
In this article Andy Avenell, Crowcon’s Fixed Systems Product Manager, considers the shift towards infrared (IR) gas sensor technology in the oil and gas industry.
Combustible gases and vapors can present considerable dangers in many industrial applications, none more so than the processes involved in extracting, transporting and processing oil and gas. Fast and reliable detection of gas accumulations in sub-LEL (Lower Explosive Limit) levels is essential in order to prevent potential explosions. The longest established and most prevalent sensor technology employed for detecting combustible gas is the Catalytic Bead (or Pellistor as it is otherwise known).
Catalytic Bead Technology
Catalytic beads were originally developed for the mining industry during the early 1960s; earlier simple platinum coil sensors were unsuitable for continuous operation due to their high power consumption and excessive zero drift.
Catalytic bead detectors consist of two matched platinum coils, each embedded in a bead of alumina. The detecting element is coated with a catalyst which promotes oxidation when in contact combustible gases; the compensating element is treated so that catalytic oxidation does not occur. The compensating element is fitted to ensure that signals are not generated due to environmental effects (eg changes in ambient temperature or gas flow rate)

Figure 1 - Catalytic Beads
Catalytic bead based systems operate in a Wheatstone Bridge circuit whereby the catalyzed bead and compensator bead in the detector represent one half of the bridge, the other half being fitted to the control card usually located in the control room (see Figure 2). The control card supplies a voltage to the bridge (typically 2V to 3.5Vdc), which generates a current flow and raises the temperature of the beads to a level where oxidation of gases will occur (>300°C). The control card measures a small voltage offset in the bridge due to the increased resistance in the catalyzed bead element when gas is present. This voltage is then amplified and used to display the gas level and activate alarms.
Because catalytic beads are relatively high power devices; and as they operate at a temperature that will ignite combustible gases they need to be sealed behind a flame arrestor (sinter). Catalytic beads are typically fitted within a stainless steel housing, mounted on an Exd (Explosion-proof) or Exe (Increased Safety) certified junction box. The detector is connected to the control equipment via a 3-core (or sometimes 4-core) cable.

Figure 2 - Wheatstone Bridge Circuit
Advantages and Disadvantages of Catalytic Bead Technology
Advantages:
Disadvantages:

Figure 3 - Typical Catalytic Bead Gas Detector
Infrared Technology
Gases which contain more than one type of atom absorb infrared (IR) radiation. Therefore hydrocarbons and other gases such as carbon dioxide and carbon monoxide can be detected by this means, but gases such as oxygen, hydrogen, helium and chlorine cannot.
Specific gases are detected by measuring their absorption at particular frequencies of infrared light which correspond to the resonance of the molecular bonding between dissimilar atoms. For example the wavelength at which the carbon atom and each of the four hydrogen atoms resonate in a methane molecule is 3.3µ (microns). Most commonly encountered hydrocarbons absorb IR energy in the range 3.3µ to 3.4µ. IR gas detectors are therefore filtered to respond to IR absorption in this range. Carbon dioxide absorbs IR energy in the 4.2µ range and thus different filters are required for a CO2 detector.
The output from the IR sensor is non-linear, and will vary with ambient temperature (due to thermal expansion effects on optical components). Therefore IR detectors use sophisticated software algorithms to 'linearize' the output signal to correspond to 0-100% LEL for the target gas, and also compensate for temperature shifts. The sensor will respond differently to each gas or vapor, and therefore a unique 'linearization' algorithm must be developed for each target gas. Depending on sensor quality and/or production repeatability, individual sensors may need linearizing.
In order to differentiate between IR absorption due to gas and other substances such as dust, dirt or water, an additional sensor with a bandwidth of (typically) 2.7-3.0µ is employed: hydrocarbon gases do not absorb IR energy at this wavelength. This prevents false alarms occurring and compensates for a reduction in signal from the interfering substance. This 'Dual Beam' design is also used to provide a fault alarm to notify operators of contamination of optical components.

Figure 4 - IR Detector Layout
In a typical fixed point detector, the IR source(s) and receiver(s) are mounted in the main body of the housing, with the light beam being reflected by a mirror at the far end of the housing. Parts of the light beam are exposed to atmosphere so that, using natural or forced diffusion, gas can intersect the beam. As the gas concentration increases more infrared energy is absorbed by the gas and less reaches the sensors. Using this method, received energy is inversely proportional to gas concentration.

Figure 5 - IR Gas Detector
Advantages and Disadvantages of IR Technology
Advantages:
Disadvantages:
The Move Towards IR Technology
IR gas detectors (in combination with other detector technologies such as Open-Path Infrared and Acoustic sensors) are now the accepted technology for protecting oil and gas installations against combustible gas hazards.
Independent reference to the market shift from catalytic beads to IR gas detectors is made in the 2006 Frost and Sullivan report F868-32 [1].
It is now common practise to validate safety systems in accordance with IEC61508 [2] ("Functional Safety of electrical/electronic/programmable electronic safety-related systems"); it is however difficult to achieve a satisfactory SIL rating (Safety Integrity Level) using catalytic bead based gas detectors. This is due to the significant possibility of un-revealed failures of sensors due to poisoning or sinters becoming blocked (the sensor is electrically operational, but will fail to respond to gas).
IR detectors also provide significant maintenance cost reductions: catalytic beads require very regular testing (by application of test gas). Some offshore platforms test sensors as often as every six weeks. Many platforms have 400+ gas detectors fitted, and thus such a regular test regime, combined with the need to replace sensors every 3-5 years represents a huge cost. Sinter-free IR detectors are self-checking (ie lamps, sensors, windows, mirrors, software) and thus the risk of an un-revealed failure is minimal. This combined with very low levels of zero and sensitivity drift means that calibration/testing routines can be extended to six or even twelve months on IR detectors. Routine maintenance is usually restricted to cleaning optical components, and a test with calibration gas. IR sensors typically last in excess of 10 years and thus parts replacement is usually restricted to consumables such as filters that may be needed for very dusty environments.
IR detector prices have fallen significantly in recent years, and although the price per point is still higher than catalytic bead based detectors, industry experience confirms that IR detectors quickly pay for themselves by reducing operational/maintenance costs.
Upgrading From Catalytic Beads to IR
Replacing catalytic bead based detectors usually means that the control equipment will also need upgrading. This is due to the mV bridge type signal interface between detector and controller (refer to the Catalytic Bead Technology section for details): IR detectors typically require a power supply of between 12 and 30 Volts dc, and provide a 4-20mA signal to the controller. Thus a catalytic bead control card is inherently incompatible with conventional IR gas detectors.
'Catalytic Bead Replacement' IR gas detectors simulate a catalytic bead mV type signal and are specifically designed to replace catalytic bead sensors with IR technology, whilst retaining the original control equipment, cabling and detector junction box.
In some locations, for example offshore platforms, replacing control systems is a hugely costly and complex operation. North America currently has a fleet of 365 offshore platforms (source www.rigzone.com), 156 of which are currently contracted in the Gulf of Mexico. Many of the older platforms are still fitted with catalytic bead type detectors and mV only compatible control systems; and thus catalytic bead IR replacement detectors provide a solution to upgrading safety at minimal cost.
Catalytic bead replacement IR detectors are typically fitted with a mounting spigot compatible with the most commonly used junction boxes (eg ½"NPT thread). This enables the unit to be directly screwed into the original detector junction box. Catalytic bead replacement IR detectors are certified for use in hazardous areas (usually to UL [5], ATEX [3], and/or IECEx [4] standards), and thus can be installed in any area for which the original detector would have been certified. The detector wires are simply connected to the original terminals (and thus the original cable). Sophisticated catalytic bead replacement IR detectors operate from the voltage source from the original control card, and are zeroed and calibrated in exactly the same way as the original sensor: no adjustments are necessary at the detector.
Operation and Maintenance
One of the more difficult problems to over-come with catalytic bead IR replacement technology is signal drift. Systems operating using a mV (Wheatstone) bridge, such as catalytic bead based systems, are very vulnerable to this problem. In order for a control card to show a zero gas reading the four resistances in the bridge must be balanced. Resistance imbalances can however be introduced by poor cable connections either due to loose terminals, temperature effects or through oxidation of conductors. Any cable/terminal resistance changes are manifested as zero drift on the control card. The challenge is that to be a genuine catalytic bead replacement, an IR detector must have very low power consumption (ie less than 1 Watt), and a well designed power supply so that potential cable influences on the signal are negated.
Combustible gas detectors are often installed in areas that may be difficult to access. To enable testing and calibration detectors may be fitted with a pipe connector. A flexible pipe can then be fixed to the connector and run to a more accessible point. Calibration gas can then be applied to the pipe, and the performance of the detector can be verified without needing to access the detector directly. More advanced IR detectors may actually be calibrated via this means, as oppose to the traditional method of temporarily replacing the detectors' weather-cap with a calibration cap.
Routine maintenance should be restricted to gas testing (with re-calibration only as required: typically annually at most) and cleaning of optical components (algorithms are utilized to provide a fault signal if the window or mirror are more then 75% obscured by contaminants).
Some catalytic bead replacement IR detectors utilize sinters to achieve Exd Explosion-proof compliance. Sinters slow the response time of the IR detector significantly (T90 response time may actually be longer than achieved by catalytic beads), and are vulnerable to blocking. Sinters blocked by contaminants will prevent gas reaching the sensor; this represents a potentially dangerous 'un-revealed failure' which necessitates regular testing to avoid.
Catalytic bead replacement IR detectors need to operate continuously in very harsh environments. 316 stainless steel construction and an effective weather-cap are essential to protect the optical components.

Figure 6 - Catalytic Bead Replacement IR Gas Detector
Performance and Testing
Catalytic bead replacement IR detectors should be rigorously designed and tested to ensure reliable operation at all times. High integrity products are designed to comply with the demanding requirements of IEC61508 [2] (ideally to SIL 2) in terms of both hardware and software. Gas detection performance (response time, short and long-term stability, linearity, accuracy, temperature stability etc) should be verified to a performance standard such as EN61779:2000 [6].
Finally, independent verification of the product by a recognized testing body should have been conducted. The product should be performance tested in simulated offshore conditions to ensure reliable performance in even the most extreme conditions.
References
[1] Frost and Sullivan Report F868-32, 2006: World Industrial Gas Sensors Detectors and Analyzers markets. Relevant references are made on pages 3-2 and 3-42.
[2] International Electrotechnical Commission (IEC), IEC61508 Functional Safety of electrical/electronic/programmable electronic safety-related systems
[3] ATEX: European Directive defining standards for equipment for use in potentially explosive atmospheres.
[4] IECEx: is an international certification scheme created by the IEC to facilitate international trade in electrical equipment intended for use in explosive atmospheres.
[5] UL: Underwriters Laboratories Inc is a privately owned company that tests to make sure that products meet safety standards.
[6] EN61779:2000: Electrical apparatus for the detection and measurement of combustible gases. General requirements and test methods.