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    • 2. 发明授权
    • Stratifier apparatus for engines
    • 发动机分层装置
    • US5899195A
    • 1999-05-04
    • US21627
    • 1998-02-09
    • Joseph C. Firey
    • Joseph C. Firey
    • F02B17/00F02M59/30F02M59/32F02M69/00F02M71/00
    • F02M59/30F02B17/00F02M59/32F02M69/00F02M71/00Y02T10/12
    • Engine stratifier apparatus is described, for use with piston internal combustion engines, to create stratified air fuel vapor mixtures within the engine combustion chamber. A fuel rich air fuel vapor mixture is created within a separate chamber, and then displaced into the engine combustion chamber, where it mixes with air and contained therein. The consequently leaner air fuel vapor mixture is spark ignited following mixing, and burning takes place. Very lean overall air fuel ratios can be used since a stratified mixture is created. Hence intake air throttling is unnecessary and thus engine efficiency is improved. The essential absence of liquid fuel during burning in the engine combustion chamber, largely prevents the formation of soot, and thus reduces undesirable exhaust smoke.
    • 发动机分层装置描述为与活塞内燃机一起使用,以在发动机燃烧室内产生分层的空气燃料蒸汽混合物。 在独立的室内产生富燃料的空气燃料蒸气混合物,然后移入发动机燃烧室,在那里它与空气混合并容纳在其中。 因此,较稀的空气燃料蒸汽混合物在混合之后被火花点燃,并且发生燃烧。 可以使用非常精细的总体空气燃料比,因为产生分层混合物。 因此,进气空气节流是不必要的,因此发动机效率提高。 在发动机燃烧室燃烧过程中基本不存在液体燃料,很大程度上防止了烟灰的形成,从而减少了不期望的废气烟雾。
    • 4. 发明授权
    • Steady work output rate apparatus for cyclic solid with gas reactors
    • 具有气体反应器的循环固体稳定工作输出率装置
    • US4889539A
    • 1989-12-26
    • US349526
    • 1989-05-09
    • Joseph C. Firey
    • Joseph C. Firey
    • C10J3/04C10J3/20C10J3/78F01K25/00
    • F01K25/00C10J3/04C10J3/20C10J3/723C10J3/78
    • The use of pressure regulating values and tanks on compressor outlets and expander inlets of cyclic solid with gas reaction plants is described, together with the use of separate changeable gas flow passages and connection places into the reaction chambers from separate compressor and expander.With thee pressure regulating values and tanks the net rate of work of a cyclic solid with gas reaction plant need not fluctuate and can be held steady.With these separate gas flow passages the flow of reactant gas into the solid reactant during compression will be different in place from the flow of reacted gas out of the solid reactant during expansion. These differences of gas flow place can be useful for securing complete reaction of the solid reactant and for preventing carryover of soaid materials into the expander.
    • 描述了使用气体反应设备在压缩机出口和循环固体的膨胀器入口处使用压力调节值和罐,以及使用单独的可变气流通道和从单独的压缩机和膨胀器连接到反应室中。 随着压力调节值和油箱的循环固体与气体反应装置的净工作效率无波动,可以保持稳定。 利用这些单独的气体流动通道,在压缩过程中进入固体反应物的反应物气体的流动将在膨胀期间与反应气体流出固体反应物的位置不同。 气流位置的这些差异可用于确保固体反应物的完全反应并且用于防止所堆积的材料进入膨胀机。
    • 7. 发明授权
    • Cyclic char gasifier
    • 循环焦炭气化炉
    • US4509957A
    • 1985-04-09
    • US552398
    • 1983-11-16
    • Joseph C. Firey
    • Joseph C. Firey
    • C10J3/04C10J3/20C10J3/30C10J3/78E21B43/243C10J3/00C10J3/22
    • E21B43/243C10J3/04C10J3/20C10J3/30C10J3/721C10J3/723C10J3/78C10J3/82C10J2200/09C10J2300/0916C10J2300/092C10J2300/093C10J2300/0946C10J2300/0956C10J2300/0959C10J2300/0976C10J2300/1253C10J2300/1671C10J2300/1823C10J2300/1846Y10S48/06
    • A cyclic char gasifier process and apparatus are described wherein reactant gases are first compressed into the pores of a char fuel to react and then the reacted gases are expanded out of the char fuel pores. This cycle of compression and expansion is repeated with fresh reactant gases supplied for each compression and with reacted gases removed at each expansion. Air and steam are preferred reactant gases when the char fuel is to be gasified by oxidation. Reacted gases from such an oxidation gasifier plant are preferred reactant gases when the char fuel is to be partially gasified by devolatilization. Rapid reaction to a rich product gas can occur over the large surface area inside the char pores and the undesireable Neumann reversion reaction is suppressed by the strongly reducing conditions prevailing therein. The gases of devolatilization gasification can be used to enrichen the gases of oxidation gasification by using two cyclic char gasifier plants in a combination system. The char fuel can be placed into sealed pressure vessel containers or can be gasified in place within an underground coal formation. These cyclic char gasifier plants and systems can produce a net work output, one or more fuel gases, a devolatilized char, and a partially oxidized coke as principal products and the proportions of these products can be adjusted over a wide range to match market needs.
    • 描述了一种循环焦化气化器工艺和装置,其中首先将反应气体压缩到焦炭燃料的孔中进行反应,然后反应的气体从焦炭燃料孔中膨胀出来。 用每次压缩提供的新鲜反应气体和每次膨胀时除去反应的气体来重复这种压缩和膨胀循环。 当炭燃料通过氧化气化时,空气和蒸汽是优选的反应气体。 来自这种氧化气化炉设备的反应气体是当焦炭燃料通过脱挥发分部分气化时的优选的反应气体。 对丰富的产物气体的快速反应可以发生在焦炭孔内的大表面积上,并且不期望的诺依曼逆转反应被其中主要的强烈还原条件抑制。 挥发气化气体可用于通过在组合系统中使用两个循环气化炉装置来浓缩氧化气化气体。 炭燃料可以放置在密封的压力容器容器中,或者可以在地下煤层内气化到位。 这些循环焦化气化炉工厂和系统可以产生净工作产出,一种或多种燃料气体,脱挥发分焦炭和部分氧化焦炭作为主要产品,并且可以在广泛的范围内调整这些产品的比例以匹配市场需求。