Process for operating a heat exchanger
    5.
    发明授权
    Process for operating a heat exchanger 失效
    用于操作热交换器的工艺

    公开(公告)号:US5233839A

    公开(公告)日:1993-08-10

    申请号:US907707

    申请日:1992-07-02

    Abstract: The invention aims at preventing the risks of deformation and breaking down of the heat exchanger which is part of a plant for the batch treatment of fluids, of the type in which, during active periods which are separated from one another by rest periods, at least one refrigerating fluid is allowed to circulate in first ducts of the exchanger, from the cold end to the hot end of the latter, and at least one calorigenic fluid is circulated in second ducts of the exchanger, from the hot end to the cold end of the latter, characterized in that, during rest periods, heat is introduced at the hot end and cold is introduced at the cold end of the exchanger so as to maintain these two ends at temperatures which are relatively close to those corresponding to the active periods, at least one of these two inputs being supplied by means of a reserve fluid of the plant.

    Abstract translation: 本发明旨在防止作为用于批量处理流体的工厂的一部分的热交换器的变形和分解的风险,其中在活动期间彼此相隔休息的至少 允许一个制冷流体在交换器的第一管道中循环,从冷端到后端的热端,并且至少一个热量流体在交换器的第二管道中循环,从热端到冷端 后者的特征在于,在休息期间,在热端引入热量,并且在换热器的冷端引入冷,以便将这两个端部保持在相对接近与活动周期相对应的温度的温度, 这两个输入中的至少一个通过工厂的储备流体供应。

    Process for adjusting the verticality of an article disposed in a closed
envelope and assembly for carrying this process
    6.
    发明授权
    Process for adjusting the verticality of an article disposed in a closed envelope and assembly for carrying this process 失效
    调整封闭式封装中处置的物品的垂直度的方法和装配本工艺的组件

    公开(公告)号:US5205042A

    公开(公告)日:1993-04-27

    申请号:US774220

    申请日:1991-10-09

    Abstract: The article of which the verticality is critical, for example a distillation column disposed in a closed envelope, is associated with an indicator of verticality comprising a suspended mass and a locating ring. The envelope, which contains the various inner articles, is placed on a base by means of supports and its inclination with respect to the base is adjusted by controlling the relative position of the mass with respect to the ring. Application for example to cold boxes for the in situ production of gas from air.

    Abstract translation: 垂直度是关键的物品,例如设置在封闭封套中的蒸馏塔,与垂直度的指示器相关联,包括悬挂质量和定位环。 包含各种内部物品的信封通过支撑件放置在基座上,并且通过控制质量块相对于环的相对位置来调整其相对于基座的倾斜度。 应用于例如用于从空气中原位生产气体的冷箱。

    Indirect heat exchanger
    8.
    发明授权
    Indirect heat exchanger 失效
    间接换热器

    公开(公告)号:US5333683A

    公开(公告)日:1994-08-02

    申请号:US989387

    申请日:1992-12-11

    Abstract: Indirect heat exchanger, of the type comprising a series of parallel plates (7) delimiting between themselves passages (8A, 8B; 28, 42, 60) of generally plate form containing undulant spacers (9; 32, 34, 36, 37, 44, 47, 48, 53 to 56). A first assembly (8A; 28, 60) of these passages constitutes thermal exchange passages having structure (3 to 5; 39 to 41, 51) for inlet and outlet of fluids adapted to exchange heat with each other. Over at least a portion of its length and of its width, the exchanger has added passages (8B; 42), in reduced or no heat exchange relation with the thermal exchange passages (8A; 28, 60) and provided to fulfill at least one function in addition to the exchange of heat, namely a function of storing liquid and/or recirculation of liquid and/or liquid-vapor separation.

    Abstract translation: 间接热交换器,其类型包括一系列平行板(7),所述平行板(7)在其自身通道(8A,8B; 28,42,60)之间界定,所述通道具有包含起伏间隔件(9; 32,34,36,37,44 ,47,48,53至56)。 这些通道的第一组件(8A; 28,60)构成具有结构(3至5; 39至41,51)的热交换通道,用于适于彼此交换热量的流体的入口和出口。 在其长度和宽度的至少一部分上,交换器具有与热交换通道(8A; 28,60)减少或不与热交换关系的通道(8B; 42),并且被设置成满足至少一个 功能除了交换热量,即存储液体和/或液体和/或液体 - 气体分离的再循环的功能。

    Process for the production of nitrogen by cryogenic distillation of
atmospheric air
    9.
    发明授权
    Process for the production of nitrogen by cryogenic distillation of atmospheric air 失效
    通过大气空气的低温蒸馏生产氮气的方法

    公开(公告)号:US5325674A

    公开(公告)日:1994-07-05

    申请号:US843940

    申请日:1992-02-18

    Abstract: A process for producing gaseous nitrogen from a mixture to be treated in a distillation column, said mixture comprising nitrogen and oxygen, said process comprising the steps of:a) compressing the mixture to be treated to a pressure at least equal to the column pressure;b) cooling the compressed gas mixture and subjecting at least a first portion of said cooled mixture to expansion through a turbine to produce the required refrigeration and thereafter fractionated distillation in the column to obtain at the bottom of the column, an oxygen-enriched fraction and, at the top of the column, a nitrogen-enriched fraction,c) drawing off at least a portion of the nitrogen-enriched fraction as nitrogen product;d) compressing the remaining portion of the nitrogen-enriched fraction;e) recycling at least a portion of the compressed remaining portion of the nitrogen-enriched fraction to the bottom reboiler of the column where it condenses to provide reboil for the column;f) introducing at least a portion of the condensed nitrogen stream of step e) to the top of the column as additional reflux; andg) drawing off an oxygen-enriched fraction in liquid form from the bottom of the column and expanding at least a portion of said fraction to a pressure less than the column pressure and vaporizing this portion by heat exchange with the condensing nitrogen-enriched fraction at the top of the column.

    Abstract translation: 一种从蒸馏塔中待处理混合物生产气态氮的方法,所述混合物包括氮气和氧气,所述方法包括以下步骤:a)将待处理的混合物压缩至至少等于柱压力的压力; b)冷却压缩气体混合物并使所述冷却的混合物的至少第一部分通过涡轮膨胀以产生所需的制冷,然后在塔中分馏蒸馏以在塔的底部获得富氧馏分和 在柱的顶部,富氮馏分,c)抽出至少一部分富氮馏分作为氮产物; d)压缩剩余部分的富氮馏分; e)将富氮馏分的压缩剩余部分的至少一部分再循环到塔的底部再沸器中,在其中冷凝以提供塔的再沸腾; f)将步骤e)的至少一部分冷凝的氮气流作为附加回流引入塔顶; 并且g)从塔的底部抽出液态的富氧级分,并将至少一部分所述级分膨胀至小于柱压的压力,并通过与冷凝富氮级分的热交换来汽化该部分 在列的顶部。

    Installation and process for the distribution of very high purity
nitrogen
    10.
    发明授权
    Installation and process for the distribution of very high purity nitrogen 失效
    安装和加工用于分配非常高纯度的氮

    公开(公告)号:US5287873A

    公开(公告)日:1994-02-22

    申请号:US976102

    申请日:1992-11-13

    Applicant: Francois Venet

    Inventor: Francois Venet

    Abstract: The conduits (1-4) of length L have a linear section S.sub.1 and contain a volumetric flow rate of nitrogen Q such that, to obtain a molar concentration of impurities upon out-gassing less than C.sub.max, Q/S.sub.1 is not less than 9.5.times.10.sup.-9 L/C.sub.max. The conduits are of stainless steel with a low carbon content, not electropolished and/or chemically treated. The joints (6, 7, 9, 11) between the conduits and/or the active members (5) are maintained externally in a neutral protective atmosphere confined in a sealed casing (8, 9 . . . ) Application particularly to electronic industries.

    Abstract translation: 长度为L的管道(1-4)具有线性部分S1并且包含氮气的体积流量Q,使得为了获得低于C max的排气时的杂质的摩尔浓度,Q / S1不小于9.5 * 10-9 L / Cmax。 导管是不锈钢,具有低碳含量,不经电解抛光和/或化学处理。 管道和/或有源构件(5)之间的接头(6,7,9,11)在外部保持在限制在密封壳体(8,9 ...)中的中性保护气氛中,特别适用于电子工业。

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