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    • 1. 发明申请
    • DAMPFERZEUGER
    • 蒸汽发生器
    • WO2009021861A2
    • 2009-02-19
    • PCT/EP2008/060149
    • 2008-08-01
    • SIEMENS AKTIENGESELLSCHAFTHEINRICHS, Fred
    • HEINRICHS, Fred
    • F22B37/24F22B15/00
    • F22B37/242F22B15/00
    • Ein Dampferzeuger (1) mit einem in einer annähernd horizontalen Heizgasrichtung (x) von einem Heizmedium durchströmbaren Heizgaskanal (6) soll mit besonders gering gehaltenem Aufwand und in besonders einfacher Bauweise eine zuverlässige Aufnahme der genannten Lasten, insbesondere der durch den Auslegungs-Innendruck des Heizgases gegebenen zusätzlichen Lasten, gewährleisten. Dazu ist der Heizgaskanal (6) erfindungsgemäß von einer Anzahl von in Heizgasrichtung (x) gesehen hintereinander angeordneten Stützrahmen/Bandagen (14) umfasst, wobei zumindest zwei der Stützrahmen (14) über eine Anzahl von Horizontalscheiben (16) miteinander verbunden sind.
    • 从通过该加热气体管道(6)被设计为具有特别低的手持努力并且在一个特别简单的结构,可靠记录的加热介质的蒸汽发生器(1)用在大致水平的加热气体方向(x)所述的负载,特别是由加热气体的结构,内部压力 保证给予额外负荷。 为了这个目的,根据从众多的加热气体方向(x)的观察到的本发明的加热气体管道(6)依次包括设置支撑框架/桶(14),其中至少两个经由多个水平板(16)的支撑框架(14)的被连接在一起。
    • 2. 发明申请
    • HEAT EXCHANGER WITH PIPE BUNDLE
    • WO2020253924A1
    • 2020-12-24
    • PCT/DK2020/050170
    • 2020-06-15
    • AALBORG CSP A/S
    • THOMSEN, PeterCHRISTENSEN, Ivan BoPELLE, Jens TaggartSØRENSEN, KeldBUNDGAARD, Svante
    • F28D1/047F28D1/02F22B1/00F22B15/00F28D7/08F28D20/00F28D21/00
    • A heat exchanger (10) is disclosed for providing heat exchange between fluids (24, 25), comprising a pipe bundle (17) extending between first and second pipe connectors (13, 14) and configured to guide a second fluid (25) between the first and second pipe connectors (13, 14), the pipes (17a-17n) being distributed in layers (22) of pipes (17a-17n), wherein a plurality of pipes (17a-17n) of each of said layers (22) of pipes each comprises two bends (B1, B2), so that the respective pipe provides three substantially parallel flow path sections (S1, S2, S3), wherein the length (L1) of a longer (S1) of said flow path sections of the respective pipe is at least 1.7 times greater than the length (L2) of the other two shorter flow path sections (S2, S3) of said pipe, wherein a first (B1) of said bends (B1, B2) is provided between the longer flow path section (S1) and a first of said shorter flow path section (S2), and wherein the other (B2) of said bends is provided between said first, shorter flow path section (S2) and the other shorter flow path section (S3), wherein each of said layers of pipes (17a-17n) comprises two pipe subgroups (SG1, SG2), wherein the longer (S1) of said flow path sections of one of said subgroups (SG1, SG2) is connected to a first of said pipe connectors (13, 14), and wherein the longer (S1) of said flow path sections of the other of said subgroups (SG1, SG2) is connected to the other of said pipe connectors (13, 14), and wherein the bend (B2) between the two shorter flow path sections (S2, S3) of the respective pipes in one of said pipe subgroups (SG1) in the pipe layer (22) is arranged substantially opposite to bends (B2) extending between the two shorter flow path sections (S2, S3) of pipes in the other pipe subgroup (SG2) of the same pipe layer (22).
    • 3. 发明申请
    • DIRECT HEAT EXCHANGER FOR ORGANIC RANKINE CYCLE SYSTEMS
    • 直接换热器用于有机朗肯循环系统
    • WO2017145057A1
    • 2017-08-31
    • PCT/IB2017/050993
    • 2017-02-22
    • TURBODEN SPA
    • BINI, RobertoGAIA, Mario
    • F01K25/08F22B15/00F22B21/02F22B21/40
    • F01K25/08F22B15/00F22B21/02F22B21/40
    • Heat exchanger (100) to direct exchange between hot gases of a hot source and a working fluid of an Organic Rankine Cycle system, comprising at least two tube bundles (200, 201) having a plurality of tubes (106) inside them the working fluid flows, an inlet manifold (103) from which the working fluid enters and an outlet manifold (105) from which the working fluid in a vapor phase comes out, said heat exchanger (100) also comprising: a first portion (102) crossed downward along the vertical direction of the heat exchanger (100) by the hot gases a second portion (101) crossed upward along he vertical direction of the heat exchanger (100) by the hot gases coming from the portion (102), an intermediate manifold (104) positioned between a last row of tubes (110) of the second portion (101) and a first row of tubes (111) of the first portion (102).
    • (100),用于引导热源的热气体与有机朗肯循环系统的工作流体之间的交换,所述热交换器包括至少两个管束(200,201),所述管束具有多个管 其中工作流体流动的入口歧管(106),工作流体从其进入的入口歧管(103)和出口歧管(105),气相工作流体从出口歧管出来,所述热交换器(100)还包括: 第一部分(102)沿着热交换器(100)的竖直方向通过热气向下交叉,第二部分(101)沿着热交换器(100)的竖直方向向上通过来自该部分 (102),位于第二部分(101)的最后一排管(110)和第一部分(102)的第一排管(111)之间的中间歧管(104)。