Inflection Point Engineering IPE-TM-200 Heaters

Automatic Shutdown of Fired Heaters

IPE-TM-200-01

1. Purpose

This procedure provides the Inflection Point Engineering design requirements for automatic shutoff of fuel to fired process heaters.

2. General

Automatic fuel shutoff systems are required to safely shutdown a fired heater for malfunctions in the process flow through the heater tubes, fuel system or combustion air supply, or other abnormal process conditions. The following shutdown system design requirements are the minimum that Inflection Point Engineering considers necessary. Changes to the Inflection Point Engineering system design shall only be considered upon specific written instructions from the client.

These requirements are based on a quantitative risk analysis carried out by Inflection Point Engineering to insure our designs are compliant with the national and international standards regarding safety instrumented systems. This analysis included the determination of the required SIL (safety integrity level) for each automatic function and the typical hardware configuration recommended by Inflection Point Engineering to achieve the SIL.

Inflection Point Engineering does not specify automated vent or drain valves between the two shutoff valves in series on fired heater fuel systems. For fuel gas Inflection Point Engineering does show a manual vent valve to allow for depressuring the piping between the two valves during any maintenance that might be required. Automation of this vent valve is not recommended by Inflection Point Engineering as the potential hazards of this valve being opened during normal operation are significant.

3. Natural or Forced or Forced/Induced Draft Heaters

This section applies to all heaters. Table 1 summarizes the action to be taken for the anticipated malfunctions. The safety related instrumentation for each function needs to meet SIL 2, unless noted otherwise.

3.1 Safety Instrumented Functions (SIF)

The recommended transmitter configuration is 2 out of 3 voting for the low pressure detection.

Individual heater pass control valves shall have a mechanical limit stop to prevent the control valve from closing completely. An exception to this is feed control valves to reactor charge heaters. Another exception occurs for level control valves (or flow control valves with level cascaded to the flow controllers).

The recommended transmitter configuration is 2 out of 3 voting for the low flow detection. This measurement should include three separate heater passes when available. The voting system is intended for detection of loss of the pump or compressor. 1 out of X on all passes is not recommended by Inflection Point Engineering since this will lead to more spurious trips.

For dual feed source designs (e.g. Charge/Recycle Gas), simultaneous loss of both feed sources to the heater shall shutoff all fuels to the heater, except pilot gas.

For dual feed source designs, loss of one feed source (e.g. loss of recycle gas for Charge/Recycle Gas) to the heater shall shutoff all fuels to the heater, except pilot gas, when analysis shows that the flow from the remaining feed source will not prevent the tubes from overheating and/or coking.

Flow through a convection section waste heat recovery coil is NOT Primary Service. Low flow through the waste heat recovery coil shall shutdown the main fuel burners unless the heater specification explicitly states that this coil shall be designed for no flow condition.

A double block configuration shall be used for isolating the pilot gas on fired heaters. Each of the two block valves is actuated by two solenoid valves connected together such that the failure of one solenoid valve does not shut the block valve. The use of two shutdown valves allows the time period between valve testing to be extended while maintaining the required safety factor. The use of two solenoid valves decreases the spurious trip factor.

A double block configuration shall be used for isolating the fuel gas on fired heaters. Each of the two block valves is actuated by two solenoid valves connected together such that the failure of one solenoid valve does not shut the block valve. The use of two shutdown valves allows the time period between valve testing to be extended while maintaining the required safety factor. The use of two solenoid valves decreases the spurious trip factor.

A double block configuration shall be used for isolating the fuel oil supply on fired heaters. Each of the two block valves is actuated by two solenoid valves connected together such that the failure of one solenoid valve does not shut the block valve. The use of two shutdown valves allows the time period between valve testing to be extended while maintaining the required safety factor. The use of two solenoid valves decreases the spurious trip factor.

The recommended valve configuration is a single valve. This valve shares the solenoid valves from one of the supply shutdown valves. Only one valve is required since the return line from the heater has a check valve in it also.

A process vent line discharging into a fired heater shall have automatic shutoff valves actuated by the same signal(s) that shutdown the main fuel burners. Vent gas diversion to a safe location must usually be provided.

A double block configuration shall be used for isolating combustible vent gas flow to fired heater fireboxes. Each of the two block valves is actuated by two solenoid valves connected together such that the failure of one solenoid valve does not shut the block valve. The use of two shutdown valves allows the time period between valve testing to be extended while maintaining the required safety factor. The use of two solenoid valves decreases the spurious trip factor.

Note: If the vent gas is not combustible, then the process vent line shutdown is an interlock function (and not a safety instrumented function).

3.2 Interlock Functions

The features mentioned below were determined to be for equipment protection and therefore are not safety related.

A single transmitter configuration is used for the low pressure detection. An exception is the Oleflex reactor heaters which use 2 out of 3 to minimize spurious trips. This is due to the complexity of the Oleflex, risk to equipment such as reactor screens during a shutdown, and the time consuming operations required to restart the unit.

A single transmitter configuration is used for the low differential pressure detection.

Oleflex: low pressure of the fuel gas downstream of the control valve to any heater shall shutoff the fuel gas to all of the heaters.

Platforming: low pressure of the fuel gas downstream of the control valve to any heater (furnace cell) only shuts off the fuel gas to that heater. If the heater also has fuel oil, then the low fuel gas pressure trip signal shall also shutdown fuel oil to that heater. The Platforming process cannot tolerate radiant coil fouling. Loss of effective radiant process surface area could potentially result on loss of fuel gas firing and continued fuel oil firing because of the potential of creating coil metal dusting / and metal catalyzed coke formation under certain process conditions. To reduce this risk (of radiant coil fouling) fuel oil firing will be stopped in any heater (furnace cell) that has lost fuel gas firing capability. Low pressure of the fuel oil downstream of the control valve to any heater shall shutoff the fuel oil to that heater only. Fuel gas firing will continue. A differential temperature override control on each heater shall always be provided to prevent overheating downstream heaters, caused by fuel shutoff to one heater.

A process vent line discharging into a fired heater shall have automatic shutoff valves actuated by the same signal(s) that shutdown the main fuel burners. Vent gas diversion to a safe location must usually be provided.

The following interlocks are not Inflection Point Engineering standard practice, but some guidance is given as to implementation should they be requested by a customer.

3.3 Manual Shutdowns

3.4 Additional Design Detail Requirements

Follow the design detail requirements mentioned below exactly because they are an integral part of the risk analysis done by Inflection Point Engineering. Any deviation will impact the risk analysis resulting in re-work of the specified instrumentation. No detailed instructions or automated equipment are specified by Inflection Point Engineering for testing and bypassing of safety instrumented systems. These details are left to the contractor and owner to determine based on factors such as operating cycle length, local codes and sophistication of automation for testing.

3.5 Miscellaneous Information

4. Forced Draft Heaters or Forced/Induced Draft Heaters

Table 2 summarizes the action to be taken for anticipated malfunctions in the forced draft system. Table 2 shutdowns are provided in addition to those described in Table 1.

4.1 Safety Instrumented Functions

The recommended transmitter configuration is 2 out of 3 voting for the low pressure detection.

4.2 Interlock Functions

A single transmitter configuration is used for the high temperature detection.

Table 1
Natural or Forced or Forced/Induced Draft Heaters
Malfunction Pilots Fuel GasFuel Oil Supply and Return Other (1)
1. Emergency Shutdown SwitchesXXXX
2. Low pilot gas pressure (6)XXXX
3. Low Process Flow (Primary Service) to Heater Coil
a. Vapor only~XXX
b. Charge/Recycle Gas (3)~XXX
c. All Liquid~XXX
4. Low Process Flow - Waste Heat Removal (5)
a. Steam Superheater~XXX
b. Hot Oil~XXX
c. Reboiler Coil~XXX
d. Circ. Water for Steam Gen. (2)~XXX
5. Other abnormal process conditions (as required)~XXX
6. Low fuel gas burner pressure~X (4)~X
7. Low fuel oil burner pressure~~X (4)X
8. Low Atomizing Steam (Air) vs. Fuel Oil Differential Pressure (6)~~X (4)X

X = Shutoff Device Actuated

Notes:

1. Such as waste gas: In addition to shutoff, an additional diversion valve to an alternate vent destination is usually required.

2. If spare circulating water pump has auto start, a time delay is added to the shutdown to allow the pump to come up to speed.

3. Low recycle gas flow activates shutdown.

4. See text of Interlock Functions for requirements for reactor heaters that are in series.

5. The low flow heater shutdown may be deleted provided that the heater specification clearly states that design of the coil must be based on no flow condition. Note: Depending on heater arrangement, a start-up bypass may be required.

6. A time delay is added to avoid nuisance trips due to “blips”.

Table 2
Forced Draft Burners or Forced/Induced Draft Heaters
Malfunction Pilots (1) Fuel GasFuel Oil Supply and Return Other (3)
1. Emergency Shutdown Switches (4, 5)XXXX
(shuts off fans also)(shuts off fans also)(shuts off fans also)(shuts off fans also)
2. Low Combustion Air pressure (2)~XXX
3. High I.D. Fan Inlet Temperatureshuts off induced draft fan onlyshuts off induced draft fan onlyshuts off induced draft fan onlyshuts off induced draft fan only

X = Shutoff Device Actuated

Notes:

1. Pilots are specified as inspirating type which operate independently of forced draft system.

2. A time delay is added to avoid nuisance trips due to “blips”.

3. Such as waste gas: In addition to shutoff, an additional diversion valve to an alternate vent destination is usually required.

4. These shutdown switches take the place of the individual Emergency Shutdown switches on natural draft heaters. For forced draft heaters there are no individual Emergency Shutdown switches at each heater.

5. All fans are stopped.