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    • 1. 发明授权
    • Process for passivation of reactive coal char
    • 活性炭钝化工艺
    • US5711769A
    • 1998-01-27
    • US525235
    • 1995-09-08
    • Franklin George RinkerDeane Avent HorneDennis Wayne CoolidgeErnest Peter Esztergar
    • Franklin George RinkerDeane Avent HorneDennis Wayne CoolidgeErnest Peter Esztergar
    • C10L9/08C10B39/00C10B49/04C10L5/00C10L9/00C10L9/06C10B21/18
    • C10L9/00C10B39/00
    • A continuous process for treating coal to form stable coal char by passivating the coal and then rehydrating and cooling the product thereof to prevent spontaneous ignition. The process includes the steps of pyrolyzing the coal to vaporize and remove low end volatile materials and to mobilize high end volatile materials and cooling to demobilize the high end volatile materials within the at least partially collapsed micropores of the coal char to pyrolytically passivate the coal char and form a char having about 14-22 wt % high end volatiles. The pyrolytically passivated coal char is then conveyed to a reaction vessel wherein a process gas having about 3%-21% by volume oxygen flows through the reaction vessel to at least partially fluidize the coal char and oxidatively passivate the coal by chemisorption of oxygen. The passivated coal char is then substantially simultaneously rehydrated and cooled to form a stable coal char having about 5-10 wt % moisture.
    • 一种连续的方法,用于通过钝化煤来处理煤形成稳定的煤焦炭,然后再水化和冷却其产物以防止自发点火。 该方法包括以下步骤:将煤焦化以蒸发和除去低端挥发性物质,并动员高端挥发性物质并冷却以使煤焦炭的至少部分塌陷的微孔内的高端挥发性物质复原,以热解钝化煤焦 并形成具有约14-22wt%高端挥发物的炭。 然后将热解钝化的煤炭输送到反应容器,其中具有约3体积%-21体积%的氧气的工艺气体流过反应容器以至少部分地使煤炭流化,并通过化学吸附氧气来氧化煤。 然后将钝化的煤炭基本上同时再水合并冷却,形成约5-10重量%水分的稳定的煤焦炭。
    • 2. 发明授权
    • Process for treating noncaking coal to form passivated char
    • 处理不结块煤形成钝化炭的方法
    • US5601692A
    • 1997-02-11
    • US565851
    • 1995-12-01
    • Franklin G. RinkerDeane A. HorneDennis W. CoolidgeErnest P. Esztergar
    • Franklin G. RinkerDeane A. HorneDennis W. CoolidgeErnest P. Esztergar
    • C10L9/02C10G1/00C10G1/02C10L9/00C10L9/06C10L9/08C10L9/10
    • C10L9/06C10L9/00
    • A continuous process for treating a noncaking coal to form stable char. The process includes the sequential steps of drying the coal to remove moisture therefrom and form a dry coal; pyrolyzing the dry coal by progressively heating substantially all of the coal to a temperature sufficient to vaporize and remove low end volatile materials from the coal to form char and sufficient to mobilize at least a portion of high end volatile materials within the char and at least partially collapse micropores within the char. The char is then cooled to a temperature sufficient to demobilize the volatile materials within the at least partially collapsed micropores of the char to pyrolytically passivate the char. The char is then conveyed to a reaction vessel wherein a process gas having about 3%-21% by volume oxygen flows through the reaction vessel to oxidatively passivate the coal by chemisorption of oxygen. The oxidatively passivated char is then substantially simultaneously rehydrated and cooled to form a char having about 5-10 wt % moisture and then conveyed to a final passivation vessel wherein a process gas having about 3%-21% by volume oxygen flows through the vessel to finally passivate the rehydrated char by chemisorption of oxygen.
    • 一种用于处理不凝煤以形成稳定炭的连续方法。 该方法包括干燥煤以从其中除去水分并形成干燥煤的顺序步骤; 通过将基本上所有的煤逐渐加热到足以蒸发并从煤中除去低端挥发性物质以形成炭并足以在焦炭中至少部分地移动至少一部分高端挥发性物质的温度来热解干煤, 在焦炭内折叠微孔。 然后将炭冷却至足以使焦炭的至少部分收缩的微孔内的挥发性物质复活以使焦炭热解钝化的温度。 然后将炭输送到反应容器,其中具有约3体积%〜21体积%氧气的工艺气体流过反应容器,以通过化学吸附氧气来对煤进行氧化钝化。 然后将氧化钝化的炭基本上同时再水合并冷却以形成具有约5-10重量%水分的焦炭,然后输送至最终钝化容器,其中具有约3体积%-21体积%的氧气的工艺气体流过容器至 最后通过化学吸附氧来钝化再水化的炭。
    • 3. 发明授权
    • Method and apparatus for removing particulate and gaseous pollutants
from a gas stream
    • 从气流中除去微粒和气态污染物的方法和装置
    • US5582807A
    • 1996-12-10
    • US334595
    • 1994-11-04
    • Chung F. LiaoMark A. Siddoway
    • Chung F. LiaoMark A. Siddoway
    • B01D47/06B01D53/50B01D53/79B01D53/78
    • B01D53/79B01D47/06B01D53/501
    • An apparatus and method for removing particulate and gaseous pollutants from flue gas. The flue gas enters a presaturation section and is treated with a coarse spray of solution recovered from the system. The saturated gas enters a primary contacting section and is contacted by an ultrafine mist of fresh solution containing a gaseous pollutant absorption agent. The fine mist has an average droplet size of approximately 20 microns. The gas moves to a secondary contacting section where it is contacted by a coarse spray of recirculated solution. If necessary, the gas is demisted. Finally, the gas is discharged into the environment. Usable spent solution is regenerated and reused. Unusable water byproducts containing contaminants are discharged.
    • 一种从烟气中除去颗粒物和气态污染物的设备和方法。 烟气进入预饱和部分,并用从系统中回收的粗溶液进行处理。 饱和气体进入初级接触部分,并与含有气态污染物吸收剂的新鲜溶液的超细雾接触。 细雾具有约20微米的平均液滴尺寸。 气体移动到二次接触部分,在该二次接触部分中,其被再循环溶液的粗喷液体接触。 如有必要,气体被分离。 最后,气体排放到环境中。 可用的废弃解决方案被重新生成并重新使用。 排出含有污染物的不合适的水副产物。