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gabrielserrao

pyResToolbox MCP Server

gas_viscosity

Calculate gas viscosity at reservoir conditions using the Lee-Gonzalez-Eakin correlation for accurate flow rate and pressure drop analysis in petroleum engineering.

Instructions

Calculate gas viscosity (μg).

CRITICAL GAS PVT PROPERTY - Computes gas viscosity at reservoir conditions using Lee, Gonzalez & Eakin (1966) correlation, industry standard for natural gas. Viscosity affects flow rates, pressure drops, and well performance. Gas viscosity increases with pressure and temperature, opposite to liquid behavior.

Parameters:

  • sg (float, required): Gas specific gravity (air=1.0). Valid: 0.55-3.0. Typical: 0.6-1.2. Example: 0.7.

  • degf (float, required): Reservoir temperature in °F. Valid: -460 to 1000. Typical: 100-400°F. Example: 180.0.

  • p (float or list, required): Pressure(s) in psia. Must be > 0. Can be scalar or array. Example: 3500.0 or [1000, 2000, 3000, 4000].

  • h2s (float, optional, default=0.0): H2S mole fraction (0-1). Typical: 0-0.05. Example: 0.02.

  • co2 (float, optional, default=0.0): CO2 mole fraction (0-1). Typical: 0-0.20. Example: 0.05.

  • n2 (float, optional, default=0.0): N2 mole fraction (0-1). Typical: 0-0.10. Example: 0.01.

  • zmethod (str, optional, default="DAK"): Z-factor method for viscosity calculation. Options: "DAK", "HY", "WYW", "BUR". DAK recommended.

Viscosity Behavior:

  • Increases with pressure (gas molecules closer together)

  • Increases with temperature (molecular motion increases)

  • Typical range: 0.01-0.05 cP at reservoir conditions

  • At standard conditions: ~0.01 cP

Lee-Gonzalez-Eakin Correlation: Uses Z-factor internally to account for real gas behavior. More accurate than ideal gas assumptions, especially at high pressures.

Returns: Dictionary with:

  • value (float or list): Viscosity in cP (matches input p shape)

  • method (str): "Lee-Gonzalez-Eakin"

  • units (str): "cP"

  • inputs (dict): Echo of input parameters

Common Mistakes:

  • Using separator temperature instead of reservoir temperature

  • Pressure in barg/psig instead of psia (must be absolute)

  • Not accounting for non-hydrocarbon fractions

  • Confusing gas viscosity (increases with P) with oil viscosity (decreases with P)

  • Temperature in Celsius instead of Fahrenheit

Example Usage:

{
    "sg": 0.7,
    "degf": 180.0,
    "p": [1000, 2000, 3000, 4000],
    "h2s": 0.0,
    "co2": 0.05,
    "n2": 0.01,
    "zmethod": "DAK"
}

Result: Viscosity increases from ~0.012 cP at 1000 psia to ~0.025 cP at 4000 psia.

Note: Gas viscosity is much lower than oil viscosity (typically 0.01-0.05 cP vs 0.5-10 cP). Always use reservoir conditions, not separator conditions. Account for all non-hydrocarbon components for accuracy.

Input Schema

TableJSON Schema
NameRequiredDescriptionDefault
requestYes

Implementation Reference

  • The gas_viscosity tool handler function. Calculates gas viscosity using pyrestoolbox.gas.gas_ug with Lee-Gonzalez-Eakin correlation. Handles scalar and array inputs, converts numpy arrays to lists for JSON, and returns structured response.
    @mcp.tool()
    def gas_viscosity(request: GasViscosityRequest) -> dict:
        """Calculate gas viscosity (μg).
    
        **CRITICAL GAS PVT PROPERTY** - Computes gas viscosity at reservoir conditions
        using Lee, Gonzalez & Eakin (1966) correlation, industry standard for natural gas.
        Viscosity affects flow rates, pressure drops, and well performance. Gas viscosity
        increases with pressure and temperature, opposite to liquid behavior.
    
        **Parameters:**
        - **sg** (float, required): Gas specific gravity (air=1.0). Valid: 0.55-3.0.
          Typical: 0.6-1.2. Example: 0.7.
        - **degf** (float, required): Reservoir temperature in °F. Valid: -460 to 1000.
          Typical: 100-400°F. Example: 180.0.
        - **p** (float or list, required): Pressure(s) in psia. Must be > 0.
          Can be scalar or array. Example: 3500.0 or [1000, 2000, 3000, 4000].
        - **h2s** (float, optional, default=0.0): H2S mole fraction (0-1).
          Typical: 0-0.05. Example: 0.02.
        - **co2** (float, optional, default=0.0): CO2 mole fraction (0-1).
          Typical: 0-0.20. Example: 0.05.
        - **n2** (float, optional, default=0.0): N2 mole fraction (0-1).
          Typical: 0-0.10. Example: 0.01.
        - **zmethod** (str, optional, default="DAK"): Z-factor method for viscosity calculation.
          Options: "DAK", "HY", "WYW", "BUR". DAK recommended.
    
        **Viscosity Behavior:**
        - Increases with pressure (gas molecules closer together)
        - Increases with temperature (molecular motion increases)
        - Typical range: 0.01-0.05 cP at reservoir conditions
        - At standard conditions: ~0.01 cP
    
        **Lee-Gonzalez-Eakin Correlation:**
        Uses Z-factor internally to account for real gas behavior. More accurate than
        ideal gas assumptions, especially at high pressures.
    
        **Returns:**
        Dictionary with:
        - **value** (float or list): Viscosity in cP (matches input p shape)
        - **method** (str): "Lee-Gonzalez-Eakin"
        - **units** (str): "cP"
        - **inputs** (dict): Echo of input parameters
    
        **Common Mistakes:**
        - Using separator temperature instead of reservoir temperature
        - Pressure in barg/psig instead of psia (must be absolute)
        - Not accounting for non-hydrocarbon fractions
        - Confusing gas viscosity (increases with P) with oil viscosity (decreases with P)
        - Temperature in Celsius instead of Fahrenheit
    
        **Example Usage:**
        ```python
        {
            "sg": 0.7,
            "degf": 180.0,
            "p": [1000, 2000, 3000, 4000],
            "h2s": 0.0,
            "co2": 0.05,
            "n2": 0.01,
            "zmethod": "DAK"
        }
        ```
        Result: Viscosity increases from ~0.012 cP at 1000 psia to ~0.025 cP at 4000 psia.
    
        **Note:** Gas viscosity is much lower than oil viscosity (typically 0.01-0.05 cP
        vs 0.5-10 cP). Always use reservoir conditions, not separator conditions.
        Account for all non-hydrocarbon components for accuracy.
        """
        method_enum = getattr(z_method, request.zmethod)
    
        ug = gas.gas_ug(
            sg=request.sg,
            degf=request.degf,
            p=request.p,
            h2s=request.h2s,
            co2=request.co2,
            n2=request.n2,
            zmethod=method_enum,
        )
    
        # Convert numpy array to list for JSON serialization
        if isinstance(ug, np.ndarray):
            value = ug.tolist()
        else:
            value = float(ug)
    
        return {
            "value": value,
            "method": "Lee-Gonzalez-Eakin",
            "units": "cP",
            "inputs": request.model_dump(),
        }
  • Pydantic model defining the input schema for gas_viscosity tool, including validation for fields like sg, degf, p (scalar or list), non-hydrocarbon fractions, and zmethod.
    class GasViscosityRequest(BaseModel):
        """Request model for gas viscosity calculation."""
    
        sg: float = Field(
            ..., ge=0.5, le=2.0, description="Gas specific gravity (air=1, dimensionless)"
        )
        degf: float = Field(
            ..., gt=-460, lt=1000, description="Temperature (degrees Fahrenheit)"
        )
        p: Union[float, List[float]] = Field(
            ..., description="Pressure (psia) - scalar or array"
        )
        h2s: float = Field(
            0.0, ge=0.0, le=1.0, description="H2S mole fraction (dimensionless)"
        )
        co2: float = Field(
            0.0, ge=0.0, le=1.0, description="CO2 mole fraction (dimensionless)"
        )
        n2: float = Field(
            0.0, ge=0.0, le=1.0, description="N2 mole fraction (dimensionless)"
        )
        zmethod: Literal["DAK", "HY", "WYW", "BUR"] = Field(
            "DAK", description="Z-factor calculation method"
        )
    
        @field_validator("p")
        @classmethod
        def validate_pressure(cls, v):
            """Validate pressure values."""
            if isinstance(v, list):
                if not all(p > 0 for p in v):
                    raise ValueError("All pressure values must be positive")
            else:
                if v <= 0:
                    raise ValueError("Pressure must be positive")
            return v
  • Imports and calls register_gas_tools(mcp), which defines and registers the gas_viscosity tool (among others) using @mcp.tool() decorator.
    from .tools.gas_tools import register_gas_tools
    from .tools.inflow_tools import register_inflow_tools
    from .tools.simtools_tools import register_simtools_tools
    from .tools.brine_tools import register_brine_tools
    from .tools.layer_tools import register_layer_tools
    from .tools.library_tools import register_library_tools
    
    register_oil_tools(mcp)
    register_gas_tools(mcp)

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