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    • 1. 发明授权
    • Process gas cooler
    • 工艺气体冷却器
    • US3915224A
    • 1975-10-28
    • US47998674
    • 1974-06-17
    • UHDE GMBH FRIEDRICH
    • RICHTER HANS-HMUNDO KLAUS
    • F22G1/00F22B1/18F22G3/00F28D7/08F28D7/04
    • F22B1/1884F28D7/08Y10S165/408
    • A cooler for process gas of temperatures in excess of 750* C in which the gas passes through tubes, the cooling length of which is subdivided into three sections. The sections comprise; first, a hot or inlet section where the tubes are surrounded by a vaporizing liquid; secondly, a medium temperature or intermediate section where the tubes are arranged in a steam space and cooled by the saturated steam produced; and, thirdly, a cool discharge section where the tubes are surrounded by the vaporizing liquid. The tubes are of inverted U-shape and preferably are of serpentine form where one arm of the U has portions overlapping the other arm for greater heat exchange. Vaporizing liquid is recirculated, added to, and cooled by feedwater.
    • 用于气体通过管的超过750℃的过程气体的冷却器,其冷却长度被细分为三个部分。 这些部分包括 第一,热管或入口部分,其中管被汽化液体包围; 其次,中间温度或中间部分,其中管被布置在蒸汽空间中并由产生的饱和蒸汽冷却; 以及第三,冷却放电部分,其中管被汽化液体包围。 管是倒U形的,并且优选地是蛇形形式,其中U的一个臂具有与另一个臂重叠的部分以进行更大的热交换。 蒸发液再循环,加入并由给水冷却。
    • 6. 发明授权
    • Process for the recovery of co2 of very high purity
    • 回收非常高纯度的co2的方法
    • US3193986A
    • 1965-07-13
    • US10246961
    • 1961-04-12
    • UHDE GMBH FRIEDRICH
    • FRITZ FORSTER
    • B01D19/00C01B32/50C10K1/10
    • B01D19/0036C01B32/50C10K1/101Y02P20/131
    • Carbon dioxide is recovered from a gas containing CO2 by countercurrently scrubbing the gas with a liquid capable of absorbing carbon dioxide at 5-100 Atm., reducing the pressure of the liquid in a turbine to 20-80% of the scrubber pressure and separating the gas, containing the greater part of non-CO2 gas, in a separator; the liquid is then passed to one or more vessels in which the pressure is reduced to 0.3-3.0 Atm. below the pressure in the separator and each preceding vessel, the gas is separated and the liquid passed to a second turbine at a pressure 0.2-2 Atm. higher than the static pressure of the column of liquid between the second turbine and the gas collector in which pure CO2 is separated from the liquid passing from the second turbine and which is located above this turbine. The scrubbing liquid may be water, an aqueous alkaline solution, or an anhydrous liquid absorbent e.g. an aqueous solution of ammonia or an organic derivative or of an alkali metal salt of a weak acid. Gas containing CO2, CO, H2, N2, A and CH4 at 28 Atm. is mixed with gas from separator 3 containing CO2, CO and H2 which is compressed by 4. The mixed gas containing 29% CO2 is fed to scrubber containing H2O at 28 Atm. and is treated to leave 0.3% CO2. Scrubbing H2O from 1 is passed to turbine 2 at 8.9 Atm. yielding gas to 3. H2O from 3 is passed to vessel 5 at 7 Atm. yielding a gas containing CO2, CO and H2 which is vented to atmosphere. H2O from 5 is fed to turbine 6 at a pressure of the water column from 6 to degasifier 7 where 99.2% pure CO2 is obtained. H2O from > is freed from dissolved gases in 8 by aeration and then returned to 1 via pump 9 driven by motor 10 supplementing turbines 2 and 6.
    • 9. 发明授权
    • Process for the recovery of nitrogen monoxide
    • 回收一氧化氮的方法
    • US3915675A
    • 1975-10-28
    • US37440773
    • 1973-06-28
    • UHDE GMBH FRIEDRICH
    • SCHEIBLER ERICHHOPFER KLAUS
    • C01B21/26C01B21/40B01D47/00
    • C01B21/26Y02P20/129
    • A process for the recovery of very pure nitrogen monoxide from a gas stream originating preferably from an ammonia oxidation process and containing nitric oxides, the acid condensates being processed to obtain nitric acid of medium concentration, and water vapour condensate. A mixture of nitric oxides and steam is cooled by a cooling fluid and scrubbed with condensate from a nitric acid distillation unit. The combined acid condensates are degassed and the gas obtained to the product line ahead of the gas scrubbing unit is recycled. The effluent from the degassing unit is distilled to a nitric acid concentration, and the noncondensible gas components are withdrawn from the condenser of the nitric acid distillation unit and admixed to the hot gas stream ahead of the first process step.
    • 一种从优选由氨氧化过程产生并含有一氧化氮的气流中回收非常纯的一氧化氮的方法,该酸缩合物被加工以获得中等浓度的硝酸和水蒸汽冷凝物。 将一氧化氮和蒸汽的混合物通过冷却流体冷却并用来自硝酸蒸馏装置的冷凝物洗涤。 将合并的酸性冷凝物脱气,并将气体洗涤单元前面的产品线获得的气体再循环。 将来自脱气单元的流出物蒸馏至硝酸浓度,并将不可冷凝气体组分从硝酸蒸馏单元的冷凝器中取出,并在第一工艺步骤之前与热气流混合。