# Result Table - Knock Out Pot

The available results that are listed in the table vary depending upon the fluid phase state and upon the visible properties that you have selected. Figure 1 shows all of the available results for a liquid phase state. Figure 2 shows the normal or default rows. You can choose the rows you wish to display in the results table via the Set Visible Results Dialog. Figure 1: Available results for a Knock-Out Pot. Only descriptions for the default results are shown in this section. If you wish to see the definition for other values click here. -- ID -- (aka User Number): All flowsheet elements have a unique number that is assigned by FluidFlow. It is not possible for the user to change this number because it is used as a unique identifier by the scripting module. Node numbering starts from 1, incrementing upwards, and pipe numbering starts from -1, decrementing downwards. Composition Mass %: This is the fluid mass composition. FluidFlow determines the composition of the fluid at a knock-out pot, based on a component mass balance. Density: The fluid density at the knock-out pot. Density depends on temperature and pressure of the fluid. Stagnation Pressure: The average stagnation pressure at the knock-out pot. This is the sum of kinetic and pressure energies (static pressure + velocity pressure). Temperature: This is the stagnation temperature at the knock-out pot. The stagnation temperature is the temperature that the fluid would reach if it were brought to rest isentropically, converting its kinetic energy to enthalpy. Viscosity: The fluid dynamic viscosity at the knock-out pot. Viscosity is a measure of the resistance of the fluid to deformation. For Non-Newtonian fluids viscosity depends on shear rate as well as fluid temperature and pressure.