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    • 2. 发明申请
    • PROCESS FOR PRODUCING CEMENT USING A SECONDARY FUEL
    • 使用二次燃料生产水泥的工艺
    • WO2017001638A1
    • 2017-01-05
    • PCT/EP2016/065444
    • 2016-06-30
    • SUBCOAL INTERNATIONAL B.V.
    • JENNISSEN, LarsROBERTS, Neville
    • C04B7/44C10L5/40
    • C04B7/4423C10L5/363C10L5/40C10L5/403C10L5/406C10L5/44C10L5/442C10L5/445C10L2250/06Y02E50/10Y02E50/30Y02P40/126
    • The invention provides a process for producing cement, the process comprising providing heat to a cement manufacturing process using a secondary fuel, wherein the secondary fuel comprises cellulose and plastic and is in the form of pellets of a size between about 3-25 mm thickness, having a calorific value of about 16 GJ/ton or more, and wherein said secondary fuel is supplied at a place between the kiln inlet and the first cyclone, wherein after formation of the cement clinker, the cement clinker is cooled and milled to cement powder. Preferably, the secondary fuel is supplied to the riser pipe or to a pre-kiln combustion chamber. Generally, the secondary fuel is provided at a place which allows the pellets to burn before coming in contact with the cement materials in the kiln, while it also does not rise into the cyclone, thereby preventing blocking of the cyclones.
    • 本发明提供了一种生产水泥的方法,该方法包括使用二次燃料向水泥制造过程提供热量,其中二次燃料包括纤维素和塑料,并且是尺寸在约3-25mm厚度之间的颗粒形式, 具有约16GJ /吨以上的发热量,并且其中所述二次燃料在窑入口和第一旋风器之间的地方供应,其中在形成水泥熟料之后,将水泥熟料冷却并研磨成水泥粉 。 优选地,二次燃料被供应到提升管或预窑燃烧室。 通常,二次燃料设置在允许颗粒在与窑内的水泥材料接触之前燃烧的地方,同时它也不会进入旋风分离器,从而防止旋风分离器的堵塞。
    • 4. 发明申请
    • POWDERY ALTERNATIVE FUEL
    • WO2022248626A1
    • 2022-12-01
    • PCT/EP2022/064334
    • 2022-05-25
    • SUBCOAL INTERNATIONAL B.V.
    • JENNISSEN, Lars
    • C10L5/40
    • The invention relates to a method to produce powdery alternative fuel by milling pellets, which pellets are produced by: (i) providing waste material comprising one or more thermoplastic material(s) of more than 40%, based on the total dry weight of the waste and one or more cellulosic material(s) of more than 30%, based on the total dry weight of the waste, wherein the waste has a particle size distribution with more than 80 wt% larger than 5 mm and more than 95 wt% smaller than 60 mm, having a water content of about 8 wt% or less; (ii) subjecting the waste material through a pelletiser with holes between 4-8 mm, and a length ratio of more than 10, such that the output temperature is about 85 ºC or lower, (iii) subjecting the pellets through a second pelletiser with holes between 2 and 8 mm, and a length ratio of more than 14, such that the output temperature is about 110 ºC or higher; (iv) to provide pellets, (v) and the pellets are cooled to a temperature of about 30 ºC or lower. The powdery alternative fuel can be transported in bulk and through blowing lines.