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    • 41. 发明授权
    • Apparatus for applying sprout inhibitor
    • 用于施用芽苗抑制剂的装置
    • US4226179A
    • 1980-10-07
    • US960876
    • 1978-11-15
    • Dwight M. Sheldon, IIIF. Lee Beezhold
    • Dwight M. Sheldon, IIIF. Lee Beezhold
    • A23B7/144A23B7/154A23B7/16A23B4/04
    • A23B7/16A23B7/144A23B7/154
    • A method and apparatus for application of sprout-inhibiting chemical agents to surface-sprouting produce. Liquid sprout-inhibiting chemical such as isopropyl N-3 chlorophenylcarbamate (CIPC), either without solvent or with a relatively small amount of solvent, is atomized at a temperature less than 250.degree. F. to form an aerosol of liquid particles. The aerosol is preferably formed in a fogger having a cylindrical mist chamber in which ultrasonic resonance nozzles atomize the chemical agent. A tangentially introduced air flow and a helical baffle plate in the mist chamber cause centrifugal separation and leave smaller particles near the center of the mist chamber. A chamber contains a supply of sprout-inhibiting chemical and also collects chemical agent of such large particle size that it has been separated from the aerosol. A thermostatically controlled heater located in the sump warms the sprout-inhibiting chemical in the sump to a temperature above ambient but below 250.degree. F. prior to its being pumped to the atomizer nozzles to reduce its viscosity without thereby also decomposing the chemical.
    • 用于将芽抑制性化学试剂施用于表面发芽产品的方法和装置。 液体发芽抑制化学物质如N-3氯苯基氨基甲酸异丙酯(CIPC),无溶剂或相对少量溶剂,在低于250°F的温度下雾化,形成液体颗粒气溶胶。 气溶胶优选形成在具有圆柱形雾室的喷雾器中,超声共振喷嘴使化学试剂雾化。 在雾室中切向引入的空气流和螺旋挡板导致离心分离,并在雾室的中心附近留下较小的颗粒。 一个室含有抑制发芽的化学物质,并且还收集了与气溶胶分离的这种大粒径的化学试剂。 位于贮槽中的恒温控制的加热器在贮槽中将发芽抑制化学物质加热至高于环境温度但低于250°F的温度,然后将其泵送到雾化器喷嘴以降低其粘度,而不会分解化学品。
    • 44. 发明授权
    • Method of and installation for the fractionation of a gaseous mixture by adsorption
    • 通过吸附分解气体混合物的方法和安装
    • US3796022A
    • 1974-03-12
    • US3796022D
    • 1972-11-20
    • AIR LIQUIDE
    • SIMONET GPIVARD C
    • A23B7/144A23B7/12B01D53/04B01D53/047C01B21/02C01B21/04
    • B01D53/0476B01D53/261B01D2253/104B01D2253/108B01D2256/10B01D2256/12B01D2257/102B01D2257/104B01D2257/504B01D2257/80B01D2259/40052B01D2259/4006B01D2259/40062B01D2259/401B01D2259/403B01D2259/4062B01D2259/655C01B21/02Y02C10/08Y02P20/152
    • A method of fractionation of a gaseous mixture by adsorption, utilizing at least one adsorption line including an adsorption zone having an adsorbent mass adsorbing primarily a first constituent and secondarily a second constituent of said mixture, said method employing at least one elementary adsorption cycle employing said adsorption line, and further comprising an adsorption phase in which said mixture is introduced into the adsorption zone at an adsorption pressure, an elution phase in which a gaseous fraction enriched in said first constituent circulates in the adsorption zone at a pressure lower than said adsorption pressure while enriching said fraction in said second desorbed constituent, a desorption phase in which a gaseous fraction enriched in said first constituent is extracted from the inlet of said adsorption zone under a pressure lower than said elution pressure, and a pressure-rise or inflation phase in which the pressure in the adsorption zone is increased to the adsorption pressure. The invention also covers the installations for carrying the method and its alternatives into effect, and is especially applicable to the fractionation of atmospheric air into nitrogen, oxygen and water.
    • 一种通过吸附分离气体混合物的方法,所述方法利用至少一个吸附管线,该吸附管线包括吸附区,所述吸附区具有主要吸收第一组分的吸附剂质量,其次是所述混合物的第二组分,所述方法采用至少一个基本吸附循环, 吸附管线,并且还包括吸附阶段,其中所述混合物在吸附压力下被引入吸附区,洗脱阶段,其中富集所述第一组分的气体馏分在低于吸附压力的压力下在吸附区中循环 同时富集所述第二解吸组分中的所述级分,其中富集所述第一组分的气体级分在低于所述洗脱压力的压力下从所述吸附区的入口提取的解吸阶段,以及压力升高或膨胀阶段 吸附区中的压力增加到吸附 压力。 本发明还包括用于承载该方法及其替代方案的装置,并且特别适用于将大气分解成氮气,氧气和水。