### Operational Decision Support with Online Models

### Abstract

A review of the wide-ranging ROMeo projects at Shell's Scotford site that moved offline production and safety systems online. Projects include fired heater vaporization, column relief load, column loading, preheat hydraulics, heater and exchanger cleaning, and advanced process control (APC) coordination. The motivation, implementation, benefits, and future work is discussed.

Presentation, AVEVA World Conference - North America, November 12, 2019

### Orifice Meter Flow Correction and Compensation

### Overview

Flow measurements using orifice meters are commonly configured to indicate mass flowrate. This calculation assumes that the fluid being measured is at the same conditions as the fluid used in the meter’s design. Flow correction and compensation factors can be applied to increase meter accuracy. If a meter is re-designed using revised fluid properties, a correction factor can be applied to historic mass flow measurements. If measurements of flowing conditions are available, a mass flow compensation factor can be applied.

This post describes the following,

- Calculation of mass flowrate of a vapour at design conditions
- Correction of vapour mass flowrates at revised design conditions
- Compensation of vapour mass flowrates to measured/flowing conditions
- Calculation of vapour standard volumetric flowrate from mass flowrate

### Background

Measurement of vapour mass flow through an orifice meter can be described by the following,

{F_M}={N}{C_d}{E_v}{Y}{d^2}\sqrt{\rho_{T,P}}\sqrt{\Delta{P}} (1)

where,

F_M is mass flowrate of gas

N is units conversion factor

C_d is discharge coefficient

E_v is velocity approach factor

Y is gas expansion factor

d is orifice bore size

\rho_{T,P} is gas density, flowing conditions

\Delta{P} is pressure drop across orifice

Orifice meters can be designed using Flowel® software (Emerson) using the Exact Flow Calculation mode at typical operating (i.e. design) conditions. Coefficients in (1) are considered to change little over the operating conditions of the meter and are considered constant. Equation (1) then becomes,

F_D = F_{max}\sqrt{\Delta{P}} (2)

where,

F_D is mass flowrate at design conditions

F_{max} is maximum mass flowrate (flow at full-scale pressure drop)

Equation (2) also assumes that fluid density is also at the design conditions. Compensation of F_D for deviations from design conditions to measured/flowing conditions is described below.

### Flow Correction for Meter Re-Design

Meter accuracy is increased when the meter design conditions are close to the actual operating conditions. When an orifice meter is re-designed using updated operating conditions it’s possible to apply the new design to historic flowrates. Since orifice meter design calculates F_{max}, it’s possible to calculate a meter range correction factor (RCF) as,

RCF=\frac{F_{max,2}}{F_{max,1}} (3)

where,

RCF is meter range correction factor

F_{max,1} is maximum mass flowrate (flow at full-scale pressure drop), previous design

F_{max,2} is maximum mass flowrate (flow at full-scale pressure drop), new design

From equation (1), the mass flowrate using the new meter design simply becomes,

{F_{D,2}}={(RCF)}{F_{D,1}} (4)

where,

F_{D,1} is mass flowrate at design conditions, previous design

F_{D,2} is mass flowrate at design conditions, new design

### Flow Compensation

Meters don’t operate at the conditions used in meter design. If suitable measurements are available a mass flowrate compensation factor (MCF) can be calculated to compensate for changes in measured/flowing density (i.e. fluids not at \rho_{T,P}, in equation (1) above) and improve meter accuracy. For orifice meters in vapour service configured to indicate mass flowrate, the compensation factor is,

MCF=\sqrt{\left[\frac{M_M}{M_D}\right]\left[\frac{P_M}{P_D}\right]\left[\frac{Z_D}{Z_M}\right]\left[\frac{T_D}{T_M}\right]} (5)

where,

M_M is molecular weight, measured/flowing conditions

M_D is molecular weight, design conditions

P_M is operating pressure (absolute), measured/flowing conditions

P_D is operating pressure (absolute), design conditions

T_M is operating temperature (absolute), measured/flowing conditions

T_D is operating temperature (absolute), design conditions

Z_M is ideal gas compressibility factor, measured/flowing conditions

Z_D is ideal gas compressibility factor, design conditions

The compensated vapour mass flowrate is therefore,

F_M=(MCF)F_D (6)

and, when a meter correction factor also needs to be applied,

F_M=\left(RCF\right)(MCF)F_D (7)

### Calculation of Standard Volumetric Flow

The standard volumetric flowrate can be calculated from corrected and compensated mass flowrate as,

V_M=F_M{v/M}_M (8)

where,

V_M is volumetric flowrate of gas, standard conditions

F_M is mass flowrate of gas

v is molar volume of gas, standard conditions

M_M is molecular weight of gas