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38 条记录 (耗时 0.018 秒)

    Process and installation for producing high pressure oxygen
    22.
    发明授权
    Process and installation for producing high pressure oxygen 失效
    生产高压氧气的工艺和安装

    公开(公告)号：US5735142A

    公开(公告)日：1998-04-07

    申请号：US788640

    申请日：1997-01-27

    申请人： Maurice Grenier

    发明人： Maurice Grenier

    IPC分类号： F25J3/04 ,  F25J3/00

    CPC分类号： F25J3/04084 ,  F25J3/0409 ,  F25J3/0423 ,  F25J3/04296 ,  F25J3/04412 ,  F25J3/04678 ,  F25J3/04727 ,  F25J3/04739 ,  F25J2250/20 ,  Y10S62/94

    摘要： A process and a plant in which gaseous oxygen is produced directly at the desired high pressure by pumping liquid oxygen drawn off in the vessel of the low-pressure column (11). The air to be distilled is split into three flows: a flow at the medium pressure of the double distillation column (1), a flow at a high pressure, higher than approximately 60 bars, and a flow at an intermediate pressure which, after partial cooling, is expanded to the medium pressure in a turbine (8). The intermediate pressure is chosen so that the air treated in the turbine is near its dew point at the entry of the turbine wheel. Liquid product is simultaneously drawn off (at 24) from the plant.

    摘要翻译： 一种工艺和工厂，其中通过泵送在低压塔（11）的容器中排出的液体氧，在期望的高压下直接产生气态氧。 要蒸馏的空气被分成三个流：在双蒸馏塔（1）的中压下的流量，高压大于约60巴的流量和中间压力的流量，在部分 冷却，在涡轮（8）中膨胀到中压。 选择中间压力使得在涡轮机处理的空气在涡轮机叶片进入处接近其露点。 液体产品同时从植物中排出（在24处）。

    Process and apparatus for the liquefaction of hydrogen
    23.
    发明授权
    Process and apparatus for the liquefaction of hydrogen 失效
    用于液化氢气的方法和装置

    公开(公告)号：US5579655A

    公开(公告)日：1996-12-03

    申请号：US399923

    申请日：1995-03-07

    申请人： Maurice Grenier

    发明人： Maurice Grenier

    IPC分类号： C01B3/00 ,  F25J1/02 ,  F25J1/00

    CPC分类号： F25J1/001 ,  F25J1/005 ,  F25J1/0052 ,  F25J1/0055 ,  F25J1/0072 ,  F25J1/0215 ,  F25J1/0249 ,  F25J1/025 ,  F25J1/0279 ,  Y02E60/324 ,  Y10S62/913

    摘要： A process and apparatus for the liquefaction of hydrogen, of the type using a refrigeration cycle whose cycle fluid comprises mostly hydrogen, and a closed liquid nitrogen refrigeration cycle. The cycle fluid is hydrogen and a mixture of C.sub.2 + hydrocarbons. The hydrocarbons are liquefied and expanded to form fluids which vaporize in a substantially continuous manner between a temperature of the order of -120.degree. C. and a temperature adjacent ambient temperature. More particularly, the mixture of hydrocarbons is saturated C.sub.2, C.sub.3, and C.sub.5 hydrocarbons, and if desired C.sub.4, and separated liquefied fractions of these hydrocarbons are expanded at respective temperatures before expansion of the order of 0.degree. C. to -10.degree. C., -40.degree. C. to -50.degree. C. and -110.degree. C. to -120.degree. C., to form refrigerant liquids adapted to be vaporized.

    摘要翻译： 用于液化氢的方法和装置，其类型使用循环流体主要包含氢的制冷循环和封闭的液氮制冷循环。 循环流体是氢气和C2 +烃的混合物。 烃被液化并膨胀以形成在约-20℃的温度和邻近环境温度的温度之间基本上连续的方式蒸发的流体。 更具体地说，烃的混合物是饱和的C 2，C 3和C 5烃，如果需要，C4，并且这些烃的分离的液化馏分在扩展到0℃至-10℃之前的相应温度下膨胀。 -40℃至-50℃和-110℃至-120℃，以形成适于蒸发的制冷剂液体。

    Ozone-producing plant
    25.
    发明授权
    Ozone-producing plant 失效
    臭氧生产厂

    公开(公告)号：US4863497A

    公开(公告)日：1989-09-05

    申请号：US230153

    申请日：1988-08-09

    申请人： Maurice Grenier ,  Pierre Petit

    发明人： Maurice Grenier ,  Pierre Petit

    IPC分类号： B01J8/02 ,  B01J8/10 ,  C01B13/10

    CPC分类号： B01J8/10 ,  B01J8/0214 ,  B01J8/0257 ,  C01B13/10 ,  B01D2256/14 ,  B01J2208/021 ,  B01J2208/028

    摘要： Each ozonization loop (1) which includes a compressor (2), an ozonizer (3), and a heat exchanger (8) for cooling the oxygen-ozone mixture, is associated with three cylinders (4,5,6) filled with silica gel. Each cylinder operates in succession in a cocurrent adsorption, in countercurrent desorption by a substitution gas, and in scavenging by taking off a part of the flow circulating in the loop. The scavenging flow is recovered and combined with the substitution gas. The substitution gas may be in particular impure nitrogen supplied by an air distillation apparatus producing the necessary oxygen.

    摘要翻译： 包括用于冷却氧 - 臭氧混合物的压缩机（2），臭氧发生器（3）和热交换器（8）的每个臭氧化环路（1）与填充有二氧化硅的三个汽缸（4,5,6）相关联 凝胶。 每个气缸连续工作在并流吸附中，通过置换气体进行逆流解吸，并且通过取出循环中循环的一部分流动进行清除。 清除流量被回收并与替代气体组合。 取代气体可以特别是由产生所需氧气的空气蒸馏装置供应的不纯的氮气。

    Process and installation for producing nitrogen under pressure
    26.
    发明授权
    Process and installation for producing nitrogen under pressure 失效
    在压力下生产氮气的过程和安装

    公开(公告)号：US4717410A

    公开(公告)日：1988-01-05

    申请号：US837049

    申请日：1986-03-06

    申请人： Maurice Grenier

    发明人： Maurice Grenier

    IPC分类号： F25J3/04 ,  F25J3/02

    CPC分类号： F25J3/04254 ,  F25J3/04284 ,  F25J3/04321 ,  F25J3/04412 ,  F25J2200/20 ,  F25J2200/54 ,  F25J2210/42 ,  F25J2235/42 ,  F25J2245/42 ,  Y10S62/913

    摘要： The rich liquid received at the base of the main column (3) at high pressure is expanded in two stages. After the first expansion to medium pressure, it is distilled so as to produce an addition of pure nitrogen. The second expansion achieves the reflux in the medium pressure column (4). Liquid nitrogen is pumped from this column to the high pressure column (3) and all the nitrogen can be produced at high pressure.

    摘要翻译： 在主塔（3）的底部在高压下接收的富液体分两个阶段扩展。 第一次膨胀至中压后，将其蒸馏，以产生纯氮的添加。 第二次膨胀在中压塔（4）中达到回流。 将液氮从该塔泵送到高压塔（3），并且可以在高压下产生所有的氮气。

    Gasification of coal
    28.
    发明授权
    Gasification of coal 失效
    煤气化

    公开(公告)号：US4479540A

    公开(公告)日：1984-10-30

    申请号：US381623

    申请日：1982-05-24

    申请人： Maurice Grenier

    发明人： Maurice Grenier

    IPC分类号： E21B43/28 ,  E21B7/14 ,  E21B36/02 ,  E21B43/243 ,  E21C43/00

    CPC分类号： E21B7/14 ,  E21B36/02 ,  E21B43/243 ,  Y10S48/06

    摘要： This invention relates to the gasification of coal. An oxygen jet having a pointed flame is engendered in situ, so as to strike the coal with a sheath of steam. The resultant fuel gas is drawn off while flowing in counterflow with the jet of oxygen and is brought to the surface through the same bore which had served the purpose of supplying oxygen. The invention is particularly applicable to the underground gasification of coal in situ.

    摘要翻译： 本发明涉及煤的气化。 具有尖锐的火焰的氧气射流原位产生，以便用蒸汽鞘击打煤。 所产生的燃料气体在与氧气射流反向流动的同时被抽出，并通过相同的孔被带到表面，这个孔用于供氧。 本发明特别适用于原位煤的地下气化。

    Process and installation for the production of gaseous oxygen under pressure
    29.
    发明授权
    Process and installation for the production of gaseous oxygen under pressure 失效
    在压力下生产气态氧气的过程和安装

    公开(公告)号：US5596885A

    公开(公告)日：1997-01-28

    申请号：US419555

    申请日：1995-04-10

    申请人： Maurice Grenier

    发明人： Maurice Grenier

    IPC分类号： C01B13/02 ,  F25J3/04 ,  F25J3/02

    CPC分类号： F25J3/04236 ,  F25J3/04018 ,  F25J3/04024 ,  F25J3/04054 ,  F25J3/04084 ,  F25J3/0409 ,  F25J3/04145 ,  F25J3/04296 ,  F25J3/04303 ,  F25J3/04393 ,  F25J3/04412 ,  F25J2215/52 ,  F25J2215/54 ,  F25J2290/62 ,  Y10S62/913

    摘要： An air separation process of the "pumped" type, in which liquid oxygen is removed from a double distillation column and is pumped to a higher production pressure and then vaporized under that pressure. The incoming air is divided into several streams. A first stream is compressed to the medium pressure, cooled and sent to the double distillation column (7). A second stream is compressed above about 25 bars, but below its condensation pressure during vaporization of the liquid oxygen under pressure, then cooled to an intermediate temperature, at which a portion of the air continues its cooling and is liquified (in 20A), then expanded (in 21A) and sent to the double column, while the rest is work expanded (in 4). Use in large size installations for the production of oxygen.

    摘要翻译： “泵送”型的空气分离过程，其中液体氧从双蒸馏塔中除去并被泵送到较高的生产压力，然后在该压力下蒸发。 进入的空气被分成几个流。 将第一流压缩至中压，冷却并送至双蒸馏塔（7）。 第二流在压力下在液体氧气蒸发期间被压缩在约25巴以上，但低于其冷凝压力，然后冷却至中间温度，在该温度下，一部分空气继续冷却并液化（以20A计） 扩展（在21A）并发送到双列，而其余的工作扩展（在4）。 用于大型安装用于生产氧气。