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    • 6. 发明公开
    • METHOD FOR PREPARING COAL FOR COKE MAKING
    • VERFAHREN ZUR HERSTELLUNG VON KOHLE ZUR KOKSHERSTELLUNG
    • EP2977429A1
    • 2016-01-27
    • EP15182966.0
    • 2013-02-25
    • JFE Steel Corporation
    • DOHI, YusukeSHIMOYAMA, IzumiFUKADA, KiyoshiSUMI, Hiroyuki
    • C10B57/04C10L5/04
    • C10L5/08C10B57/04C10L5/04C10L9/10G01N11/04
    • A method for preparing coal for coke making, on the basis of the relationship between a critical permeation distance and a Gieseler maximum fluidity obtained using permeation distances and the values of Gieseler maximum fluidity of one or more brands of coal or caking additive, the size of particles of an individual brand of coal or caking additive is controlled prior to arrival at a coke plant so that the content of particles having a diameter of 6 mm or more in the individual brand of coal or caking additive reaches 30% by mass or less when the permeation distance of the individual brand of coal or caking additive is larger than or equal to a critical permeation distance calculated from a Gieseler maximum fluidity of the individual brand of coal or caking additive on the basis of the relationship between the critical permeation distance and the Gieseler maximum fluidity.
    • 基于通过使用渗透距离获得的临界渗透距离和Gieseler最大流动性与一种或多种品牌的煤或结块添加剂的Gieseler最大流动性之间的关系,制备用于焦炭的煤的方法, 单个品牌的煤或结块添加剂的颗粒在到达焦炭厂之前被控制,使得单个品牌的煤或结块添加剂中具有6mm或更大直径的颗粒的含量达到30质量%以下 单个品牌的煤或结块添加剂的渗透距离大于或等于根据单个品牌煤或结块添加剂的Gieseler最大流动性计算的临界渗透距离,其基于临界渗透距离和 Gieseler最大流动性。
    • 9. 发明公开
    • PROCEDURE AND EQUIPMENT FOR THE PRODUCTION OF SOLID FUEL FROM WASTEWATER SLUDGE
    • 方法和装置固体燃料的污水淤泥研制
    • EP2739711A2
    • 2014-06-11
    • EP12787067.3
    • 2012-07-31
    • Vereckey, IstvánIfj. Vereckey, IstvánBognár, BélaErcsey, László
    • Vereckey, IstvánIfj. Vereckey, IstvánBognár, BélaErcsey, László
    • C10L5/08C10L5/28C10L5/46C10L5/36C02F11/12
    • C10L5/48C02F11/121C02F11/122C02F11/127C02F11/18C10L5/08C10L5/28C10L5/363C10L5/46Y02E50/10Y02E50/30
    • The subject of the invention relates to the production of solid fuel from wastewater sludge, during which the wastewater sludge containing 2-8% dry material is first subjected to mechanical water removal, during which the absorption water is removed and we produce wastewater sludge with a dry material content of at least 25-30%. The significant proportion of the remaining capillary water, favourably at least half of it, is removed by an accelerated evaporation process, drying. The essence of the procedure is that we pre-dry the wastewater sludge containing at least 25-30% dry material using the heat of the flue gas of the burning equipment operated by us to a dry material content of 50-55%, we extract the steam created and gases released during pre-drying, filtering them if necessary and utilise them by returning them to the burning equipment. We pelletize the wastewater sludge containing 50-55% dry material at a high pressure of, favourably, 800-900 bar, then we perform final drying of the pellet product created in this way to a dry material content of at least 80-85% by making further use of the heat of the flue gas of the burning equipment operated by us. We use a part of the solid pellet final product, favourably at least 30-50% of it as fuel in the burning equipment operated by us. A further subject of the invention relates to equipment for the production of solid fuel from wastewater sludge, which is connected to a mechanical dehydration unit (2) for the feeding of the wastewater sludge (1). The output of this is connected to a final dryer (5) through a pre- dryer (3) and pelletizer extruder (4). Furthermore it contains burning equipment (6) connected to the pre-dryer (3) and final dryer (5). The equipment is set up in such a way that the pre- dryer (3) is a double-walled drum, and there is a spiral-shaped mixing blade fixed inside this drum. The final dryer (5) is fitted with stainless steel bands, and the flue gas output (61) of the burning equipment (6) runs between the steel bands via a heat exchanger (62). The forced- flow air extraction (50) of the final dryer (5) is connected to the input (34) between the two walls of the double-walled drum of the pre-dryer (3), the suction connector (35) of the drum is connected with the combustion chamber of the burning equipment (6), favourably through a filter (64). Furthermore, the output (51) of the final dryer (5) at the end of the steel bands is connected to the burning equipment (6) through the fuel feeder (65).
    • 过程用于从废水污泥生产固体燃料的,和设备适合于进行其制造。
    • 10. 发明公开
    • Method for producing peat
    • Verfahren zur Herstellung von Torf
    • EP2444471A2
    • 2012-04-25
    • EP11186065.6
    • 2011-10-21
    • VAPO OY
    • Mutka, Kari
    • C10F5/02F26B3/28F26B9/10C10L5/08C10L5/36C05F11/04
    • C10F5/02C05F11/02C10L5/08C10L5/363F26B9/10F26B2200/02Y02P20/134
    • The invention relates to a method for producing peat, particularly horticultural and fuel peat, in which
      - the peat is detached from a bog from a deep-peat lifting area (10),
      - the detached peat is transferred, as a high-consistency mass from the lifting area (10) to a drying field (12), where the transferred peat is spread in a thin layer on the surface of the drying field (12) and dried mainly by exploiting solar energy,
      - after drying, the dried peat is transferred from the drying field (12) to further use.
      The drying field (12) is formed on a shallow-peat lifting area (10'), by moving the peat mass of the shallow-peat lifting area (10') from the strips (14) adjacent to the drying field (12) to a stack strip (14') forming the drying field (12), after which the drying field (12) is levelled and compacted before the moving of the peat from the deep-peat lifting area (10) to the drying field (12).
    • 本发明涉及一种用于生产泥炭,特别是园艺和燃料泥炭的方法,其中 - 泥炭从深泥泥提升区域(10)从沼泽分离, - 分离的泥炭被转移,作为高稠度质量 从提升区域(10)到干燥场(12),其中转移的泥炭在干燥区域(12)的表面上以薄层铺展,主要通过利用太阳能干燥,干燥后干燥的泥炭 从干燥场(12)转移到进一步使用。 通过从邻近干燥场(12)的条带(14)移动浅泥炭提升区域(10')的泥炭块,形成在浅泥炭提升区域(10')上的干燥场(12) 到形成干燥场(12)的堆垛条(14'),然后在泥炭从深泥泥提升区域(10)移动到干燥区域(12)之前,干燥区域(12)被平整和压实 )。