{
  "schemaVersion": "1.0",
  "module": "HAB6",
  "contentVersion": "legacy-e619f6b1db68",
  "supportLevel": "legacy-bootstrap",
  "title": {
    "de": "HAB6 - HAB6-e",
    "en": "HAB6 - HAB6-e"
  },
  "summary": {
    "de": "Bestehende LVS-Modulhilfe. Variablen und Bedienregeln müssen vor Änderungen mit dem aktuellen MCP-Laufzeitzustand abgeglichen werden.",
    "en": "Existing LVS module help. Variables and operating rules must be reconciled with current MCP runtime state before making changes."
  },
  "humanHelp": {
    "de": "/output/HAB6/index_de.html",
    "en": "/output/HAB6/index_en.html"
  },
  "knowledgeBase": null,
  "helpTopics": [
    {
      "language": "en",
      "title": "HAB6 - HAB6-e",
      "url": "/output/HAB6/HAB6-e_en.html",
      "excerpt": "HAB6 - HAB6-e DE HAB6 HAB6-e Contents HAB6-e On this page eReference Springer Verlag Variable 56 – Heat transfer coefficient of substance 1 Variable 57 – Heat transfer coefficient of substance 2 Variable 58 – Factor A0 Variables Variable 56 – Heat transfer coefficient of substance 1 Variable 57 – Heat transfer coefficient of substance 2 Variable 58 – Factor A0 HAB6-e eReference Springer Verlag VDI Heat Atlas eReference Variables Variable 56 – Heat transfer coefficient of substance 1 Heat transfer coefficients α 0 at p 0 * = 0.1, R a0 = 1 · 10 -6 m and reference values of the heat flux q 0 Fluid Formula Crit. pressure α 0 P c α 0,exp bar W/(m²K) Methane CH 4 45.99 7200 Ethene H 2 C=CH 2 50.42 4200 Ethane CH 3 CH 3 48.72 4600 Propene H 2 C=CHCH 3 45.55 4200 Propane CH 3 CH 2 CH 3 42.51 4300 n-Butane C 4 H 10 37.96 3600 i-Butane C 4 H 10 36.29 3700 n-Pentane C 5 H 12 33.70 3300 i-Pentane C 5 H 12 33.78 3200 n-Hexane C 6 H 14 30.34 3200 Cyclohexane C 6 H 12 40.75 3000 n-Heptane C 7 H 16 27.36 2900 Benzene C 6 H 6 48.94 2900 Toluene C 7 H 8 41.26 2800 Diphenyl C 12 H 10 38.47 2100 Methanol CH 3 OH 82.16 5150 Ethanol CH 3 CH 2 OH 61.31 4350 n-Propanol CH 3 CH 2 CH 2 OH 50.50 3750 2-Propanol CH 3 CHOHCH 3 47.60 3950 n-Butanol CH 3 CH 2 CH 2 CH 2 OH 44.10 2600 i-Butanol CH 3 CH 3 CHCH 2 OH 42.95 4500 2-Butanol CH 3 CHOHCH 2 CH 3 41.94 3400 Ethanal CH 3 CHO 55.50 3500 Acetone CH 3 COCH 3 47.0 3300 Fluid Formula ASHRAE Crit. pressure α 0 P c α 0,exp bar W/(m²K) Trifluoromethane CHF 3 R"
    },
    {
      "language": "en",
      "title": "HAB6",
      "url": "/output/HAB6/HAB6_en.html",
      "excerpt": "HAB6 DE HAB6 Contents HAB6 On this page eReference Springer Verlag Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Variable 57 – Wärmeübergangskoeffizient von Stoff 2 Variable 58 – Faktor A0 Variablen Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Variable 57 – Wärmeübergangskoeffizient von Stoff 2 Variable 58 – Faktor A0 HAB6 eReference Springer Verlag Zum Springer Wärmeatlas 11. Auflage Variablen Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Normierte Wärmeübergangskoeffizienten α 0 bei Verdampfung im Mantelraum Wärmeübergangskoeffizienten α 0 (bei p0*, q0. Ra,0) für 57 Fluide beim Blasensieden an einzelnen horizontalen Cu-Rohren bei Verdampfung im Mantelraum Fluid Formel Krit. Druck α 0 P c α 0,exp bar W/(m²K) Methan CH 4 45.99 7200 Ethen H 2 C=CH 2 50.42 4200 Ethan CH 3 CH 3 48.72 4600 Propen H 2 C=CHCH 3 45.55 4200 Propan CH 3 CH 2 CH 3 42.51 4300 n-Butan C 4 H 10 37.96 3600 i-Butan C 4 H 10 36.29 3700 n-Pentan C 5 H 12 33.70 3300 i-Pentan C 5 H 12 33.78 3200 n-Hexan C 6 H 14 30.34 3200 Cyclohexan C 6 H 12 40.75 3000 n-Heptan C 7 H 16 27.36 2900 Benzol C 6 H 6 48.94 2900 Toluol C 7 H 8 41.26 2800 Diphenyl C 12 H 10 38.47 2100 Methanol CH 3 OH 82.16 5150 Ethanol CH 3 CH 2 OH 61.31 4350 n-Propanol CH 3 CH 2 CH 2 OH 50.50 3750 2-Propanol CH 3 CHOHCH 3 47.60 3950 n-Butanol CH 3 CH 2 CH 2 CH 2 OH 44.10 2600 i-Butanol CH 3 CH 3 CHCH 2 OH 42.95 4500 2-Butanol CH 3 CHOHCH 2 CH 3 41.94 3400 Acetaldehyd CH 3 CHO 55.50 3500 Aceton CH 3 COCH 3 47.0 3300 Fluid Formel A"
    }
  ],
  "variables": [
    {
      "varNr": 56,
      "semanticStatus": "legacy-help-only",
      "label": {
        "de": "HAB6 - Variable 56 – Wärmeübergangskoeffizient von Stoff 1",
        "en": "HAB6 - Variable 56 – Heat transfer coefficient of substance 1"
      },
      "description": {
        "de": "HAB6 - Variable 56 – Wärmeübergangskoeffizient von Stoff 1 HAB6 Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Navigation eReference Springer Verlag Engineering Your Best Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Variable 57 – Wärmeübergangskoeffizient von Stoff 2 Variable 58 – Faktor A0 Variablen Engineering Your Best Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Normierte Wärmeübergangskoeffizienten α 0 bei Verdampfung im Mantelraum Wärmeübergangskoeffizienten α 0 (bei p0*, q0. Ra,0) für 57 Fluide beim Blasensieden an einzelnen horizontalen Cu-Rohren bei Verdampfung im Mantelraum Fluid Formel Krit. Druck α 0 P c α 0,exp bar W/(m²K) Methan CH 4 45.99 7200 Ethen H 2 C=CH 2 50.42 4200 Ethan CH 3 CH 3 48.72 4600 Propen H 2 C=CHCH 3 45.55 4200 Propan CH 3 CH 2 CH 3 42.51 4300 n-Butan C 4 H 10 37.96 3600 i-Butan C 4 H 10 36.29 3700 n-Pentan C 5 H 12 33.70 3300 i-Pentan C 5 H 12 33.78 3200 n-Hexan C 6 H 14 30.34 3200 Cyclohexan C 6 H 12 40.75 3000 n-Heptan C 7 H 16 27.36 2900 Benzol C 6 H 6 48.94 2900 Toluol C 7 H 8 41.26 2800 Diphenyl C 12 H 10 38.47 2100 Methanol CH 3 OH 82.16 5150 Ethanol CH 3 CH 2 OH 61.31 4350",
        "en": "HAB6 - Variable 56 – Heat transfer coefficient of substance 1 HAB6 Variable 56 – Heat transfer coefficient of substance 1 Contents eReference Springer Verlag Engineering Your Best Variable 56 – Heat transfer coefficient of substance 1 Variable 57 – Heat transfer coefficient of substance 2 Variable 58 – Factor A0 Variables Engineering Your Best Variable 56 – Heat transfer coefficient of substance 1 Variable 56 – Heat transfer coefficient of substance 1 Heat transfer coefficients α 0 at p 0 * = 0.1, R a0 = 1 · 10 -6 m and reference values of the heat flux q 0 Fluid Formula Crit. pressure α 0 P c α 0,exp bar W/(m²K) Methane CH 4 45.99 7200 Ethene H 2 C=CH 2 50.42 4200 Ethane CH 3 CH 3 48.72 4600 Propene H 2 C=CHCH 3 45.55 4200 Propane CH 3 CH 2 CH 3 42.51 4300 n-Butane C 4 H 10 37.96 3600 i-Butane C 4 H 10 36.29 3700 n-Pentane C 5 H 12 33.70 3300 i-Pentane C 5 H 12 33.78 3200 n-Hexane C 6 H 14 30.34 3200 Cyclohexane C 6 H 12 40.75 3000 n-Heptane C 7 H 16 27.36 2900 Benzene C 6 H 6 48.94 2900 Toluene C 7 H 8 41.26 2800 Diphenyl C 12 H 10 38.47 2100 Methanol CH 3 OH 82.16 5150 Ethanol CH 3 CH 2 OH 61.31 4350 n-Propanol CH 3 CH 2 CH 2 OH 50.50 3750 2-Propanol CH 3 CHOHCH 3 47.60 3950 n-B"
      },
      "help": {
        "de": [
          "/output/HAB6/varhelp/variable56wrmebergangskoeffizientvonstoff1_de.html"
        ],
        "en": [
          "/output/HAB6/varhelp/variable56heattransfercoefficientofsubstance1_en.html"
        ]
      }
    },
    {
      "varNr": 57,
      "semanticStatus": "legacy-help-only",
      "label": {
        "de": "HAB6 - Variable 57 – Wärmeübergangskoeffizient von Stoff 2",
        "en": "HAB6 - Variable 57 – Heat transfer coefficient of substance 2"
      },
      "description": {
        "de": "HAB6 - Variable 57 – Wärmeübergangskoeffizient von Stoff 2 HAB6 Variable 57 – Wärmeübergangskoeffizient von Stoff 2 Navigation eReference Springer Verlag Engineering Your Best Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Variable 57 – Wärmeübergangskoeffizient von Stoff 2 Variable 58 – Faktor A0 Variablen Engineering Your Best Variable 57 – Wärmeübergangskoeffizient von Stoff 2 Variable 57 – Wärmeübergangskoeffizient von Stoff 2 Normierte Wärmeübergangskoeffizienten α 0 bei Verdampfung im Mantelraum Wärmeübergangskoeffizienten α 0 (bei p0*, q0. Ra,0) für 57 Fluide beim Blasensieden an einzelnen horizontalen Cu-Rohren bei Verdampfung im Mantelraum Fluid Formel Krit. Druck α 0 P c α 0,exp bar W/(m²K) Methan CH 4 45.99 7200 Ethen H 2 C=CH 2 50.42 4200 Ethan CH 3 CH 3 48.72 4600 Propen H 2 C=CHCH 3 45.55 4200 Propan CH 3 CH 2 CH 3 42.51 4300 n-Butan C 4 H 10 37.96 3600 i-Butan C 4 H 10 36.29 3700 n-Pentan C 5 H 12 33.70 3300 i-Pentan C 5 H 12 33.78 3200 n-Hexan C 6 H 14 30.34 3200 Cyclohexan C 6 H 12 40.75 3000 n-Heptan C 7 H 16 27.36 2900 Benzol C 6 H 6 48.94 2900 Toluol C 7 H 8 41.26 2800 Diphenyl C 12 H 10 38.47 2100 Methanol CH 3 OH 82.16 5150 Ethanol CH 3 CH 2 OH 61.31 4350",
        "en": "HAB6 - Variable 57 – Heat transfer coefficient of substance 2 HAB6 Variable 57 – Heat transfer coefficient of substance 2 Contents eReference Springer Verlag Engineering Your Best Variable 56 – Heat transfer coefficient of substance 1 Variable 57 – Heat transfer coefficient of substance 2 Variable 58 – Factor A0 Variables Engineering Your Best Variable 57 – Heat transfer coefficient of substance 2 Variable 57 – Heat transfer coefficient of substance 2 Heat transfer coefficients α 0 at p 0 * = 0.1, R a0 = 1 · 10 -6 m and reference values of the heat flux q 0 Fluid Formula Crit. pressure α 0 P c α 0,exp bar W/(m²K) Methane CH 4 45.99 7200 Ethene H 2 C=CH 2 50.42 4200 Ethane CH 3 CH 3 48.72 4600 Propene H 2 C=CHCH 3 45.55 4200 Propane CH 3 CH 2 CH 3 42.51 4300 n-Butane C 4 H 10 37.96 3600 i-Butane C 4 H 10 36.29 3700 n-Pentane C 5 H 12 33.70 3300 i-Pentane C 5 H 12 33.78 3200 n-Hexane C 6 H 14 30.34 3200 Cyclohexane C 6 H 12 40.75 3000 n-Heptane C 7 H 16 27.36 2900 Benzene C 6 H 6 48.94 2900 Toluene C 7 H 8 41.26 2800 Diphenyl C 12 H 10 38.47 2100 Methanol CH 3 OH 82.16 5150 Ethanol CH 3 CH 2 OH 61.31 4350 n-Propanol CH 3 CH 2 CH 2 OH 50.50 3750 2-Propanol CH 3 CHOHCH 3 47.60 3950 n-B"
      },
      "help": {
        "de": [
          "/output/HAB6/varhelp/variable57wrmebergangskoeffizientvonstoff2_de.html"
        ],
        "en": [
          "/output/HAB6/varhelp/variable57heattransfercoefficientofsubstance2_en.html"
        ]
      }
    },
    {
      "varNr": 58,
      "semanticStatus": "legacy-help-only",
      "label": {
        "de": "HAB6 - Variable 58 – Faktor A0",
        "en": "HAB6 - Variable 58 – Factor A0"
      },
      "description": {
        "de": "HAB6 - Variable 58 – Faktor A0 HAB6 Variable 58 – Faktor A0 Navigation eReference Springer Verlag Engineering Your Best Variable 56 – Wärmeübergangskoeffizient von Stoff 1 Variable 57 – Wärmeübergangskoeffizient von Stoff 2 Variable 58 – Faktor A0 Variablen Engineering Your Best Variable 58 – Faktor A0 Variable 58 – Faktor A 0 Experimentelle Werte für die Größe A 0 in Gl. 23 Stoffsystem A 0 Methanol – Ethanol 1.39 Methanol – Benzol 1.08 Methanol – Amylalkohol 0.80 Methanol – Wasser 0.56 Ethanol – Benzol 0.42 Ethanol – Cyclohexan 1.31 Ethanol – Wasser 1.21 an Kupfer 0.81 an Nickel Propanol – Wasser 3.29 Isopropanol – Wasser 2.04 Aceton – Ethanol 0.75 Aceton – Butanol 1.18 Aceton –Methanol 1.19 Aceton – Wasser 1.40 an Kupfer 0.81 an Nickel Wasser – Glykol 1.47 Wasser – Glyzerin 1.50 Wasser – Pyridin 3.56 Wasser – Toluol 1.44 Heptan – Methylcyclohexan 1.95 Methylethylketon – Toluol 1.32 Methylethylketon – Wasser 1.21 © Springer Verlag Berlin-Heidelberg 2006",
        "en": "HAB6 - Variable 58 – Factor A0 HAB6 Variable 58 – Factor A0 Contents eReference Springer Verlag Engineering Your Best Variable 56 – Heat transfer coefficient of substance 1 Variable 57 – Heat transfer coefficient of substance 2 Variable 58 – Factor A0 Variables Engineering Your Best Variable 58 – Factor A0 Variable 58 – Factor A 0 Experimental values for factor A 0 in eq. 23 System A 0 Methanol – Ethanol 1.39 Methanol – Benzene 1.08 Methanol – Amyl alcohol 0.80 Methanol – Water 0.56 Ethanol – Benzene 0.42 Ethanol – Cyclohexane 1.31 Ethanol – Water 1.21 on copper 0.81 on nickel Propanol – Water 3.29 Isopropanol – Water 2.04 Aceton – Ethanol 0.75 Aceton – Butanol 1.18 Aceton – Methanol 1.19 Aceton – Water 1.40 on copper 0.81 on nickel Water – Glycol 1.47 Water – Glycerol 1.50 Water – Pyridine 3.56 Water – Toluol 1.44 Heptane – Methylcyclohexane 1.95 Methyl ethyl ketone – Toluol 1.32 Methyl ethyl ketone – Water 1.21 © Springer Verlag Berlin-Heidelberg 2013"
      },
      "help": {
        "de": [
          "/output/HAB6/varhelp/variable58faktora0_de.html"
        ],
        "en": [
          "/output/HAB6/varhelp/variable58factora0_en.html"
        ]
      }
    }
  ],
  "mcp": {
    "readBeforeUse": true,
    "workflow": [
      "Read this context and the human module help.",
      "Inspect the live module definition and current values through MCP.",
      "Resolve materials through the material workflow when material selectors are present.",
      "Set only runtime-confirmed input variables; never infer writable state from a legacy help filename.",
      "Calculate, inspect validation messages and read back governing results."
    ],
    "limitations": [
      "This bootstrap context preserves the complete legacy help but does not yet contain a curated semantic variable contract.",
      "Runtime MCP metadata is authoritative when it differs from this legacy snapshot."
    ]
  },
  "migration": {
    "curated": false,
    "target": "Create content/modules/<MODULE>/module.json and bilingual HTML fragments using B1 as the reference.",
    "sourceRepository": "lvs",
    "sourceCommit": "e619f6b1db68045fa49935d6f5f807b9acd1bc1d",
    "catalogConfigurations": [
      {
        "configId": "",
        "displayName": "H2.4",
        "designType": null,
        "defaultBauform": null
      }
    ]
  }
}