Name | Fluid_State_Pty_Set |
---|---|
Entity Type | Table |
Description | The fluid properties recorded during a particular fluid analysis that are dependent on the pressure and the temperature state of the fluid. |
Submodel | Fluid_Analysis |
Entity Scope | Project |
Primary Key | Id |
Natural Key | Fluid_Sample_Id , Material_Type , Pressure , Temperature , Fluid_State_Code , Fluid_Analysis_Id , Fluid_Analysis_Stage_Id , Existence_Kind , Version |
Generalizations | IT_Object , Tracked_Object |
Specializations |
Name | Value Domain | Property / Storage Unit | Description | Required / Default | Type |
---|---|---|---|---|---|
API_Oil_Gravity | double | API_Oil_Gravity dAPI |
API gravity of Oil. The measure of the density of liquid petroleum products; derived from relative density in accordance with the following equation: API Gravity at 60 degrees F = [141.5 /relative density at 60 degrees F] - 131.5. API Gravity is expressed in degrees API, 10 degrees API being equivalent to 1.0, the relative density of water." | No |
NUMBER |
Boiling_Point_Pressure | double | Pressure kPa |
The pressure at which the material starts to boil. | No |
NUMBER |
Boiling_Point_Temperature | double | Temperature degC |
The temperature at which the material starts to boil. | No |
NUMBER |
Bubble_Point_Pressure | double | Pressure kPa |
The observed pressure when the material starts to bubble. | No |
NUMBER |
Bubble_Point_Temperature | double | Temperature degC |
The temperature at which the material starts to bubble. | No |
NUMBER |
CTE_Final_Temperature | double | Temperature degC |
The final temperature of the sample when calculating the coefficient of thermal expansion. | No |
NUMBER |
CTE_Initial_Temperature | double | Temperature degC |
The initial temperature of the sample when calculating the coefficient of thermal expansion. | No |
NUMBER |
Compressibility | double | Compressibility 1E-6 1/Pa |
Indicates the change in bulk volume as a function of change in confinement pressure for the material. | No |
NUMBER |
Corrected_GCR | double | Gas_To_Liquid_Ratio m3/m3 |
The corrected gas condensate ratio for the sample. | No |
NUMBER |
Cricondentherm | double | Temperature degC |
The maximum temperature at which a liquid phase can exist in a multi-phase fluid system. | No |
NUMBER |
Cumulative_Specific_Gravity | double | Dimensionless |
The specific gravity of the gas that has been liberated since the start of the analysis. | No |
NUMBER |
Dead_Oil_Gravity | double | API_Oil_Gravity dAPI |
The API gravity of the oil at sufficiently low pressure that it contains no dissolved gas or a relatively thick oil or residue that has lost its volatile components. | No |
NUMBER |
Density | double | Density g/cm3 |
The density of the sample. | No |
NUMBER |
Dew_Point_Pressure | double | Pressure kPa |
The pressure of the sample when the dew point was measured. | No |
NUMBER |
Dew_Point_Temperature | double | Temperature degC |
The temperature of the sample when the dew point was measured. | No |
NUMBER |
Dissolved_Gas_Volume | double | Volume m3 |
The amount of gas that is dissolved in the sample. | No |
NUMBER |
Dissolved_Solid_Volume | double | Volume m3 |
The amount of solid material that is dissolved in the sample. | No |
NUMBER |
Electric_Conductivity | double | Conductivity mS/m |
A measure of the electric conductivity of the sample (1/resistivity). | No |
NUMBER |
Electric_Resistivity | double | Resistivity ohm.m |
A measure of the electric resistivity of the sample. | No |
NUMBER |
Equilibrium_Ratio | double | Dimensionless |
The equilibrium vaporization ratio: ratio of the mole fraction of a fluid system component in the vapor phase divided by the mole fraction of the same component in the liquid phase. [Finder] | No |
NUMBER |
Existence_Kind | REF_EXISTENCE_KIND | NA |
A reference value that describes the state of existence in the lifecycle of the entity, for example, Planned, Predicted, Required, Simulated, and Actual. | Yes Actual |
VARCHAR2(64) |
Fluid_Analysis_Id | Fluid_Analysis |
|
The identifier of the fluid analysis activity that resulted in these fluid "state" properties being recorded. | No |
NUMBER(38) |
Fluid_Analysis_Stage_Id | Fluid_Analysis_Stage |
|
The identifier of the fluid analysis stage that resulted in these fluid "state" properties being recorded. | No |
NUMBER(38) |
Fluid_Color | CODE | NA |
The color of the fluid. | No |
VARCHAR2(64) |
Fluid_Sample_Id | Fluid_Sample |
|
The identifier of the fluid sample described by this set of fluid properties. | Yes |
NUMBER(38) |
Fluid_State_Code | R_Fluid_State |
|
A value that describes the temperature and pressure conditions associated with the fluid analysis measurements. (i.e. Standard, Dew point, Reservoir). | Yes |
VARCHAR2(64) |
Formation_Volume_Factor | double | Liquid_To_Liquid_Ratio m3/m3 |
The ratio of the volume of fluid under reservoir conditions compared with the volume under standard temperature and pressure conditions. | No |
NUMBER |
GCR | double | Gas_To_Liquid_Ratio m3/m3 |
The ratio of gas volume to condensate volume. | No |
NUMBER |
GOR | double | Gas_To_Liquid_Ratio m3/m3 |
The Gas to Oil Ratio. | No |
NUMBER |
GUID | STRING128 | NA |
Globally Unique IDentifier for an instance of a class. USAGE NOTES: There are two cases: 1) GUID is not populated or used; and 2) it is populated with a value that is globally unique. If the GUID is populated there are two means of doing so for a given project: 2a) Seabed automatically generates and populates the GUID when an instance is created (valid only on Oracle based systems); and 2b) the GUID is generated and populated by an application (other than Seabed) on instance creation. Whether Seabed automatically generates GUIDs for a project is determined by the Auto_GUID flag in SDS_Account. Note that techniques 2a and 2b can coexist in the same project. When GUIDs are automatically generated an application can override the automatically generated GUID with its own GUID by simply supplying the GUID value. Applications that generate their own GUIDs and populate the GUID column will function correctly on projects which have automatic GUID generation turned on. | No |
VARCHAR2(128) |
Gas_Expansion_Factor | double | Dimensionless |
Y Factor. The factor that accounts for the change in gas density due to pressure changes, as across an orifice. This factor is the ratio of the upstream density divided by the downstream density. | No |
NUMBER |
Gravity_Temperature | double | Temperature degC |
The temperature at which the specific gravity of the sample was measured. | No |
NUMBER |
Heat_Capacity | double | Specific_Heat_Capacity J/(kg.K) |
The amount of heat required to change the temperature by one degree. | No |
NUMBER |
Id | ID | No_Unit |
Unique identifier for this entity. | Yes |
NUMBER(38) |
Insert_Date | DATE | NA |
Date the entity was created in the repository | No |
DATE |
Insert_User | STRING64 | NA |
The name of the user responsible for the creation of this entity in the repository. | No |
VARCHAR2(64) |
Kinematic_Viscosity | double | Flowrate_Per_Length m3/(h.m) |
The dynamic viscosity of the fluid divided by the density of the fluid. | No |
NUMBER |
Material_Type | R_Production_Material |
|
A value that describes the material whose state properties are being measured. | No |
VARCHAR2(64) |
PVT_Correlation_Name | STRING64 | NA |
The name of the PVT correlation used. Examples are Peng Robinson or SRK or Standing and Lasseter. This is only valid if the properties in this table are calculated rather than measured. | No |
VARCHAR2(64) |
Plastic_Viscosity | double | Dynamic_Viscosity cP |
The tangential shearing force (in excess of the yield point value) required to induce a unit rate of shear in the material. It assumes that the material obeys the Bingham law of plastic flow. A newtonian fluid has a yield point value of zero. if a Fann viscometer is used then this could be quoted, in units of centipoise (cP), as the 600 rpm reading - 300 rpm reading. | No |
NUMBER |
Pressure | double | Pressure kPa |
The pressure of the fluid sample whose properties are being analyzed. | No |
NUMBER |
Produced_By | STRING64 | NA |
The name of application role that created the entity, for data created programmatically. | No |
VARCHAR2(64) |
Relative_Density | double | No_Unit |
The ratio of the density of the fluid sample to the density of the standard fluid. For liquids water is considered the standard fluid. | No |
NUMBER |
Remarks | REMARKS_STR | NA |
A general description or remark of the state dependent properties of a fluid analysis. | No |
VARCHAR2(999) |
Residue_Density | double | Density g/cm3 |
The density of the residue sample. | No |
NUMBER |
Resistivity_Temperature | double | Temperature degC |
The temperature at which the resistivity of the sample was measured. | No |
NUMBER |
Retrograde_Volume | double | Volume m3 |
The volume of the condensed fluid that remains in the reservoir. Used for Retrograde Condensation. It is expressed as a percentage of the hydrocarbon pore space. | No |
NUMBER |
Retrograde_Volume_Factor | double | Dimensionless |
The ratio of the volume of the retrograde fluid under reservoir conditions compared with the volume under standard temperature and pressure conditions. | No |
NUMBER |
SDAT_Label | int | No_Unit |
Label used by the security system for entitlements. SDAT is Secure Data Access Technology. | No |
NUMBER(10) |
Saturation_Pressure | double | Pressure kPa |
The pressure for a corresponding saturation temperature at which the sample boils into its vapor phase | No |
NUMBER |
Shrinkage_Factor | double | Dimensionless |
The ratio of the volume of fluid under standard temperature and pressure conditions compared with the volume under reservoir conditions. The reciprocal of formation volume factor. | No |
NUMBER |
Solubility | double | Dimensionless |
The relative amount of a solid substance which will dissolve into aqueous ions at their standard states of unit molality. This is based on the Gibbs free energy of formation of the solid and aqueous ionic forms of the chemical compound. [Finder] | No |
NUMBER |
Solubility_GOR | double | Gas_To_Liquid_Ratio m3/m3 |
The solubility of gas in oil. | No |
NUMBER |
Specific_Gravity | double | Dimensionless |
The ratio of the weight of a given volume of the material at a given temperature to the weight of an equal volume of a standard substance at the same temperature. In determining the specific gravity of gases, the comparison is made with the standard of air or hydrogen. | No |
NUMBER |
Specific_Heat_Mass | double | Specific_Heat_Capacity J/(kg.K) |
The quantity of heat needed to raise the temperature of a unit mass of the substance by one degree Celsius. | No |
NUMBER |
Specific_Heat_Mole | double | Molar_Heat_Capacity J/(mol.K) |
The quantity of heat needed to raise the temperature of one mole of the substance by one degree Celsius. | No |
NUMBER |
Specific_Heat_Volume | double | Volumetric_Heat_Capacity kg/(K.m.s2) |
The quantity of heat needed to raise the temperature of unit of volume of the substance by one degree Celsius. | No |
NUMBER |
Steam_Quality | double | Dimensionless |
The mass fraction of water in the vapor phase with respect to the total mass of water in both the vapor and liquid phases. | No |
NUMBER |
Surface_Tension | double | Force_Per_Length N/m |
The amount of energy that is stored at the surface of the sample | No |
NUMBER |
Suspended_Solid_Conc | double | Mass_Per_Volume kg/m3 |
The amount of solid suspended in the sample. | No |
NUMBER |
Temperature | double | Temperature degC |
The temperature of the fluid sample whose properties are being analyzed. | No |
NUMBER |
Thermal_Conductivity | double | Thermal_Conductivity W/(m.K) |
The heat flux or thermal energy per unit length and temperature. The capacity of the material to conduct or pass thermal energy. | No |
NUMBER |
Thermal_Diffusivity | double | Thermal_Diffusivity cm2/s |
The rate at which heat is conducted through a material. It is a measure of transient heat flow and is defined as the thermal conductivity divided by the product of specific heat times density. | No |
NUMBER |
Update_Date | DATE | NA |
Date of the most-recent modification to the entity. | No |
DATE |
Update_User | STRING64 | NA |
The name of the user responsible for the last modification to this entity. | No |
VARCHAR2(64) |
Vapor_Pressure | double | Pressure kPa |
The pressure of the vapor over a liquid at equilibrium. | No |
NUMBER |
Version | STRING255 | NA |
The form or variant of the entity. | Yes 1 |
VARCHAR2(255) |
Viscosity | double | Dynamic_Viscosity cP |
A measure of the resistance of the sample to flow. | No |
NUMBER |
Viscosity_100F | double | Dynamic_Viscosity cP |
The viscosity of the sample when the temperature is 100 degrees Fahrenheit. | No |
NUMBER |
Viscosity_120F | double | Dynamic_Viscosity cP |
The viscosity of the sample when the temperature is 120 degrees Fahrenheit. | No |
NUMBER |
Volumetric_Therm_Expansion | double | Dimensionless |
The relative change in volume of the material due to a change in the temperature under isobaric conditions. | No |
NUMBER |
Yield_Stress | double | Shear_Stress Pa |
Resistance to initial flow; the stress required to start fluid movement. Specifically, shear stress at 0 shear rate for Bingham Plastic (BP) theological model, otherwise named Bingham yield value or yield point. | No |
NUMBER |
Z_Factor | double | Dimensionless |
Gas deviation factor. The ratio of the actual volume of a gas from at specific temperature/pressure to the volume of the gas calculated by the ideal gas law. It is defined by the real (non-ideal) gas equation of state, pV = znRT. | No |
NUMBER |
pH | double | Dimensionless |
Indicates the degree of acidity of the material. A value of 7 denotes a neutral fluid, lower values correspond to acidic fluids and higher values to basic fluids | No |
NUMBER |
pH_Temperature | double | Temperature degC |
The temperature at which the pH of the sample was measured. | No |
NUMBER |
From Entity | Link | Description | Implementation Technique | Required |
---|---|---|---|---|
Gas_Fluid_Analysis_DOV | Fluid_State_Pty_Set | READ ONLY: Unique identifier for the Fluid State Property Set. | Cascade | No |
Oil_Fluid_Analysis_DOV | Fluid_State_Pty_Set | READ ONLY: Unique identifier for the Fluid State Property Set. | Cascade | No |
Production_Test_DOV | Fluid_State_Pty_Set | READ ONLY: Unique identifier for the fluid property set. | Cascade | No |
Link | To Entity | Description | Implementation Technique | Required |
---|---|---|---|---|
Fluid_Sample | Fluid_Sample | The identifier of the fluid sample described by this set of fluid properties. | Cascade | Yes |
Fluid_State_Code | R_Fluid_State | A value that describes the temperature and pressure conditions associated with the fluid analysis measurements. (i.e. Standard, Dew point, Reservoir). | Restrict | Yes |
Fluid_Analysis_Stage | Fluid_Analysis_Stage | The identifier of the fluid analysis stage that resulted in these fluid "state" properties being recorded. | Cascade | No |
Fluid_Analysis | Fluid_Analysis | The identifier of the fluid analysis activity that resulted in these fluid "state" properties being recorded. | Cascade | No |
Material_Type | R_Production_Material | A value that describes the material whose state properties are being measured. | Restrict | No |