Atmosphere compositions and methods of using same for surface treating
ferrous metals
    2.
    发明授权
    Atmosphere compositions and methods of using same for surface treating ferrous metals 失效
    大气组合物及其使用方法用于表面处理黑色金属

    公开(公告)号:US4049472A

    公开(公告)日:1977-09-20

    申请号:US643348

    申请日:1975-12-22

    Inventor: Edward J. Arndt

    CPC classification number: C21D1/76 C23C8/22 C23C8/32

    Abstract: Atmosphere compositions and processes utilizing the compositions for heat treating ferrous metal articles under a controlled furnace atmosphere to either maintain or change the surface chemistry of the article being treated are disclosed in the following specification.The invention features atmosphere compositions or mixtures which are blended from normally gaseous components outside the furnace and the mixture or blend is injected into the furnace to provide a carburizing, decarburizing, carbonitriding or neutral hardening atmosphere inside the furnace.

    Abstract translation: 在以下说明书中公开了利用组合物在受控炉气氛下处理黑色金属制品以保持或改变待处理制品的表面化学性质的气氛组合物和方法。

    Process for preparing hydrogen or nitrogen and hydrogen under pressure
    3.
    发明授权
    Process for preparing hydrogen or nitrogen and hydrogen under pressure 失效
    在压力下制备氢气或氮气和氢气的方法

    公开(公告)号:US3720625A

    公开(公告)日:1973-03-13

    申请号:US3720625D

    申请日:1970-11-05

    Inventor: KAPP E BECKER P

    Abstract: Process for producing hydrogen and/or a hydrogen-nitrogen mixture for the synthesis of ammonia, which process comprises a gasification of solid or liquid sulfur-containing fuels with oxygen and steam; a desulfurization of the crude gas; conversion of the carbon monoxide contained in the raw gas with hydrogen to form carbon dioxide and hydrogen in two stages using an iron oxide-chromium oxide catalyst and temperatures of 350*-500*C in the first stage and a copper-containing catalyst and temperatures of 190*-280*C in the second stage; scrubbing the gas which is now rich in hydrogen to remove carbon dioxide; and a final purification of the remaining built up raw hydrogen by a removal of residual carbon dioxide and carbon monoxide.

    Abstract translation: 用于生产用于合成氨的氢气和/或氢 - 氮混合物的方法,该方法包括用氧气和蒸汽气化固体或液体含硫燃料; 原油脱硫; 使用氧化铁 - 氧化铬催化剂将原料气体中所含的一氧化碳与氢气二次转化成二氧化碳和氢气,第一阶段的温度为350-500℃,含铜催化剂和温度 在第二阶段为190°-280℃; 洗涤现在富含氢气的气体以除去二氧化碳; 并通过去除残留的二氧化碳和一氧化碳来最终净化剩余的原始氢。

    Production of nitrogen-rich gas mixtures
    4.
    发明授权
    Production of nitrogen-rich gas mixtures 失效
    生产富氮气体混合物

    公开(公告)号:US4119566A

    公开(公告)日:1978-10-10

    申请号:US801138

    申请日:1977-05-27

    CPC classification number: C01B3/36 Y02P20/123

    Abstract: A nitrogen-rich inert gas mixture is produced by the partial oxidation of a hydrocarbonaceous feed containing substantially no metals nor noncombustible materials with air in a free-flow, unpacked, refractory-lined gas generator at a temperature in the range of about 1300.degree. to 3000.degree. F. and a pressure in the range of about 1 to 250 atmospheres. The product gas will comprise a mixture of nitrogen, argon and carbon dioxide and may contain small amounts of hydrogen and carbon monoxide, depending on the O/C atomic ratio selected. The atomic ratio of free oxygen in said air to carbon in said hydrocarbonaceous fuel is in the range of about 1.7 to stoichiometric, or slightly less than stoichiometric. By operating at this level of O/C atomic ratio, the H.sub.2 + CO content of the product gas may be minimized or deleted, substantially all of the particulate carbon may be oxidized, substantially no NO.sub.x is produced, and the product gas contains substantially no free oxygen. Further, the sensible heat recovered from the product gas may be used to manufacture by-product high pressure steam for export. The nitrogen-rich product gas may be used for oil formation flooding, or as a pressurizing or blanketing gas. Costly gas compressors may be avoided since the product gas may be produced at or above use pressure.

    Abstract translation: 通过在自由流,未包装的耐火材料衬里的气体发生器中在大约1300℃至大约1300℃的温度范围内部分氧化含有基本上不含金属和不可燃材料的空气的含烃原料来生产富氮惰性气体混合物 3000°F,压力范围约为1至250大气压。 产物气体将包含氮气,氩气和二氧化碳的混合物,并且可能含有少量氢气和一氧化碳,这取决于所选择的O / C原子比。 所述烃类燃料中所述空气中的碳与碳之间的游离氧的原子比在约1.7至化学计量的范围内,或略小于化学计量。 通过以这种O / C原子比水平操作,产物气体的H 2 + CO含量可以被最小化或者被消除,基本上所有的颗粒碳都可能被氧化,基本上没有产生NOx,并且产物气体基本上不含 游离氧气。 此外,从产物气体回收的显热可用于制造用于出口的副产物高压蒸汽。 富氮产物气体可用于油层淹没,或用作加压或覆盖气体。 因为可以在或高于使用压力下产生产品气体,所以可以避免成本高的气体压缩机。

    Production of nitrogen rich gas mixtures
    7.
    发明授权
    Production of nitrogen rich gas mixtures 失效
    生产富氮气体混合物

    公开(公告)号:US4057510A

    公开(公告)日:1977-11-08

    申请号:US617601

    申请日:1975-09-29

    CPC classification number: C01B3/36 Y02P20/123

    Abstract: A nitrogen-rich inert gas mixture is produced by the partial oxidation of a hydrocarbonaceous feed containing substantially no metals nor noncombustible materials with air in a free-flow, unpacked, refractory-lined gas generator at a temperature in the range of about 1300.degree. to 3000.degree. F. and a pressure in the range of about 1 to 250 atmospheres. The product gas will comprise a mixture of nitrogen, argon and carbon dioxide and may contain small amounts of hydrogen and carbon monoxide, depending on the O/C atomic ratio selected. The atomic ratio of free oxygen in said air to carbon in said hydrocarbonaceous fuel is in the range of about 1.7 to stoichiometric, or slightly less than stoichiometric. By operating at this level of O/C atomic ratio, the H.sub.2 + CO content of the product gas may be minimized or deleted, substantially all of the particulate carbon may be oxidized, substantially no NO.sub.x is produced, and the product gas contains substantially no free oxygen. Further, the sensible heat recovered from the product gas may be used to manufacture by-product high pressure steam for export. The nitrogen-rich product gas may be used for oil formation flooding, or as a pressurizing or blanketing gas. Costly gas compressors may be avoided since the product gas may be produced at or above use pressure.

    Abstract translation: 通过在自由流,未包装的耐火材料衬里的气体发生器中在大约1300℃至大约1300℃的温度范围内部分氧化含有基本上不含金属和不可燃材料的空气的含烃原料来生产富氮惰性气体混合物 3000°F,压力范围约为1至250大气压。 产物气体将包含氮气,氩气和二氧化碳的混合物,并且可能含有少量氢气和一氧化碳,这取决于所选择的O / C原子比。 所述烃类燃料中所述空气中的碳与碳之间的游离氧的原子比在约1.7至化学计量的范围内,或略小于化学计量。 通过以这种O / C原子比水平操作,产物气体的H 2 + CO含量可以被最小化或者被消除,基本上所有的颗粒碳都可能被氧化,基本上没有产生NOx,并且产物气体基本上不含 游离氧气。 此外,从产物气体回收的显热可用于制造用于出口的副产物高压蒸汽。 富氮产物气体可用于油层淹没,或用作加压或覆盖气体。 因为可以在或高于使用压力下产生产品气体,所以可以避免成本高的气体压缩机。

    Breath alcohol test medium
    8.
    发明授权
    Breath alcohol test medium 失效
    呼吸酒精测试介质

    公开(公告)号:US3951855A

    公开(公告)日:1976-04-20

    申请号:US377383

    申请日:1973-07-09

    Abstract: A standard breath alcohol test medium comprises a canister containing a charge of nitrogen and vaporized alcohol having a predetermined amount of alcohol per unit of volume therein, and means on the canister accommodating discharge of the nitrogen and alcohol mixture therefrom, preferably by pressure discharge or hypodermic extraction through a self-sealing septum in the wall of the canister. A method for filling the containers with a predetermined amount of alcohol vapor is also disclosed.

    Abstract translation: 标准的呼吸酒精测试介质包括含有氮气的罐和其中具有每单位体积的预定量的醇的汽化醇,以及容纳氮气和醇混合物的罐的装置,优选通过压力放电或皮下注射 通过罐壁上的自密封隔膜提取。 还公开了一种用预定量的醇蒸气填充容器的方法。

    Reforming process
    9.
    发明授权
    Reforming process 失效
    改造工艺

    公开(公告)号:US3827987A

    公开(公告)日:1974-08-06

    申请号:US12784571

    申请日:1971-03-24

    Applicant: DU PONT

    Inventor: GREEN R

    CPC classification number: C01B3/38 C01B3/384

    Abstract: I THE MANUFACTURE OF AMMONIA OR HYDROGEN, NATURAL GAS IS REFORMED WITH STEAM OVER A NICKEL CATALYST IN THE TUBES OF A REFORMER TO PRODUCE HYDROGEN AND CARBON MONOXIDE. IF HYDROGEN IS ADDED TO THE STEAM-NATURAL GAS MIXTURE FED TO THE REFORMER, CATALYST, CATALYST TUBE LIFE, AND PLANT UTILITY WILL BE IMPROVED.

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