HIGH PORE VOLUME UTILIZATION CARBON AND ELECTRIC DOUBLE LAYER CAPACITOR
    6.
    发明申请
    HIGH PORE VOLUME UTILIZATION CARBON AND ELECTRIC DOUBLE LAYER CAPACITOR 有权
    高孔体积碳和电双层电容器

    公开(公告)号:US20160042879A1

    公开(公告)日:2016-02-11

    申请号:US14804462

    申请日:2015-07-21

    Abstract: An electric double layer capacitor electrode, including: an activated carbon having: a pore volume utilization efficiency (PVUE) of from about 200 to 290 F/cm3, wherein PVUE is the ratio of the activated carbon gravimetric capacitance (F/g) to the pore volume (cm3/g) of the activated carbon; a low non-linearity value of from 0.1 to 5%; and a total pore volume of from 0.32 to 0.56 cm3/g. Also disclosed is a method of making an electric double layer capacitor electrode, and a method of characterizing the performance of activated carbon, and the electrode, in an electric double layer capacitor (EDLC) device, as defined, herein.

    Abstract translation: 一种双电层电容器电极,包括:具有约200至290F / cm 3的孔体积利用效率(PVUE)的活性炭,其中PVUE是活性炭重量比电容(F / g)与 活性炭的孔体积(cm3 / g); 低非线性值为0.1〜5%; 并且总孔体积为0.32至0.56cm 3 / g。 还公开了如本文所定义的双电层电容器(EDLC)器件中制造双电层电容器电极的方法,以及表征活性炭性能的方法和电极。

    Process for Pure Carbon Production, Compositions, and Methods Thereof
    7.
    发明申请
    Process for Pure Carbon Production, Compositions, and Methods Thereof 有权
    纯碳生产工艺,组成及方法

    公开(公告)号:US20160002049A1

    公开(公告)日:2016-01-07

    申请号:US14772629

    申请日:2014-03-14

    Inventor: Alfred Stiller

    Abstract: The disclosure provides for methods of oxidizing carbide anions, or negative ions, from salt like carbides at temperatures from about 150 ° C. to about 750 ° C. In another aspect, the disclosure provides for reactions with intermediate transition metal carbides. In yet another aspect, the disclosure provides for a system of reactions where salt-like carbide anions and intermediate carbide anions are oxidized to produce pure carbon of various allotropes.

    Abstract translation: 本公开提供了在约150℃至约750℃的温度下从像碳化物这样的碳化物阴离子或负离子氧化的方法。在另一方面,本公开提供了与中间过渡金属碳化物的反应。 在另一方面,本公开提供了一种反应系统,其中盐状碳酸根阴离子和中间碳酸根阴离子被氧化以产生各种同素异形体的纯碳。

    PROCESS FOR PURE CARBON PRODUCTION
    8.
    发明申请
    PROCESS FOR PURE CARBON PRODUCTION 有权
    纯碳生产工艺

    公开(公告)号:US20140271441A1

    公开(公告)日:2014-09-18

    申请号:US14213533

    申请日:2014-03-14

    Inventor: Alfred STILLER

    Abstract: The disclosure provides for methods of oxidizing carbide anions, or negative ions, from salt like carbides at low temperatures below about 600° C. In another aspect, the disclosure provides for reactions with intermediate transition metal carbides. In yet another aspect, the disclosure provides for a system of reactions where salt-like carbide anions and intermediate carbide anions are oxidized to produce pure carbon of various allotropes.

    Abstract translation: 本公开提供了在低于约600℃的低温下从像碳化物这样的碳化物阴离子或负离子氧化的方法。在另一方面,本公开提供了与中间过渡金属碳化物的反应。 在另一方面,本公开提供了一种反应系统,其中盐状碳酸根阴离子和中间碳酸根阴离子被氧化以产生各种同素异形体的纯碳。

    Process for the reactivation of activated carbon
    9.
    发明授权
    Process for the reactivation of activated carbon 失效
    活性炭再活化的方法

    公开(公告)号:US06423657B1

    公开(公告)日:2002-07-23

    申请号:US08985082

    申请日:1997-12-04

    Abstract: A process and a set of equipment for reactivating spent activated carbon onto which pollutants were adsorbed. The present process comprises subjecting the activated carbon to be reactivated in a mixed solution consisting of ethanol, sodium hydroxide solution and water to effectuate the desorption of the pollutants adsorbed on the activated carbon. The equipment includes (A) a mixing tank for mixing given amounts of water, ethanol and sodium hydroxide solution which are supplied from the respective receptacles thereof; (B) a reactivation reactor for receiving the mixed solution from the mixing tank and subjecting the spent activated carbon filled therein to the mixed solution to effect the desorption of the pollutants adsorbed on the spent activated carbon, wherein the reactivation reactor includes a unit for regulating temperature of the mixed solution; and (C) a storage tank for receiving the reactivated carbon.

    Abstract translation: 一种用于重新吸附污染物的废活性炭的工艺和一套设备。 本方法包括使活性炭在由乙醇,氢氧化钠溶液和水组成的混合溶液中再活化,以实现吸附在活性炭上的污染物的解吸附。 该设备包括(A)混合罐,用于混合从其各自的容器供给的给定量的水,乙醇和氢氧化钠溶液; (B)还原反应器,用于接收来自混合罐的混合溶液并将填充在其中的废活性炭进行混合溶液以实现吸附在废活性炭上的污染物的解吸附,其中再活化反应器包括用于调节 混合溶液的温度; 和(C)用于接收再活化碳的储罐。

    Methane for regenerating activated carbon
    10.
    发明授权
    Methane for regenerating activated carbon 失效
    用于再生活性炭的甲烷

    公开(公告)号:US3639265A

    公开(公告)日:1972-02-01

    申请号:US3639265D

    申请日:1970-03-13

    Applicant: WESTVACO CORP

    Inventor: JOHNSON HOMER R

    CPC classification number: C01B17/164 B01D53/526 C01B32/36 Y10S502/517

    Abstract: In a process where sulfur oxides have been removed from gas streams by adsorption onto activated carbon in the form of sulfuric acid, regeneration of the sulfuric acid laden activated carbon is accomplished in two stages by first contact the carbon at a temperature below 570* F. with hydrogen sulfide to form sulfur dioxide, which is recovered, and elemental sulfur which remains adsorbed on the carbon. The carbon with elemental sulfur adsorbed thereon is then contacted in the second stage with methane or natural gas at temperatures between from 800* to 1,300* F. to form hydrogen sulfide for the first stage and carbon disulfide. The addition of water, as steam, to the second stage converts the carbon disulfide to additional amounts of hydrogen sulfide for use in the first stage.

    Abstract translation: 在通过以硫酸的形式吸附到活性炭上将硫氧化物从气流中除去的过程中,负载硫酸的活性炭的再生通过首先在低于570°F的温度下接触碳来分两步完成。 与硫化氢反应形成二氧化硫,并回收残留在碳上的元素硫。 然后在其上吸附有元素硫的碳在800至1300℃之间的温度下与甲烷或天然气接触,以形成第一阶段的硫化氢和二硫化碳。 将水作为蒸汽加入到第二阶段将二硫化碳转化成额外量的硫化氢以用于第一阶段。

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