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    • 3. 发明申请
    • Central processor for memory tag
    • 中央处理器的内存标签
    • US20060123186A1
    • 2006-06-08
    • US11294479
    • 2005-12-06
    • Weng LohFraser DickinThomas Rathbone
    • Weng LohFraser DickinThomas Rathbone
    • G06F12/00
    • G06F9/30101
    • This invention provides a processor 200, especially for use as the central processing unit of a memory tag 1200. The processor 200 has a minimal footprint in Silicon or other suitable material. It also is driven by the data that it receives. The processor includes a plurality 206, 212, 214, 224 of registers configured to receive in parallel data that are input to the processor, and to process in parallel the received data, and a micro sequencer and instruction decoder module 202 adapted to select two or more of the plurality of registers to receive the data that are input to the processor, and to control the processing of the received data by the end or more selected registers. A memory 1200 device utilising such a processor, and a method of processing instructions are also provided
    • 本发明提供一种处理器200,特别是用作存储器标签1200的中央处理单元。 处理器200在硅或其它合适的材料中具有最小的占地面积。 它也由它接收的数据驱动。 处理器包括多个寄存器206,212,214,224,其被配置为并行地接收输入到处理器的数据,并且并行处理接收的数据;以及微定序器和指令解码器模块202,适于选择两个或 多个寄存器中的多个用于接收输入到处理器的数据,并且通过结束或更多选择的寄存器控制接收的数据的处理。 还提供了利用这种处理器的存储器1200设备,以及处理指令的方法
    • 4. 发明授权
    • Air separation
    • 空气分离
    • US5609041A
    • 1997-03-11
    • US572230
    • 1995-12-13
    • Thomas RathboneBrian A. Keenan
    • Thomas RathboneBrian A. Keenan
    • F25J3/04F25J3/00
    • F25J3/04169F25J3/04018F25J3/0409F25J3/04127F25J3/04303F25J3/04448F25J3/04545F25J3/04575F25J3/04606F25J2200/20F25J2200/50F25J2200/54F25J2200/90F25J2205/62F25J2240/42F25J2245/40
    • A first flow of air is compressed in a first air compressor associated with a gas turbine and is purified in an adsorptive purification unit which separates water vapour and carbon dioxide from the air. The purified first flow of air is further compressed to a pressure at least 5 bar higher than that at which it is purified in a second air compressor whose outlet pressure is independent of fluctuations in the power output of the gas turbine, is cooled in a main heat exchanger, is passed through an expansion valve, and is introduced into a higher pressure rectification column. A second flow of air is compressed in a third air compressor which is independent of the gas turbine. The compressed second flow of air is purified in an adsorptive purification unit by the separation of water vapour and carbon dioxide therefrom. The purified second flow of air is cooled in the main heat exchanger and is introduced into the higher pressure rectification column. The air flows are rectified in the higher pressure rectification column and an associated lower pressure rectification column operating at pressures above 2 bar. A nitrogen product is withdrawn from the top of the lower pressure rectification column and a liquid oxygen product from the bottom thereof. The liquid oxygen is revised in pressure to at least 25 bar by a pump and is warmed to ambient temperature in the main heat exchanger.
    • 第一空气流在与燃气轮机相关联的第一空气压缩机中被压缩,并且在从空气中分离水蒸气和二氧化碳的吸附净化单元中被净化。 净化的第一空气流进一步被压缩至比第二空气压缩机净化出的压力高至少5巴的压力,其第二空气压缩机的出口压力与燃气轮机功率输出的波动无关,主要被冷却 热交换器通过膨胀阀,并被引入高压精馏塔。 第二空气流在与燃气轮机独立的第三空气压缩机中被压缩。 通过从其中分离水蒸汽和二氧化碳,在吸附净化单元中净化压缩的第二空气流。 净化的第二次空气在主热交换器中被冷却并被引入高压精馏塔。 空气流在高压精馏塔和在2巴以上的压力下运行的相关的低压精馏塔进行整流。 从低压精馏塔的顶部和底部的液氧产物中取出氮气产物。 液体氧通过泵在压力下修正至至少25巴,并在主热交换器中升温至环境温度。
    • 7. 发明申请
    • METHOD AND DEVICE FOR PRODUCING A GASEOUS PRESSURIZED OXYGEN PRODUCT BY CRYOGENIC SEPARATION OF AIR
    • 通过空气分离生产气体加压氧化产物的方法和装置
    • US20120174625A1
    • 2012-07-12
    • US13389862
    • 2010-08-10
    • Thomas RathboneFrances Masterson
    • Thomas RathboneFrances Masterson
    • F25J3/04
    • F25J3/04175F25J3/04054F25J3/04066F25J3/0409F25J3/04296F25J3/04381F25J3/04393F25J2230/20F25J2240/04
    • Process and apparatus for producing a pressurized gaseous oxygen product by cryogenic air separationThe process and the apparatus serve for producing a pressurized gaseous oxygen product by cryogenic air separation in a distillation column system which has at least one separating column. Feed air is compressed in an air compressor. A first partial stream (2, 4, 6, 7) of the compressed feed air is expanded (5, 8) while performing work. A second partial stream (3) of the compressed feed air (1) is cooled and liquefied or pseudo-liquefied and subsequently introduced into the distillation column system. A liquid oxygen product stream (51) is removed from the distillation column system, brought to a first increased pressure in the liquid state (52), vaporized or pseudo-vaporized under this first increased pressure by indirect heat exchange (10) with the second partial stream (3) of the compressed feed air, warmed to approximately ambient temperature (10) and finally drawn off as a gaseous product stream (55). The vaporized or pseudo-vaporized oxygen product stream (53) is brought further to a second increased pressure, which is higher than the first increased pressure, in a cold compressor (13). The product stream (54) is warmed to approximately ambient temperature under this second increased pressure (10). At least part of the mechanical energy produced in the work-performing expansion (5, 8) of the first partial stream (3) is used for driving the cold compressor (13).
    • 用于通过低温空气分离生产加压气态氧产物的方法和装置该方法和装置用于在具有至少一个分离塔的蒸馏塔系统中通过低温空气分离产生加压气态氧产物。 进料空气在空气压缩机中被压缩。 在执行工作时,压缩进料空气的第一部分流(2,4,6,7)膨胀(5,8)。 压缩进料空气(1)的第二部分流(3)被冷却并液化或伪液化并随后引入蒸馏塔系统。 从蒸馏塔系统中除去液氧产物流(51),在液态(52)中达到第一增加的压力,在该第一增加压力下通过间接热交换(10)蒸发或假蒸发,第二 压缩的进料空气的部分气流(3)加热到大约环境温度(10),最后作为气态产物流(55)排出。 蒸发的或假蒸发的氧产物流(53)在冷压缩机(13)中被进一步升至高于第一增加压力的第二增压压力。 在该第二增压(10)下将产物流(54)加热至约环境温度。 在第一部分流(3)的工作执行膨胀(5,8)中产生的机械能的至少一部分用于驱动冷压缩机(13)。
    • 10. 发明授权
    • Air separation
    • 空气分离
    • US06244072B1
    • 2001-06-12
    • US09505120
    • 2000-02-16
    • Thomas Rathbone
    • Thomas Rathbone
    • F25C100
    • F25J3/04387F25J3/0409F25J3/04296F25J3/04448F25J3/04545F25J3/04575F25J3/04593F25J2200/50F25J2240/10F25J2240/80
    • Air is separated in a double rectification column comprising a higher pressure column and a lower pressure column, the latter operating at pressures of less than 2 bar absolute. An oxygen product is withdrawn from the column by a pump. A first vaporous nitrogen stream is taken from the top of the higher pressure column, is compressed in a compressor and is used in a gas turbine. Feed to the lower pressure column is derived from a stream of the bottom oxygen-enriched liquid fraction obtained in the higher pressure column. To this end, this stream is subjected to further separation (typically in further rectification column) to form a vaporous nitrogen fraction (a flow of which is condensed and is used as reflux in the lower pressure column) and an oxygen-containing feed to the lower pressure column which flows via an outlet and a condenser to the column. At least 60% of the nitrogen product flowing to the gas turbine is taken from the higher pressure column.
    • 空气在包括高压塔和低压塔的双精馏塔中分离,后者在小于2巴绝对压力下操作。 通过泵将氧产物从塔中取出。 从高压塔的顶部取出第一气态氮气流,在压缩机中压缩并用于燃气轮机。 进料到低压塔是从在高压塔中获得的底部富氧液体馏分的流导出的。 为此,将该物流进一步分离(通常在另一精馏塔中)以形成蒸气氮馏分(其流动被冷凝并在低压塔中用作回流)和含氧进料 低压塔通过出口和冷凝器流到塔。 流入燃气轮机的至少60%的氮产品是从高压塔中取出的。