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    • 42. 发明申请
    • Hybrid Energy System
    • 混合动力系统
    • US20080314726A1
    • 2008-12-25
    • US12066185
    • 2006-09-08
    • Edek Choros
    • Edek Choros
    • C10B49/02C10B47/06C10B53/00C10G1/02
    • C10B53/00C01B2203/0233C01B2203/065C01B2203/84C10G1/002C10G1/02F01K23/064F02C3/22F02C6/18
    • A hybrid method for producing energy from a carbonaceous material including the steps of: heating the carbonaceous material under a reduced oxygen atmosphere in a distillation plant to generate distillate vapours; processing the resulting distillate vapours; transferring the char residue from the distillation plant to a power station boiler; and combusting the char residue in the power station boiler for the generation of electrical power. The char residue is transferred to a power station boiler while the char residue retains heat from the heating in the distillation plant. An integrated energy conversion system including: a distillation plant for the destructive distillation of carbonaceous material to afford distillate vapours and a char residue; a power station boiler; a means of transferring the char residue at a temperature between 300 to 700° C. from the distillation plant to the bed power station; and collection means for the distillate vapours.
    • 一种用于从碳质材料制备能量的混合方法,包括以下步骤:在蒸馏设备中在还原氧气氛下加热碳质材料以产生蒸馏蒸汽; 处理生成的蒸馏蒸气; 将焦炭残余物从蒸馏设备转移到电站锅炉; 并在发电厂锅炉中燃烧焦炭以产生电力。 焦炭残渣转移到电站锅炉,而焦炭残留物则保留了蒸馏设备中加热的热量。 一种综合能量转换系统,包括:用于碳质材料的破坏性蒸馏以提供馏出物蒸气和焦炭残渣的蒸馏设备; 电站锅炉; 将焦炭残余物在300-700℃的温度从蒸馏设备转移到床发电站的方法; 以及用于蒸馏蒸汽的收集装置。
    • 44. 发明申请
    • Smokeless porous carbon production method and its production system
    • 无烟多孔碳生产方法及其生产体系
    • US20050051918A1
    • 2005-03-10
    • US10487510
    • 2002-07-26
    • Shigeo MuramatsuMotohiro Shigyo
    • Shigeo MuramatsuMotohiro Shigyo
    • C10B49/02C10B53/02C01B31/02B29C67/20
    • C10B53/02C10B49/02Y02E20/12Y02E50/10Y02E50/14Y02E50/30
    • A smokeless porous carbon production method and its production system in which porous carbon is produced by heat treating a large amount of material, e.g. wood or bamboo, efficiently in a short time with thermal energy generated by combusting combustible gas produced by heating the material, without combusting the material completely by regulating inflow of air. The smokeless porous carbon production system comprises a sequential carbonization chamber (12) for heating a material M, e.g. wood or bamboo, charged in from a material charging opening from below to carbonize the material sequentially and to generate combustible gas, a high heat treatment chamber (13) disposed below the sequential carbonization chamber continuously thereto, a residual gas combustion chamber (16) communicating with the high heat treatment chamber through a lower opening, an exhaust pipe (17) disposed continuously to the residual gas combustion chamber while being directed upward, and means for taking out an intermediate carbide subjected to high heat treatment in the high heat treatment chamber to the outside of a furnace, wherein air regulation openings (15) for taking in an appropriate amount of outer air are provided in the outer walls of the high heat treatment chamber and the residual gas combustion chamber.
    • 无烟多孔碳制造方法及其制造方法,其中通过热处理大量的材料,例如, 木材或竹子,在短时间内有效地通过燃烧通过加热材料产生的可燃气体而产生的热能,而不会通过调节空气的流入而完全燃烧材料。 无烟多孔碳生产系统包括用于加热材料M的顺序碳化室(12),例如, 木材或竹子,从下方的材料加料口装入,以顺序地碳化材料并产生可燃气体;连续地设置在顺序碳化室下方的高热处理室,连接到连续碳化室的残余气体燃烧室, 通过下开口的高热处理室,连续设置在残留气体燃烧室的同时朝向上方的排气管(17),以及用于取出在高热处理室中进行高热处理的中间碳化物的装置 在高温处理室和残留气体燃烧室的外壁上设置有用于吸入适量外部空气的空气调节开口(15)的炉外部。
    • 46. 发明授权
    • Counterflow mild gasification process and apparatus
    • 逆流温和气化工艺及装置
    • US4967673A
    • 1990-11-06
    • US285503
    • 1988-12-16
    • Robert D. Gunn
    • Robert D. Gunn
    • C10B49/02C10B53/00C10J3/02
    • C10B53/00C10B49/02C10J3/02C10J3/32C10J2200/156C10J2200/158C10J2300/0956C10J2300/0959C10J2300/1276Y02P20/145
    • This counterflow mild gasification process and apparatus utilizes reverse or counterflow combustion to pyrolyze or dry and gasify a carbonaceous reactant, such as a solid fossil fuel or solid biological waste. The solid carbonaceous material fills an elongated combustion chamber where it is ignited to create an advancing combustion front. An oxidant is introduced such that it flows in a direction opposite the advance of the combustion front. The system temperature and velocity of combustion front are controlled by pressure, the purity of the oxidant, and the moisture content of the carbonaceous reactant, as well as by the inlet temperature and flow rate of the oxidant and the initial bed temperature of the carbonaceous reactant. For example, either increasing the pressure, increasing the purity of the oxidant, or decreasing the moisture content of the carbonaceous reactant reduces the system temperature of the combustion chamber and increases the combustion front velocity to result in higher quality end product gases, including hydrocarbons and methane.
    • 这种逆流温和气化过程和装置利用反向或逆流燃烧来热解或干燥并气化碳质反应物,例如固体化石燃料或固体生物废物。 固体碳质材料填充细长的燃烧室,其中它被点燃以产生前进的燃烧前沿。 引入氧化剂使得其沿与燃烧前沿的前方相反的方向流动。 燃烧前沿的系统温度和速度通过压力,氧化剂的纯度和碳质反应物的水分含量以及氧化剂的入口温度和流速以及碳质反应物的初始床温度来控制 。 例如,增加压力,提高氧化剂的纯度或降低含碳反应物的含水量可降低燃烧室的系统温度,并增加燃烧前沿速度,从而产生更高质量的最终产品气体,包括烃类和 甲烷。
    • 47. 发明授权
    • Pyrolysis and combustion apparatus
    • 热解和燃烧装置
    • US4732092A
    • 1988-03-22
    • US947866
    • 1986-12-30
    • Orval E. Gould
    • Orval E. Gould
    • C10B1/04C10B49/02C10B53/00C10B53/07C10J3/66F23G5/027F23G5/24F23G5/44F23G5/12
    • C10B49/02C10B1/04C10B53/00C10B53/07C10J3/40C10J3/66C10J3/723F23G5/027C10J2200/156C10J2300/0946C10J2300/1606C10J2300/165Y02P20/143
    • A system for pyrolysis and combustion of combustible solid material, such as waste, which comprises a pyrolysis chamber having a series of spaced vertically disposed movable grates, forming a plurality of stages in the pyrolysis chamber and permitting downward movement of solid feed material at a controlled rate countercurrent to the upward flow of hot gaseous products, the movable grates being synchronized for successive actuation whereby the charge of feed material is successively passed through each of the stages to the bottom of the pyrolysis chamber. Inlet lines are provided for introducing air into each of such stages and into the bottom of the pyrolysis chamber. A feed-lock apparatus is provided for feeding combustible solid feed material into the upper section of the pyrolysis chamber; the feed-lock apparatus includes a hopper for receiving particulate feed material and a ram for compressing the particulate feed material into a compacted block which temporarily functions as a gas seal from the pyrolysis chamber, and for introducing the compacted block into the upper section of the pyrolysis chamber. An exit conduit is also provided for removing overhead fuel gas from the pyrolysis chamber, and an ejector is provided for introducing the overhead fuel gas from the exit conduit into a combustion chamber, and for passage of the combustion gases to a heat load. A diverter valve and throttle valve are provided in the exit conduit for selectively diverting overhead fuel gas or for throttling the process, when desired, e.g., for safety reasons. A water-filled discharge conveyor is provided for quenching the ash and other non-combustible material and carbon in the bottom of the pyrolysis chamber, and removing the resulting slurry therefrom.
    • 用于热解和燃烧可燃固体材料(例如废物)的系统,其包括具有一系列间隔开的垂直设置的可移动格栅的热解室,在热解室中形成多个级,并允许固体进料在受控的 速率与热气体产物的向上流动逆流,可移动格栅同步以进行连续致动,由此进料的进料依次通过每个级到达热解室的底部。 提供入口管线用于将空气引入每个这样的阶段并进入热解室的底部。 提供了一种进料锁定装置,用于将可燃固体进料输送到热解室的上部; 进给锁定装置包括用于接收颗粒状进料的料斗和用于将颗粒状进料输送到临时用作来自热解室的气体密封件的压块中的压头,并将压实块引入到 热解室。 还提供出口导管,用于从热解室中除去顶部燃料气体,并且提供喷射器用于将塔顶燃料气体从出口导管引入燃烧室,并使燃烧气体通过热负荷。 在需要的情况下,例如为了安全起见,在出口管道中设置有分流阀和节流阀,用于选择性地转向架空燃料气体或用于节流过程。 提供了一种充水排放输送机,用于淬火热解室底部的灰分和其他不可燃材料和碳,并从中除去得到的浆料。
    • 48. 发明授权
    • Process for heating recycle gas in oil shale retorting
    • 在油页岩蒸煮中加热回收气体的方法
    • US4436611A
    • 1984-03-13
    • US510291
    • 1983-07-01
    • Louis H. JaquayMark Venetti
    • Louis H. JaquayMark Venetti
    • C10G1/02C10B49/02C10B53/06
    • C10G1/02
    • Recycle gas for the indirect retorting of oil shale, is heated after the oil has been recovered from the gas, utilizing the residual carbon in hot oil depleted shale. The hot oil depleted shale is charged into a vertical shaft furnace where it is combusted by the introduction of air into the upper portion of the furnace. The heat so generated is recovered from the lower part of the furnace for heating the recycle gas and cooling the spent shale. A portion of the coarse fraction of the cooled spent shale discharged from the bottom of the furnace is recycled to the top to regulate the temperature of combustion. The recycle gas may be heated directly by countercurrent contact with the hot, spent shale in the lower portion of the furnace or indirectly in a heat exchanger by an inert gas which is circulated through the lower portion of the furnace. The gaseous products of stoichiometric combustion of the residual carbon from the upper part of the furnace are withdrawn at an intermediate level with, and as a component of, the recycle or inert gas withdrawn from the bottom of the furnace.
    • 油页岩的间接蒸馏回收利用气体,在石油从天然气中回收之后被加热,利用热油耗尽的页岩中的残留碳。 将热油耗尽的页岩充入垂直竖炉中,其中通过将空气引入炉的上部而燃烧。 所产生的热量从炉的下部回收,用于加热循环气体并冷却废页岩。 从炉底部排出的冷却的废页岩的粗部分的一部分被再循环到顶部以调节燃烧温度。 循环气体可以直接通过与炉的下部的热的废页岩逆流接触或通过在炉的下部循环的惰性气体在热交换器中间接加热。 来自炉上部的残留碳的化学计量燃烧的气态产物在与从炉底排出的再循环或惰性气体的中间水平作为中间水平被排出。
    • 50. 发明授权
    • Method and apparatus for conservation of heat from sludge produced by a
retort
    • 由蒸馏器生产的污泥保存热量的方法和装置
    • US4226699A
    • 1980-10-07
    • US925468
    • 1978-07-17
    • John F. Nutter
    • John F. Nutter
    • C10G1/02C10B49/02
    • C10G1/02
    • In a process for the retorting of oil shale wherein hot flue gases containing oxygen are used for preheating the raw oil shale and wherein, additionally, a combustible sludge containing particulate matter and bottoms oil is produced, method and apparatus are disclosed for forming a combustible mixture of the sludge and the gases whereby the sludge is combusted to raise the temperature of the gases and produce only entrained particulate matter as a by-product. By so doing, the requirement for additional fuel to heat the gases to operational temperatures is reduced and the sludge is eliminated as a by-product of the process requiring separate disposal. Rather, the entrained particulate matter is removed and disposed of along with particulate matter normally produced within the process.
    • 在用于对含有氧气的热烟道气进行预热的油页岩进行蒸馏的方法中,另外还生产含有颗粒物和底部油的可燃性污泥,用于形成可燃混合物的方法和装置 的污泥和气体,由此污泥被燃烧以升高气体的温度,并且仅产生作为副产物的夹带的颗粒物质。 通过这样做,减少了将气体加热到操作温度的额外燃料的需求,并且作为需要单独处理的过程的副产物消除污泥。 相反,夹带的颗粒物质被除去并与在该过程中通常产生的颗粒物质一起处理。