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    • 3. 发明专利
    • Titania catalyst carrier
    • 泰坦尼亚催化剂载体
    • JP2003311151A
    • 2003-11-05
    • JP2002117288
    • 2002-04-19
    • Ishikawajima Harima Heavy Ind Co Ltd石川島播磨重工業株式会社
    • OKA AKIHIROMIWA KEIICHI
    • C02F1/74B01J21/16B01J32/00C02F11/08
    • PROBLEM TO BE SOLVED: To provide a new titania catalyst carrier which can be produced at a low cost, and surely avoid the corrosion of the components of an extruder when performing extrusion molding.
      SOLUTION: In the titania catalyst carrier 20 made by extruding a green body mainly comprising a titania powder and an inorganic binder to be a prescribed shape and then baking it, a material where an alkaline neutralizing agent in addition to an organic binder, a plasticizer, a lubricant, and water is added to a mixture of the strongly acidic titania powder and the inorganic mixture is used as the green body. Thereby the green body is neutralized and the acidity is surely decreased, which enables the use of the strongly acidic but inexpensive titania power and the prevention of the corrosion of the extruder.
      COPYRIGHT: (C)2004,JPO
    • 要解决的问题:提供可以低成本生产的新的二氧化钛催化剂载体,并且当进行挤出成型时可以避免挤出机的组分的腐蚀。 解决方案:在通过将主要包含二氧化钛粉末和无机粘合剂的生坯体以规定形状挤出然后烘烤而制成的二氧化钛催化剂载体20中,除了有机粘合剂之外还含有碱性中和剂的材料, 将增塑剂,润滑剂和水加入强酸性二氧化钛粉末和无机混合物的混合物中作为生坯。 因此,生坯被中和,酸度确实降低,这使得能够使用强酸性但便宜的二氧化钛功率和防止挤出机的腐蚀。 版权所有(C)2004,JPO
    • 4. 发明专利
    • Method for converting organic waste into biogas
    • 将有机废物转化为生物的方法
    • JP2003039036A
    • 2003-02-12
    • JP2001227359
    • 2001-07-27
    • Ishikawajima Harima Heavy Ind Co Ltd石川島播磨重工業株式会社
    • KITANO MAKOTOFUJII MAMORUMIWA KEIICHI
    • C12P5/02B01D19/00B01J3/00B09B3/00C02F11/04C02F11/08C12N1/00
    • Y02E50/343
    • PROBLEM TO BE SOLVED: To digest even organic wastes having a high nitrogen content.
      SOLUTION: A slurry of organic wastes 1 is heated to 150-350°C in a hydrothermal treater 9 to convert the wastes into hydrothermally solubilized solubles 14. The hot solubles 14 are cooled to about 100°C with a cooler and simultaneously reduced in pressure to the atmospheric pressure by means of a pressure reducing valve 13, and it is transferred to a flashing tank 11 where it is allowed to stay for a necessary time. Most of the ammonia contained in the solubles 14 is stripped by the flashing. The formed ammonia vapor 23 together with steam 22 is withdrawn from the ammonia withdrawal port 15 of the tank 11. The solubles 14 with an ammonia concentration lowered by stripping ammonia is transferred to a digester 4, where it is anaerobically digested to form a biogas 5. The effluent 6 from the digester is denitrified in a wastewater treater 7 and then discharged.
      COPYRIGHT: (C)2003,JPO
    • 要解决的问题:消化氮含量高的有机废物。 解决方案:在水热处理器9中将有机废物1的浆料加热至150-350℃,将废物转化成水热溶解的可溶物14.热可溶物14用冷却器冷却至约100℃,同时还原 通过减压阀13对大气压进行压力,并且将其传送到闪光罐11,在此允许它停留一段必要的时间。 可溶物14中包含的大部分氨被闪光剥离。 形成的氨蒸汽23与蒸汽22一起从罐11的氨排出口15排出。通过汽提氨将氨浓度降低的可溶物14被转移到蒸煮器4,在其中厌氧消化以形成沼气5 来自消化器的废水6在废水处理器7中脱氮,然后排出。