IP Library › Granted Patent US 11,365,886
Granted Patent B2
US 11,365,886 · App. 16/011,600 · Granted Jun 21, 2022

Remote monitoring of fired heaters

Inventors: Theodore Peter Faiella (Evanston, IL); Raul A. Ohaco (Glenview, IL); Colin J. Deller (Tulsa, OK)
Assignee: UOP LLC
F24B1/1886F23D91/04F23N1/022F24B1/1808F24B1/195F24C3/122F23N2223/08F23N2225/00F23N2237/00
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Quick Facts
Patent No.
US 11,365,886
App. No.
16/011,600
Granted
Jun 21, 2022
Kind
B2
Abstract

A chemical plant may include one or more fired heaters for heating of process streams. A fired heater may include a direct-fired heat exchanger that uses the hot gases of combustion to raise the temperature of a process fluid feed flowing through tubes positioned within the heater. Fired heaters may deliver feed at a predetermined temperature to the next stage of the reaction process or perform reactions such as thermal cracking. Systems and methods are disclosed to optimize the performance of fired heaters or reduce energy consumption of fired heaters.

Claims (22)

1. Non-transitory computer-readable media storing executable instructions that, when executed by one or more processors, cause a system to:

receive sensor data comprising operating information for a fired heater unit of a plant at a first operating condition representing a current operating condition for an element of the fired heater unit;

receive sensor data comprising operating information for the fired heater unit of the plant at a second operating condition, the second operating condition determined using a predictive model, wherein the predictive model determines a relationship between energy consumption and operating parameters of the plant comprising fuel gas flow, fuel composition, excess air flow, and emissions of the plant;

analyze the sensor data comprising the operating information to determine at least a one of the operating parameters of the plant comprising the fuel gas flow input information for the plant, the excess air information for the plant, and the emissions information four the plant;

determine an adjustment to an operating parameter of the plant at the second operating condition which has a lower energy consumption compared with the first operating condition, wherein the determining is based on one or more of: the fuel input information for the plant, the air information for the plant, and the emissions information for the plant, and wherein the determining is performed with an iterative method based on the predictive model to determine the minimal energy consumption by adjusting the fuel flow and the air flow subject to emissions, pressure drop in the fired heater unit, process temperature and fired heater tube wall temperature constraints; and,

transmit a command configured to cause the adjustment to the operating parameter of the plant.

2. The non-transitory computer-readable media of claim 1 , wherein the executable instructions, when executed, cause the system to:

use one or more design parameter of the plant to determine a status of the fired heater unit of the plant, wherein the one or more design parameters comprise an operating condition at which the fired heater was designed to operate at, below, or above.

3. The non-transitory computer-readable media of claim 1 , wherein the executable instructions, when executed, cause the system to:

check a raw value of the sensor data to determine whether the raw value of the sensor data comprises a bad value; and

based on determining that the raw value of the sensor data comprises the bad value, replace the raw value of the sensor data comprising the bad value with null data.

4. The non-transitory computer-readable media of claim 1 , wherein the executable instructions, when executed, cause the system to:

receive information about one or more of: a gas concentration level of the plant, an emissions level of the plant, a temperature of the plant, a pressure of the plant, an efficiency of the plant, or a production level of the plant; and,

provide, via a dashboard, the received information about the one or more of a gas concentration level of the plant, an emissions level of the plant, a temperature of the plant, a pressure of the plant, an efficiency of the plant, or a production level of the plant.

5. The non-transitory computer-readable media of claim 1 , wherein the executable instructions, when executed, cause the system to:

determine an optimum level at which the fired heater unit should be operated to achieve an optimization goal; and

provide, via a dashboard, information regarding the optimum level at which the fired heater unit should be operated to achieve the optimization goal.

6. The non-transitory computer-readable media of claim 5 , wherein the executable instructions, when executed, cause the system to:

use one or more operational characteristics of the fired heater unit or design characteristics of the fired heater unit to determine the optimum level at which the fired heater unit should be operated to achieve the optimization goal.

7. The non-transitory computer-readable media of claim 6 , wherein the executable instructions, when executed, cause the system to:

receive information about an O 2 concentration in a stack of the fired heater unit of the plant; and,

display, via the dashboard, a graph of the O 2 concentration in the stack of the fired heater unit of the plant.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 24, 2019
From: FAIELLA, THEODORE PETER; OHACO, RAUL A.; DELLER, COLIN J.
To: UOP LLC
Reel/Frame 050814/0021 →
Continuity (2)
Provisional Application 62521967 · Jun 19, 2017
Related Publication 20180363914A1 · Dec 20, 2018
Cited By (1)
US 12,462,901