| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 1 | 水泥制造设备的运转方法 | CN201480054046.X | 2014-06-30 | CN105579415B | 2017-09-22 | 小松卓哉; 高山佳典 |
| 本发明提供可将煅烧炉中的燃烧和热耗率这两者同时最优化的水泥制造设备的运转方法。本发明涉及水泥制造设备的运转方法，所述方法在煅烧炉中供给第1燃料，在水泥窑中同时供给将内部保持为烧成温度的第2燃料和燃烧用的1次空气，并且在冷却器中导入冷却水泥熟料的空气，将该空气的一部分作为2次空气供给至上述水泥窑中，作为3次空气供给至上述煅烧炉中，与此同时将余量从该冷却器排出，其中，预先求得煅烧炉的废气出口的第1氧浓度与通过上述第1燃料和上述第2燃料确定的热耗率的关系、以及预热器的废气出口的第2氧浓度与上述热耗率的关系，调整上述2次空气和上述3次空气的量，使得上述第1氧浓度和第2氧浓度均在包含上述热耗率为最小的上述氧浓度值的范围内。 | ||||||
| 2 | 水泥制造设备的运转方法 | CN201480054046.X | 2014-06-30 | CN105579415A | 2016-05-11 | 小松卓哉; 高山佳典 |
| 本发明提供可将煅烧炉中的燃烧和热耗率这两者同时最优化的水泥制造设备的运转方法。本发明涉及水泥制造设备的运转方法，所述方法在煅烧炉中供给第1燃料，在水泥窑中同时供给将内部保持为烧成温度的第2燃料和燃烧用的1次空气，并且在冷却器中导入冷却水泥熟料的空气，将该空气的一部分作为2次空气供给至上述水泥窑中，作为3次空气供给至上述煅烧炉中，与此同时将余量从该冷却器排出，其中，预先求得煅烧炉的废气出口的第1氧浓度与通过上述第1燃料和上述第2燃料确定的热耗率的关系、以及预热器的废气出口的第2氧浓度与上述热耗率的关系，调整上述2次空气和上述3次空气的量，使得上述第1氧浓度和第2氧浓度均在包含上述热耗率为最小的上述氧浓度值的范围内。 | ||||||
| 3 | 从水泥生料混合物生产水泥熟料的方法与系统 | CN201380045689.3 | 2013-07-02 | CN104583148A | 2015-04-29 | S·弗里耶; S·奥伯豪泽尔 |
| 本发明涉及一种用于从水泥生料生产水泥熟料的工艺与设施，其中水泥生料的一部分在煅烧炉预热器中预热，并且水泥生料的其余部分在炉预热器中预热，经预热的水泥生料在运行氧-燃料工艺的煅烧炉中被预煅烧，预煅烧的水泥生料在炉中被烧制，烧制的水泥生料在冷却器中被冷却，煅烧炉预热器使用来自煅烧炉的煅烧炉废气来运行，炉预热器使用来自炉的炉废气来运行，夹带流反应器被用作煅烧炉，其中在已在煅烧炉预热器中加以利用之后，煅烧炉废气的一部分被再循环到煅烧炉，以及炉废气(23)经历CO2的后燃烧去除。 | ||||||
| 4 | 有机液体的保存 | CN200880110007.1 | 2008-08-04 | CN101932251A | 2010-12-29 | G·J·布拉顿; N·M·阿尔弗特; K·G·曼纳灵; R·L·布朗 |
| 本发明提供了一种用于保存可以是冷、热或在油炸操作期间的烹饪油的方法，该方法包括用至少一个可渗透油的水泥体原位处理所述油，该可渗透油的水泥体已经从包含例如白OPC水泥熔渣和白OPC水泥的水泥熔渣和水泥的糊料水力硬化。本发明还包括在其中具有至少一个可渗透油的水泥体的烹饪油，该可渗透油的水泥体已经从包含水泥熔渣和水泥的糊料水力硬化，和用于上述方法中的可渗透油的水泥体。 | ||||||
| 5 | 有机液体的保存 | CN201310695947.4 | 2008-08-04 | CN103691390A | 2014-04-02 | G·J·布拉顿; N·M·阿尔弗特; K·G·曼纳灵; R·L·布朗 |
| 本发明提供了一种用于保存可以是冷、热或在油炸操作期间的烹饪油的方法，该方法包括用至少一个可渗透油的水泥体原位处理所述油，该可渗透油的水泥体已经从包含例如白OPC水泥熔渣和白OPC水泥的水泥熔渣和水泥的糊料水力硬化。本发明还包括在其中具有至少一个可渗透油的水泥体的烹饪油，该可渗透油的水泥体已经从包含水泥熔渣和水泥的糊料水力硬化，和用于上述方法中的可渗透油的水泥体。 | ||||||
| 6 | 一种轻质隔热耐火浇注料 | CN201010137501.6 | 2010-03-30 | CN101792294A | 2010-08-04 | 罗巍; 欧阳德刚; 刘文清; 吴建鹏; 蒋扬虎; 吴杰; 张超; 张可建; 朱善合; 李明晖; 田大鹏; 罗安智; 陈超; 宋中华; 丁翠娇; 刘占增; 杨超; 王海青; 胡清明 |
| 本发明涉及一种轻质隔热耐火浇注料，它包括以下重量百分比的组分：化学改性轻质骨料，40～60％；电熔莫来石，10～20％；蓝晶石粉，5～10％；高铝熟料粉，5～10％；二氧化硅微粉，3～8％；α-Al2O3微粉，3～8％；高铝水泥，5～10％；含锆高铝耐火纤维，0.5～10％；耐热钢纤维，1.5～4％；三聚氰胺，0.1～1％；有机防爆纤维，0.05～0.10％；所述电熔莫来石的粒度小于等于1mm；二氧化硅微粉的粒度和α-Al2O3微粉的粒度均小于等于5μm；所述化学改性轻质骨料为轻质骨料在无机化学溶液或溶胶中浸泡后干燥而成。本发明轻质隔热耐火浇注料能提高炉辊寿命，降低生产消耗成本，减少换辊造成的非作业时间，提高生产效率。 | ||||||
| 7 | 大掺量煤矸石复合水泥及其制备方法 | CN200310108988.5 | 2003-12-01 | CN1546410A | 2004-11-17 | 王培铭; 蒋正武; 孙振平 |
| 本发明为一种大掺量煤矸石复合水泥，由煤矸石、硅酸盐水泥熟料、激发剂、石膏调凝剂、矿物掺和料按适当的重量配比经一定的工艺混合组成。其中煤矸石的含量为20－80％的重量比。本发明的复合水泥的和稠度、凝结时间、安定性等物理性能指标均满足国家标准和行业要求。并具有高强度、优异耐久性、低环境负荷的特征，可适用于制造各种混凝土构筑物，特别适用于大体积混凝土构筑物。 | ||||||
| 8 | 用于喷涂防火料中的含水合水的集料 | CN94119977.0 | 1994-12-22 | CN1108291A | 1995-09-13 | P·L·本尼堡; A·J·弗赖塔斯; R·皮萨图罗 |
| 提供用于结构钢件的可喷涂的防火组合物，其中包括胶合料如波特兰水泥和含水合水的硬集料，该硬集料使防火组合物有强度，也提高耐热性能。组合物加水后成为可喷涂的浆料，可泵送到进行喷涂的地点。该浆料附着于结构件上，凝固后亦附着良好，提供优等的耐热防火效果。 | ||||||
| 9 | 从水泥生料混合物生产水泥熟料的方法与系统 | CN201380045689.3 | 2013-07-02 | CN104583148B | 2016-10-19 | S·弗里耶; S·奥伯豪泽尔 |
| 本发明涉及一种用于从水泥生料生产水泥熟料的工艺与设施，其中水泥生料的一部分在煅烧炉预热器中预热，并且水泥生料的其余部分在炉预热器中预热，经预热的水泥生料在运行氧‑燃料工艺的煅烧炉中被预煅烧，预煅烧的水泥生料在炉中被烧制，烧制的水泥生料在冷却器中被冷却，煅烧炉预热器使用来自煅烧炉的煅烧炉废气来运行，炉预热器使用来自炉的炉废气来运行，夹带流反应器被用作煅烧炉，其中在已在煅烧炉预热器中加以利用之后，煅烧炉废气的一部分被再循环到煅烧炉，以及炉废气(23)经历CO2的后燃烧去除。 | ||||||
| 10 | 膨胀充填材料 | CN201010300671.1 | 2010-01-25 | CN101792291B | 2012-08-15 | 石建新; 闫国强 |
| 一种膨胀充填材料，属于建筑物、水体、铁路下采煤技术领域，其特征是，所述充填材料是由粉煤灰、膨胀剂、延缓剂、速凝剂、固化剂和水组成的料浆；其固液比为1∶1.2～1.5，比重为1.35，膨胀率为10～30％。本发明解决了中厚以下煤层采空区充填的主动施压接顶和长距离自流输送问题，对改善我国采煤生态环境，提高资源回收率具有十分重要的意义。 | ||||||
| 11 | 一种轻质隔热耐火浇注料 | CN201010137501.6 | 2010-03-30 | CN101792294B | 2012-05-30 | 罗巍; 欧阳德刚; 刘文清; 吴建鹏; 蒋扬虎; 吴杰; 张超; 张可建; 朱善合; 李明晖; 田大鹏; 罗安智; 陈超; 宋中华; 丁翠娇; 刘占增; 杨超; 王海青; 胡清明 |
| 本发明涉及一种轻质隔热耐火浇注料，它包括以下重量百分比的组分：化学改性轻质骨料，40～60％；电熔莫来石，10～20％；蓝晶石粉，5～10％；高铝熟料粉，5～10％；二氧化硅微粉，3～8％；α-Al2O3微粉，3～8％；高铝水泥，5～10％；含锆高铝耐火纤维，0.5～10％；耐热钢纤维，1.5～4％；三聚氰胺，0.1～1％；有机防爆纤维，0.05～0.10％；所述电熔莫来石的粒度小于等于1mm；二氧化硅微粉的粒度和α-Al2O3微粉的粒度均小于等于5μm；所述化学改性轻质骨料为轻质骨料在无机化学溶液或溶胶中浸泡后干燥而成。本发明轻质隔热耐火浇注料能提高炉辊寿命，降低生产消耗成本，减少换辊造成的非作业时间，提高生产效率。 | ||||||
| 12 | 高水膨胀充填材料 | CN201010300671.1 | 2010-01-25 | CN101792291A | 2010-08-04 | 石建新 |
| 一种高水膨胀充填材料，属于建筑物、水体、铁路下采煤技术领域，其特征是，所述充填材料是由粉煤灰、膨胀剂、延缓剂、速凝剂、固化剂和水组成的料浆；其固液比为1∶1.2～1.5，比重为1.35，膨胀率为10～30％。本发明解决了中厚以下煤层采空区充填的主动施压接顶和长距离自流输送问题，对改善我国采煤生态环境，提高资源回收率具有十分重要的意义。 | ||||||
| 13 | 用于喷涂防火料中的含水合水的集料 | CN94119977.0 | 1994-12-22 | CN1052032C | 2000-05-03 | P·L·本尼堡; A·J·弗赖塔斯; R·皮萨图罗 |
| 提供用于结构钢件的可喷涂的防火组合物，其中包括胶合料如波特兰水泥和含水合水的硬集料，该硬集料使防火组合物有强度，也提高耐热性能。组合物加水后成为可喷涂的浆料，可泵送到进行喷涂的地点。该浆料附着于结构件上，凝固后亦附着良好，提供优等的耐热防火效果。 | ||||||
| 14 | Method for operating cement plant | US14916465 | 2014-06-30 | US10131576B2 | 2018-11-20 | Takuya Komatsu; Yoshinori Takayama |
| There is provided a method for operating a cement plant capable of simultaneously optimizing both combustion in a calciner and a heat consumption rate. The method for operating a cement plant includes: feeding first fuel to a calciner; feeding second fuel for maintaining the inside at a burning temperature to a cement kiln along with combustion primary air, and introducing air for cooling cement clinker to a cooler; and feeding a part of the air as secondary air to the cement kiln, feeding as tertiary air to the calciner, and discharging the rest of the air from the cooler, wherein relation between a first oxygen concentration at an exhaust gas outlet of the calciner and a heat consumption rate determined by the first fuel and the second fuel, and relation between a second oxygen concentration at an exhaust gas outlet of the preheater and the heat consumption rate are beforehand obtained, and amounts of the secondary air and the tertiary air are adjusted such that both the first oxygen concentration and the second oxygen concentration fall within a range including values of the oxygen concentrations at which the heat consumption rate becomes at its minimum. | ||||||
| 15 | NOVEL SULFOALUMINATE CLINKER BASED HYDRAULIC BINDER AND USE THEREOF IN A PROCESS FOR TREATING POLLUTED SOILS | US14400865 | 2013-05-13 | US20150158063A1 | 2015-06-11 | Emmanuel Moudilou; Cyril Guerandel; Bruno Le Rolland; Stephanie Delair |
| A hydraulic binder based on a sulfoaluminate clinker including the mineralogical phases ye'elimite C4A3$, mayenite C12A7, free lime CaO, and optionally belite C2S, characterized in that, in the clinker, the mineralogical phases are 20% to 50% by weight of ye'elimite C4A3$ phase, 5% to 80% by weight of mayenite C12A7 phase, and 1% to 5% by weight of free lime CaO, the weight ratio between the mayenite C12A7 and ye'elimite C4A3$ phases being between 0.1 and 10. The binder can be used to treat polluted soils, in particular soils with a leachable fraction greater than 0.4% that contains predominantly anions and/or heavy metal cations by mixing the soil with the hydraulic binder, in soil/binder weight proportions of between 1 and 40 parts of binder for 100 parts of soil. It makes it possible to stabilize soils which are polluted or to stabilize soils before dumping. | ||||||
| 16 | Method and system for producing cement clinker from raw cement mixture | US14412504 | 2013-07-02 | US09630879B2 | 2017-04-25 | Sebastian Frie; Sebastian Oberhauser |
| The invention relates to a method and a system for producing cement clinker from raw cement mixture, wherein one part of the raw cement mixture is preheated in a calciner preheater, and the other part of the raw cement mixture is preheated in an oven preheater, the preheated raw cement mixture is pre-calcined in a calciner which is operated according to the oxyfuel method, the pre-calcined raw cement mixture is fired in an oven, the fired raw cement mixture is cooled in a cooler, the calciner preheater is operated using exhaust gases of the calciner, the oven preheater is operated using exhaust gases of the oven, an entrained flow reactor is used as the calciner, a part of the calciner exhaust gas being recirculated to the calciner after being used in the calciner preheater, and the oven exhaust gas undergoes a post-combustion CO2 separation. | ||||||
| 17 | METHOD FOR OPERATING CEMENT PLANT | US14916465 | 2014-06-30 | US20160214893A1 | 2016-07-28 | Takuya KOMATSU; Yoshinori TAKAYAMA |
| There is provided a method for operating a cement plant capable of simultaneously optimizing both combustion in a calciner and a heat consumption rate. The method for operating a cement plant includes: feeding first fuel to a calciner; feeding second fuel for maintaining the inside at a burning temperature to a cement kiln along with combustion primary air, and introducing air for cooling cement clinker to a cooler; and feeding a part of the air as secondary air to the cement kiln, feeding as tertiary air to the calciner, and discharging the rest of the air from the cooler, wherein relation between a first oxygen concentration at an exhaust gas outlet of the calciner and a heat consumption rate determined by the first fuel and the second fuel, and relation between a second oxygen concentration at an exhaust gas outlet of the preheater and the heat consumption rate are beforehand obtained, and amounts of the secondary air and the tertiary air are adjusted such that both the first oxygen concentration and the second oxygen concentration fall within a range including values of the oxygen concentrations at which the heat consumption rate becomes at its minimum. | ||||||
| 18 | Sulfoaluminate clinker based hydraulic binder and use thereof in a process for treating polluted soils | US14400865 | 2013-05-13 | US09764365B2 | 2017-09-19 | Emmanuel Moudilou; Cyril Guerandel; Bruno Le Rolland; Stephanie Delair |
| A hydraulic binder based on a sulfoaluminate clinker including the mineralogical phases ye'elimite C4A3$, mayenite C12A7, free lime CaO, and optionally belite C2S, characterized in that, in the clinker, the mineralogical phases are 20% to 50% by weight of ye'elimite C4A3$ phase, 5% to 80% by weight of mayenite C12A7 phase, and 1% to 5% by weight of free lime CaO, the weight ratio between the mayenite C12A7 and ye'elimite C4A3$ phases being between 0.1 and 10. The binder can be used to treat polluted soils, in particular soils with a leachable fraction greater than 0.4% that contains predominantly anions and/or heavy metal cations by mixing the soil with the hydraulic binder, in soil/binder weight proportions of between 1 and 40 parts of binder for 100 parts of soil. It makes it possible to stabilize soils which are polluted or to stabilize soils before dumping. | ||||||
| 19 | METHOD AND SYSTEM FOR PRODUCING CEMENT CLINKER FROM RAW CEMENT MIXTURE | US14412504 | 2013-07-02 | US20150183686A1 | 2015-07-02 | Sebastian Frie; Sebastian Oberhauser |
| The invention relates to a method and a system for producing cement clinker from raw cement mixture, wherein one part of the raw cement mixture is preheated in a calciner preheater, and the other part of the raw cement mixture is preheated in an oven preheater, the preheated raw cement mixture is pre-calcined in a calciner which is operated according to the oxyfuel method, the pre-calcined raw cement mixture is fired in an oven, the fired raw cement mixture is cooled in a cooler, the calciner preheater is operated using exhaust gases of the calciner, the oven preheater is operated using exhaust gases of the oven, an entrained flow reactor is used as the calciner, a part of the calciner exhaust gas being recirculated to the calciner after being used in the calciner preheater, and the oven exhaust gas undergoes a post-combustion CO2 separation. | ||||||
| 20 | Dry mortar mixture | US418816 | 1989-10-04 | US4985080A | 1991-01-15 | Fritz Jung |
| A dry mortar mix based on an inorganic bonding agent and optionally additives, plastics, fibres, and other conventional concrete additives is proposed especially to protect concrete structures and/or to eliminate surface damage to such structures. In addition to the inorganic bonding agent, the dry mortar mix contains a granular additive to increase alkalinity, this having a reaction speed that is a considerably lower than that of the granular bonding agent. This "reserve alkalinity" serves to counteract the diffusion of CO.sub.2 and SO.sub.2 from the air into the concrete, and the damage to the concrete that is attendant on such diffusion. | ||||||
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