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    • 3. 发明授权
    • Process for operating a heat exchanger
    • 用于操作热交换器的工艺
    • US5233839A
    • 1993-08-10
    • US907707
    • 1992-07-02
    • Lucien GreterFrancois Venet
    • Lucien GreterFrancois Venet
    • F25J3/00F25J3/04
    • F25J5/002F25J3/04787F25J3/04824F25J3/04842F25J2210/42F25J2245/90F25J2280/20F25J2280/30F25J2290/42Y10S62/903
    • 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.
    • 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。
    • 9. 发明授权
    • Process for the production of nitrogen by cryogenic distillation of
atmospheric air
    • 通过大气空气的低温蒸馏生产氮气的方法
    • US5325674A
    • 1994-07-05
    • US843940
    • 1992-02-18
    • Sophie GastinneFrancois VenetBao HaNaohiko Yamashita
    • Sophie GastinneFrancois VenetBao HaNaohiko Yamashita
    • F25J3/04F25J3/00
    • F25J3/04393F25J3/0429F25J3/04296F25J3/04351F25J3/04357F25J3/044F25J3/0443F25J3/04509F25J2200/50F25J2200/52F25J2200/54F25J2215/44F25J2220/42F25J2245/40F25J2245/42Y10S62/901Y10S62/913Y10S62/939
    • 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.
    • 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。