Flare Monitoring and Control Method and Apparatus

Patent metadata

Field	Value
Publication number	US-2019242575-A1
Application number	US-201916262445-A
Country	US
Kind code	A1
Filing date	Jan 30, 2019
Priority date	Feb 5, 2018
Publication date	Aug 8, 2019
Grant date	—

Abstract

Disclosed herein are embodiments of a flare control method and a flare apparatus for automatically controlling, in real-time, the flow of one or more of fuel, steam, and air to a flare. The disclosed embodiments advantageously allow for automated control over a wide spectrum of operating conditions, including emergency operations, and planned operations such as startup and shutdown.

First claim

What is claimed is:

1 . A method comprising:
measuring a concentration of at least one hydrocarbon of a vent gas in a vent gas stream upstream of a combustion zone of a flare; feeding the vent gas in the vent gas stream to the flare; and controlling, in real-time based at least in part on the concentration of the at least one hydrocarbon, a flow of steam or air to the flare.

2 . The method of claim 1 , wherein the flow of steam to the flare is controlled, wherein the step of controlling a flow of steam to the flare comprises:
calculating a molecular weight of the vent gas in the vent gas stream using the concentration of the at least one hydrocarbon and a molecular weight of the at least one hydrocarbon; measuring a velocity of the vent gas in the vent gas stream; calculating a mass flow rate of the vent gas in the vent gas stream using the measured vent gas velocity, a molar volume of 385.3 SCF/LB-MOL, and the calculated molecular weight; determine a current flow rate of steam to the flare; calculating a total steam:vent gas mass ratio for smokeless operation of the flare using the concentration of the at least one hydrocarbon in the vent gas stream multiplied by a standard steam:hydrocarbon ratio required for smokeless operation of the flare for the at least one hydrocarbon; calculating a required steam flow rate for the flow of steam to the flare using the total steam:vent gas mass ratio and the vent gas mass flow rate; and adjusting the flow of steam to the flare to the required steam flow rate.

3 . The method of claim 1 , wherein the flow of air to the flare is controlled, wherein the step of controlling a flow of air to the flare comprises:
calculating a molecular weight of the vent gas in the vent gas stream using the concentration of the at least one hydrocarbon and a molecular weight of the at least one hydrocarbon; measuring a velocity of the vent gas in the vent gas stream; calculating a volumetric flow rate of the vent gas in the vent gas stream using the calculated velocity; calculating a total air:vent gas mole ratio for smokeless operation of the flare using the concentration of the at least one hydrocarbon in the vent gas stream multiplied by a standard air:hydrocarbon ratio required for smokeless operation of the flare for the at least one hydrocarbon; calculating a required air flow rate for the flow of air to the flare by multiplying the total air:vent gas mole ratio by the volumetric flow rate of the vent gas in the vent gas stream; and adjusting a flow of air to the flare to the required air flow rate.

4 . The method of claim 1 , further comprising:
controlling, in real-time based at least in part on the concentration of the at least one hydrocarbon, a flow of natural gas or fuel gas into the vent gas stream.

5 . The method of claim 4 , wherein controlling a flow of natural gas or fuel gas comprises:
calculating a net heating value of the vent gas in the vent gas stream using the concentration of the at least one hydrocarbon and a net heating value for the at least one hydrocarbon; calculating a first flow rate for the natural gas or fuel gas that is required to change the net heating value of the vent gas in the vent gas stream to meet a first setpoint value, wherein the first setpoint value is optionally defined as equal to or greater than a minimum net heating value for a vent gas specified by regulation; calculating a net heating value in a combustion zone of the flare using the flow rate of the vent gas in the vent gas stream, a flow rate of steam to the flare, and the net heating value for the vent gas; calculating a second flow rate for the natural gas or fuel gas that is required to change the net heating value in the combustion zone to meet a second setpoint value, wherein the second setpoint value is optionally defined as equal to or greater than a minimum net heating value for a combustion zone specified by regulation; determining and selecting which one of the net heating value of the vent gas in the vent gas stream and the net heating value in the combustion zone is a selected net heating value that requires more natural gas or fuel gas to meet the respective setpoint value (or alternatively stated, determining which one of the first flow rate and the second flow rate is greater, and identifying the greater one as a selected flow rate); and adjusting a flow of the natural gas or fuel gas to the selected flow rate.

6 . The method of claim 4 , wherein controlling a flow of natural gas or fuel gas comprises:
calculating a net heating value of the vent gas in the vent gas stream using the concentration of the at least one hydrocarbon and a net heating value for the at least one hydrocarbon; calculating a first flow rate for the natural gas or fuel gas that is required to change the net heating value of the vent gas in the vent gas stream to meet a first setpoint value, wherein the first setpoint value is optionally defined as equal to or greater than a minimum net heating value for a vent gas specified by regulation; calculating a net heating value dilution parameter in a combustion zone of the flare using the flow rate of the vent gas in the vent gas stream, a flow rate of air to the flare, the net heating value for the vent gas, and a diameter of a tip of the flare; calculating a second flow rate for the natural gas or fuel gas that is required to change the net heating value dilution parameter of the combustion zone to meet a second setpoint value, wherein the second setpoint value is optionally defined as equal to or greater than a minimum net heating value dilution parameter for a combustion zone specified by regulation; determining and selecting which one of the net heating value of the vent gas in the vent gas stream and the net heating value dilution parameter for the combustion zone is a selected net heating value that requires more natural gas or fuel gas to meet the respective setpoint value (or alternatively stated, determining which one of the first flow rate and the second flow rate is greater, and identifying the greater one as a selected flow rate); and adjusting the flow of the natural gas or fuel gas to the selected flow rate.

7 . The method of claim 4 , wherein controlling a flow of natural gas or fuel gas comprises:
calculating a first net heating value of the vent gas in the vent gas stream using the concentration of the at least one hydrocarbon that is received from a first gas analyzer and a net heating value for the at least one hydrocarbon; calculating a second net heating value of the vent gas in the vent gas stream using the concentration of the at least one hydrocarbon that is received from a second gas analyzer and a net heating value for the at least one hydrocarbon; multiplying the first net heating value of the vent gas by a ratio of the second net heating value of the vent gas to the first net heating value of the vent gas to obtain a reconciled net heating value of the vent gas; calculating a first flow rate for the natural gas or fuel gas that is required to change the reconciled net heating value of the vent gas in the vent gas stream to meet a first setpoint value, wherein the first setpoint value is optionally defined as equal to or greater than a minimum net heating value for a vent gas specified by regulation; calculating a first net heating value dilution parameter in a combustion zone of the flare using the flow rate of the vent gas in the vent gas stream, a flow rate of steam to the flare, and the first net heating value for the vent gas calculated using the concentration of the at least one hydrocarbon that is received from the first gas analyzer; calculating a second net heating value dilution parameter in the combustion zone of the flare using the f

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Fisher Charles F
• Green Lee N
• Hendrickson Gregory G
• Lessard Thomas A
• Moore Kenneth B
• Peneguy Daniel W

Classifications

• F23K2900/05004

  Mixing two or more fluid fuels · CPC title

• F23G7/085 Primary

  in stacks · CPC title

• F23G2207/10

  Arrangement of sensing devices · CPC title

• F23G2207/112

  for waste supply flowrate · CPC title

• F23G2900/55011

  Detecting the properties of waste to be incinerated, e.g. heating value, density · CPC title