{ "schemaVersion": 1, "date": "2026-09-07", "packageId": "heat-transfer", "scope": "Configured membership and registered descriptions, not live licensing or calculation certification", "web": { "commit": "1cd12e8b173ba72aa5c95c98a14772b7ee537997", "branch": "main13.0", "dirty": true }, "desktop": { "commit": "40606b705b2df95e550ffef5e98ab733ccc66229", "branch": "fix-iteration/v10", "dirty": false }, "files": [ { "repo": "LV-Atlas-Web", "path": "src/LvAtlasWeb.Api/App_Data/module-groups.json", "sha256": "d0da0a140fc83c6515f154d00c04a7d4c71d98adbb7a615b9f0301412cb1e80f" }, { "repo": "LV-Atlas-Web", "path": "src/modules/xml/ModuleInfoList.xml", "sha256": "09d40bef101969fdcc2c17efbd30c5945ec2d8b3c3e19283a21784f9daec0c7e" }, { "repo": "LV-Atlas-Web", "path": "src/modules/info/Modules.info.json", "sha256": "6fe0be8839983494b89eb757aded9ac817c2b59a5b9a7e8f9ae1f1d6dfda93d1" }, { "repo": "LV-Atlas-Web", "path": "src/modules/info/ModuleWebUi.json", "sha256": "57634dac5bd6d9a5fffb58f6e4f6f2e1cb0a75b476dc678be8e10534ff1358a5" }, { "repo": "All-Dev", "path": "LvDataFolder/DotNet_Module/GB_.Net/LvGB.NET/GB.Properties.Id.vb", "sha256": "e79b67a95116cbfabb8061c759d5bc5a10e4008bb90f7695318a18d80c70945f" }, { "repo": "All-Dev", "path": "LvDataFolder/DotNet_Module/GB_.Net/LvGB.NET/KAPGB.vb", "sha256": "9f9c0cb185b8d9fd7086fb8b753bdcaf1568ac55fac0767a6548cc70c65064a2" } ], "members": [ { "token": "AC", "displayName": "AC", "registered": true, "description": { "de": "Auslegung von Wärmeübertragern mit rechteckigen Bündeln. Es können verschiedene Medien in und um die Rohre ausgewählt werden. Der Wärmeübergang kann einphasig angenommen werden, aber auch Verdampfung (nur in den Rohren) und Kondensation von Reinstoffen werden berechnet.", "en": "Design of heat exchangers with rectangular bundles. Different media can be selected in and around the tubes. The heat transfer can be assumed to be single-phase, but also evaporation (only in the tubes) and condensation of pure substances can be calculated." }, "headlines": [ { "de": "", "en": "" }, { "de": "Auslegung von Rohrregisterübertragern", "en": "Design of tube register heat exchangers" } ], "source": { "de": "Verfahrenstechnische Berechnungsmethoden, Teil 1, VCH Weinheim & VDI Wärmeatlas", "en": "" } }, { "token": "ACOI", "displayName": "ACOI", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei der Strömung um Rohrwendeln", "en": "Heat transfer during flow around tube spirals" } ], "source": { "de": "", "en": "" } }, { "token": "BEHE", "displayName": "BEHE", "registered": true, "description": { "de": "Mit dem Modul BEHE kann die erforderliche Anzahl an Begleitheizungsrohren ermittelt werden. Die Wärmeübergangszahl, die Verlustwärme und der Heizmittelbedarf werden bestimmt.\nFür einphasige Fluide wird unterschieden, ob die Begleitheizungsrohre mit oder ohne Wärmeleitzement verlegt sind. Zudem kann die Nennweite anhand der Strömungsgeschwindigkeit optimiert werden.", "en": "The BEHE module can be used to determine the required number of trace heating pipes. The heat transfer coefficient, the heat loss and the heating medium requirement are determined.\n\nFor single-phase fluids, a distinction is made as to whether the heat-tracing pipes are laid with or without thermal conduction cement. In addition, the nominal diameter can be optimised on the basis of the flow velocity." }, "headlines": [ { "de": "", "en": "" }, { "de": "Begleitheizungen", "en": "Trace heating system" } ], "source": { "de": "", "en": "" } }, { "token": "BIFL", "displayName": "BIFL", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Bilanzierung feuchter Luft: Enthitzung und Kondensation", "en": "" }, { "de": "", "en": "" } ], "source": { "de": "", "en": "" } }, { "token": "BREN", "displayName": "BREN", "registered": true, "description": { "de": "Das Modul berücksichtigt verschiedene geometrische Konfigurationen der Rohrwendeln und somit die unterschiedlichsten Fahrweisen für das Wärmeträgeröl. Die Brennraum- und Konvektivzonenwendel können seriell oder parallel durchfahren werden. Das Thermalöl kann im Brennerbereich eingespeist oder entnommen werden (Gegenstrom- oder Gleichstrom-Fahrweise). Die Wendeln können unterschiedliche Rohrabmessungen haben und aus mehreren ineinander gedrehten Wendeln bestehen.", "en": "The module considers different geometric coil configurations for the most widely differing operating modes of thermal oil heaters. The radiation and convection coils may arranged in series or parallel. The thermal oil can be supplied or withdrawn in the burner area (countercurrent or co-current operation). The coils can have different tube dimensions and consist of several coils twisted into each other." }, "headlines": [ { "de": "", "en": "" }, { "de": "Berechnung der Filmtemperatur in Thermalölerhitzern", "en": "Calculation of film temperature in thermal oil heaters" } ], "source": { "de": "VDI Wärmeatlas, Walter Wagner: \"Wärmetechnik mit organischen Medien\" Reschverlag München", "en": "VDI Heat Atlas, Walter Wagner: \"Thermal engineering with organic media\" Resch Publishing Munich" } }, { "token": "CA", "displayName": "C1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertrager: Berechnungsmethoden", "en": "Heat Exchangers: Calculation Methods" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "CB", "displayName": "C2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertrager: Wärmedurchgang und Wärmedurchgangskoeffizienten", "en": "Heat Exchangers: Heat Transfer and Heat Transfer Coefficients" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "CD", "displayName": "C4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragungsnetzwerke", "en": "Heat Transfer Networks" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "CIRC", "displayName": "CIRC", "registered": true, "description": { "de": "Das Modul berechnet den Druckverlust und den Wärmeübergang im Außenraum von Rohrbündelwärmeübertragern mit Kreisringen und Kreisscheiben als Umlenkbleche.\nDie Daten des Rohrspiegels können aus dem Modul SPIE übernommen werden. Das Modul CIRC kann zur Berechnung von kompletten Wärmeübertragern in das Programmpaket WTS integriert werden.", "en": "The module calculates the pressure loss and heat transfer in the outer space of shell-and-tube heat exchangers with disk and doughnut baffles.\nThe tube sheet data can be transferred from the SPIE module. The CIRC module can be integrated into the WTS program package for the calculation of complete heat exchangers." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang und Druckverlust in Rohrbündelwärmeübertragern mit Kreisring / Kreisscheibe", "en": "Heat transfer and pressure drop for shell and tube heat exchanger with disk and doughnut baffles" } ], "source": { "de": "Verfahrenstechnische Berechnungsmethoden, Teil 1, VCH Weinheim", "en": "" } }, { "token": "COIL", "displayName": "COIL", "registered": true, "description": { "de": "Mit dem Programm COIL können Rohrschlangen-Wärmeübertrager/Rohrwendel-Wärmeübertrager für gasförmige und flüssige Medien sowie für kondensierende reine Stoffe ausgelegt werden. Es wird keine Verdampfung berechnet.", "en": "With the COIL program, coil heat exchangers can be designed for gaseous and liquid media as well as for condensing pure substances. Evaporation is not calculated" }, "headlines": [ { "de": "", "en": "" }, { "de": "Rohrschlangen-Wärmeübertrager", "en": "Coil heat exchangers" } ], "source": { "de": "VDI Wärmeatlas", "en": "VDI Heat Atlas" } }, { "token": "DEE", "displayName": "M11", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeleitfähigkeit von Schüttschichten", "en": "Thermal Conductivity of Beds" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "DNK", "displayName": "DNK", "registered": true, "description": { "de": "Mit dem Modul DNK kann die Zustandsänderung von überhitztem Dampf zur unterkühlten Flüssigkeit und die damit verbundene Erwärmung von Luft in hintereinander geschalteten Wärmetauschern berechnet werden.", "en": "The DNK module calculates the heating of air by steam, starting from superheating condition to the supercooled liquid region." }, "headlines": [ { "de": "", "en": "" }, { "de": "Dampf-Nachdampf-Kondensation in Wärmetauschergruppen", "en": "Steam residual-steam condensation in heat exchanger groups" } ], "source": { "de": "VDI - Wärmeatlas, Heat Exchanger Design Handbook, Hemisphere Publishing Corporation, New York", "en": "VDI - Heat Atlas, Heat Exchanger Design Handbook, Hemisphere Publishing Corporation, New York" } }, { "token": "DRLL", "displayName": "DRLL", "registered": true, "description": { "de": "Das Modul DRLL berechnet auf der Grundlage experimenteller Ansätze den Wärmeübergangskoeffizienten und den Widerstandsbeiwert bzw. Druckverlust in durchströmten Drallrohren.", "en": "On the basis of experimental approaches, the DRLL module calculates the heat transfer coefficient and the resistance coefficient or pressure loss in flow-through corrugated tubes." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang und Druckverlust in durchströmten Drallrohren", "en": "Heat transfer and pressure drop in corrugated tubes" } ], "source": { "de": "", "en": "" } }, { "token": "DSTR", "displayName": "DSTR", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Dampferzeuger-Strahlungsverlust", "en": "Steam generator radiation loss" } ], "source": { "de": "Energietechnische Arbeitsmappe 14. Auflage: 1995", "en": "" } }, { "token": "EA", "displayName": "E1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Stationäre Wärmeleitung", "en": "Steady conduction of heat" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "EB", "displayName": "E1.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeverlust von Wänden und Rohrleitungen", "en": "Heat loss of walls and pipeworks" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "EC", "displayName": "E2", "registered": false, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeleitung - instationär", "en": "Heat conduction - unsteady" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "FA", "displayName": "F2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Wärmeübertragung bei freier Konvektion", "en": "Heat transfer with natural convection" }, { "de": "Mischkonvektion: Komponentenansatz", "en": "Combined natural and forced convection: Component balance" }, { "de": "Horizontal gekrümmte Flächen: Würfel", "en": "Horizontally curved surfaces: Cubes" }, { "de": "Horizontal gekrümmte Flächen: Kugeln", "en": "Horizontally curved surfaces: Spheres" }, { "de": "Horizontal gekrümmte Flächen: Rippenrohre", "en": "Horizontally curved surfaces: Fin tubes" }, { "de": "Horizontal gekrümmte Flächen: Zylinder (External flows)", "en": "Horizontally curved surfaces: Cylinder" }, { "de": "Horizontale ebene Flächen", "en": "Horizontal plane surfaces" }, { "de": "Geneigte ebene Flächen", "en": "Inclined flat surfaces" }, { "de": "Vertikale Zylinder (Außenströmung)", "en": "Vertical cylinders" }, { "de": "Vertikale ebene Flächen", "en": "Vertical flat surfaces" }, { "de": "Grundlagen", "en": "Fundamentals" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "FB", "displayName": "F5", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Wärmeabgabe von Heizkörpern beim Betrieb mit Warmwasser", "en": "Thermal output of heating appliances operating with hot water" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "FC", "displayName": "F3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Wärmeübertragung bei freier Konvektion: Innenströmungen", "en": "Heat transfer with natural convection: Internal flows" }, { "de": "Grundlegende Beziehungen", "en": "General relations" }, { "de": "Schichten (horizontal, geneigt oder vertikal)", "en": "Layers (horizontal, inclined or vertical)" }, { "de": "Ringspalte (horizontal oder vertikal)", "en": "Annuli (horizontal or vertical)" }, { "de": "Poröse Schichten", "en": "Porous layers" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "FD", "displayName": "F4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Wärmeübertragung bei freier Konvektion: Sonderfälle", "en": "Heat transfer with natural convection: special cases" }, { "de": "Senkrechte Kanäle", "en": "Vertical channels" }, { "de": "Geneigte Kanäle", "en": "Inclined channels" }, { "de": "Offener vertikaler Ringspalt", "en": "Open vertical annuli" }, { "de": "Überlagerte erzwungene Konvektion", "en": "Superimposed forced convection" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "FE", "displayName": "F2.5", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Mischkonvektion", "en": "Combined natural and forced convection" }, { "de": "Ebene Platte: Ebene vertikale oder geneigte Platten", "en": "Flat plates: Plane vertical or inclined plates" }, { "de": "Ebene Platte: Horizontale Platte", "en": "Flat plates: Horizontal plates" }, { "de": "Horizontaler, querangeströmter Zylinder", "en": "Cylinder in horizontal crossflow" }, { "de": "Kugeln", "en": "Spheres" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "G8SC", "displayName": "Unterkühlung", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang und Druckverlust in der Unterkühlungszone eines Kondensators", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 11. Auflage 2013, G8 & L1.5", "en": "VDI Heat Atlas, 11. Edition 2013, G8 & L1.5" } }, { "token": "GA", "displayName": "G4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Längsumströmte ebene Wände", "en": "Heat transfer with forced convection: Longitudinal flow past plane walls" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GB", "displayName": "G1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Durchströmte Rohre", "en": "Heat transfer with forced convection: Pipe flow" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GC", "displayName": "G3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Durchströmte Rohrwedeln", "en": "Heat transfer with forced convection: Flow-though coils" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GD", "displayName": "G2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Konzentrischer Ringspalt und ebener Spalt", "en": "Heat transfer with forced convection: Concentric annulus and rectilinear gap" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GE", "displayName": "G6", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Querumströmte einzelne Rohre, Drähte und Profilzylinder", "en": "Heat transfer with forced convection: Cross-flow around individual tubes, wires, and profiled cylinders" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GEV8", "displayName": "G5", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Bewegte Oberflächen mit paralleler Überströmung", "en": "Heat transfer with forced convection: Moving surfaces with parallel overflow" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GF", "displayName": "G7", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Querdurchströmte Rohrreihen und Rohrbündel", "en": "Heat transfer with forced convection: Cross flow though single tube rows and through tube bundles" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GG", "displayName": "G8", "registered": false, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Außenraum von Rohrbündel-Wärmeübertrager mit Umlenkblechen", "en": "Heat transfer with forced convection: Shell side in baffeled shell and tube heat exchangers" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GGLR", "displayName": "GGLR", "registered": true, "description": { "de": "Das Modul GGLR berechnet für längsberippte Rohrbündel den Wärmeübergang und den Druckverlust im Außenraum von Rohrbündelwärmeübertragern ohne Einbauten. Die Rippenquerschnitte können rechteckig oder trapezförmig sein. Berechnet werden der Wärmeübergang und der Druckverlust sowohl für laminare als auch für turbulente Strömung.", "en": "The GGLR module calculates the heat transfer and pressure drop in longitudinal fin tube bundles of shell-and-tube heat exchangers. The fin cross sections may be rectangular or trapezoidal. The heat transfer and the pressure drop are calculated for laminar and turbulent flow." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang und Druckverlust in Rohrbündelwärmeübertragern mit längsberippten Rohren", "en": "Heat transfer and pressure drop in shell and tube heat exchangers with lengthwise finned tubes" } ], "source": { "de": "", "en": "" } }, { "token": "GGO", "displayName": "GGO", "registered": true, "description": { "de": "Das Modul GGO berechnet für Mantelräume ohne Umlenkbleche den Wärmeübergangskoeffizienten und den Druckverlust. Berechnungsgrundlage sind die Untersuchungen an der Universität Karlsruhe, die auf der GVC-Tagung 1994 publiziert wurden. Die Berechnung nimmt insbesondere auf das Durchmesser/Bündellänge-Verhältnis und auf die Größe und Lage der Stutzen Rücksicht. Somit sind auch die Erhöhungen des Wärmeüberganges am Eintrittsstutzen erfaßt.", "en": "The GGO module calculates the heat transfer coefficient and the pressure loss for shells without baffles. The calculation is based on the investigations at the University of Karlsruhe, which were published at the GVC conference in 1994. The calculation takes particular account of the diameter/bundle length ratio and the size and position of the nozzles. Thus also the increases of the heat transfer at the inlet nozzle are recorded." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung und Druckverlust in längsdurchströmten Rohrbündelwärmeübertragern", "en": "Heat transfer and pressure drop in lengthwise flown shell and tube heat exchangers" } ], "source": { "de": "", "en": "" } }, { "token": "GGRI", "displayName": "GGRI", "registered": true, "description": { "de": "Was kann das Programm?\n\nDas Modul GGRI berechnet den Wärmeübergang um berippte Rohrbündel, mit Segmentblech (Kreuzstrom). Die Berechnung bezieht sich auf das HEDH (Heat Exchanger Design Handbook), die von Kreisrippenrohren mit niedriger Rippenhöhe ausgeht. Die Rohre sind charakterisiert mit ca. 630 – 1000 Rippen / m (16 – 26 fins / in ) und einer Rippenhöhe von 1 bis 2 mm.\n\nNiedrig berippte Rohre sind nicht geeignet bei laminarer Strömung (Re < 1000) und für kondensierenden Dampf.", "en": "The GGRI module calculates the shell-side heat transfer coefficient in low fin tube bundles with segmental baffles (crossflow). The theory is presented in the Heat Exchanger Design Handbook, where results obtained for circular fin tubes are extended to the case of low fin tubes. Low fin tubes are defined as 630 – 1000 fins / m (16 – 26 fins / in) with a fin height of 1 to 2 mm.\n\nLow fin tubes are not recommended for laminar flow (Re < 1000) and not for condensing steam." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang an niedrig berippten Rohren in Rohrbündelwärmeübertragern mit Segmentumlenkblechen", "en": "Heat transfer in external low fin tubes in shell and tube heat exchangers with segmental baffles" } ], "source": { "de": "", "en": "" } }, { "token": "GH", "displayName": "G9", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Durchströmte Haufwerke", "en": "Heat transfer with forced convection: Flow through beds of solids" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GK", "displayName": "G10", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei erzwungener Konvektion: Prallströmung", "en": "Heat transfer with forced convection: Impingement flow" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "GVLV", "displayName": "GVLV", "registered": true, "description": { "de": "Das Modul GVLV wird von WTS angesteuert und ist nicht separat aufrufbar; die Werte werden in GV im Hintergrund berechnet und an WTS übergeben. Die Dokumentation erfolgt innerhalb von WTS.\n\nNicht berechnet werden:\n\n Übertrager mit 2 mantelseitigen Durchgängen. Längsleitblech TEMA Typ F\n\n Übertrager mit Umlenkblechen vom Typ Kreisring / Kreisscheiben\n\n Übertrager mit außen niedrigberippten Rohren", "en": "The GVLV module is controlled by WTS and cannot be called separately; the values are calculated in GV in the background and transferred to WTS. The documentation takes place within WTS.\n\nNot to be calculated:\n\n Exchangers with 2 shell-side passes Longitudinal baffle TEMA Type F\n\n Exchangers with disc and doughnut baffles\n\n Exchangers with low finned tubes" }, "headlines": [ { "de": "", "en": "" }, { "de": "Rohrbündel Schwingungsanalyse", "en": "Tube bundle vibration analysis" } ], "source": { "de": "", "en": "" } }, { "token": "HAB1", "displayName": "H2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Behältersieden reiner Stoffe und von Gemischen", "en": "Pool boiling of pure substances and mixtures" }, { "de": "Sieden in freier Konvektion ohne Blasenbildung", "en": "Boiling with natural convection without bubble formation" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HAB2", "displayName": "H2.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Sieden in freier Konvektion ohne Blasenbildung", "en": "Boiling in natural convection without bubble formation" }, { "de": "Bezugswert a0 für das Blasensieden nach Stephan und Preußer", "en": "Reference value a0 for nucleate boiling acc. to Stephan and Preusser" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HAB3", "displayName": "H2.3.5.1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Behältersieden reiner Stoffe und von Gemischen", "en": "Pool boiling of pure substances and mixtures" }, { "de": "Blasensieden reiner Stoffe: Formen von Heizwänden", "en": "Nucleate boiling of pure substances: Shapes of heating walls" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HAB4", "displayName": "H2.3.5.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Behältersieden reiner Stoffe und von Gemischen", "en": "Pool boiling of pure substances and mixtures" }, { "de": "Blasensieden reiner Stoffe: Rippenrohre und andere Hochleistungsrohre", "en": "Nucleate boiling of pure substances: Fin tubes and other high performance pipes" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HAB5", "displayName": "H2.3.5.3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Behältersieden reiner Stoffe und von Gemischen", "en": "Pool boiling of pure substances and mixtures" }, { "de": "Blasensieden reiner Stoffe: Horizontales Rohrbündel", "en": "Nucleate boiling of pure substances: Horizontal tube bundles" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HAB6", "displayName": "H2.4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Behältersieden reiner Stoffe und von Gemischen", "en": "Pool boiling of pure substances and mixtures" }, { "de": "Blasensieden von Gemischen", "en": "Nucleate boiling of mixtures" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HAB7", "displayName": "H2.5.1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Behältersieden reiner Stoffe und von Gemischen", "en": "Pool boiling of pure substances and mixtures" }, { "de": "Maximale Wärmestromdichte qcrit des Blasensiedens", "en": "Critical heat flux qcrit in nucleate boiling" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "HAB8", "displayName": "H2.6", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Behältersieden reiner Stoffe und von Gemischen: Filmsieden", "en": "Pool boiling (natural convection):Film boiling" }, { "de": "Filmsieden", "en": "Film boiling" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HABA", "displayName": "HABA", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Bezugswert für den Wärmeübergangskoeffizienten beim Blasensieden an glatten Rohren und ebenen Wänden (Behältersieden, Strömungssieden)", "en": "Reference value of heat transfer coefficient for nucleate boiling on bare tubes and flat walls (pool boiling, flow boiling of saturated liquids)" } ], "source": { "de": "", "en": "" } }, { "token": "HBA", "displayName": "H3.4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Strömungssieden unterkühlter Flüssigkeiten", "en": "Flow boiling of subcooled liquids" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HBB1", "displayName": "H3.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Strömungssieden – Strömungsformen in Verdampferrohren", "en": "Flow boiling – Flow forms in evaporator tubes" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "HBB2", "displayName": "H3.5.1.1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Strömungssieden gesättigter, reiner Flüssigkeiten: Konvektives Strömungssieden in senkrechten Rohren", "en": "Flow boiling of saturated, pure liquids: Convective flow boiling in vertical tubes" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HBB3", "displayName": "H3.5.1.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Strömungssieden gesättigter, reiner Flüssigkeiten: Konvektives Strömungssieden in horizontalen Rohren", "en": "Flow boiling of saturated, pure liquids: Convective flow boiling in horizontal tubes" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HBB4", "displayName": "H3.5.2.1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Strömungssieden gesättigter, reiner Flüssigkeiten: Blasensieden in senkrechten Rohren", "en": "Flow boiling of saturated, pure liquids: Nucleate boiling in vertical tubes" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HBB5", "displayName": "H3.5.2.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Strömungssieden gesättigter, reiner Flüssigkeiten: Blasensieden in waagrechte Rohren", "en": "Flow boiling of saturated, pure liquids: Nucleate boiling in horizontal tubes" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HBC", "displayName": "H3.6", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Strömungssieden - Kritische Siedezustände", "en": "Flow boiling - Critical boiling states" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HBD", "displayName": "H3.7", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Strömungssieden - Wärmeübergang nach der Siedekrise", "en": "Flow boiling - Post boiling crisis heat transfer" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "HEAT", "displayName": "HEAT", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Kondensationswärme Inkrementale Berechnung", "en": "Condensation heat Incremental calculation" } ], "source": { "de": "", "en": "" } }, { "token": "HFO", "displayName": "HFO", "registered": true, "description": { "de": "Das Modul ermittelt die Stoffwerte von schweren Heizölen und Diesel\nFolgende Schweröle sind im Modul HFO enthalten:\n HFO 30\n HFO 60\n HFO 100\n HFO 180\n HFO 380\n HFO 420\n HFO 640\n HFO 700\n Lubeoil", "en": "The module determines the physical properties of heavy fuel oils and diesel.\nThe following heavy oils are contained in the HFO module:\n HFO 30\n HFO 60\n HFO 100\n HFO 180\n HFO 380\n HFO 420\n HFO 640\n HFO 700\n Lubeoil" }, "headlines": [ { "de": "", "en": "" }, { "de": "Stoffwerte von schweren Heizölen", "en": "Properties of heavy fuel oils" } ], "source": { "de": "", "en": "" } }, { "token": "INLR", "displayName": "INLR", "registered": true, "description": { "de": "Das Modul INLR berechnet den inneren Wärmeübergangskoeffizienten und den inneren Druckverlust in Abhängigkeit der Rohr- und Rippengeometrie, der Stoffwerte und der Strömungsbedingungen.", "en": "The INLR module calculates the internal heat transfer coefficient and the internal pressure loss as a function of the tube and fin geometry, the physical properties and the flow conditions." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung und Druckverlust in innenberippten Rohren", "en": "Heat transfer and pressure drop in internally finned tubes" } ], "source": { "de": "", "en": "" } }, { "token": "JA3", "displayName": "J1.3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Filmkondensation reiner Dämpfe: Kondensation an senkrechten Flächen", "en": "Film condensation of pure vapours: Condensation on vertical surfaces" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "JA4", "displayName": "J1.4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Filmkondensation reiner Dämpfe: Kondensation an waagrechten Rohren", "en": "Film condensation of pure vapours: Condensation at horizontal tubes" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "JA5", "displayName": "J1.3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Filmkondensation reiner Dämpfe: Kondensation im waagrechten Rohren", "en": "Film condensation of pure vapours: Condensation in horizontal tubes" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "JA6A", "displayName": "J1.6.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Filmkondensation reiner Dämpfe: Kondensation von Metalldämpfen", "en": "Film condensation of pure vapours: Condensation of metal vapours" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "JA6B", "displayName": "J1.6.3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Filmkondensation reiner Dämpfe: Kondensation von überhitztem Dampf", "en": "Film condensation of pure vapours: Condensation of superheatet vapour" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "JBA", "displayName": "J2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Kondensation von Mehrstoffgemischen", "en": "Condensation of multicomponent mixtures" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "JC", "displayName": "J3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Tropfenkondensation", "en": "Dropwise condensation" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "JDB", "displayName": "J4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Misch- und Sprühkondensation", "en": "Mix and injection condensation" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "KA", "displayName": "K1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmestrahlung technischer Oberflächen", "en": "Surface heat radiation" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "KB", "displayName": "K2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmestrahlung - Sichtfaktoren (Einstrahlzahlen)", "en": "Heat radiation - View factors" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "KC", "displayName": "K3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmestrahlung von Gasen und Gasgemischen", "en": "Heat radiation from gases and gas mixtures" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "KD", "displayName": "K4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmestrahlung von Gas-Feststoff-Gemischen", "en": "Thermal radiation from gas-solids mixtures" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "KE", "displayName": "K5", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmestrahlung in Brennräumen", "en": "Thermal radiation in furnaces" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "KF", "displayName": "K6", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmestrahlung - Superisolierungen", "en": "Heat radiation - Superinsulations" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "KON1", "displayName": "KON1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Kondensation in waagerechten Rohren Inkrementale Berechnung", "en": "Condensation in horizontal tubes Incremental calculation" } ], "source": { "de": "", "en": "" } }, { "token": "KON2", "displayName": "KON2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Kondensation in senkrechten Rohren Inkrementale Berechnung", "en": "Condensation in vertical tubes Incremental calculation" } ], "source": { "de": "", "en": "" } }, { "token": "KOND", "displayName": "KOND", "registered": true, "description": { "de": "Es können Reinstoff-Kondensatoren mit Enthitzungs-, Kondensations- und Unterkühlungszone berechnet werden. Bei der Kondensation im Mantelraum an horizontalen Rohren wird die Unterkühlung des Kondensats nicht berechnet. Die Kondensation kann im Mantelraum oder im Rohrraum erfolgen, ist aber auf reine Stoffe (keine Gemische) beschränkt.\nDie Berechnung ist auf Kondensatoren mit einem rohrseitigen Durchgang beschränkt.", "en": "Shell-and-tube condensers with enthalpy, condensation and subcooling zones can be calculated. The subcooling of the condensate is not calculated for shell-side condensation at horizontal tubes. The condensation can either take place around the tubes or in the tubes but it is restricted to pure vapours (no mixtures)\nKOND can only calculate condensers with one tube side pass." }, "headlines": [ { "de": "", "en": "" }, { "de": "Kondensatoren für reine Dämpfe", "en": "Condensers for pure vapours" } ], "source": { "de": "VDI Wärmeatlas", "en": "VDI Heat Atlas" } }, { "token": "KV", "displayName": "KV", "registered": true, "description": { "de": "Berechnung des Kv Wertes\n für inkompressible, kompressible Medien sowie für Sattdampf und überhitzten Dampf\n für Zweiphasenströmung\n\nBerechnung des Schallpegels\n für inkompressible Medien\n für kompressible Medien unter Berücksichtigung von Kavitation\n\nBerechnung der transienten Strömung in einem Einzelrohr", "en": "Calculation of the Kv value\n for incompressible, compressible media as well as for saturated steam and superheated steam\n for two-phase flow\n\nCalculation of the sound level\n for incompressible media\n for compressible media under consideration of cavitation\n\nCalculation of the transient flow in a single pipe" }, "headlines": [ { "de": "", "en": "" }, { "de": "Regel- und Absperrarmaturen", "en": "Fittings" } ], "source": { "de": "DIN IEC 534", "en": "" } }, { "token": "LAMO", "displayName": "LAMO", "registered": true, "description": { "de": "La Mont-Prinzip", "en": "La Mont Principle" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang in Verdampferrohren bei Zwangsumlauf", "en": "Heat transfer in forced-flow boilers" } ], "source": { "de": "", "en": "" } }, { "token": "LB", "displayName": "L1.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Druckverlust in durchströmten Rohren", "en": "Pressure drop in flowed through pipes" }, { "de": "Druckverlust bei der Strömung durch Rohre mit Kreisquerschnitt", "en": "Pressure drop in flowed through circular pipes" }, { "de": "Druckverlust bei der Strömung durch Rohre mit nicht kreisförmigem Querschnitt", "en": "Pressure drop in flowed through noncircular pipes" }, { "de": "Rohrwendeln", "en": "Coils" }, { "de": "Ringspalte", "en": "Annuli" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LBA", "displayName": "L2.1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Berechnung der Phasenanteile bei Gas-Flüssigkeitsströmungen", "en": "Calculation of phase fractions for gas-liquid flows" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LBB", "displayName": "L2.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Druckabfall von Gas-Flüssigkeitsströmungen in Rohren, Leitungselementen und Armaturen", "en": "Pressure drop of gas-liquid flows in pipes, line elements and fittings" }, { "de": "", "en": "" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LBG", "displayName": "L2.7", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Nasser Druckverlust und Leerblasen von Kolonnenböden", "en": "Wet pressure loss and emptying of tower trays" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LC", "displayName": "L1.3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Druckverlust in durchströmten Leitungen mit Querschnittsänderungen", "en": "Pressure drop in flowed through pipes with changes in cross section" }, { "de": "Querschnittsverengungen und -erweiterung", "en": "Cross section narrowing and widening" }, { "de": "Normblenden, Normdüsen und Normventuridüsen", "en": "Standard orifices, standard nozzles and standard venturi nozzles" }, { "de": "Recht- und schiefwinklige T-Stücke", "en": "Tees" }, { "de": "Umlenkungen", "en": "Bends" }, { "de": "Ventile und Schieber", "en": "Valves and slides" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LD", "displayName": "L1.4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Druckverluste in querumströmten Rohrbündeln", "en": "Pressure drop of tube bundles in cross flow" }, { "de": "Rohrbündel aus glatten Kreis- oder Ovalrohren", "en": "Tube bundle with plain circular or oval tubes" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LDA", "displayName": "L4.1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Bildung und Bewegung von Tropfen und Blasen in technischen Apparaten", "en": "Formation and movement of droplets and bubbles in technical apparatus" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LDB", "displayName": "L1.4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Druckverlust in querumströmten Rohrbündeln", "en": "Pressure drop of tube bundles in cross flow" }, { "de": "Rohrbündel aus berippten Kreis- oder Ovalrohren", "en": "Tube bundle with finned circular or oval tubes" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LE", "displayName": "L1.6", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Druckverlust in durchschtrömten Schüttungen", "en": "Pressure drop in flow through beds" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019, L1.6" } }, { "token": "LF", "displayName": "L3.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Strömungsformen und Druckverlust in Wirbelschichten", "en": "Flow patterns and pressure drop in fluidized beds" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LG", "displayName": "H3.3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Strömungssieden - Druckverlust in durchströmten Verdampferrohren", "en": "Flow Boiling – Pressure drop in flow through evaporator tubes" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LJA", "displayName": "L3.4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Zyklone zum Abscheiden fester Partikel aus Gasen", "en": "Cyclones to separate particles" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "LJB", "displayName": "L4.3.3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Tropfenabscheidung in technischen Apparaten: Zyklone", "en": "Droplet separation in technical apparatus: Cyclones" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LJC", "displayName": "L4.3.4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Lamellentropfenabscheider", "en": "Lamellar drop separator" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LL", "displayName": "L2.6", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Druckverlust und Flutgrenze in berieselten Packungen", "en": "Pressure drop and flood point in trickled beds of packing" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "LM", "displayName": "L1.5", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Druckverlust in umströmten Rohrbündeln in Wärmeübertragern mit und ohne Umlenkbleche", "en": "Pressure drop tube overflowed bundles in shell and tube heat exchangers with and without baffles" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "" } }, { "token": "LN", "displayName": "N3.3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung und Leistungsaufnahme in Rührkesseln: Rührleistung", "en": "Heat transfer and Power consumption in stirred vessels: Stirring Power" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "LOMA", "displayName": "LOMA", "registered": true, "description": { "de": "Strömungssieden gesättigter Flüssigkeiten – Ermittlung der Strömungsform im Lockhart-Martinelli-Diagramm\n\nDas Modul LOMA berechnet alle erforderlichen Parameter gemäß Kapitel H3.4 des VDI Wärmeatlas und ermittelt die Art der Zweiphasenströmung. Die Lage der vorliegenden Zweiphasenströmung wird in der Strömungsformenkarte (Lockhart-Martinelli-Diagramm) eingetragen.", "en": "Flow Boiling of Saturated Liquids – Determination of the Flow Pattern in the Lockhart-Martinelli Diagram\n\nThe LOMA module calculates all necessary parameters according to chapter H3.4 of the VDI Wärmeatlas and determines the type of two-phase flow. The position of the present two-phase flow is entered in the flow map (Lockhart-Martinelli diagram)." }, "headlines": [ { "de": "", "en": "" }, { "de": "Strömungsformendiagramm für 2 Phasenströmung Lockhart-Martinelli-Diagramm", "en": "Flow type diagram for two-phase flow Lockhart-Martinelli diagram" } ], "source": { "de": "VDI Wärmeatlas", "en": "VDI Heat Atlas" } }, { "token": "LUFT", "displayName": "LUFT", "registered": true, "description": { "de": "Stoffwerte trockener Luft.\nDie Kenntnis der Stoffeigenschaften von Luft ist in vielen verfahrenstechnischen Prozessen notwendig. So sind z.B. bei der Auslegung von luftgekühlten Wärmeübertragern ständig die Stoffwerte temperatur- und druckabhängig zu bestimmen.", "en": "Physical properties of dry air\nKnowledge of the physical properties of air is necessary in many process engineering processes. For example, in the design of air-cooled heat exchangers, the properties of the media must always be determined as a function of temperature and pressure." }, "headlines": [ { "de": "", "en": "" }, { "de": "Stoffwerte von Luft", "en": "Properties of air" } ], "source": { "de": "VDI Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "MA", "displayName": "N3.2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung und Leistungsaufnahme in Rührkesseln: Wärmeübergang", "en": "Heat transfer and Power consumption in stirred vessels: Heat transfer" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "MB", "displayName": "M1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang an berippten Rohren", "en": "Heat transfer on finned tubes" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "MC", "displayName": "M2", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmedurchgang durch Wände mit aufgeschweißten Rohrschlangen", "en": "Heat transfer through walls clad with welded tubes" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "MD", "displayName": "M3", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang an senkrechten Rieselfilmen", "en": "Heat transfer to vertical falling films" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "ME", "displayName": "M4", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang an nichtnewtonschen Flüssigkeiten", "en": "Heat transfer to non-newtonian liquids" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "MF", "displayName": "M5", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung in Wirbelschichten", "en": "Heat transfer in fluidized beds" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "MG", "displayName": "M6", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung von einer Heizfläche an ruhende oder mechanisch durchmischte Schüttungen", "en": "Heat transfer from a heated surface to fixed or stirred beds" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "MK", "displayName": "M8", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Be- und Entfeuchten von Luft", "en": "Moistening and dehumidify of air" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "ML", "displayName": "N5", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmerohre", "en": "Heatpipe" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "MM", "displayName": "N6", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Druckverlust und Wärmeübergang in Plattenwärmeübertragern", "en": "Pressure drop and heat transfer in plate heat exchangers" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "MO", "displayName": "M10", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung und Strömung in verdünnten Gasen", "en": "Heat transfer and heat flow in rarefied gas" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "N2", "displayName": "N2", "registered": true, "description": { "de": "Das Modul berechnet die Stoffwerte von Stickstoff (einphasig oder siedend).\nGültigkeitsbereiche\n\neinphasig\nTemperatur: -175 °C bis 1000 °C\nDruck: 1 bar bis 1000 bar\n\nsiedend\nTemperatur: -210 °C bis -147 °C", "en": "The module calculates the physical properties of nitrogen (single-phase or boiling).\nRanges of validity\n\nsingle-phase\nTemperature: -175 °C to 1000 °C\nPressure: 1 bar to 1000 bar\n\nboiling\nTemperature: -210 °C to -147 °C" }, "headlines": [ { "de": "", "en": "" }, { "de": "Stoffwerte von Stickstoff", "en": "Properties of nitrogen" } ], "source": { "de": "VDI Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "NAVE", "displayName": "NAVE", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung in Verdampfern", "en": "" } ], "source": { "de": "", "en": "" } }, { "token": "NH3", "displayName": "NH3", "registered": true, "description": { "de": "Das Modul berechnet die Stoffwerte von Ammoniak (einphasig oder siedend).\nGültigkeitsbereiche\n\neinphasig\nTemperatur: -50 °C bis 300 °C\nDruck: 1 bar bis 500 bar\n\nsiedend\nTemperatur: -75 °C bis 130 °C", "en": "The module calculates the physical properties of ammonia (single-phase or boiling).\nRanges of validity\n\nsingle-phase\nTemperature: -50 °C to 300 °C\nPressure: 1 bar to 500 bar\n\nboiling\nTemperature: -75 °C to 130 °C" }, "headlines": [ { "de": "", "en": "" }, { "de": "Stoffwerte von Ammoniak", "en": "Properties of ammonia" } ], "source": { "de": "VDI Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "O2", "displayName": "O2", "registered": true, "description": { "de": "Das Modul berechnet die Stoffwerte von Sauerstoff (einphasig oder siedend).\nGültigkeitsbereiche\n\neinphasig\nTemperatur: -200 °C bis 100 °C\nDruck: 1 bar bis 500 bar\n\nsiedend\nTemperatur: -218 °C bis -120 °C", "en": "The module calculates the physical properties of oxygen (single-phase or boiling).\nRanges of validity\n\nsingle-phase\nTemperature: -200 °C to 100 °C\nPressure: 1 bar to 500 bar\n\nboiling\nTemperature: -218 °C to -120 °C" }, "headlines": [ { "de": "", "en": "" }, { "de": "Stoffwerte von Sauerstoff", "en": "Properties of oxygen" } ], "source": { "de": "VDI Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas, 12. Edition 2019" } }, { "token": "OPTD", "displayName": "OPTD", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Optimierung von Druckverlusten von Rohrbündelwärmeübertragern nach VDI", "en": "Optimisation of pressure drops in shell-and-tube heat exchangers according to VDI" } ], "source": { "de": "", "en": "" } }, { "token": "RBSA", "displayName": "RBSA", "registered": true, "description": { "de": "Untersucht werden sowohl Rohrbündelwärmeübertrager mit zwei festen Rohrplatten als auch U-Rohr Wärmeübertrager. Die Berechnung erfolgt nach TEMA (Tubular Exchanger Manufacturers Association). Aufgrund der Komplexität der Problemstellung, deckt die TEMA-Garantie Schwingungsschäden jedoch nicht ab.\nBerechnet wird die Schwingungsanregung der Rohre und des Rohrbündels durch folgende Mechanismen:\nFluidelastische Instabilität\nWirbelanregung\nTurbulenzanregung", "en": "Both shell-and-tube heat exchangers with two fixed tube plates and U-tube heat exchangers are investigated. The calculation is performed according to TEMA (Tubular Exchanger Manufacturers Association). However, due to the complexity of the problem, the TEMA warranty does not cover vibration damage.\nRBSA calculates the vibration excitation of the tubes and the tube bundle by the following mechanisms:\nFluid-elastic instability\nVortex excitation\nTurbulence excitation" }, "headlines": [ { "de": "", "en": "" }, { "de": "Rohrbündel Schwingungs-Analyse", "en": "Tube bundle vibration analysis" } ], "source": { "de": "TEMA, 9. Auflage 2007, Abschnitt 6 & VDI-Wärmeatlas, 12. Auflage 2019, O2", "en": "TEMA, 9th Edition 2007, Section 6 & VDI Heat Atlas, 12. Edition 2019, O2" } }, { "token": "REG", "displayName": "N1", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung in Regeneratoren", "en": "Heat transfer in regenerators" } ], "source": { "de": "VDI-Wärmeatlas, 12. Auflage 2019", "en": "VDI Heat Atlas , 12. Edition 2019" } }, { "token": "RIES", "displayName": "RIES", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang in Rieselfilmen an waagrechten Rohren", "en": "Heat transfer in falling films at horizontal tubes" } ], "source": { "de": "", "en": "" } }, { "token": "RS3", "displayName": "RS3", "registered": true, "description": { "de": "Aus den Vorgaben der beteiligten Medien im Zentralrohr und in den beiden Ringspalten sowie der Vereinbarung der Stromführung (Gleichstrom, Gegenstrom) werden die Wärmeübergänge Zentralrohr - Ringspalt 1 und Ringspalt 1-Ringspalt 2 getrennt ermittelt und ausgewiesen.", "en": "From the specifications of the media involved in the central tube and in the two annular gaps as well as the agreement of the current guidance (direct current, counter current), the heat transitions central tube - annular gap 1 and annular gap 1 - annular gap 2 are determined and shown separately." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung und Druckverlust in Tripelrohren", "en": "Heat transfer and pressure drop in triple tubes" } ], "source": { "de": "VDI Wärmeatlas", "en": "VDI Heat Atlas" } }, { "token": "SOWU", "displayName": "SOWU", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Plattenwärmeübertrager", "en": "Plate heat exchangers" } ], "source": { "de": "VDI Wärmetlas", "en": "VDI Heat Atlas" } }, { "token": "SPIR", "displayName": "SPIR", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei der Strömung durch Rohre mit/ohne innenliegendem Spiralband", "en": "Heat transfer in pipe flow with and without twisted-tape inserts" } ], "source": { "de": "", "en": "" } }, { "token": "TANK", "displayName": "TANK", "registered": true, "description": { "de": "Das Modul Tank berechnet den Wärmeverlust von isolierten und nicht isolierten Lagertanks. Der Grundriss des Lagertanks kann rund oder rechteckig sein.", "en": "The Tank module calculates the heat loss of insulated and non-insulated storage tanks. The ground plan of the storage tank may be round or rectangular." }, "headlines": [ { "de": "", "en": "" }, { "de": "Ermittlung der Wärmeverluste von Lagertanks", "en": "Calculation of heat loss of storage tanks" } ], "source": { "de": "", "en": "" } }, { "token": "TAVA", "displayName": "TAVA", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Druckverlauf beim Abkühlen von heißen Lagertanks mit Vakuumbrechern", "en": "Pressure curve during cooling of hot storage tanks with vacuum breakers" } ], "source": { "de": "", "en": "" } }, { "token": "TOIL", "displayName": "T-OIL", "registered": true, "description": { "de": "Stoffwerte und Einsatzbereiche von mehr als 100 Wärmeträgerölen\nDas Programm stellt dem Benutzer eine Datenbank über Wärmeträgeröle zur Verfügung. Diese Thermalöle können nach den verschiedensten Kriterien wie maximale Einsatztemperatur, Name, Hersteller, maximale Filmtemperatur etc. ausgewählt werden.", "en": "Physical properties and application ranges of more than 100 heat transfer oils\nThe program provides the user with a database of heat transfer oils. These thermal oils can be selected according to various criteria such as maximum operating temperature, name, manufacturer, maximum film temperature, etc." }, "headlines": [ { "de": "", "en": "" }, { "de": "Stoffwerte von Thermalölen", "en": "Properties of thermal oils" } ], "source": { "de": "Produktinformationen der Hersteller", "en": "Manufacturers' product information" } }, { "token": "TWIS", "displayName": "TWIS", "registered": true, "description": { "de": "Das Modul TWIS berechnet auf der Grundlage experimenteller Ansätze den Wärmeübergangskoeffizienten und den Druckverlust in laminar durchströmten Rohren mit Schraubeneinbauten.", "en": "On the basis of experimental approaches, the TWIS module calculates the heat transfer coefficient and the pressure loss in laminar flow tubes with twisted-tape inserts." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei der Strömung durch Rohre mit/ohne Schraubeneinbauten", "en": "Laminar flow heat transfer in tubes with/without helical inserts" } ], "source": { "de": "", "en": "" } }, { "token": "VERD", "displayName": "VERD", "registered": true, "description": { "de": "Das Verdampfer-Programm dient zur Auslegung und Simulation von Reinstoff-Verdampfern ohne Vorwärmung der Flüssigkeit und ohne Überhitzung des Dampfes. Die Verdampfer sind zwangsdurchströmt.", "en": "The evaporator program serves for the design and simulation of pure substance evaporators without preheating of the liquid and without superheating of the steam. The evaporators have a forced flow." }, "headlines": [ { "de": "", "en": "" }, { "de": "Verdampfung reiner Stoffe in Rohrbündel- oder Doppelrohr-Wärmeübertragern", "en": "Vaporization of pure substances in shell-and-tube or double pipe heat exchangers" } ], "source": { "de": "VDI Wärmeatlas", "en": "VDI Heat Atlas" } }, { "token": "WAK", "displayName": "WAK", "registered": true, "description": { "de": "Das Programm WAK dient zur Berechnung von Abhitzewärmetauschern in Rohrwendelbauweise. Es können Warmwasser– oder Thermalölerhitzer berechnet werden. Um die Rohre wird Rauchgas geführt. Die Zusammensetzung des Rauchgases kann eingegeben werden oder man wählt Standardzusammensetzungen für typische Gas-, Heizöl- oder Feststoffverbrennungen.", "en": "The WAK program designs coil type economizers with multiple helical tube bundles. Hot water or thermal oil heaters can be calculated. The standard medium is hot oil on the tube side and flue gas on the shell side. The composition of the flue gas can be entered or standard compositions for typical gas, fuel oil or solid fuel combustion can be selected." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wendelrohr-Abhitzekessel", "en": "Flue gas heat exchanger" } ], "source": { "de": "VDI Wärmeatlas, F. Brandt, Wärmeübertragung in Dampferzeugern und Wärmetauschern, Vulkan Verlag 1995\nH. Hausen, Wärmeübertragung im Gegenstrom, Gleichstrom und Kreuzstrom, Springer 1976", "en": "VDI Heat Atlas, F. Brandt, Wärmeübertragung in Dampferzeugern und Wärmetauschern, Vulkan Verlag 1995\nH. Hausen, Wärmeübertragung im Gegenstrom, Gleichstrom und Kreuzstrom, Springer 1976" } }, { "token": "WROK", "displayName": "WROK", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübertragung bei Querströmung durch Rohrbündel mit kleiner Längsteilung", "en": "Heat transfer during cross flow through tube bundles with small tube pitch" } ], "source": { "de": "", "en": "" } }, { "token": "WTS", "displayName": "WTS", "registered": true, "description": { "de": "Mit dem Modulpaket WTS können Rohrbündel-Wärmetauscher für gasförmige und flüssige Medien sowie für kondensierende reine Stoffe ausgelegt werden. Der Funktionsumfang von WTS kann durch Zusatzmodule erweitert werden", "en": "With the WTS module package, tube bundle heat exchangers can be designed for gaseous and liquid media as well as for condensing pure substances. The range of features of WTS can be extended by additional modules." }, "headlines": [ { "de": "", "en": "" }, { "de": "Thermische und hydraulische Berechnung von Rohrbündel- und Doppelrohr-Wärmeübertragern", "en": "Thermal and hydraulic design of shell and tube and double pipe heat exchangers" } ], "source": { "de": "VDI Wärmeatlas", "en": "VDI Heat Atlas" } }, { "token": "ZIKT", "displayName": "PILLOW", "registered": true, "description": { "de": "", "en": "" }, "headlines": [ { "de": "Wärmeübergang und Druckverlust in Kühltaschen", "en": "" }, { "de": "", "en": "" } ], "source": { "de": "", "en": "" } }, { "token": "SPIE", "displayName": "SPIE", "registered": true, "description": { "de": "Das Modul SPIE ist ein Programm zur Erzeugung von Rohrspiegeln für Rohrbündel-Wärmeübertrager. Es besteht aus einem graphischen und einem numerischen Teil. Der Rohrspiegel kann vom Benutzer in allen Einzelheiten selbst erstellt werden. Es können 30.000 Rohre dargestellt und einzeln editiert werden. Zuganker und Blindrohre können vorgesehen werden.", "en": "The SPIE module is a program for the generation of tube sheets for tube bundle heat exchangers. It consists of a graphical and a numerical part. The tube sheet can be designed by the user in all details. 30,000 pipes can be represented and individually edited. Tie rods and dummy tubes can be used." }, "headlines": [ { "de": "", "en": "" }, { "de": "Rohrspiegeldaten", "en": "Tube sheet data" } ], "source": { "de": "", "en": "" } }, { "token": "ELLU", "displayName": "ELLU", "registered": true, "description": { "de": "Auslegung von elektrischen Erhitzern mit rechteckigen Bündeln. Es können verschiedene Medien um die Heizstäbe ausgewählt werden; der Wärmeübergang ist einphasig, maximale Oberflächen- und Kanalwandtemperaturen werden überprüft.", "en": "Design of electric heaters with rectangular tube bundles. Different media can be selected around the heating rods; the heat transfer is single-phase and the maximum surface and duct wall temperatures are checked." }, "headlines": [ { "de": "", "en": "" }, { "de": "Auslegung von elektrisch beheizten Rohrregistern", "en": "Design of electric tube register heaters" } ], "source": { "de": "Verfahrenstechnische Berechnungsmethoden, Teil 1, VCH Weinheim & VDI Wärmeatlas", "en": "" } }, { "token": "RIR", "displayName": "RIR", "registered": true, "description": { "de": "Wärmeübergang und Druckverlust in Doppelrohr-Einsteck-(\"Rohr-in-Rohr\")-Elementen: Berechnung der Wärmeübergangskoeffizienten und Druckverluste im Innenrohr und im Ringspalt.", "en": "Heat transfer and pressure drop in double-pipe (\"tube-in-tube\") elements: calculation of heat transfer coefficients and pressure drops in the inner tube and in the annulus." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmeübergang und Druckverlust in Doppelrohr-Einsteck ('Rohr-in-Rohr') Elementen", "en": "Heat transfer and pressure drop in doublepipe-plugin ('tube-in-tube') elements" } ], "source": { "de": "", "en": "" } }, { "token": "WAKO", "displayName": "WAKO", "registered": true, "description": { "de": "Berechnung des Wärmedurchgangs durch mehrschichtige ebene Wände und Rohre aus den Schichtdicken, Wärmeleitfähigkeiten und den Wärmeübergangskoeffizienten innen und außen.", "en": "Calculation of the heat transmission through multilayer plane walls and pipes from the layer thicknesses, thermal conductivities and the heat transfer coefficients on the inside and outside." }, "headlines": [ { "de": "", "en": "" }, { "de": "Wärmedurchgang durch mehrschichtige ebene Wände und Rohre", "en": "Heat transmission through multilayer plane walls and pipes" } ], "source": { "de": "", "en": "" } } ], "reusedWtsReference": { "schemaVersion": 1, "date": "2026-09-07", "webCommit": "33e53dbff07255f2d6a3159a62208cb20dcd8218", "desktopCommit": 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"id": 3, "module": "EGAS" }, { "id": 4, "module": "EGAS" }, { "id": 5, "module": "LUFT" }, { "id": 6, "module": "NH3" }, { "id": 7, "module": "NH3" }, { "id": 8, "module": "HX" }, { "id": 9, "module": "PROP" }, { "id": 11, "module": "TOIL" }, { "id": 12, "module": "RGAS" }, { "id": 13, "module": "OEL" }, { "id": 14, "module": "FRIG" }, { "id": 15, "module": "GLYC" }, { "id": 16, "module": "N2" }, { "id": 17, "module": "STAB" }, { "id": 18, "module": "H2SO" }, { "id": 19, "module": "HNO3" }, { "id": 20, "module": "HCL" }, { "id": 21, "module": "HE" }, { "id": 22, "module": "SAC" }, { "id": 23, "module": "CO2" }, { "id": 24, "module": "CO2" }, { "id": 25, "module": "N2H2" }, { "id": 26, "module": "SAWA" }, { "id": 27, "module": "EGAS" }, { "id": 28, "module": "BIER" }, { "id": 29, "module": "NAOH" }, { "id": 30, "module": "HFO" }, { "id": 31, "module": "O2" } ], "wtsVariables": [ { "id": 1, "de": "Massenstrom innen m_i", "en": "Mass flow (inside) m_i", "symbol": "_Massenstrom_innen_m_i" }, { "id": 2, "de": "Massenstrom aussen m_a", "en": "Mass flow outside m_a", "symbol": "_Massenstrom_aussen_m_a" }, { "id": 3, "de": "Volumenstrom innen V_i", "en": "Volume flow inside", "symbol": "_Volumenstrom_innen_V_i" }, { "id": 4, "de": "Volumenstrom aussen V_a", "en": "Volume flow outside", "symbol": "_Volumenstrom_aussen_V_a" }, { "id": 5, "de": "_Dichte Medium innen Rho_i", "en": "_Density tube side", "symbol": "_Dichte_Medium_innen_Rho_i" }, { "id": 6, "de": "_Dichte Medium aussen Rho_a", "en": "_Density shell side", "symbol": "_Dichte_Medium_aussen_Rho_a" }, { "id": 7, "de": "_Spezifische Wärmekapazität Medium innen cp_i", "en": "_Specific heat capacity tube side", "symbol": "_Spezifische_Waermekapazitaet_Medium_innen_cp_i" }, { "id": 8, "de": "_Spezifische Wärmekapazität Medium aussen cp_a", "en": "_Specific heat capacity shell side", "symbol": "_Spezifische_Waermekapazitaet_Medium_aussen_cp_a" }, { "id": 9, "de": "Eintrittstemperatur Medium innen te_i", "en": "Inlet temperature (inside) te_i", "symbol": "_Eintrittstemperatur_Medium_innen_te_i" }, { "id": 10, "de": "Austrittstemperatur Medium innen ta_i", "en": "Outlet temperature (inside) ta_i", "symbol": "_Austrittstemperatur_Medium_innen_ta_i" }, { "id": 11, "de": "Eintrittstemperatur Medium aussen te_a", "en": "Inlet temperature (outside) te_a", "symbol": "_Eintrittstemperatur_Medium_aussen_te_a" }, { "id": 12, "de": "Austrittstemperatur Medium aussen ta_a", "en": "Outlet temperature (outside) ta_a", "symbol": "_Austrittstemperatur_Medium_aussen_ta_a" }, { "id": 13, "de": "Leistung innen Q_i", "en": "Heat duty inside Q_i", "symbol": "_Leistung_innen_Q_i" }, { "id": 14, "de": "Leistung aussen Q_a", "en": "Heat duty outside Q_o", "symbol": "_Leistung_aussen_Q_a" }, { "id": 15, "de": "Verlustwärmestrom Q_v", "en": "Heat loss flux Q_v", "symbol": "_Verlustwaermestrom_Q_v" }, { "id": 16, "de": "_Wärmeübergangskoeffizient innen alpha_i", "en": "_Heat transfer coefficient inside Ó_i", "symbol": "_Waermeuebergangskoeffizient_innen_alpha_i" }, { "id": 17, "de": "_Wärmeübergangskoeffizient aussen alpha_a", "en": "_Heat transfer coefficient outside Ó_a", "symbol": "_Waermeuebergangskoeffizient_aussen_alpha_a" }, { "id": 18, "de": "Wärmeleitfähigkeit der Rohre lam", "en": "Thermal conductivity tube", "symbol": "_Waermeleitfaehigkeit_der_Rohre_lam" }, { "id": 19, "de": "Dicke der Übertragerfläche s", "en": "Thickness of heat exchange area s", "symbol": "_Dicke_der_Uebertragerflaeche_s" }, { "id": 20, "de": "Verschmutzungswiderstand f", "en": "Fouling resistance Rf", "symbol": "_Verschmutzungswiderstand_f" }, { "id": 21, "de": "Erforderliche Übertragerfläche A", "en": "Required heat transfer area A", "symbol": "_Erforderliche_Uebertragerflaeche_A" }, { "id": 22, "de": "_Mittlere log. Temperaturdifferenz (LMTD)", "en": "_Log. mean temperature difference (LMTD)", "symbol": "_Mittlere_log__Temperaturdifferenz__LMTD_" }, { "id": 23, "de": "_Wärmedurchgangskoeffizient k", "en": "_Overall heat transfer coefficient k", "symbol": "_Waermedurchgangskoeffizient_k" }, { "id": 24, "de": "Rohrdurchmesser aussen", "en": "Outside tube diameter", "symbol": "_Rohrdurchmesser_aussen" }, { "id": 25, "de": "Rohrdurchmesser innen", "en": "Inside tube diameter", "symbol": "_Rohrdurchmesser_innen" }, { "id": 26, "de": "Flag: Gegenstrom = 0, Gleichstrom = 1", "en": "Countercurrent flow = 0, Cocurrent flow = 1", "symbol": "_Flag__Gegenstrom___0__Gleichstrom___1" }, { "id": 27, "de": "Zusatzvariable für Gleichstrom", "en": "Zusatzvariable für Gleichstrom", "symbol": "_Zusatzvariable_fuer_Gleichstrom" }, { "id": 28, "de": "", "en": "", "symbol": "_Placeholder_Name_28" }, { "id": 29, "de": "_Mittlere Berechnungstemperatur innen", "en": "_Mean calculation temperature inside", "symbol": "_Mittlere_Berechnungstemperatur_innen" }, { "id": 30, "de": "_Mittlere Berechnungstemperatur aussen", "en": "_Mean calculation temperature outside", "symbol": "_Mittlere_Berechnungstemperatur_aussen" }, { "id": 31, "de": "_Mittlere Wandtemperatur innen", "en": "_mean wall temperature inside", "symbol": "__Mittlere_Wandtemperatur_innen" }, { "id": 32, "de": "_Mittlere Wandtemperatur aussen", "en": "_mean wall temperature outside", "symbol": "__Mittlere_Wandtemperatur_aussen" }, { "id": 33, "de": "_Verdampfungsenthalpie innen", "en": "_Enthalpy of evaporation (inside)", "symbol": "_Verdampfungsenthalpie_innen" }, { "id": 34, "de": "_Verdampfungsenthalpie aussen", "en": "", "symbol": "_Verdampfungsenthalpie_aussen" }, { "id": 35, "de": "_Dampfanteil am Eintritt innen", "en": "_Vapour fraction inlet inside", "symbol": "_Dampfanteil_am_Eintritt_innen" }, { "id": 36, "de": "_Dampfanteil am Eintritt aussen", "en": "_Vapour fraction inlet outside", "symbol": "_Dampfanteil_am_Eintritt_aussen" }, { "id": 37, "de": "Stoffart innen", "en": "Property inside", "symbol": "_Stoffart_innen" }, { "id": 38, "de": "Stoffart aussen", "en": "Property outside", "symbol": "_Stoffart_aussen" }, { "id": 39, "de": "Eintrittsdruck innen", "en": "Inlet pressure inside", "symbol": "_Eintrittsdruck_innen" }, { "id": 40, "de": "Eintrittsdruck außen", "en": "Inlet pressure outside", "symbol": "_Eintrittsdruck_aussen" }, { "id": 41, "de": "Manteldurchmesser außen", "en": "Shell diameter außen", "symbol": "_Manteldurchmesser_aussen" }, { "id": 42, "de": "Mantelwanddicke", "en": "Shell wall thickness", "symbol": "_Mantelwanddicke" }, { "id": 43, "de": "Rohrteilung quer zur Strömungsrichtung", "en": "Tube pitch crosswise to direction of flow", "symbol": "_Rohrteilung_quer_zur_Stroemungsrichtung" }, { "id": 44, "de": "Rohrteilung längs in Strömungsrichtung", "en": "Tube pitch in direction of flow", "symbol": "_Rohrteilung_laengs_in_Stroemungsrichtung" }, { "id": 45, "de": "Gassenbreite (Trennblech) b", "en": "Tube lane width b", "symbol": "_Gassenbreite__Trennblech__b" }, { "id": 46, "de": "Erforderliche Bündellänge l", "en": "Required bundle length l", "symbol": "_Erforderliche_Buendellaenge_l" }, { "id": 47, "de": "Gesamte Rohrzahl R", "en": "Total number of tubes R", "symbol": "_Gesamte_Rohrzahl_R" }, { "id": 48, "de": "Stoffwert innen", "en": "Property inside", "symbol": "_Stoffwert_innen" }, { "id": 49, "de": "Stoffwert außen", "en": "Property outside", "symbol": "_Stoffwert_aussen" }, { "id": 50, "de": "Alpha innen", "en": "Alpha inside", "symbol": "_Alpha_innen" }, { "id": 51, "de": "Rohrspiegel neu design", "en": "New design of tubesheet", "symbol": "_Rohrspiegel_neu_design" }, { "id": 52, "de": "Rohrspiegel", "en": "Tubesheet", "symbol": "_Rohrspiegel" }, { "id": 53, "de": "Strömungsgeschwindigkeit in den Rohren", "en": "Fluid velocity in the tubes", "symbol": "_Stroemungsgeschwindigkeit_in_den_Rohren" }, { "id": 54, "de": "_Manteldurchmesser innen", "en": "_shell diameter (inside)", "symbol": "_Manteldurchmesser_innen" }, { "id": 55, "de": "Anzahl der rohrseitigen Durchgänge", "en": "Number of tube-side passes", "symbol": "_Anzahl_der_rohrseitigen_Durchgaenge" }, { "id": 56, "de": "Fensterhöhe", "en": "Baffle cut", "symbol": "_Fensterhoehe" }, { "id": 57, "de": "_Abstand Bündel - Mantel", "en": "_Bundle-shell distance", "symbol": "_Abstand_Buendel___Mantel" }, { "id": 58, "de": "Abstand der Umlenkbleche", "en": "Baffle spacing", "symbol": "_Abstand_der_Umlenkbleche" }, { "id": 59, "de": "Abstand Boden 1. Umlenkblech", "en": "Distance between tubesheet and 1st baffle", "symbol": "_Abstand_Boden_1__Umlenkblech" }, { "id": 60, "de": "Ausgeführte Bündellänge", "en": "Actual length of bundle", "symbol": "_Ausgefuehrte_Buendellaenge" }, { "id": 61, "de": "Gewünschte Strömungsgeschwindigkeit Rohr", "en": "Desired tube-side velocity", "symbol": "_Gewuenschte_Stroemungsgeschwindigkeit_Rohr" }, { "id": 62, "de": "Gewünschte Strömungsgeschwindigkeit Mantel", "en": "Desired shell-side velocity", "symbol": "_Gewuenschte_Stroemungsgeschwindigkeit_Mantel" }, { "id": 63, "de": "Mindest Abstand Umlenkbleche", "en": "Minimum baffle pitch", "symbol": "_Mindest_Abstand_Umlenkbleche" }, { "id": 64, "de": "_Druckverlust rohrseitig", "en": "_Pressure drop tube side", "symbol": "__Druckverlust_rohrseitig" }, { "id": 65, "de": "_Druckverlust mantelseitig", "en": "_Pressure drop shell side", "symbol": "__Druckverlust_mantelseitig" }, { "id": 66, "de": "Dampfgeschwindigkeit innen", "en": "Vapour velocity tube side", "symbol": "_Dampfgeschwindigkeit_innen" }, { "id": 67, "de": "_Dampfdichte innen", "en": "_Density of vapour (inside)", "symbol": "_Dampfdichte_innen" }, { "id": 68, "de": "Dampfgeschwindigkeit", "en": "Vapour velocity", "symbol": "_Dampfgeschwindigkeit" }, { "id": 69, "de": "_Dampfdichte außen", "en": "_Density of vapour outside", "symbol": "_Dampfdichte_aussen" }, { "id": 70, "de": "Innendurchmesser des Eintrittsstutzens Rohrseite", "en": "Inside diameter of inlet nozzle tube side", "symbol": "_Innendurchmesser_des_Eintrittsstutzens_Rohrseite" }, { "id": 71, "de": "Innendurchmesser des Austrittsstutzens Rohrseite", "en": "Inside diameter of outlet nozzle tube side", "symbol": "_Innendurchmesser_des_Austrittsstutzens_Rohrseite" }, { "id": 72, "de": "Innendurchmesser des Eintrittsstutzens Mantelseite", "en": "Inside diameter inlet nozzle shell side", "symbol": "_Innendurchmesser_des_Eintrittsstutzens_Mantelseite" }, { "id": 73, "de": "Innendurchmesser des Austrittsstutzens Mantelseite", "en": "Inside diameter of outlet nozzle shell side", "symbol": "_Innendurchmesser_des_Austrittsstutzens_Mantelseite" }, { "id": 74, "de": "Geschwindigkeit im Eintrittsstutzen Rohrseite", "en": "Velocity inlet tube side", "symbol": "_Geschwindigkeit_im_Eintrittsstutzen_Rohrseite" }, { "id": 75, "de": "Geschwindigkeit im Austrittsstutzen Rohrseite", "en": "Velocity outlet tube side", "symbol": "_Geschwindigkeit_im_Austrittsstutzen_Rohrseite" }, { "id": 76, "de": "Geschwindigkeit im Eintrittsstutzen Mantelseite", "en": "Velocity inlet shell side", "symbol": "_Geschwindigkeit_im_Eintrittsstutzen_Mantelseite" }, { "id": 77, "de": "Geschwindigkeit im Austrittsstutzen Mantelseite", "en": "Velocity outlet shell side", "symbol": "_Geschwindigkeit_im_Austrittsstutzen_Mantelseite" }, { "id": 78, "de": "Tema Flag", "en": "TEMA Flag", "symbol": "_Tema_Flag" }, { "id": 79, "de": "Proper Flag", "en": "Proper Flag", "symbol": "_Proper_Flag" }, { "id": 80, "de": "_FN Faktor", "en": "_FN Factor", "symbol": "_FN_Faktor" }, { "id": 81, "de": "_Zulässige Dampfüberhitzung bei Kondensation", "en": "_Allowable steam superheat at condensation", "symbol": "_Zulaessige_Dampfueberhitzung_bei_Kondensation" }, { "id": 82, "de": "Flag Rohrspiegel designed", "en": "Flag tubesheet designed", "symbol": "_Flag_Rohrspiegel_designed" }, { "id": 83, "de": "Strömungsrichtung", "en": "Flow direction", "symbol": "_Stroemungsrichtung" }, { "id": 84, "de": "_Wärmeleitfähigkeit Medium innen", "en": "_Thermal conductivity medium inside", "symbol": "_Waermeleitfaehigkeit_Medium_innen" }, { "id": 85, "de": "_Dynamische Viskosität Medium innen", "en": "_Dynamic viscosity medium insdide", "symbol": "_Dynamische_Viskositaet_Medium_innen" }, { "id": 86, "de": "_Wärmeleitfähigkeit Medium außen", "en": "_Thermal conductivity shell side", "symbol": "_Waermeleitfaehigkeit_Medium_aussen" }, { "id": 87, "de": "_Dynamische Viskosität Medium aussen", "en": "_Dynamic viscosity (outside)", "symbol": "_Dynamische_Viskositaet_Medium_aussen" }, { "id": 88, "de": "", "en": "", "symbol": "_Placeholder_Name_88" }, { "id": 89, "de": "Anzahl der seriell geschalteten Wärmeübertrager", "en": "Number of heat exchangers in series", "symbol": "_Anzahl_der_seriell_geschalteten_Waermeuebertrager" }, { "id": 90, "de": "Nach Tema rechnen", "en": "Calculation according to TEMA", "symbol": "_Nach_Tema_rechnen" }, { "id": 91, "de": "Verschmutzungswiderstand f innen", "en": "Fouling resistance f tube side", "symbol": "_Verschmutzungswiderstand_f_innen" }, { "id": 92, "de": "Verschmutzungswiderstand f außen", "en": "Fouling resistance f shell side", "symbol": "_Verschmutzungswiderstand_f_aussen" }, { "id": 93, "de": "Teilungswinkel", "en": "Pitch angle", "symbol": "_Teilungswinkel" }, { "id": 94, "de": "Strömungsgeschwindigkeit Mantel", "en": "Fluid velocity shell side", "symbol": "_Stroemungsgeschwindigkeit_Mantel" }, { "id": 95, "de": "Leistungsdifferential", "en": "Temperature differential of transf. Coefficient", "symbol": "_Leistungsdifferential" }, { "id": 96, "de": "Übertragerfläche A vorhanden", "en": "Actual exchanger area A", "symbol": "_Uebertragerflaeche_A_vorhanden" }, { "id": 97, "de": "Anzahl der mantelseitigen Durchgänge", "en": "Number of shell-side passes", "symbol": "_Anzahl_der_mantelseitigen_Durchgaenge" }, { "id": 98, "de": "Anzahl Rohre alt", "en": "Number of tubes old", "symbol": "_Anzahl_Rohre_alt" }, { "id": 99, "de": "Frostsicherheit bei Glykol (innen)", "en": "Frost resistance (Glycol tube-side)", "symbol": "_Frostsicherheit_bei_Glykol__innen_" }, { "id": 100, "de": "Prandtl Wand innen", "en": "Prandtl wall inside", "symbol": "_Prandtl_Wand_innen" }, { "id": 101, "de": "Prandtl Wand außen", "en": "Prandtl wall outside", "symbol": "_Prandtl_Wand_aussen" }, { "id": 102, "de": "Eta Wand innen", "en": "Eta wall inside", "symbol": "_Eta_Wand_innen" }, { "id": 103, "de": "Eta Wand außen", "en": "Eta wall outside", "symbol": "_Eta_Wand_aussen" }, { "id": 104, "de": "Mindest Bündel Mantel Abstand", "en": "Minimum bundle-shell distance", "symbol": "_Mindest_Buendel_Mantel_Abstand" }, { "id": 105, "de": "Gewünschter Cut", "en": "Desired cut", "symbol": "_Gewuenschter_Cut" }, { "id": 106, "de": "", "en": "", "symbol": "_Placeholder_Name_106" }, { "id": 107, "de": "_Stoffart innen", "en": "_Kind of medium inside", "symbol": "_Stoffart_innen_2" }, { "id": 108, "de": "_Stoffart aussen", "en": "_Kind of medium outside", "symbol": "_Stoffart_aussen_2" }, { "id": 109, "de": "Durchmesser der Bohrungen im Umlenkblech", "en": "Bore diameter in baffle", "symbol": "_Durchmesser_der_Bohrungen_im_Umlenkblech" }, { "id": 110, "de": "Anpassung Bohrung an TEMA", "en": "Adaption borehole in the baffle to TEMA", "symbol": "_Anpassung_Bohrung_an_TEMA" }, { "id": 111, "de": "Maximale Rohrlänge", "en": "Maximum tube length", "symbol": "_Maximale_Rohrlaenge" }, { "id": 112, "de": "Maximales Verhältnis l/Di", "en": "Maximum ratio l/Di", "symbol": "_Maximales_Verhaeltnis_l_Di" }, { "id": 113, "de": "Minimales Verhältnis l/Di", "en": "Minimum ratio l/Di", "symbol": "_Minimales_Verhaeltnis_l_Di" }, { "id": 114, "de": "Anpassung Geometrie (Design Kriteria)", "en": "Adaption geometry (Design criteria)", "symbol": "_Anpassung_Geometrie__Design_Kriteria_" }, { "id": 115, "de": "Anzahl der Umlenkbleche pro Gang", "en": "Number of baffles per pass", "symbol": "_Anzahl_der_Umlenkbleche_pro_Gang" }, { "id": 116, "de": "Flag Joule Thomson in den Rohren", "en": "Flag Joule-Thomson in the tubes", "symbol": "_Flag_Joule_Thomson_in_den_Rohren" }, { "id": 117, "de": "Durchmesser der Umlenkbleche", "en": "Baffle diameter", "symbol": "_Durchmesser_der_Umlenkbleche" }, { "id": 118, "de": "Anzahl der Dichtungsstreifenpaare", "en": "Number of sealing strip pairs", "symbol": "_Anzahl_der_Dichtungsstreifenpaare" }, { "id": 119, "de": "_Rippendurchmesser", "en": "_Fin diameter", "symbol": "_Rippendurchmesser" }, { "id": 120, "de": "_Rippenteilung", "en": "_Fin pitch", "symbol": "_Rippenteilung" }, { "id": 121, "de": "_Rippendicke", "en": "_Fin thickness", "symbol": "_Rippendicke" }, { "id": 122, "de": "Flag Niedrig berippte Rohre", "en": "Flag low finned tubes", "symbol": "_Flag_Niedrig_berippte_Rohre" }, { "id": 123, "de": "Übertragerfläche Innen", "en": "Exchanger area inside", "symbol": "_Uebertragerflaeche_Innen" }, { "id": 124, "de": "Flag: 0=Segmentumlenkbl. 1=ohne Einbauten 2=Disk/Doughnut 3=kontinuierlich 4=diskontinuierlich", "en": "Flag: 0=Segmentumlenkbl. 1=ohne Einbauten 2=Disk/Doughnut 3=kontinuierlich 4=diskontinuierlich", "symbol": "_Flag__0_Segmentumlenkbl__1_ohne_Einbauten_2_Disk_Doughnut_3_kontinuierlich_4_diskontinuierlich" }, { "id": 125, "de": "Produkt aus Fläche und Wärmedurchgang", "en": "Product of (area x heat transfer)", "symbol": "_Produkt_aus_Flaeche_und_Waermedurchgang" }, { "id": 126, "de": "Einstellung für Stoffmodule 1 innen", "en": "Property module 1 (inside)", "symbol": "_Einstellung_fuer_Stoffmodule_1_innen" }, { "id": 127, "de": "Einstellung für Stoffmodule 2 innen", "en": "Property module 2 (inside)", "symbol": "_Einstellung_fuer_Stoffmodule_2_innen" }, { "id": 128, "de": "Einstellung für Stoffmodule 3 innen", "en": "Property module 3 (inside)", "symbol": "_Einstellung_fuer_Stoffmodule_3_innen" }, { "id": 129, "de": "Einstellung für Stoffmodule 1 aussen", "en": "Property module 1 (outside)", "symbol": "_Einstellung_fuer_Stoffmodule_1_aussen" }, { "id": 130, "de": "Einstellung für Stoffmodule 2 aussen", "en": "Property module 2 (outside)", "symbol": "_Einstellung_fuer_Stoffmodule_2_aussen" }, { "id": 131, "de": "Einstellung für Stoffmodule 3 aussen", "en": "Property module 3 (outside)", "symbol": "_Einstellung_fuer_Stoffmodule_3_aussen" }, { "id": 132, "de": "Frostsicherheit bei Glykol (aussen)", "en": "Frost resistance (Glycol shell-side)", "symbol": "_Frostsicherheit_bei_Glykol__aussen_" }, { "id": 133, "de": "Flag Abstand RB-U > d_S", "en": "Flag distance RB-U > d_S", "symbol": "_Flag_Abstand_RB_U___d_S" }, { "id": 134, "de": "Aufruf RBSA-Modul", "en": "Call RBSA Module", "symbol": "_Aufruf_RBSA_Modul" }, { "id": 135, "de": "Bündeltyp", "en": "Bundle type", "symbol": "_Buendeltyp" }, { "id": 136, "de": "Innendurchmesser Schalung (Siemens-KWU)", "en": "Diameter of bundle (KWU-exchanger)", "symbol": "_Innendurchmesser_Schalung__Siemens_KWU_" }, { "id": 137, "de": "Geschwindigkeit an der ersten Rohrreihe", "en": "Fluid velocity in first tube row", "symbol": "_Geschwindigkeit_an_der_ersten_Rohrreihe" }, { "id": 138, "de": "Flag für Einbauten in den Rohren", "en": "Flag for fittings in the tubes", "symbol": "_Flag_fuer_Einbauten_in_den_Rohren" }, { "id": 139, "de": "Flag für Rippen in den Rohren", "en": "Flag for fins in the tubes", "symbol": "_Flag_fuer_Rippen_in_den_Rohren" }, { "id": 140, "de": "_Anzahl der Rippen/Rohr (Innenrippe)", "en": "_Number of fins/tube (internal fin)", "symbol": "_Anzahl_der_Rippen_Rohr__Innenrippe_" }, { "id": 141, "de": "_Rippenhöhe (Innenrippe)", "en": "_Fin height (internal fin)", "symbol": "_Rippenhoehe__Innenrippe_" }, { "id": 142, "de": "_Rippendicke an der Rippenschneide (Innenrippe)", "en": "_Fin thickness at fin tip (internal fin)", "symbol": "_Rippendicke_an_der_Rippenschneide__Innenrippe_" }, { "id": 143, "de": "_Rippendicke am Rippenfuß (Innenrippe)", "en": "_Fin thickness at fin root (internal fin)", "symbol": "_Rippendicke_am_Rippenfuss__Innenrippe_" }, { "id": 144, "de": "Flag für Standardwerte", "en": "Flag for standard value", "symbol": "_Flag_fuer_Standardwerte" }, { "id": 145, "de": "Dubioses Flag in Gleichung 28", "en": "dubious flag in Equation 28", "symbol": "_Dubioses_Flag_in_Gleichung_28" }, { "id": 146, "de": "Flag für WTSELECT", "en": "Flag for ´WTSELECT´", "symbol": "_Flag_fuer_WTSELECT" }, { "id": 147, "de": "Flag für Rohrspiegel eingefroren", "en": "Flag for locked tubesheet", "symbol": "_Flag_fuer_Rohrspiegel_eingefroren" }, { "id": 148, "de": "Einstellung für Stoffmodule 4 innen", "en": "Property module 4 (inside)", "symbol": "_Einstellung_fuer_Stoffmodule_4_innen" }, { "id": 149, "de": "Einstellung für Stoffmodule 4 aussen", "en": "Property module 4 (outside)", "symbol": "_Einstellung_fuer_Stoffmodule_4_aussen" }, { "id": 150, "de": "---- muß frei bleiben ----------------", "en": "--- release---------------------------", "symbol": "______muss_frei_bleiben_________________" }, { "id": 151, "de": "Stoffname für Proper innen", "en": "Name of medium inside for PROPER", "symbol": "_Stoffname_fuer_Proper_innen" }, { "id": 152, "de": "Stoffname für Proper aussen", "en": "Name of medium outside for PROPER", "symbol": "_Stoffname_fuer_Proper_aussen" }, { "id": 153, "de": "Flag längsberippte Rippenrohre", "en": "Flag for lengthwise-finned tubes", "symbol": "_Flag_laengsberippte_Rippenrohre" }, { "id": 154, "de": "_Anzahl der Rippen pro Rohr", "en": "_Number of fins per tube", "symbol": "_Anzahl_der_Rippen_pro_Rohr" }, { "id": 155, "de": "Rippenhöhe", "en": "Fin height", "symbol": "_Rippenhoehe" }, { "id": 156, "de": "_Rippendicke am Rippenfuß", "en": "_Fin thickness at fin root", "symbol": "_Rippendicke_am_Rippenfuss" }, { "id": 157, "de": "_Wärmeleitfähigkeit der Rippen", "en": "_Thermal conductivity of the fins", "symbol": "_Waermeleitfaehigkeit_der_Rippen" }, { "id": 158, "de": "Dichte Wand innen", "en": "Density of tube-side fluid at wall temperature", "symbol": "_Dichte_Wand_innen" }, { "id": 159, "de": "Rohroberfläche außen für 1 Rohr mit 1 m Länge", "en": "Tube outside area for one tube with a length of 1 m", "symbol": "_Rohroberflaeche_aussen_fuer_1_Rohr_mit_1_m_Laenge" }, { "id": 160, "de": "Rohroberfläche innen für 1 Rohr mit 1 m Länge", "en": "Tube inside area for one tube with a length of 1 m", "symbol": "_Rohroberflaeche_innen_fuer_1_Rohr_mit_1_m_Laenge" }, { "id": 161, "de": "Dichte Wand aussen", "en": "Density of shell-side fluid at wall temperature", "symbol": "_Dichte_Wand_aussen" }, { "id": 162, "de": "Zeiger flüssig/gasförmig (für GGLR)", "en": "Pointer liquid/vapour (for GGLR)", "symbol": "_Zeiger_fluessig_gasfoermig__fuer_GGLR_" }, { "id": 163, "de": "Flag für Doppelrohr", "en": "Flag for double pipe", "symbol": "_Flag_fuer_Doppelrohr" }, { "id": 164, "de": "", "en": "", "symbol": "_Placeholder_Name_164" }, { "id": 165, "de": "Durchmesser Kreisscheibe", "en": "Disk diameter", "symbol": "_Durchmesser_Kreisscheibe" }, { "id": 166, "de": "Durchmesser Kreisring", "en": "Diameter doughnut", "symbol": "_Durchmesser_Kreisring" }, { "id": 167, "de": "_Steigungswinkel", "en": "_Helix angle", "symbol": "_Steigungswinkel" }, { "id": 168, "de": "Rippendurchmesser", "en": "Fin diameter", "symbol": "_Rippendurchmesser_2" }, { "id": 169, "de": "Alpha innen setzen nein = 0 ja = 1", "en": "Set alpha inside? ", "symbol": "_Alpha_innen_setzen_nein___0_ja___1" }, { "id": 170, "de": "Alpha aussen setzen nein = 0 ja = 1", "en": "Set alpha outside? ", "symbol": "_Alpha_aussen_setzen_nein___0_ja___1" }, { "id": 171, "de": "Flag für Lamellenblock 1 = Lamellen", "en": "Flag for lamellar block 1 = lamellas", "symbol": "_Flag_fuer_Lamellenblock_1___Lamellen" }, { "id": 172, "de": "Abstand Rohrboden 1. Umlenkblech anpassen", "en": "Adapt distance tubesheet - 1st baffle", "symbol": "_Abstand_Rohrboden_1__Umlenkblech_anpassen" }, { "id": 173, "de": "Phasenzustand innen: ,flüssig = 0, gas = 1, Kond = 2", "en": "Phase inside: ,liquid = 0, gas = 1, cond = 2", "symbol": "_Phasenzustand_innen___fluessig___0__gas___1__Kond___2" }, { "id": 174, "de": "Phasenzustand aussen: flüssig = 0, gas = 1, Kond = 2", "en": "Phase outside: liquid = 0, gas = 1, cond = 2", "symbol": "_Phasenzustand_aussen__fluessig___0__gas___1__Kond___2" }, { "id": 175, "de": "Flag Drallrohre", "en": "Flag Drallrohre", "symbol": "_Flag_Drallrohre" }, { "id": 176, "de": "_Stoffart innen nähere Bezeichnung", "en": "_Medium inside; detailed name", "symbol": "_Stoffart_innen_naehere_Bezeichnung" }, { "id": 177, "de": "_Stoffart aussen nähere Bezeichnung", "en": "_Medium outside; detailed name", "symbol": "_Stoffart_aussen_naehere_Bezeichnung" }, { "id": 178, "de": "Geometriebeschreibung innen", "en": "Geometry description tube-side", "symbol": "_Geometriebeschreibung_innen" }, { "id": 179, "de": "Geometriebeschreibung aussen", "en": "Geometry description shell-side", "symbol": "_Geometriebeschreibung_aussen" }, { "id": 180, "de": "_Tatsächliche Eintrittstemperatur Medium innen", "en": "_Real temperature inlet medium inside", "symbol": "_Tatsaechliche_Eintrittstemperatur_Medium_innen" }, { "id": 181, "de": "_Tatsächliche Eintrittstemperatur Medium aussen", "en": "_Real temperature inlet medium outside", "symbol": "_Tatsaechliche_Eintrittstemperatur_Medium_aussen" }, { "id": 182, "de": "Flag Austrittstemperaturen simulieren", "en": "Flag simulate outlet temperature", "symbol": "_Flag_Austrittstemperaturen_simulieren" }, { "id": 183, "de": "_Strömungsgeschwindigkeit im Fenster", "en": "", "symbol": "__Stroemungsgeschwindigkeit_im_Fenster" }, { "id": 184, "de": "Flag Mantelmaterial ETS-Kunden-CD", "en": "Flag Mantelmaterial ETS-Kunden-CD", "symbol": "_Flag_Mantelmaterial_ETS_Kunden_CD" }, { "id": 185, "de": "_Normdichte Gas aussen", "en": "_Standard density gas shell side", "symbol": "_Normdichte_Gas_aussen" }, { "id": 186, "de": "_Normdichte Gas innen", "en": "_Standard density gas tube side", "symbol": "_Normdichte_Gas_innen" }, { "id": 187, "de": "_Norm-Volumenstrom aussen V_N_a", "en": "_Standard volume flow shell sideV_N_a", "symbol": "_Norm_Volumenstrom_aussen_V_N_a" }, { "id": 188, "de": "_Norm-Volumenstrom innen V_N_i", "en": "_Standard volume flow tube side V_N_i", "symbol": "_Norm_Volumenstrom_innen_V_N_i" }, { "id": 189, "de": "Kapitelnummer aufrufendes KOND oder UVERD", "en": "", "symbol": "_Kapitelnummer_aufrufendes_KOND_oder_UVERD" }, { "id": 190, "de": "Flag Mantel wurde ausgewählt", "en": "Flag Mantel wurde ausgewählt", "symbol": "_Flag_Mantel_wurde_ausgewaehlt" }, { "id": 191, "de": "Einbaulage", "en": "Installation position", "symbol": "_Einbaulage" }, { "id": 192, "de": "Zusätzliches Flag für Rohrspiegel", "en": "Extra flag for tubesheet", "symbol": "_Zusaetzliches_Flag_fuer_Rohrspiegel" }, { "id": 193, "de": "Korrekturfaktor für alpha innen", "en": "Correction factor for alpha tubeside", "symbol": "_Korrekturfaktor_fuer_alpha_innen" }, { "id": 194, "de": "Silageart FUOSO", "en": "Silageart FUOSO", "symbol": "_Silageart_FUOSO" }, { "id": 195, "de": "Behr-Flag 1 Flechtrohrbündel", "en": "Behr-Flag 1 Flechtrohrbündel", "symbol": "_Behr_Flag_1_Flechtrohrbuendel" }, { "id": 196, "de": "Gesamte Rohrlänge (incl. Rohrböden)", "en": "Total tube length (incl. tubesheet)", "symbol": "_Gesamte_Rohrlaenge__incl__Rohrboeden_" }, { "id": 197, "de": "Flag für Bauform Stoffwertmodule innen", "en": "Flag für Bauform Stoffwertmodule innen", "symbol": "_Flag_fuer_Bauform_Stoffwertmodule_innen" }, { "id": 198, "de": "Flag für Bauform Stoffwertmodule außen", "en": "", "symbol": "_Flag_fuer_Bauform_Stoffwertmodule_aussen" }, { "id": 199, "de": "Bezeichnung der Bauform in Bibliothek", "en": "Name of type in library", "symbol": "_Bezeichnung_der_Bauform_in_Bibliothek" }, { "id": 200, "de": "Flag: Keine Rohre in den Fenstern", "en": "Flag: No tubes in window", "symbol": "_Flag__Keine_Rohre_in_den_Fenstern" }, { "id": 201, "de": "_Fw Korrekturfaktor Wärmeleitung Längsleitblech", "en": "_Fw correction factor thermal conductivity longitudinal baffle", "symbol": "_Fw_Korrekturfaktor_Waermeleitung_Laengsleitblech" }, { "id": 202, "de": "Flag Universal Hydraulik", "en": "Flag Universal Hydraulik", "symbol": "_Flag_Universal_Hydraulik" }, { "id": 203, "de": "Anzahl Rohrreihen in der Querströmungszone", "en": "Number of tube rows in the cross flow zone", "symbol": "_Anzahl_Rohrreihen_in_der_Querstroemungszone" }, { "id": 204, "de": "Fensterhöhe", "en": "Baffle cut", "symbol": "_Fensterhoehe_2" }, { "id": 205, "de": "_Flächenreserve", "en": "_Oversize", "symbol": "_Flaechenreserve" }, { "id": 206, "de": "Flag WTSC-Aufruf", "en": "Flag WtsC-Aufruf", "symbol": "_Flag_WTSC_Aufruf" }, { "id": 207, "de": "Beschreibung der Umlenkbleche", "en": "Baffle type", "symbol": "_Beschreibung_der_Umlenkbleche" }, { "id": 208, "de": "Kaltstarttemperatur innen", "en": "Inside temperature at start-up", "symbol": "_Kaltstarttemperatur_innen" }, { "id": 209, "de": "Kaltstarttemperatur außen", "en": "Outside temperature at start-up", "symbol": "_Kaltstarttemperatur_aussen" }, { "id": 210, "de": "Dichte Medium innen bei Kaltstarttemperatur", "en": "Density medium inside at start-up temperature", "symbol": "_Dichte_Medium_innen_bei_Kaltstarttemperatur" }, { "id": 211, "de": "Dichte Medium außen bei Kaltstarttemperatur", "en": "Density medium outside at start-up temperature", "symbol": "_Dichte_Medium_aussen_bei_Kaltstarttemperatur" }, { "id": 212, "de": "Spez. Wärmekapazität Medium innen Kaltstart", "en": "Spec. heat capacity medium inside at start-up temperature", "symbol": "_Spez__Waermekapazitaet_Medium_innen_Kaltstart" }, { "id": 213, "de": "Spez. Wärmekapazität Medium außen Kaltstart", "en": "Spec. heat capacity medium outside at start-up temperature", "symbol": "_Spez__Waermekapazitaet_Medium_aussen_Kaltstart" }, { "id": 214, "de": "Dyn. Viskosität Medium innen bei Kaltstartt.", "en": "Dyn. viscosity Medium medium inside at start-up temperature", "symbol": "_Dyn__Viskositaet_Medium_innen_bei_Kaltstartt_" }, { "id": 215, "de": "Dyn. Viskosität Medium außen bei Kaltstartt.", "en": "Dyn. Viscosity medium outside at start-up temperature", "symbol": "_Dyn__Viskositaet_Medium_aussen_bei_Kaltstartt_" }, { "id": 216, "de": "Wärmeleitfähigkeit Medium innen bei Kaltstartt.", "en": "Thermal conductivity medium inside at start-up temperature", "symbol": "_Waermeleitfaehigkeit_Medium_innen_bei_Kaltstartt_" }, { "id": 217, "de": "Wärmeleitfähigkeit Medium außen bei Kaltstartt.", "en": "Thermal conductivity medium outside at start-up temperature", "symbol": "_Waermeleitfaehigkeit_Medium_aussen_bei_Kaltstartt_" }, { "id": 218, "de": "Druckverlust bei Kaltstart innen", "en": "Inside pressure drop at start-up temperature", "symbol": "_Druckverlust_bei_Kaltstart_innen" }, { "id": 219, "de": "Druckverlust bei Kaltstart außen", "en": "Outside pressure drop at start-up temperature", "symbol": "_Druckverlust_bei_Kaltstart_aussen" }, { "id": 220, "de": "Flag NewCool", "en": "Flag NewCool", "symbol": "_Flag_NewCool" }, { "id": 221, "de": "Flag Siemens-Kondensator", "en": "Flag Siemens-Kondensator", "symbol": "_Flag_Siemens_Kondensator" }, { "id": 222, "de": "Anzahl der Bohrungen", "en": "Number of holes", "symbol": "_Anzahl_der_Bohrungen" }, { "id": 223, "de": "_Tatsächliche Austrittstemperatur Medium innen", "en": "_Real temperature inside", "symbol": "_Tatsaechliche_Austrittstemperatur_Medium_innen" }, { "id": 224, "de": "_Tatsächliche Austrittstemperatur Medium außen", "en": "_Real temperature outside", "symbol": "_Tatsaechliche_Austrittstemperatur_Medium_aussen" }, { "id": 225, "de": "Flag Visual Beendet", "en": "Flag Visual Beendet", "symbol": "_Flag_Visual_Beendet" }, { "id": 226, "de": "Salzgehalt Rohrseite", "en": "Salinity tube-side", "symbol": "_Salzgehalt_Rohrseite" }, { "id": 227, "de": "Salzgehalt Mantelseite", "en": "Salinity shell-side", "symbol": "_Salzgehalt_Mantelseite" }, { "id": 228, "de": "Gassenbreite (Trennblech) vertikal", "en": "Path width vetical", "symbol": "_Gassenbreite__Trennblech__vertikal" }, { "id": 229, "de": "Enthalpie innen ein", "en": "Enthalpy inside inlet", "symbol": "_Enthalpie_innen_ein" }, { "id": 230, "de": "Enthalpie innen aus", "en": "Enthalpy insude outlet", "symbol": "_Enthalpie_innen_aus" }, { "id": 231, "de": "Enthalpie aussen ein", "en": "Enthalpy outside inlet", "symbol": "_Enthalpie_aussen_ein" }, { "id": 232, "de": "Enthalpie aussen aus", "en": "Enthalpy outside outlet", "symbol": "_Enthalpie_aussen_aus" }, { "id": 233, "de": "Enthalpie h' innen", "en": "Enthalpy h' inside", "symbol": "_Enthalpie_h__innen" }, { "id": 234, "de": "Enthalpie h''innen", "en": "Enthalpy h'' inside", "symbol": "_Enthalpie_h___innen" }, { "id": 235, "de": "Enthalpie h' aussen", "en": "Enthalpy h' outside", "symbol": "_Enthalpie_h__aussen" }, { "id": 236, "de": "Enthalpie h'' aussen", "en": "Enthalpy h'' outside", "symbol": "_Enthalpie_h___aussen" }, { "id": 237, "de": "Siedetemperatur innen", "en": "Boiling temperature inside", "symbol": "_Siedetemperatur_innen" }, { "id": 238, "de": "Siededruck innen", "en": "Boiling pressure inside", "symbol": "_Siededruck_innen" }, { "id": 239, "de": "Siedetemperatur aussen", "en": "Boiling temperature outside", "symbol": "_Siedetemperatur_aussen" }, { "id": 240, "de": "Siededruck aussen", "en": "Boiling pressure outside", "symbol": "_Siededruck_aussen" }, { "id": 241, "de": "_Dampfanteil am Austritt innen", "en": "_Vapour fraction outlet inside", "symbol": "_Dampfanteil_am_Austritt_innen" }, { "id": 242, "de": "_Dampfanteil am Austritt aussen", "en": "_Vapour fraction outlet outside", "symbol": "_Dampfanteil_am_Austritt_aussen" }, { "id": 243, "de": "Rho · v² innen Eintritt", "en": "Rho · v² inside inlet", "symbol": "_Rho___v__innen_Eintritt" }, { "id": 244, "de": "Rho · v² Eintrittsstutzen Mantelseite", "en": "Rho · v² inlet nozzle shell side", "symbol": "_Rho___v__Eintrittsstutzen_Mantelseite" }, { "id": 245, "de": "Dicke des Längsleitbleches", "en": "Thickness longitudinal baffle", "symbol": "_Dicke_des_Laengsleitbleches" }, { "id": 246, "de": "Wärmeleitfähigkeit des Längsleitbleches", "en": "Thermal conductivity longitudinal baffle", "symbol": "_Waermeleitfaehigkeit_des_Laengsleitbleches" }, { "id": 247, "de": "Länge des Längsleitbleches", "en": "Lenght longitudinal baffle", "symbol": "_Laenge_des_Laengsleitbleches" }, { "id": 248, "de": "Geschwindigkeit um Kreisscheibe", "en": "Velocity around the disk", "symbol": "_Geschwindigkeit_um_Kreisscheibe" }, { "id": 249, "de": "Geschwindigkeit in Öffnung Kreisring", "en": "Velocity in opening of doughnut", "symbol": "_Geschwindigkeit_in_Oeffnung_Kreisring" }, { "id": 250, "de": "_Rohrspiegel-Typ", "en": "_Tubesheet type", "symbol": "_Rohrspiegel_Typ" }, { "id": 251, "de": "_Kondensat-Massenstrom bei feuchten Gasen innen", "en": "_Mass flow condensate humid gas inside", "symbol": "_Kondensat_Massenstrom_bei_feuchten_Gasen_innen" }, { "id": 252, "de": "_Kondensat-Massenstrom bei feuchten Gasen außen", "en": "_Mass flow condensate humid gas outside", "symbol": 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