We have extensive experience in gas flaring and recovery processes, allowing us to offer the most appropriate solution for the specifications and requirements of each case.
Elevated (for large gas discharges, with a visible flame and high impact sonic and subsonic radiation, assisted by air/steam, gas, or special flares for low calorific value), ground (for emergency relief with reduced light radiation, multi-stage burners, partially or fully enclosed with or without temperature control), biogas (elevated and concealed, high-temperature flares with burn rate control incorporating state-of-the-art systems and custom-designed), pit burners (for emergency discharges of gas-liquid mixtures), replacement burners (interchangeable with existing equipment, redesigned to suit the client), cold vents (emergency flameless gases), and auxiliary equipment.
Oxidation or incineration of fluids (gaseous/liquid) in a controlled combustion chamber, with adequate residence time to ensure the elimination of harmful components and high thermal destruction to control emissions.
They can be horizontal chambers with forced/induced draft, vertical chambers with forced/natural draft, recuperative, with or without auxiliary equipment (energy recovery, steam generation, DeNOx systems, stack with sampler, etc.).
By adding an ammonia/urea solution to the flue gases, NOx can be converted to N2+H2O.
If this injection is performed into the flue gases at high temperatures, we have a non-catalytic reactor (SNCR).
When more restrictive levels need to be met, it may be necessary to work with a catalyst reactor (SCR) at a lower temperature to increase the efficiency of nitrogen oxide conversion.
Or vapor combustion units safely and efficiently oxidize explosive vapors (gas mixtures diluted in air at concentrations between the flammable limits (LEL) and the UEL) for degassing tankers or storage tanks.
Safe and efficient combustion of explosive vapors (gas mixtures diluted in air at concentrations between the LEL and the UEL) for degassing tankers or storage tanks.
Depending on the frequency of the risk, they are classified as Zone 0 or Zone 1.
Systems designed for ATEX Zone 0 incorporate three independent protection measures.
For hydrocarbon vapors, based on a pressure swing adsorption process with two activated carbon reactors, alternating in 15-minute cycles.