The Basic Process
The process is based on the combustion of hydrocarbons with air.The ratio between combustion gas and air is kept constant by means of a fully automatic ratio control. In addition the flue gas is analysed continuously on its H2 content by means of a H2 analyser. In case of a deviation of the H2 content the ratio is immediately corrected.
MEA (Mono Ethanol Amine) Boiler and CO2 Stripper
The combustion is effected in a refractory lined reaction chamber. This chamber is equipped with an electrical ignition, an ignition burner and an automatic self-controlling UV-flame monitoring device. The hot flue gas, generated by this process releases its heat by means of a heating register to the MEA-boiler for the generation of pressure-less regeneration-strip-steam. The flue gas leaves the MEA-boiler at approx. 300 °C and is routed to the CO-converter. The CO2 enriched MEA lye coming from the CO2 scrupper is removed in the CO2
stripper column.
CO2 Scrubber A regenerative organic alkaline solution (MEA = Mono Ethanol Amine) is used as CO2 absorbent.
Gas Drying
The “wet” HN protection gas is dried in a thermically regenerated two bed
adsorption plant. As drying agent molecular sieve is used. While drying takes place in the first vessel the second is regenerated at temperatures exceeding 200 °C. The dried HN protection gas is available for the customer.
[Impression of a
protective Gas HN-GAS]
[enlarged view of a
protective gas HN-GAS]
Plants in operation for more than
20 years to full satisfaction of
the customers
Several plants in operation at
leading rolling mills in Europe
On demand hydrogen content
Mahler’s HNX protective gas
Heat Treatment of steel in the
[ print view]