KRÜMMER FÜR EINEN ROHRBÜNDEL-WÄRMEAUSTAUSCHER FÜR GROSSE PRODUKTDRÜCKE, HERSTELLVERFAHREN FÜR EINEN UND ROHRBÜNDEL-WÄRMEAUSTAUSCHER MIT EINEM SOLCHEN KRÜMMER UND VERWENDUNG EINES ROHRBÜNDEL-WÄRMEAUSTAUSCHERS FÜR GROSSE PRODUKTDRÜCKE MIT EINEM SOLCHEN KRÜMMER IN EINER ZERSTÄUBUNGSTROCKNUNGSANLAGE
    3.
    发明公开
    KRÜMMER FÜR EINEN ROHRBÜNDEL-WÄRMEAUSTAUSCHER FÜR GROSSE PRODUKTDRÜCKE, HERSTELLVERFAHREN FÜR EINEN UND ROHRBÜNDEL-WÄRMEAUSTAUSCHER MIT EINEM SOLCHEN KRÜMMER UND VERWENDUNG EINES ROHRBÜNDEL-WÄRMEAUSTAUSCHERS FÜR GROSSE PRODUKTDRÜCKE MIT EINEM SOLCHEN KRÜMMER IN EINER ZERSTÄUBUNGSTROCKNUNGSANLAGE 审中-公开
    KRÜMMERFÜREINENROHRBÜNDEL-WÄRMEAUSTAUSCHERFÜRGROSSEPRODUKTDRÜCKE,HERSTELLVERFAHRENFÜREINEN UNDROHRBÜNDEL-MITWÄRMEAUSTAUSCHEREINEM SOLCHENKRÜMMERUND VERWENDUNG EINESROHRBÜNDEL-WÄRMEAUSTAUSCHERSFÜRGROSSEPRODUKTDRÜCKEMIT EINEM SOLCHENKRÜMMERIN EINERZERSTÄUBUNGSTROCKNUNGSANLAGE

    公开(公告)号:EP3183529A1

    公开(公告)日:2017-06-28

    申请号:EP15762916.3

    申请日:2015-08-13

    申请人: GEA TDS GmbH

    摘要: The invention relates to a manifold (1) with a circular cross-section having a deviation angle of 180 degrees for a tube bundle heat exchanger (100) for large product pressures, having a first and a second flange (2, 3) on each inlet (E) and outlet (A) of the manifold (1), in addition to a method for producing a tube bundle heat exchanger (100) comprising said type of manifold (1) and to the use of a tube bundle heat exchanger (100) for large product pressure having said type of manifold (1) in a spray drying system. The aim of the invention is to produce a manifold for a tube bundle heat exchanger for large product pressure, which has, amongst other things, the required strength and sustainable dimensional accuracy and is optimized in terms of flow technology during the course of the production thereof. A manifold (1) of said type can be achieved due to the following: the manifold (1) consists of two manifold halves (1.1, 1.2) which are respectively made of a single piece such that each manifold half (1.1, 1.2) comprises a joining point (V) on the end facing away from the flange (2, 3) and that the manifold halves (1.1, 1.2) are connected together in a material fit on the associated connection point (V) and that the extension of the passage cross-section of each manifold half (1.1, 1.2) is formed by rotationally symmetrical through-openings, from which at least one of the flanges (2, 3) and at least one of the associated connecting points (V) extends in the respective coaxial arrangement on the rotational axes (X1.1, Y1.1; X1.2, Y1.2), and that the first and the second rotational axes (X1.1, Y1.1) of the through openings of the first manifold halves (1,1) and the third and the fourth rotational axes (X1.2, Y1.2) of the through openings of the second manifold halves (1.2) extend on a common plane, which represents a meridian plane (M) for each flange (2, 3).

    摘要翻译: 本发明涉及一种用于大产品压力的管束式热交换器(100),具有圆形横截面的歧管(1),其具有180度的偏差角度,其中每个分别具有第一和第二法兰(2,3) 除了用于制造包括所述类型的歧管(1)的管束式热交换器(100)的方法以及管束式热交换器(1)的使用之外,歧管(1)的入口(E)和出口 100)用于在喷雾干燥系统中具有所述类型的歧管(1)的大产品压力。 本发明的目的是生产一种用于大产品压力的管束式热交换器的歧管,其具有所需的强度和可持续的尺寸精度,并且在其生产过程中在流动技术方面被优化 。 由于以下原因,所述类型的歧管(1)可以被实现:歧管(1)由两个歧管半部(1.1,1.2)组成,所述歧管半部分别由单个部件制成,使得每个歧管半部(1.1,1.2)包括 在远离所述凸缘(2,3)的端部上的连接点(V)以及所述歧管半体(1.1,1.2)以相配的连接点(V)上的材料配合连接在一起,并且所述 每个歧管半部(1.1,1.2)的通道横截面由旋转对称的通孔形成,至少一个凸缘(2,3)和至少一个相关联的连接点(V)从所述通孔横截面延伸到 在旋转轴线(X1.1,Y1.1; X1.2,Y1.2)上的相应的同轴布置以及第一和第二旋转轴线(X1.1,Y1.1)的第一和第二旋转轴线 第二歧管半部(1.2)的通孔的歧管半部(1,1)以及第三和第四旋转轴线(X1.2,Y1.2)在交流 它是每个凸缘(2,3)的子午面(M)。

    VERFAHREN UND INJEKTOR ZUM EINLEITEN EINES DAMPFFÖRMIGEN WÄRMETRÄGERS IN EIN FLÜSSIGES PRODUKT
    4.
    发明公开
    VERFAHREN UND INJEKTOR ZUM EINLEITEN EINES DAMPFFÖRMIGEN WÄRMETRÄGERS IN EIN FLÜSSIGES PRODUKT 有权
    VERFAHREN UND INJEKTOR ZUM EINLEITEN EINESDAMPFFÖRMIGENWÄRMETRÄGERSIN EINFLÜSSIGESPRODUKT

    公开(公告)号:EP3011246A1

    公开(公告)日:2016-04-27

    申请号:EP14733985.7

    申请日:2014-05-24

    申请人: GEA TDS GmbH

    IPC分类号: F28C3/06 F28C3/08

    摘要: The invention relates to a method for introducing a vaporous heat carrier into a liquid product, in particular a food product or beverage, and in this case in particular viscous products, for example desserts, sauces or concentrates, in which method the vaporous heat carrier heats the liquid product in order to form a germ-free product, and also to an injector for carrying out the method. The object of the present invention is to provide a method of the generic type and an injector for carrying out said method, with which method and injector, in particular, a reduction in the heat transfer capacity of the injector is prevented over the entire production time. In the context of the method, this is achieved in that three physical measurement variables which can be detected during operation of the injector are used as indicators of the formation of product deposits, at least one of said three physical measurement variables being detected, and in that, depending on one or more of these physical measurement variables, an automatically controlled axial movement of the displacement body is carried out in such a way that the heat transfer capacity from the vaporous heat carrier (D) into the liquid product (P) remains the same.

    摘要翻译: 将蒸气热载体引入液体产品,特别是食品或饮料,更特别是粘稠的产品,例如甜点,酱汁或浓缩物的方法包括使用载体加热产物以形成无菌产物 。 还描述了用于执行该方法的喷射器。 在整个生产时间内防止喷射器的传热能力的降低。 这是通过在注射器操作期间可以检测到的三个物理测量变量被用作产物沉积物形成的指标。 检测所述三个物理测量变量中的至少一个,并且根据这些变量,执行位移体的自动控制的轴向运动,使得从气态热载体到液体产物的传热能力保持不变。

    VERFAHREN UND VORRICHTUNG ZUR STEUERUNG DER SCHAUMBILDUNG IN EINER ENTGASUNGSVORRICHTUNG FÜR FLÜSSIGKEITEN UND REGISTERSYSTEM FÜR EINE SOLCHE VORRICHTUNG

    公开(公告)号:EP3370510A1

    公开(公告)日:2018-09-12

    申请号:EP16801128.6

    申请日:2016-10-25

    申请人: GEA TDS GmbH

    IPC分类号: A01J11/02 A01J11/04 B01D19/02

    摘要: The invention relates to a method and to a device for controlling foaming in a degassing device (10; 10.1, 10.2) for liquids (P), in particular liquid foods such as milk, semi-skimmed milk, skimmed milk, or fruit juices, and to a heat-exchanger system (20) for such a device. The aim of the invention is for the method, the device for performing the method, and the heat-exchanger system to effectively control and limit foaming and to prevent the growth of the foam beyond a tolerable amount while ensuring the sanitary and hygienic process-control requirements in the field of the treatment and processing of liquid foods. This aim is achieved in respect of process engineering, inter alia in that the growing foam (S), beginning at a first heating distance (h1) from the free surface (N) releasing the foam (S) and beginning at a second heating distance (h2) from the liquid film (F) releasing the foam (S), first experiences heating from the liquid temperature (T3) to a heating temperature (T1) in the heat-exchanger system (20), which consists of a heating heat exchanger (20.1) and a cooling heat exchanger (20.2), and that the further growing heated foam (S), beginning at a first cooling distance (k1) from the first heating distance (h1) and beginning at a second cooling distance (k2) from the second heating distance (h2), then experiences cooling to a cooling temperature (T2) in the heat-exchanger system (20).