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    • 5. 发明申请
    • HYDROCARBON RECYCLING OF CARBONIZER HOT GASES
    • 碳化炉热气的碳氢化合物回收
    • WO2017218162A1
    • 2017-12-21
    • PCT/US2017/034527
    • 2017-05-25
    • AEMERGE LLC
    • MILLER, Landon, C.G.
    • C10B49/02C10B53/06C10B53/07
    • Systems and process are provided for refining off-gases that are produced by a carbonizer with a controlled heated column. The controlled heated column performs hydro-carbon recycling, and acts as a cracking tower that takes the carbonizer off-gas as a feedstock and distills the off-gases into constituent parts under pressure and temperature conditions where the feedstock evaporates and condenses into a fractional column of distillates. The carbonizer uses anaerobic thermal transformation processing to convert waste into bio-gas; bio-oil; carbonized materials; non-organic ash, distillates, and varied further co-products. The carbonaceous waste is transformed into useful co-products that are re-introduced into the stream of commerce at various economically advantageous points including carbon, carbon- based inks and dyes, activated carbon, aerogels, bio-coke, and bio-char, as well as generate electricity, produce adjuncts for natural gas, and /or various aromatic oils, phenols, and liquids, all depending upon the input materials and parameters selected to process the waste.
    • 提供系统和方法用于精炼由具有受控加热柱的碳化器产生的废气。 受控加热塔进行碳氢化合物回收,并充当裂化塔,将碳化器尾气作为原料,并在原料蒸发并冷凝成分馏柱的压力和温度条件下将废气蒸馏成组成部分 的馏分。 碳化器使用厌氧热转化处理将废物转化为生物气体; 生物油; 碳化材料; 非有机灰分,馏分油和各种其他副产品。 碳质废物转化为有用的副产品,在包括碳,碳基油墨和染料,活性炭,气凝胶,生物焦炭和生物炭在内的各种经济有利的点处重新引入到商业流程中,作为 以及生产电力,生产天然气辅助产品和/或各种芳香油,酚类和液体,这些都取决于选择用于处理废物的输入材料和参数。
    • 6. 发明申请
    • DEVICE FOR THE CONTINUOUS THERMAL PROCESSING OF USED OR OTHERWISE DEGRADED TYRES
    • 用于连续使用或其他降级轮胎的热处理设备
    • WO2016019932A1
    • 2016-02-11
    • PCT/CZ2015/000087
    • 2015-08-06
    • ALPAJAR GROUP s.r.o
    • VAŠIČEK, Alois
    • C10B53/07C10K1/04C10B49/02C10G1/10
    • C10B49/02C10B53/07C10G1/10C10K1/026C10K1/04Y02P20/143
    • The device for the continuous processing of used or otherwise degraded tyres consists of a reactor(1) for the thermal decomposition of these waste tyres into the organic decomposition products in the form of low molecular hydrocarbons, and residual inorganic waste shares. In the upper part of the reactor (1) there is created a filling chamber (2) with a pair of filling closures (3) for filling its internal space by the waste tyres and in the bottom part of the reactor (1) there is formed the output chamber (8) of the residual inorganic shares with a pair of output closures (9), while in the lower part of the reactor (1 ) there are arranged the nozzles (5) for generating of a mild gaseous inert medium by oxidation of unreacted residues of organic matter from the processed tyres. In the upper part of the inner space of the reactor (1 ) under the filling chamber (2) is then created at least one output opening (11) of this inert gas media, which, together with the therein dispersed organic decomposed products in the form of aerosol, is led through the separator (12) of solid particles and a cooler (17) into a separator (10) of liquid particles from the cooled aerosol which is equipped with the first end output (21) of the liquid particles into the tank (22) and, second, between-operating output (23) of the gaseous particles, which are led to the direct energy use by combustion in thermal machines or in a convenient implementation they are driven Into the freezing chamber (24) for the separation of gases with a condensing temperature above the temperature in this chamber. From freezing chamber (24) there is ended up the second end output (25) of one part in it non-condensed gases and the third end output (26) of the remaining part in it non-condensed gases.
    • 用于连续处理使用的或以其他方式降级的轮胎的装置由用于将这些废轮胎热分解成低分子烃形式的有机分解产物的反应器(1)和残留的无机废物份额组成。 在反应器(1)的上部,产生一个具有一对填充封闭件(3)的填充室(2),用于通过废轮胎填充其内部空间,并且在反应器(1)的底部有 用一对输出封闭物(9)形成残余无机物份的输出室(8),而在反应器(1)的下部设有用于产生温和气态惰性介质的喷嘴(5) 从加工的轮胎中氧化未反应的有机物残留物。 然后,在填充室(2)下面的反应器(1)的内部空间的上部,形成该惰性气体介质的至少一个输出开口(11),其中分散有有机分解产物 将气溶胶的形式从固体颗粒的分离器(12)和冷却器(17)引导到液体颗粒的分离器(10)中,该冷却的气溶胶装备有液体颗粒的第一端输出(21)进入 气体颗粒的储存箱(22)和第二工作输出(23),它们通过在热机器中燃烧而被引导到直接能量使用,或者在方便的实施中被驱动到冷冻室(24)中 冷凝温度高于该室温度的气体分离。 从冷冻室(24)开始,其中一部分的第二端输出(25)为非冷凝气体,其余部分的第三端输出(26)为非冷凝气体。