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    • 1. 发明申请
    • METERING SYSTEM, DENSE PHASE CONVEYING SYSTEM AND METHOD FOR SUPPLYING BULK MATERIAL IN POWDER FORM
    • 计量,封口电流处理系统和方法喂养尘封BULK
    • WO2011042194A3
    • 2011-07-21
    • PCT/EP2010006150
    • 2010-10-08
    • CHOREN IND GMBHKRETSCHMER HORSTKLEEBERG JOERGRUEGER DIETMARSCHULZE OLAFEICHHORN CHRISTIAN
    • KRETSCHMER HORSTKLEEBERG JOERGRUEGER DIETMARSCHULZE OLAFEICHHORN CHRISTIAN
    • F23K3/02
    • C10J3/723B65G53/30B65G53/4691C10J3/503C10J2200/152C21B5/003C21B5/023C21C5/527F23K3/02F27D3/10F27D2099/0051Y02P10/216Y10T137/0318Y10T137/85938
    • The invention relates to a metering system and a dense phase conveying system for the metered supply of a light-weight bulk material from a supply device (B, SG) via conveying tubes (FR1,FR2,FR3) to a consumer. A sluice (S) comprises a discharge device (AE/S) having a powder flow control device (Fl4) which leads to a metering container (DB) the discharge device (AE/DB) of which comprises a plurality of powder flow control devices (Fl1,Fl2,Fl3) that lead to respective conveying tubes (FR1,FR2,FR3). A pressure control device of the metering device is coupled to pressure measuring devices (PIS1, PI2) of the sluice (S) and of the metering container (DB) for the purpose of differential pressure controls (PDC1-2, PDC3-R) and to pressure measuring devices (PIR, PI3) of the metering container discharge device (AE/DB) and the consumer to control the metering container pressure (Pl2) depending on the second differential pressure control (PDC3-R). The pressure control device is coupled to a pressure measuring device (PlSA4) of the supply device (SG,B) for the purpose of a differential pressure control (PlSA4-1) between the supply device (B, SG) and the sluice (S). The pressure control device controls the sluice pressure (PlS1) depending on a sluice fill level (LlS/S) and the differential pressure control (PlSA4-1) by activating at least one suction device (V) that can be connected to the sluice (S). The invention further relates to a method using the dense phase conveying system having the metering device.
    • 本发明涉及一种计量装置和用于从一个供应装置经由输送管(FR1,FR2,FR3)轻本体材料的计量供应(B,SG)给消费者密相输送系统。 为了这个目的,一个锁(S)包括一个放电装置(AE / S)与灰尘流量控制装置(FI4),其通入一个分配容器(DB),所述放电装置(AE / DB)包括多个灰尘流量控制装置(FI1,FI2,FI3)的,所述 每个开成输送管(FR1,FR2,FR3)。 所述计量装置的压力控制装置是用于压差控制(PDC1-2,PDC3-R)与锁(S)和所述计量容器(DB)的压力测量装置(PIS1,PI2),并与Dosierbehälteraustragseinrichtung(AE / DB)的压力感测装置(PIR,PI3)和 耦合到所述消费者,以控制从所述第二压差控制(PDC3-R)取决于Dosierbehälterdruck(PI2)。 对于供应装置之间的压差控制(PISA4-1)(B,SG)和锁定(S)的压力控制装置耦合到所述电源装置的压力测量装置(PISA4)(SG,B)。 压力控制装置控制上的锁级别(LIS / S)和压差控制器(PISA4-1)由至少一个与所述锁(S)连接至抽吸装置(V)的致动相关的负载锁定压力(PIS1)。 此外,本发明公开了使用密相输送系统与所述计量装置的方法。
    • 2. 发明申请
    • METERING SYSTEM, DENSE PHASE CONVEYING SYSTEM AND METHOD FOR SUPPLYING BULK MATERIAL IN POWDER FORM
    • 给料装置,密封件循环器和供应不可分离散装物品的方法
    • WO2011042193A3
    • 2011-07-14
    • PCT/EP2010006149
    • 2010-10-08
    • CHOREN IND GMBHKRETSCHMER HORSTKLEEBERG JOERGRUEGER DIETMARSCHULZE OLAFEICHHORN CHRISTIAN
    • KRETSCHMER HORSTKLEEBERG JOERGRUEGER DIETMARSCHULZE OLAFEICHHORN CHRISTIAN
    • F23K3/02
    • C10J3/723C10J3/503C10J2200/152C21B5/003C21B5/023C21C5/527F23K3/02F23K2203/006F23K2203/103F23K2203/104F23K2203/105F23K2203/201F27D3/10F27D2099/0051Y02P10/216
    • The invention relates to a metering system for the steady, continuous, metered supply of a bulk material in powder form of light-weight, polydisperse particles from a supply device (B, SG) to a plurality of conveying tubes (FR1,FR2,FR3) to a downstream consumer. The metering system comprises at least two metering containers (DB1,DB2,DB3) with respective discharge devices (AE2/1,AE2/2,AE2/3), the discharge device (AE2/1,AE2/2,AE2/3) comprising for every conveying tube (FR1,FR2,FR3) a powder flow control device (FI1/1,FI2/1,FI3/2) associated therewith and leading to said tube. A mass flow measuring probe (FIC1,FIC2,FIC3) is arranged on every conveying tube (FR1,FR2,FR3) and is coupled to the powder flow control device (FI1/1 to FI3/2) which leads to the corresponding conveying tube (FR1,FR2,FR3). The metering system further comprises a pressure control device which is coupled to pressure measuring devices (PI1/1,PI1/2,Pl1/3) arranged on the discharge devices (AE2/1,AE2/2,AE2/3) and which controls a metering container pressure (PIS2/1,PIS2/2,PIS2/3) at least depending on a metering container fill level (LIS1,LIS2,LIS3). A pump device (V) can be coupled to every metering container (DB1,DB2,DB3) and provides a pressure (PIS2/1,PIS2/2,PIS2/3) in the metering container (DB1,DB2,DB3) which is lower than the pressure in the supply device (B, SG). The invention further relates to a dense phase conveying system which comprises the metering system and to a method for the steady, continuous, metered supply of a bulk material in powder form of light-weight, polydisperse particles.
    • 本发明涉及一种用于连续的,连续的,计量的粉末状松散材料从光多分散粒子从供给装置供给(B,SG)成多个输送管(FR1,FR2,FR3)的至下游消费者的计量系统。 该计量系统包括至少两个计量(DB1,DB2,DB3),每一个具有放电装置(AE2 / 1,AE2 / 2,AE2 / 3),其中,所述放电装置(AE2 / 1,AE2 / 2,AE2 / 3)为每一个 输送管(FR1,FR2,FR3)与其相关联的一个,在这种打开灰尘流量控制装置(FI1 / 1,FI2 / 1,FI3 / 2),并且其中,在每个所述输送管的质量流量测量探针(FIC1,FIC2,FIC3)(FR1 ,FR2,FR3)布置,其耦合(与灰尘流量控制装置FI1 / 1至FI3 / 2),其打开(在相应的输送管FR1,FR2,FR3)。 此外,定量给料单元,其被布置成与所述排出装置的压力控制装置(AE2 / 1,AE2 / 2,AE2 / 3)的压力测量装置(PI1 / 1,PI1 / 2,P?1/3)被耦合,和一个Dosierbehälterdruck(PIS2 / 1,PIS2 / 2,PIS2 / 3)(至少在一个DosierbehälterfüllstandsLIS1,LIS2,LIS3)控制的依赖。 在这种情况下,泵送装置(V)与每个计量容器(DB1,DB2,DB3)(PIS2 / 3 PIS2 / 1,PIS2 / 2)可以联接,在计量容器内的压力(DB1,DB2,DB3)规定小于 作为供给装置(B,SG)中的压力。 此外,本发明公开了一种密相输送系统,其包括给料单元和用于连续的,连续的,计量的粉末状松散材料从光多分散粒子供给的方法。
    • 4. 发明申请
    • METHOD FOR PUTTING A FISCHER-TROPSCH SYNTHESIS IN A HOLDING MODE
    • 一种用于操作保持费 - 托法
    • WO2007045495A3
    • 2007-06-14
    • PCT/EP2006010144
    • 2006-10-20
    • CHOREN IND GMBHALTHAPP ANTONWOLF BODO MRUEGER DIETMARSCHULZE OLAF
    • ALTHAPP ANTONWOLF BODO MRUEGER DIETMARSCHULZE OLAF
    • C10G2/00
    • C10G2/32
    • According to the invention, when a Fischer-Tropsch synthesis has to be transferred into a holding mode due to disturbances resulting in the Fischer-Tropsch reaction no longer being under control, the reactor is not decompressed and the temperature is not lowered below the temperature at which no more Fischer-Tropsch reaction occurs after the supply of fresh synthesis gas to the Fischer-Tropsch reactor has been cut off. Instead, the reactor is impinged upon by an anticatalyst-free inert gas that is provided in a receptacle at a pressure exceeding the operating pressure of the Fischer-Tropsch synthesis until the reacting components are flushed out of the FT system via the pressure maintaining valve, the reactor only being rendered inert within a few seconds while the pressure and the temperature are maintained, thus interrupting the Fischer-Tropsch reaction. The catalyst is not damaged while there is little or no change in the liquid phase situation on the catalyst, which simplifies the subsequent starting phase.
    • 在由于具有所述费 - 托反应的非命令导致合成新鲜气体供给的分离后的反应器的干扰的必要转化成费 - 托合成的保持操作不是放松到费 - 托反应器和温度不低于温度 下降,在其下没有费 - 托反应较多,但通过催化剂无毒害的惰性气体,其被保持为费 - 托合成中具有较高压力,直到在从FT压力保持阀的反应组分的容器的操作压力采取行动 系统中冲洗掉。 同时保持在几秒钟内的压力和温度的反应器,仅由惰性和中断与它的费 - 托反应。 的催化剂劣化不会发生,并且在催化剂上的情况液相的变化被减少或不会发生,这有利于随后的启动阶段。