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    • 6. 发明申请
    • A PROCESS OF RESTORATION OF BARREN LAND DEVOID OF VEGETATION OR REQUIRING BIOLOGICAL RECULTIVATION AND A MINERAL FERTILIZER ESPECIALLY FOR THE PURPOSE OF LAND RECULTIVATION AND A METHOD FOR MANUFACTURING THE SAME
    • 恢复植被的荒地土壤或需要生物再生和矿物肥料的过程,特别是为了土地复垦的目的和生产同样的方法
    • WO2016034937A3
    • 2016-05-26
    • PCT/IB2015001518
    • 2015-09-04
    • GREEN HILLS SP Z O OMEZYK PIOTR
    • MEZYK PIOTR
    • A01G13/00B09B3/00C05D9/00C05F11/04F23G5/00
    • C05D9/00A01G13/0262A01G2013/004B09B3/0083B09C2101/00C05F11/04F23G5/20F23G7/001F23G7/10F23G2201/70F23G2201/80F23G2203/20F23G2900/50401Y02A40/284Y02E20/12C05F11/00
    • The present invention relates to a process for restoration of barren land devoid of vegetation or requiring biological recultivation,, wherein the surface of a native ground is covered with a basic layer of semi-liquid recultivation mass prepared on a basis of waste fibrous materials, the layer having thickness of several to several dozens centimeters; in that basic layer there are watering pipes uniformly distributed; after its hardening the basic layer is covered with a top layer of dry mass prepared on a basis of waste fibrous materials, the layer having thickness of several to several dozens centimeters and comprising a hydrogel, adsorbents, as well as plant seeds optionally enveloped with symbiotic mycelium and/or microorganism strains, adjusted to climatic conditions, the character and nature of the native ground, further comprising additives supporting and enhancing vegetation of those plants; and next on the surface of the thus prepared top layer, remaining plant seeds are sown and/or the plants to be cultivated or seedlings thereof are planted; and the degree of wetness of both layers is controlled according to the plants' vegetation phase and climatic conditions prevailing at the recultivated spot of land According to the invention as the additive supporting and enhancing plants' vegetation, there is used a fertilizer in form of cinder(s) and flue gas dust from high temperature process of combustion of pre-segregated and sorted, properly chipped and mixed wastes, in particular municipal wastes, that are unsuitable for a direct use as a soil-forming material, optionally with an addition of very fine grain coal and chemical compounds neutralizing aggressive substances, supplemented with missing nutritive components. The fertilizer is obtained in result of combustion of the above indicated wastes in temperature of minimum 1200°C. The invention relates also to a method for manufacturing a mineral fertilizer, especially for the purpose of land recultivation, in which the properly pre-segregated and sorted, chipped and mixed wastes that are unsuitable for a direct use as a soil-forming material, are subjected to incineration and the thus obtained - and positively verified in the course of respective chemical analysis, cinder(s) and flue gas dust free from any substance adversely affecting natural environment and plants' vegetation are optionally supplemented with missing mineral components, while the heat energy resulting from combustion of pre-segregated and sorted wastes is either utilized directly for the purpose of municipal and/or industrial heating, or cumulated for the future municipal and/or industrial heating purposes.
    • 本发明涉及用于恢复不含植物或需要生物再培养的荒地的方法,其中天然地面的表面覆盖有基于废弃纤维材料制备的半液体再生物质的碱性层,所述 厚度为几到几十厘米的层; 在该基层中有均匀分布的浇水管; 在其硬化之后,基层覆盖有基于废弃纤维材料制备的干物质的顶层,所述层具有几厘米至几十厘米的厚度并且包含水凝胶,吸附剂以及任选地被共生物包封的植物种子 调节气候条件,天然地面的特性和性质的菌丝体和/或微生物菌株,其进一步包含支持和增强那些植物植物的添加剂; 接着在如此制备的顶层的表面上播种剩余的植物种子和/或种植待栽培的植物或其幼苗; 并根据植物的植被相和气候条件来控制两层的湿度。根据本发明,作为添加剂支持和增强植物的植物,使用以煤渣形式的肥料 以及预分离和分选的,适当碎裂的和混合的废物,特别是市政废物的高温燃烧过程中不适合直接用作成土材料的烟尘和烟尘,任选地添加 非常细的煤和化学化合物中和腐蚀性物质,补充缺失的营养成分。 由于上述废物在最低1200°C的温度下燃烧,因此可获得肥料。 本发明还涉及一种用于制造矿物肥料的方法,特别是用于土地复垦的目的,其中不适合直接用作土壤形成材料的适当的预分离和分选的碎片和混合的废物是 进行焚烧并由此获得 - 并且在各自的化学分析过程中得到肯定的验证,不含对任何对自然环境和植物的植物造成不利影响的物质的煤渣和烟道气粉尘可选地补充缺失的矿物组分,而热量 由预分离和分选的废物燃烧产生的能量要么直接用于市政和/或工业加热的目的,要么为将来的市政和/或工业加热目的而累积。
    • 7. 发明申请
    • A GASIFIER
    • 气化器
    • WO2016001676A1
    • 2016-01-07
    • PCT/GB2015/051937
    • 2015-07-02
    • DPS BRISTOL (HOLDINGS) LIMITED
    • PARKINSON, David John
    • C10J3/00C10J3/30C10J3/32C10J3/36C10J3/66F23G5/28
    • C10J3/66C10J3/005C10J3/30C10J3/32C10J3/36C10J3/526C10J2200/09C10J2200/152C10J2200/158C10J2300/0946F23G5/0273F23G5/26F23G2201/303F23G2201/304F23G2203/20F23G2205/121F23G2206/10
    • There is disclosed a gasifier (500) comprising: a gasification chamber (518); a feedstock inlet (520) opening into the gasification chamber (518) for introducing feedstock material and primary combustible gas; a gas outlet (523) opening into the gasification chamber; and a flow path between the feedstock inlet (520) and the gas outlet (523) which passes through the gasification chamber (518), a portion of the flow path having an upwards component within the gasification chamber so that particulate material entrained in the primary combustible gas separates from the primary combustible gas and falls towards the bed of feedstock material. There is also disclosed a gasifier (500) comprising: a chamber wall (510) defining a gasification chamber (518); an ash grate (526) disposed in the gasification chamber (518); and a rotary crusher (532) disposed in the gasification chamber (518) above the ash grate (532) and provided with at least one crushing element (536); wherein in use rotation of the crusher causes agglomerated feedstock material in the bed to break apart between the crushing element and an opposing surface.
    • 公开了一种气化器(500),包括:气化室(518); 原料入口(520),其通向气化室(518),用于引入原料和初级可燃气体; 通向气化室的气体出口(523); 以及通过所述气化室(518)的所述原料入口(520)和所述气体出口(523)之间的流动路径,所述流动路径的一部分在所述气化室内具有向上的组分,使得夹带在所述初级 可燃气体与主要可燃气体分离,并向原料材料床落下。 还公开了一种气化器(500),包括:限定气化室(518)的室壁(510); 布置在气化室(518)中的灰篦(526); 以及设置在所述炉篦(532)上方的所述气化室(518)中并且设置有至少一个破碎元件(536)的旋转式破碎机(532); 其中在使用中,所述破碎机的旋转引起所述床中的附聚原料材料在所述破碎元件与相对表面之间分离。
    • 8. 发明申请
    • METHOD AND PROCESS FOR CO-COMBUSTION IN A WASTE-TO-ENERGY FACILITY
    • 在废物处理设施中共同燃烧的方法和方法
    • WO01059366A1
    • 2001-08-16
    • PCT/GB2001/000420
    • 2001-02-05
    • C04B7/43C04B7/44F23G5/00F23G5/16F23G5/20F23G5/46
    • C04B7/4407C04B7/43C04B2290/20F23G5/006F23G5/16F23G5/20F23G5/46F23G2201/303F23G2202/103F23G2203/20F23G2206/201F23G2900/50001F23J2219/60Y02E20/12Y02E20/363Y02P40/123
    • The co-combustion process may comprise the following unit operations: routing of hot gas (10) generated in the clinker cooling process to a rotary kiln (1); use of part of the rotary kiln exhaust gas to dry solid wastes in rotary dryers; leading the gases from both the dryer and the combustion kiln to the secondary combustion chamber (2); use of additional fuel to boost up the secondary combustion chamber reaction temperature to as high as 1200 DEG C; primary dry gas scrubbing in a precalciner or precalciners (3, 3a); heat recovery (4) and power generation; secondary gas scrubbing (5) in a semi-dry scrubber; bag filtering after activated carbon injection and returning of all the collected ash and used carbon into the waste kiln and/or a cement kiln. Detrimental materials for cement processing generated by waste combustion can be by-passed to a scrubbing system and a cement kiln. Residue slag from waste kilns can be treated and reused.
    • 共燃过程可以包括以下单元操作:将在熟料冷却过程中产生的热气(10)路由到回转窑(1); 使用部分回转窑废气将旋转干燥器中的固体废物干燥; 将来自干燥器和燃烧窑的气体引导到二次燃烧室(2); 使用额外的燃料将二次燃烧室的反应温度升高到高达1200℃; 在预分解器或预煅烧器(3,3a)中进行初级干燥气体洗涤; 热回收(4)和发电; 二次气体洗涤(5)在半干洗涤器中; 活性炭注入后的袋过滤,将所有收集的灰分和废碳返回到废窑和/或水泥窑中。 通过废物燃烧产生的水泥加工的有害材料可以被旁路到洗涤系统和水泥窑。 来自废窑的残渣可以被处理和再利用。
    • 10. 发明申请
    • PROCESS FOR DISPOSAL OF WASTE BY COMBUSTION WITH OXYGEN
    • 通过与氧气混合处理废物的方法
    • WO1989003241A1
    • 1989-04-20
    • PCT/EP1988000927
    • 1988-10-15
    • FISCHER, ReinhardMENGES, Georg
    • B01D53/34
    • F23G5/46F23G5/006F23G2203/20F23G2900/00001F23J15/025F23J2217/103F23L7/007F23L2900/07007Y02E20/344Y02P80/152
    • The process described comprises the following steps: a) combustible waste materials in solid, paste or liquid form are burnt in an incinerator with a combustion gas containing at least 50 % oxygen. Non-ferrous metals and/or non-ferrous metallic compounds and/or non-ferrous metallic oxides and/or alkaline compounds and/or alkaline earth compounds are present as a result of combustion of substances which yield them together with the waste and/or of the inclusion of corresponding compounds in the combustion plant together with the charge of waste materials or in the hot gas stream, and if necessary with the addition of additional charges to the charge of waste materials; b) the temperature in the combustion chamber is reduced to the range of 1200 to 1500 DEG C; c) the flue gases are cooled in a waste heat boiler and the waste heat is recovered; d) soot is removed in a gas purifier; e) non-combustible, non-volatile residues are removed in the form of slag.
    • 所述方法包括以下步骤:a)固体,糊状或液体形式的可燃废料在含有至少50%氧气的燃烧气体的焚化炉中燃烧。 有毒金属和/或有色金属化合物和/或有色金属氧化物和/或碱性化合物和/或碱土金属化合物由于与废物和/或 在燃烧设备中加入相应的化合物以及废物的装料或热气流,如有必要,还需要额外的费用加入废料; b)燃烧室内的温度降低到1200〜1500℃的范围; c)废气在废热锅炉中冷却,废热回收; d)在气体净化器中除去烟灰; e)以炉渣的形式除去不燃的非挥发性残留物。