{
  "schemaVersion": "1.0",
  "module": "HAB2",
  "contentVersion": "legacy-e619f6b1db68",
  "supportLevel": "legacy-bootstrap",
  "title": {
    "de": "HAB2",
    "en": "HAB2 - HAB2-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/HAB2/index_de.html",
    "en": "/output/HAB2/index_en.html"
  },
  "knowledgeBase": null,
  "helpTopics": [
    {
      "language": "en",
      "title": "HAB2 - HAB2-e",
      "url": "/output/HAB2/HAB2-e_en.html",
      "excerpt": "HAB2 - HAB2-e DE HAB2 HAB2-e Contents HAB2-e On this page eReference Springer Verlag Heat transfer coefficients α0 at shell-side evaporation Heat transfer coefficient Heat transfer coefficients α0 at shell-side evaporation HAB2-e eReference Springer Verlag VDI Heat Atlas eReference Heat transfer coefficient Heat transfer coefficients α0 at shell-side evaporation 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 R23 48.32 4800 Difluoromethane CH 2 F 2 R32 57.82 5000 Pentafluoroethane CHF 2 CF 3 R125 36.18 4400 1,1,1,2-Tetrafluoroethan"
    },
    {
      "language": "de",
      "title": "HAB2",
      "url": "/output/HAB2/HAB2_de.html",
      "excerpt": "HAB2 EN HAB2 Navigation HAB2 Auf dieser Seite eReference Springer Verlag Normierte Wärmeübergangskoeffizienten α0 bei Verdampfung im Mantelraum Wärmeübergangskoeffizient Normierte Wärmeübergangskoeffizienten α0 bei Verdampfung im Mantelraum HAB2 eReference Springer Verlag Zum Springer Wärmeatlas 11. Auflage Wärmeübergangskoeffizient Normierte Wärmeübergangskoeffizienten α0 bei Verdampfung im Mantelraum Wärmeübergangskoeffizienten α 0 (bei p 0 * , q 0 . R a,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 ASHRAE Krit. Druck α 0 P c α 0,exp bar W/(m²K) Trifluormethan CHF 3 R23 48.32 4800 Difluormethan CH 2 F 2 R32 57.82 5000 Pe"
    }
  ],
  "variables": [],
  "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": "H2.2",
        "designType": null,
        "defaultBauform": null
      }
    ]
  }
}