EP 3237825 B1 20190130 - HEAT EXCHANGER, IN PARTICULAR BLOCK-IN-SHELL HEATER WITH A SEPARATING UNIT FOR SEPARATING A GASEOUS PHASE FROM A LIQUID PHASE AND FOR DISTRIBUTING THE LIQUID PHASE
Title (en)
HEAT EXCHANGER, IN PARTICULAR BLOCK-IN-SHELL HEATER WITH A SEPARATING UNIT FOR SEPARATING A GASEOUS PHASE FROM A LIQUID PHASE AND FOR DISTRIBUTING THE LIQUID PHASE
Title (de)
WÄRMEÜBERTRAGER, INSBESONDERE BLOCK-IN-SHELL-WÄRMEÜBERTRAGER MIT EINER SEPARIEREINHEIT ZUM SEPARIEREN EINER GASFÖRMIGEN PHASE VON EINER FLÜSSIGEN PHASE SOWIE ZUM VERTEILEN DER FLÜSSIGEN PHASE
Title (fr)
ÉCHANGEUR DE CHALEUR, EN PARTICULIER ÉCHANGEUR DE CHALEUR ENCAPSULÉ DOTÉ D'UNE UNITÉ DE SÉPARATION DESTINÉE À SÉPARER UNE PHASE GAZEUSE D'UNE PHASE LIQUIDE ET À DISTRIBUER LA PHASE LIQUIDE
Publication
Application
Priority
- EP 14004381 A 20141223
- EP 2015002463 W 20151207
Abstract (en)
[origin: WO2016102047A1] The invention relates to a heat exchanger (1) for indirectly transferring heat between a first medium (4) and a second medium (4a), comprising a container (2) which has an inner chamber (I) for receiving the two-phase first medium (4), a plate heat exchanger (5) arranged inside the inner chamber (I) for indirectly transferring heat between the first medium (4) and the second medium (4a), wherein the inner chamber (I) is designed to receive the first medium (4) with a fill level (3) such that a liquid phase (38) of the first medium (4) forms a bath surrounding the plate heat exchanger (5), and an inlet (6) above the fill level (3) for introducing the first medium (4) into the inner chamber (I). According to the invention, a separating unit (8) forming a receiving chamber (7) is provided for separating the gaseous phase (39) from the liquid phase (38) of the first medium (4) in the inner chamber (I), and the separating unit (8) has at least one upward-directed receiving opening (9) for introducing the first medium (4) flowing out in the inner chamber (I) into the receiving chamber (7), and the upward-directed receiving opening (9) is arranged above the fill level (3), such that the gaseous phase (39) of the first medium (4) in the receiving chamber (7) can escape into the inner chamber (I) via the receiving opening (9).
IPC 8 full level
F28F 9/02 (2006.01); F25B 39/02 (2006.01); F28D 9/00 (2006.01); F28D 21/00 (2006.01)
CPC (source: CN EP KR RU US)
F25B 39/022 (2013.01 - KR); F25B 39/028 (2013.01 - KR); F28D 9/0006 (2013.01 - CN EP KR US); F28D 21/0017 (2013.01 - CN EP KR RU US); F28F 9/00 (2013.01 - RU); F28F 9/026 (2013.01 - CN EP KR US); F25B 39/00 (2013.01 - EP US); F25B 2339/0241 (2013.01 - EP KR US); F25B 2339/046 (2013.01 - EP KR US); F25B 2339/047 (2013.01 - EP KR US); F28D 2021/0064 (2013.01 - CN EP KR US)
Citation (examination)
"The standards of the brazed aluminium plate-fin heat exchanger manufacturer's association ALPEMA STANDARDS- Complete Document; Revision / Edition: 3", ALPEMA STAND, ALUMINIUM PLATE-FIN HEAT EXCHANGER MANUFACTURER'S ASSOCIATION (ALPEMA), US, vol. Third Edition 2010 With Amendments May 2012, 1 January 2010 (2010-01-01), pages 1 - 84, XP008169329
Designated contracting state (EPC)
AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR
DOCDB simple family (publication)
WO 2016102047 A1 20160630; AU 2015371705 A1 20170629; AU 2015371705 B2 20210225; CA 2970559 A1 20160630; CN 107110621 A 20170829; CN 107110621 B 20190910; EP 3237825 A1 20171101; EP 3237825 B1 20190130; ES 2721786 T3 20190805; JP 2018500532 A 20180111; KR 20170096051 A 20170823; MX 2017008041 A 20171020; RU 2017120983 A 20190124; RU 2017120983 A3 20190404; RU 2688126 C2 20190517; TR 201905861 T4 20190521; US 10113806 B2 20181030; US 2017363360 A1 20171221
DOCDB simple family (application)
EP 2015002463 W 20151207; AU 2015371705 A 20151207; CA 2970559 A 20151207; CN 201580070850 A 20151207; EP 15808106 A 20151207; ES 15808106 T 20151207; JP 2017534278 A 20151207; KR 20177020604 A 20151207; MX 2017008041 A 20151207; RU 2017120983 A 20151207; TR 201905861 T 20151207; US 201515534542 A 20151207