BurnerManagementSystems Pres
BurnerManagementSystems Pres
BurnerManagementSystems Pres
Introduction
Safety controls on direct-fired heaters have New legislation has been introduced to
1. Introduction
continuously evolved over the recent past, and standardise the requirements. In most
the evolution has accelerated over the last five provinces of Canada the code is CSA
2. Background years. This has been due to the introduction of B149.3, which is an adaptation of NFPA,
government legislation which actively enforces however this is currently legislated as a
~ Mandatory the application of existing codes. minimum requirement.
Purging Most operating companies within North
Heater designs and quality standards have
America are implementing BMS in new and
followed the practice of API 560. For most
existing heaters in accordance with required
~ Permissives operating companies this is now mandatory and
guidelines; however there are some
& Interlocks used as a minimum standard with individual
installations that still rely only on manual
companies adding their own requirements. With
operator intervention or the plant
Safety Controls or Burner Management
~ Safety Shut- Emergency Shutdown (ESD) as the safety
Systems, this evolution has not occurred.
off Valves control. The most common reason
provided by these companies is that they
Although some detailed and prescriptive
have operated with the manual system and
~ Pilots & guidelines have been around for many years, the
absence of flame monitoring equipment for
Ignition rate and degree of adoption varies significantly
years without incident; why should an
within the industry. Most operating companies
Systems have their own standard, which may still vary
investment be made in a BMS now?
from facility to facility. In addition to this, for The general consensus is becoming to
~ Dedicated each installation, it is not unusual for adjacent standardise the requirements of a safe and
Flame heaters built two years apart to have a different operable BMS for each heater, to ensure a
Monitoring BMS design, simply because different safe light off and normal operation while
engineering contractors built them. With reducing the amount of nuisance trips. But
Systems increasing government legislation and we all must bear in mind that the safety of
regulations as well as mounting lawsuits for personnel and environment is of the utmost
~ Alarms & accidents in which applicable codes and importance; as such a proactive approach
Shutdowns guidelines have not been adhered to, it is must be taken.
important to review the BMS requirements for
both existing and new heater installations.
~ Combustion
Draft /
Pressure
Alarms &
Controls
~ Dedicated
Logic Solver
Safety Controls and Burner Management Systems Page 2 of 12
(BMS) on Direct-Fired Multiple Burner Heaters
Background
In the past, most heaters have operated on temperature control from the outlet
temperature to a control valve in the main gas line, with a single shut-off valve upstream
on the Control valve. This shut-off valve was either automatic with the plant ESD or
operated manually with an Operator action, with each company having various additions
to this basic concept.
The following is a list of new requirements that are common to various heater and BMS
codes.
1) Mandatory Purging.
2) Permissive Interlocks
3) Double Block and Bleed systems
4) Pilots and Ignition Systems
5) Dedicated Flame Monitoring Systems
6) High / Low Pressure, Temperatures and Flow.
7) Combustion Air and Draft Pressure Alarms and Controls
8) Dedicated Logic Solver
Each of these requirements have been developed due to incidents that have occurred
because of the lack of them.
Mandatory Purging
The most important function of the heater control system is to A time to achieve the four volume changes may be
prevent the possibility of an accumulation of combustible gas calculated from the required flow rate. In the event the
followed by accidental or improper ignition sequence resulting in purge does not continue for the prescribed time or required
an explosion. Correct pre-ignition purging of the heater is crucial purge, permissives are no longer met and a re-purge is
to the safe operation of the heater. required. Only when a successful purge is completed can
any ignition source be introduced.
The normal practise for the purging of a natural draft heater has
been to allow a period of time for a heater to naturally purge. CSA B194.3-05 Section 9.2 Pre-purge
Typically this would have been 20-30 minutes on a cold light off, 9.2.1: When either an intermittent or interrupted
and would have been at the discretion of the operator. The pilot or a direct transformer spark ignitor is used to
alternative is to purge with steam, if available. Caution must be light the main burner and the combustion air supply
taken when doing so to prevent possible steam condensation from is by mechanical means, the appliance control
affecting the operation of the ignition and flame monitoring system shall provide a proven purge period prior to
instrumentation. the ignition cycle. This purge period shall provide
at least four air changes of the combustion zone
The timed purge is to be proven. The codes imply that there has to and flue passages at an airflow not less than 60% of
be a means to prove there has been four volumes changes or air in that required at maximum input.
the heater prior to light-off. It is not possible to measure the air
flowrate during a natural purge. Therefore the options available to NFPA 86 Section 5-4.1 Pre-ignition (Pre-purge, Purging
provide a proven purge are: Cycle)
a) Purge Blower or Fan 5-4.1.2: A timed pre-ignition purge shall be
b) Steam purge from radiant section provided. At least 4 standard cubic feet (scf) of
c) Induced Draft Purge (via Steam eductor in the Stack) fresh air or inert gas per cubic foot (4 m3/m3) of
heating chamber volume shall be introduced during
Furthermore, depending on the jurisdiction there may also be a the purge cycle.
minimum purge flow rate that must be adhered to.
Page 3 of 12 Safety Controls and Burner Management Systems Page 3 of 12
(BMS) on Direct-Fired Multiple Burner Heaters
The configuration discussed above works well for a single 5.3.5: An appliance that has a maximum rated input in excess
burner system but this cannot be applied to multiple burner of 10,000,000 Btu/h (3000 kW), up to an including
systems; unless they are all to operate in tandem. In order to 100,000,000 Btu/h (30 000 kW), with multiple burners that
keep the heater running in the event of a single burner failure have multiple burner flame safeguard controls shall be
the fuel gas must be isolated from the failed burner. Strict equipped with not less than two automatic safety shut-off
adherence to the codes and guidelines would require two valves per burner, certified in accordance with ANSI
separate safety shut-off valves piped in series for each burner. Z21.21/CSA 6.5 and marked C/I, one of which shall be in the
An exception is provided in NFPA that would allow for the common valve train and may be of the fast opening type.
shutdown of a single burner, provided that all burners fire into The downstream valve shall be provided with a mandatory
a common combustion chamber and certain conditions are manual-reset function to open.
met.
Safety Controls and Burner Management Systems Page 4 of 12
(BMS) on Direct-Fired Multiple Burner Heaters
5.3.9; An appliance that has a maximum rated input in excess 5-7.1.2: Each safety shut-off valve required in 5-7.2.1
of 10,000,000 Btu/h (3000 kW), up to and including and 5-7.3.1 shall automatically shut off the fuel to the
50,000,000 (15 000 kW), and a burner manifold pressure in burner system after interruption of the holding
excess of 0.5 psig (3.5 kPa) shall medium (such as electric current or fluid pressure) by
(a) have main burner shut-off valves supervised by an any one of the interlocking safety devices, combustion
approved valve proving system that prevents main burner safeguards, or operating controls.
automatic safety shut-off valves from opening when a leak is
detected; or NFPA 86 Section 5-7.2 Fuel Gas Safety Shut-off
(b) be equipped with and automatic vent valve that is Valves
(i) normally open and energized to close;
(ii) sized in accordance with Table 2;
(iii) installed in a vent line that is connected into the 5-7.2.1: Each main and pilot fuel gas burner system shall
burner valve train immediately downstream of the first be separately equipped with two safety shutoff valves
automatic safety shut-off valve in the main burner valve piped in series.
train; and
(iv) wired in parallel with the first automatic shut-off valve. 5-7.2.2: Where the main or fuel pilot gas burner system
There shall be no other valve or valves installed in the vent capacity exceeds 400,000 Btu/hr (117 kW), at least one of
line the safety valves required by 5-7.2.1 shall be proved
NFPA 86 Section 5-7 Safety Shut-off Valves (Fuel Gas or closed and interlocked with the pre-ignition purge
Oil) interval.
5-7.1.1: Safety shut-off valves shall be utilized as a key safety
control to protect against explosions and fires.
Some certified flame monitoring devices have an adjustable flame failure response time, typically from one to four seconds.
The Canadian code further requires that any flame monitor that can fail in the flame-proving mode be supplied with a
self-checking mechanism, which means the burner will remain on for longer than 24 hours. As the flame monitor is the most
critical instrument in detecting a loss of flame and initiates the isolation of the fuel gas it is recommended that a self-check
scanner be provided for all systems regardless of the firing cycle. Dependant on the size of the burner, it may only take
several seconds to accumulate an explosive mixture, which explains the need for such a device.
5-9.2: Each pilot and main burner flame shall be supervised independently.
Safety Controls and Burner Management Systems (BMS) Page 7 of 12
on Direct-Fired Multiple Burner Heaters
The alarms required for the fuel gas are common for all systems. These are high / low main fuel gas pressure, and high / low
pilot gas pressure. These are required to keep the operating pressure of the burners within the design parameters provided by
the burner manufactures. Operation outside of these limits will cause flame instability among other problems. If a forced draft
fan or blower is required to provide combustion air to the blowers, a low combustion air flow alarm and low low flow trip is to be
provided.
Other measurements and alarms should be provided in order to protect the heater itself from improper operation. A high stack
temperature will warn of possible leakage in the convection section, resulting in an uncontrolled fire, whereas a low alarm will
protect from possible acid gas condensation. A high-high stack temperature will cause a shutdown of the main burners.
Heater draft measurement and alarm will help ensure that the heater operates within the design draft profile. Operations
outside this range may cause flame instability and improper/incomplete combustion.
Dependant on the process fluid, heated low process flow alarms may be required. If the process fluid is susceptible to either
coking or degradation at temperatures above design, it is recommended that a low flow alarm be provided and a main burner
shutdown on loss of flow. Low process flow will also result in high tubeskin temperatures as not enough heat is being removed
from the tubes.
9.5.2: For appliances with inputs in excess of 400 000 Btu/h (120 kW), or with the design outlet pressure of the
appliance regulator being in excess of 0.5 psig (3.5 kPa), a low-pressure safety limit control device shall be installed
and shall initiate shut-off of the supply gas if the pressure at the point of connection drops below 50% of the lowest
normal operating pressure.
5-8.2: A high gas pressure switch shall be provide and shall be interlocked into the combustion safety circuitry. The
switch shall be located downstream of the final pressure-reducing regulator
5-8.3: Pressure switch settings shall be made in accordance with the operating limits of the burner system.
Safety Controls and Burner Management Systems Page 8 of 12
(BMS) on Direct-Fired Multiple Burner Heaters
Although this is normally not a shut-down device, it is closely linked to opening the stack damper blade. The pressure
control loop consists of a pressure transmitter located at the heater arch and an actuator on the stack damper. A low
draft pressure (high firebox pressure) alarm should be added to this transmitter. The control loop is to be configured
such that the stack damper opens when there is a low heater draft. In the event that the heater draft is still too low but
the stack damper is 100% open the burner firing rate must be reduced.
Operating philosophy
Burner Management
Systems
Power On Check Start
Permissives Purge
Continue Check
Permissives Complete
Burner Purge
Management
System
Hand
to DCS Ignite Pilot(s)
Prove
Confirm Pilots
Burner(s) Light
Burner(s)
The main function of the BMS is to allow and ensure the safe start-up, operation, and shutdown of the Fired Heater. Once the
logic is configured and the system properly commissioned the BMS will provide a safe and consistent operating sequence. The
human interface will guide the operator so that the heater may be safely operated, and if needed, be quickly and safely restarted.
Conclusion
There are a number of codes and guidelines pertaining to the safety control and burner management system for direct
fired heaters. The controlling code within Canada is CSA B149.3, but the most common guideline referred to around the
world is NFPA 86. Due to changing government legislation as well as safety and insurance concerns, there is an increase
in the necessity to upgrade or install the heater safety systems (BMS) to comply with published codes and guidelines.
These codes and guidelines are specific when in regards to the valve train and certain safety instrumentation. There is
little aid when incorporating the safety and operability aspects of the overall heater and BMS unit. Unlike boilers, there
are a variety of configurations and process fluids that a direct fired heater may be designed for. As such, there are many
safety interlock and operation permissives that must be reviewed on a case-by-case basis.
Adherence to the published codes and guidelines is a great start and will create a good foundation for the heaters safety
system. In order to design the system for maximum reliability and operability, each system should be reviewed
individually and the safety controls designed accordingly.