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    • 141. 发明申请
    • A COOLING TOWER FOR COOLING A LIQUID WITH A GAS
    • 用气体冷却液体的冷却塔
    • WO2018011539A1
    • 2018-01-18
    • PCT/GB2017/000110
    • 2017-07-13
    • FLUID TECHNOLOGIES (ENVIRONMENTAL) LIMITED
    • DAVIS, Howard PaulMISSIONS, David William
    • F28C1/02F28C3/16F28D13/00F28F25/02F28F27/00B01J19/30
    • F28D13/00B01J8/24B01J19/30B01J19/305B01J2219/30207B01J2219/30211B01J2219/30253B01J2219/30466F28C1/02F28C3/16F28F25/02F28F25/06F28F27/003
    • A cooling tower (2) for cooling a liquid (4) with a gas (6), which cooling tower (2) comprises: (i) a vessel (8) for receiving the gas (6) passing upwardly and the liquid (4) passing downwardly, with the liquid (4) being hotter than the gas (6); (ii) a gas outlet (14) which is at a top portion (16) of the vessel (8) and which is for allowing the gas (6) to pass out of the vessel (8); (iii) a support member (20) which is positioned across a bottom portion (22) of the vessel (8); (iv) a plurality of apertures (24) which are in the support member (20) and through which the gas (6) and the liquid (4) are able to pass; (v) a fluidised bed (26) of packing elements (28) on the support member (20); (vi) liquid emitting means (30) which is positioned in the vessel (8) above the fluidised bed (26), and which is for emitting the liquid (4) to be cooled such the liquid (4) passes downwardly towards the fluidised bed (26); (vii) pump means (32) for pumping the liquid to the liquid emitting means (30); and (viii) a fan (34) for blowing the gas upwardly through the fluidised bed (26), and the cooling tower (2) being such that it includes: (ix) control means (31) for controlling (a) the velocity of the gas through the vessel (8), and (b) the liquid to gas ratio in the vessel (8), whereby the fluidised bed (26) is caused to operate at a tumbling rate which when combined with the selected pre- fluidised packing height causes an approach temperature of below 10°F (5.6°C); (x) wherein the tumbling rate is controlled by a combination of controlled gas velocity and liquid to gas ratio creating turbulent mixing and tumbling of packing elements (28) in the fluidised bed (26); (xi) and wherein the pre-fluidised height of the fluidised bed (26) is from 0.15 - 1.0m.
    • (6)冷却液体(4)的冷却塔(2),该冷却塔(2)包括:(i)用于接收气体(6)的容器(8) )向上流动,液体(4)向下流动,液体(4)比气体(6)热; (ii)位于所述容器(8)的顶部(16)并且用于允许所述气体(6)流出所述容器(8)的气体出口(14); (iii)横跨容器(8)的底部(22)定位的支撑构件(20); (iv)位于支撑构件(20)中并且气体(6)和液体(4)能够穿过的多个孔(24); (v)支撑构件(20)上的填充元件(28)的流化床(26); (vi)位于流化床(26)上方的容器(8)中并用于喷射待冷却液体(4)的液体喷射装置(30),使得液体(4)向下流向流化 床(26); (vii)用于将液体泵送到液体发射装置(30)的泵装置(32); 和(viii)用于向上吹气体通过流化床(26)的风扇(34),并且冷却塔(2)包括:(ix)控制装置(31),用于控制(a)速度 (8)中的气体,和(b)容器(8)中的液体与气体的比率,由此使流化床(26)以翻转速率运行,当与所选的预先流化的 填充高度导致接近温度低于10°F(5.6℃); (x),其中翻滚速度受控制的气体速度和液体与气体的比率的组合控制,从而产生流化床(26)中的填充元件(28)的湍流混合和翻滚; (xi),并且其中流化床(26)的预流化高度为0.15-1.0m。
    • 144. 发明申请
    • A METHOD AND APPARATUS FOR TREATING A BED OF PARTICULATE MATERIAL
    • 用于处理颗粒物料的方法和装置
    • WO2012079589A3
    • 2012-08-16
    • PCT/DK2011050489
    • 2011-12-16
    • SMIDTH AS F LTOKMAN ALEXANDER FLAVIOEINARSSON AGUST OERN EINARSSON
    • TOKMAN ALEXANDER FLAVIOEINARSSON AGUST OERN EINARSSON
    • B01J8/44F28C3/16F28F27/02
    • B01J8/44B01J2208/00548B01J2208/0092B01J2208/00929F28C3/16F28F27/02
    • A description is made of a method as well as an apparatus for treating a bed (2) of particulate material which is supported by a gas distribution bottom (1) comprising a number of sections (1a), utilizing a treatment gas which via ducts (3) is conducted in sectionalized manner to and directed up through the gas distribution bottom (1) and the bed (2) of material from one or several underlying compartments (4), the flow of the treatment gas through each duct (3) being regulated by means of a flow regulator (5) provided in each duct in order to compensate, at least in part, for a changing pressure drop through the bed, each flow regulator (5) being automatically movable in direct response to the gas flow rate in the respective duct (3), where the regulation is effected continuously variably within a operational range about a datum flow rate, the regulator (5) reducing the gas passage area in the duct (3) when the flow begins to rise, and vice versa. The method and apparatus is peculiar in that an adjustable flow of treatment gas from the respective underlying compartment (4) in a section (1a) during operation of the apparatus is allowed to bypass the gas flow regulation taking place in the respective duct (3). Hereby it is obtained, that the flow rates through the respective sections of the gas distribution bottom can be changed during operation of the apparatus. This is due to the fact that the resultant flow of treatment gas to the respective section of the gas distribution bottom, besides from minor leakage gas and idle gas, consists of the sum of the treatment gas flowing through the flow regulator and the adjustable flow of treatment gas being bypassed the flow regulation. Thus, by having the opportunity during operation of the apparatus to adjust the flow of treatment gas being bypassed the flow regulation the resultant flow of treatment gas to the respective section of the gas distribution bottom can be adjusted and fine tuned during operation of the apparatus for obtaining optimum operation in terms of total pressure loss, heat recuperation etc..
    • 描述了一种方法以及用于处理由包括多个部分(1a)的气体分配底部(1)支撑的颗粒材料床(2)的装置,利用处理气体,该处理气体通过管道( 处理气体通过每个管道(3)的流动是以分段方式对来自一个或多个下面的隔室(4)的气体分配底部(1)和材料床(2) 通过设置在每个管道中的流量调节器(5)进行调节,以便至少部分地补偿通过床的变化的压降,每个流量调节器(5)可以直接响应于气体流速 在相应管道(3)中,其中在关于基准流量的操作范围内可变地连续地进行调节,当流量开始上升时,调节器(5)减少管道(3)中的气体通道面积, 反之亦然。 该方法和设备是特别的,因为允许在设备操作期间来自部分(1a)中的相应下面的隔室(4)的可调整流量的处理气体绕过相应管道(3)中发生的气体流量调节, 。 由此可知,在装置的运转过程中,能够改变通过气体分配底部各部分的流量。 这是由于除了小的泄漏气体和怠速气体之外,对气体分配底部的各部分的处理气体的合成流量由流过调节器的处理气体和可调节流量之和 处理气体绕过流量调节。 因此,通过在设备操作期间有机会调节被旁路的处理气体的流量,可以调节流动调节处理气体到气体分配底部的相应部分的流量,以便在设备的操作期间调节和微调 在总压力损失,热回收等方面获得最佳的运行。
    • 145. 发明申请
    • A METHOD AND APPARATUS FOR TREATING A BED OF PARTICULATE MATERIAL
    • 一种处理颗粒材料床的方法和设备
    • WO2012079589A2
    • 2012-06-21
    • PCT/DK2011/050489
    • 2011-12-16
    • FLSMIDTH A/STOKMAN, Alexander, FlavioEINARSSON, Agust, Ørn, Einarsson
    • TOKMAN, Alexander, FlavioEINARSSON, Agust, Ørn, Einarsson
    • B01J8/44
    • B01J8/44B01J2208/00548B01J2208/0092B01J2208/00929F28C3/16F28F27/02
    • A description is made of a method as well as an apparatus for treating a bed (2) of particulate material which is supported by a gas distribution bottom (1) comprising a number of sections (1a), utilizing a treatment gas which via ducts (3) is conducted in sectionalized manner to and directed up through the gas distribution bottom (1) and the bed (2) of material from one or several underlying compartments (4), the flow of the treatment gas through each duct (3) being regulated by means of a flow regulator (5) provided in each duct in order to compensate, at least in part, for a changing pressure drop through the bed, each flow regulator (5) being automatically movable in direct response to the gas flow rate in the respective duct (3), where the regulation is effected continuously variably within a operational range about a datum flow rate, the regulator (5) reducing the gas passage area in the duct (3) when the flow begins to rise, and vice versa. The method and apparatus is peculiar in that an adjustable flow of treatment gas from the respective underlying compartment (4) in a section (1a) during operation of the apparatus is allowed to bypass the gas flow regulation taking place in the respective duct (3). Hereby it is obtained, that the flow rates through the respective sections of the gas distribution bottom can be changed during operation of the apparatus. This is due to the fact that the resultant flow of treatment gas to the respective section of the gas distribution bottom, besides from minor leakage gas and idle gas, consists of the sum of the treatment gas flowing through the flow regulator and the adjustable flow of treatment gas being bypassed the flow regulation. Thus, by having the opportunity during operation of the apparatus to adjust the flow of treatment gas being bypassed the flow regulation the resultant flow of treatment gas to the respective section of the gas distribution bottom can be adjusted and fine tuned during operation of the apparatus for obtaining optimum operation in terms of total pressure loss, heat recuperation etc..
    • 描述了一种用于处理由气体分配底部(1)支撑的颗粒材料床(2)的方法以及设备,所述气体分配底部包括多个部分(1a), 利用通过管道(3)以分段方式将处理气体引导通过气体分配底部(1)和来自一个或多个下面的隔室(4)的物质的床(2),治疗流 通过设置在每个管道中的流量调节器(5)调节通过每个管道(3)的气体,以便至少部分地补偿流过床的变化的压降,每个流量调节器(5)可自动移动 直接响应相应管道(3)中的气体流速,其中调节在围绕基准流量的操作范围内连续可变地实现,当调节器(5)在管道(3)中的气体通道面积减小时 流量开始上升,反之亦然。 该方法和设备的特征在于,允许在设备运行期间从区段(1a)中的相应下层隔室(4)调节处理气体流量绕过在相应管道(3)中发生的气体流量调节, 。 由此获得,在设备的操作期间可以改变通过气体分配底部的各个部分的流量。 这是由于除了少量泄漏气体和惰性气体之外,到达气体分配底部的相应部分的处理气体的合成流由流经流量调节器的处理气体的总和和 处理气体绕过流量调节。 因此,通过在设备操作期间有机会调节被旁路的处理气体的流量,流量调节可以调节并且在设备的操作期间调整和微调所产生的流至气体分配底部的相应部分的处理气体的流量 在总压力损失,热量恢复等方面获得最佳操作。
    • 146. 发明申请
    • HEAT STORE SYSTEM
    • 蓄热系统
    • WO2012027769A2
    • 2012-03-08
    • PCT/AT2011000362
    • 2011-09-05
    • UNIV WIEN TECHHAIDER MARKUSEISL ROLANDHOLZLEITHNER FRANZ
    • HAIDER MARKUSEISL ROLANDHOLZLEITHNER FRANZ
    • F28D20/00
    • F24J2/34F28C3/16F28D13/00F28D17/005F28D19/00F28D19/02F28D20/0056Y02E60/142Y02P90/50
    • The invention relates to a heat store system using sand as a solid heat storage medium, which heat store system is characterized in that it comprises the following components: a storage vessel (1) for cold sand; a storage vessel (2) for hot sand; an interposed fluidized bed heat exchanger (3) which is separated from the storage vessels (1, 2) by weirs (4, 5) and is divided into a plurality of chambers (7) by weirs (6), wherein the weirs (4, 5, 6) are formed as a combination of overflow and underflow weirs; wherein in the chambers (7) of the heat exchanger (3) there are provided means (8) for transferring heat from a heat source to the sand fluidized therein, and means (9) for transmitting heat from the sand fluidized therein to a heat transport medium; and at least one blower (14), arranged below the heat exchanger (3), for fluidizing the sand.
    • 本发明涉及一种使用砂作为固体储热介质,其特点在于它包括以下组分的蓄热系统:用于冷砂的储存容器(1); 用于热砂的储罐(2); 插入的流化床热交换器(3),其通过堰划分(4,5)的储存罐(1,2)被分离和堰(6)成多个腔室(7),其中,所述堰(4- ,5,6)形成为溢流和下溢堰的组合; 其中,在所述热交换器的腔室(7)(3)的装置(8),用于从热源传递热量到流化其中的砂以及装置(9),用于从所述流化其中的砂设置有传热介质上传递热量; 和至少一个设置在热交换器(3)下方的风扇(14),用于流化沙子。
    • 149. 发明申请
    • KÜHLER FÜR SCHÜTTGUT MIT EINER ABDICHTEINRICHTUNG ZWISCHEN BENACHBARTEN FÖRDERPLANKEN
    • COOLER对于批量与密封部件之间近域资金木板
    • WO2008017500A1
    • 2008-02-14
    • PCT/EP2007/007102
    • 2007-08-10
    • CLAUDIUS PETERS TECHNOLOGIES GMBHDIKTY, MarioHILGRAF, PeterSTAAK, ThomasSPRINZ, UweMEYER, HartmutBOCK, UweKNABBE, JörnKOEBERER, Günther
    • DIKTY, MarioHILGRAF, PeterSTAAK, ThomasSPRINZ, UweMEYER, HartmutBOCK, UweKNABBE, JörnKOEBERER, Günther
    • F27D15/02B65G25/06
    • F28C3/16B65G25/065F26B17/26F27D15/0213F28F2230/00
    • Eine Vorrichtung zum Kühlen von Schüttgut mit einem von Kühlgas durchströmten Rost (5) umfasst mehrere in Förderrichtung vor- und zurückbewegte Planken (51-53) und eine Abdichteinrichtung (7) zwischen den Planken (51-53), die räumlich voneinander getrennte äußere und innere Dichteinrichtungen (70, 74) aufweist. Erfindungsgemäß ist vorgesehen, dass die Abdichteinrichtung (7) einen längs der Planken (51-53) laufenden Förderkanal (8) zwischen den Dichteinrichtungen (70, 74) aufweist, an dem eine Gaszufuhr ausgebildet ist zur Bewirkung eines Gasstroms längs des Förderkanals (8). Durch die äußere Dichteinrichtung eingedrungenes Schüttgutmaterial kann abtransportiert werden, bevor es die innere Dichteinrichtung (74) erreichen und durchwandern kann. Der unerwünschte Materialdurchfall wird erheblich reduziert. Dank der Erfindung ist es nicht erforderlich, die Dichtungen eng auszuführen, wodurch sie unweigerlich verschleißanfällig würden. Sie können vielmehr verschleißgünstig ausgeführt werden. Dies bedingt zwar einen gewissen Eintrag von Schüttgutmaterial, der aber über den erfindungsgemäßen Förderkanal (8) abtransportiert wird. Die Erfindung verbindet hervorragende Dichtwirkung mit exzellenter Verschleißfestigkeit.
    • 用于冷却散装材料的装置的通过冷却气体篦流(5)包括多个在输送方向上游侧和移回木板(51-53)和密封装置(7)的板块(51-53)之间,所述空间上分离的外和 内密封装置(70,74)。 根据本发明,提供的是所述密封装置(7)沿所述木板包含(51-53)上运行的输送通道(8)的密封装置(70,74)中,向其中一个气体供给被配置为使气体的沿着所述输送通道的流动(8)之间 , 通过外密封装置已经渗透散装材料可以被运走之后才能到达内密封元件(74)和横动。 掉落不需要的材料显著减少。 由于本发明,没有必要进行紧密密封,它们将不可避免地容易磨损哪个。 它们可以被设计成穿低相当。 这的确需要散装材料的特定条目,但是这是通过根据本发明的输送通道(8)的输送。 本发明结合了优良的耐磨损性优良的密封效果。
    • 150. 发明申请
    • METHOD AND APPARATUS FOR TREATING A BED OF PARTICULATE MATERIAL
    • 用于处理颗粒物料的方法和装置
    • WO2006119768A8
    • 2008-01-24
    • PCT/DK2006000247
    • 2006-05-08
    • FOENS TECHNOLOGY APSFOENS MOGENS JUHL
    • FOENS MOGENS JUHL
    • F28C3/16C04B7/47F27D15/02F28F27/02
    • F28C3/16C04B7/47F27B7/383F27D15/0213F28F27/02
    • A bed of particulate material 6 is supported by an air distribution bottom 5. Under the distribution bottom 5 exist one or more compartments 7, which each being supplied with cooling air from a fan installation 8. The distribution bottom 5 is sectionalised in a number of smaller areas 9. Each smaller distribution area 9 is connected to the compartment 7 by ducts 10, 11 and 12. The one duct 10 does have a fixed orifice area. The ducts 11 and 12 do have floaters 13A /13B end stop 14A/14B and bottom support 15A/15B. It is hereby obtained that the total pressure loss across the air distribution bottom can be reduced, and so that the flow of the treatment air through the material bed is distributed in a desirable manner across the entire air distribution bottom regardless of the composition of the material bed and the distribution thereon, and optimal heat exchange efficiency is obtained.
    • 颗粒材料6的床由空气分配底部5支撑。在分配底部5下方存在一个或多个隔室7,每个隔间7从风扇装置8供应冷却空气。分配底部5被分段成多个 较小的区域9.每个较小的分配区域9通过管道10,11和12连接到隔室7.一个管道10确实具有固定的孔口面积。 导管11和12具有浮子13A / 13B端部止动件14A / 14B和底部支撑件15A / 15B。 由此,可以减少空气分配底部的总压力损失,并且不管材料的组成如何,通过材料床的处理空气的流动以期望的方式分布在整个空气分配底部 床和其上的分布,并获得最佳的热交换效率。