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    • 1. 发明授权
    • Solids distributor for injection plants, blast furnaces and the like
    • 注塑厂,高炉等的固体分销商
    • US08348556B2
    • 2013-01-08
    • US12446426
    • 2007-10-22
    • Peter HilgrafDietrich SchumpeHans-Dieter NoldeVolker Goecke
    • Peter HilgrafDietrich SchumpeHans-Dieter NoldeVolker Goecke
    • B65G53/40
    • F27B1/10C21B5/003F23K3/02F23K3/06
    • A solids distributor for injection plants includes a collecting chamber having a plurality of lance lines leading away from the chamber. The chamber has a supply connection for a solid to be distributed and is surrounded by a common wall in which a plurality of ports is formed. The lance lines are connected to the ports, and an annular gap is formed in front of the ports and along the common wall. A pressure vessel is arranged geodetically above the collecting chamber, the lower part of the pressure vessel being designed as a bunker, having an outlet providing a direct and continuous junction to the supply connection and an upper part designed as a gas space. The collecting chamber may include a central displacement body which forms the annular gap with the common wall and which may be an upwardly tapering cone which projects out of the collecting chamber.
    • 用于注射装置的固体分配器包括具有从腔室导出的多个喷枪线的收集室。 该室具有用于待分布的固体的供应连接并且由形成有多个端口的公共壁包围。 喷枪线连接到端口,并且在端口的前面和沿着公共壁形成环形间隙。 压力容器位于收集室上方的地质上,压力容器的下部设计为沙坑,具有出口,该出口提供与供应连接件的直接连续的连接点和设计为气体空间的上部部件。 收集室可以包括中心位移体,其与公共壁形成环形间隙,并且可以是从收集室突出的向上锥形的锥体。
    • 3. 发明申请
    • CALCINATION METHOD AND SYSTEM
    • 计算方法与系统
    • US20110150750A1
    • 2011-06-23
    • US12991083
    • 2009-05-11
    • Volker GoeckePeter Hilgraf
    • Volker GoeckePeter Hilgraf
    • C01F11/46B01J19/00
    • C04B11/0283B01J6/002B01J6/004B01J8/1836B01J2208/00274B01J2208/00557B01J2208/0061B01J2208/00699C04B11/007C04B11/0286
    • A method for the calcination of powdery or fine-particled plaster includes steps in which the plaster is subjected to a flash-calcination in a calcinator and then post-calcinated in a reaction vessel. The post-calcination is carried out in the reaction vessel by adding humid gas, the reaction vessel not being heated. This post-calcination takes place over a long period of time, that is at least 10 times, preferably 50-100 times longer than, the amount of time taken for flash calcination. Complete calcination can take place without expending additional energy, and the remaining dihydrate produced during the flash calcination is also transformed into semi-hydrate and undesired anhydrite fractions are reduced. The method ensures consistency in the product quality and also increases product quality. The temperature in the upstream calcinator can be lowered to save energy. The method can also be used to accelerate the ageing of calcined plaster.
    • 用于煅烧粉末状或细粒状石膏的方法包括以下步骤:将石膏在煅烧器中进行闪蒸煅烧,然后在反应容器中进行后煅烧。 后处理在反应容器中通过加入潮湿气体进行,反应容器不加热。 该后煅烧发生在长时间的时间内,即闪光煅烧所花费的时间的至少10倍,优选为50-100倍。 可以进行完全煅烧而不消耗额外的能量,并且在闪速煅烧期间产生的剩余二水合物也转化为半水合物,并且不期望的无水石膏馏分被还原。 该方法确保产品质量的一致性,并提高产品质量。 可以降低上游煅烧器中的温度以节省能源。 该方法也可用于加速煅烧石膏的老化。
    • 4. 发明授权
    • Method and system for the production of hard plaster
    • 生产硬石膏的方法和制度
    • US09340455B2
    • 2016-05-17
    • US13063719
    • 2009-09-11
    • Volker GoeckeTobias Gehle
    • Volker GoeckeTobias Gehle
    • C04B28/14B01J19/00C04B11/02C04B7/04C04B11/024C04B11/032C04B11/00
    • C04B11/007
    • A method for the production of hard plaster, a calcining plant, and a retrofit reactor for calcining plants. The method includes feeding plaster material, predominantly including beta-hemihydrate plaster, to a postreactor. The temperature is set to at least a calcining temperature of 95° C. during this step. The plaster material is retreated in the postreactor to form hard plaster, the beta-hemihydrate plaster being converted directly into alpha-hemihydrate plaster at a temperature above 95° C. The hard plaster can then be discharged out of the postreactor and cooled. Conversion can be carried out in the postreactor during continuous operation, and conversion of the beta-hemihydrate plaster can occur with a dwell time in the postreactor of less than 30 minutes. Steam can be externally supplied to the postreactor and the temperature and pressure in the postreactor can be regulated so that the temperature is at least 95° C. and an over pressure prevails.
    • 用于生产硬质石膏,煅烧装置和用于煅烧植物的改造反应器的方法。 该方法包括将主要包含β-半水泥石膏的石膏材料送入后反应器。 在该步骤中将该温度设定为至少95℃的煅烧温度。 石膏材料在后反应器中退回以形成硬质石膏,β-半水泥石膏在95℃以上的温度下直接转化为α-半水泥石膏。然后将硬石膏从后反应器中排出并冷却。 在连续运行期间可以在后反应器中进行转化,并且可以在反应器中停留时间少于30分钟时,可以进行β-半水泥石膏的转化。 蒸汽可以从外部供应到后反应器,并且可以调节后反应器中的温度和压力,使得温度至少为95℃,并且过压。
    • 5. 发明申请
    • METHOD AND SYSTEM FOR THE PRODUCTION OF HARD PLASTER
    • 用于生产硬质塑料的方法和系统
    • US20110168061A1
    • 2011-07-14
    • US13063719
    • 2009-09-11
    • Volker GoeckeTabias Gehle
    • Volker GoeckeTabias Gehle
    • C04B28/14B01J19/00
    • C04B11/007
    • The invention relates to a method for the production of hard plaster made from calcined beta hemihydrate plaster, comprising adding of plaster material mainly consisting of beta hemihydrate plaster to a post reactor (3), after-treating in the post reactor (3) for forming hard plaster, wherein the beta hemihydrate plaster is directly converted into alpha hemihydrate plaster at a temperature above the calcining temperature of 95 degrees Celsius, removing the hard plaster from the post reactor (3), and cooling down. During the adding of the plaster material to the post reactor (3) the temperature is adjusted to at least the calcining temperature, the conversion is carried out in the post reactor (3) at a dwell time of less than 30 minutes while externally adding water vapor, and the temperature and the pressure in the post reactor (3) are regulated such that the temperature is at least 95 degrees Celsius and an overpressure is present.
    • 本发明涉及一种用于生产由煅烧β-半水泥石膏制成的硬石膏的方法,包括将主要由β半水泥膏组成的石膏材料添加到后反应器(3)中,在后反应器(3)中进行后处理以形成 硬膏,其中β半水泥石膏在高于95摄氏度的煅烧温度的温度下直接转化成α半水泥膏,从后反应器(3)中除去硬膏,并冷却。 在将灰泥材料添加到后反应器(3)中时,将温度调节至少至少煅烧温度,转化在后反应器(3)中在停留时间少于30分钟的时间进行,而外部加入水 蒸气,并且后反应器(3)中的温度和压力被调节为使得温度为至少95摄氏度并且存在过压。