高压精馏塔。 富氧液体流通过高压精馏塔的出口排出。 该流的一部分通过入口引入低压精馏塔。 在塔中将流分离成低压精馏成氧和氮。 另外,通过出口从低压精馏塔排出富氩蒸汽流,并在再沸器 - 冷凝器中至少部分冷凝,再沸器在氩气塔中分离氧。 所得到的至少部分冷凝的富氩氧气流的一部分通过阀通过压力减小,并通过入口引入氩塔的中间质量交换区域,在其中将其分离成氩气和氧气。 至少部分冷凝的富氩氧流的另一部分由泵返回到低压精馏塔。
    • 26. 发明授权
    • Air separation
    • 空气分离
    • US5551258A
    • 1996-09-03
    • US563554
    • 1995-11-28
    • Thomas Rathbone
    • Thomas Rathbone
    • F25J3/04F25J3/02
    • F25J3/042F25J3/0409F25J3/04212F25J3/04296F25J3/04303F25J3/04345F25J3/04418F25J3/0446F25J2200/04F25J2200/20F25J2200/54F25J2205/02F25J2235/50F25J2250/20
    • A stream of air is compressed in compressor and has water vapor and carbon dioxide removed therefrom in purification unit. A part of the resulting purified air is cooled by passage through heat exchanger and is employed to heat an intermediate reboiler in a lower pressure rectification column. The air flow from the reboiler passes into a higher pressure rectification column which supplies a stream of oxygen-enriched liquid air for separation in the lower pressure rectification column. Liquid nitrogen reflux for the higher pressure column is provided by taking nitrogen vapor from this column through an outlet and condensing it in another intermediate reboiler located above the reboiler in the lower pressure rectification column. The condensed nitrogen is returned to the top of the column. Another air stream is employed to reboil a further reboiler at the bottom of the lower pressure rectification column with the resulting condensed air stream being introduced into the higher pressure rectification column through an inlet. An impure oxygen product is withdrawn from the bottom of the lower pressure rectification column through outlet in liquid state and is vaporized in the heat exchanger. The arrangement of reboilers facilitates operation of the apparatus with a relatively low pressure ratio between the operating pressure of the higher pressure rectification column and that of the lower pressure rectification column.
    • 空气流在压缩机中被压缩并且在净化单元中从其中除去水蒸汽和二氧化碳。 所得纯化空气的一部分通过热交换器冷却并用于加热低压精馏塔中的中间再沸器。 来自再沸器的空气流进入高压精馏塔,其提供富氧液体空气流以在低压精馏塔中分离。 通过从该塔通过出口将氮蒸汽通过出口提供用于高压塔的液氮回流,并将其冷凝在位于低压精馏塔中的再沸器上方的另一个中间再沸器中。 冷凝的氮气返回到塔顶。 使用另一种空气流在低压精馏塔的底部再沸再沸器,所得的冷凝空气流通过入口引入高压精馏塔。 不纯的氧气产物通过液态出口从低压精馏塔的底部排出,并在热交换器中蒸发。 再沸器的布置有利于在高压精馏塔的操作压力和低压精馏塔的操作压力之间具有相对低的压力比的装置的操作。