At present, the main methods for the conversion of coking gas, which are widely used in industry, are catalytic partial oxidation and non catalytic partial oxidation. No matter what kind of process requires the transformation of the furnace to the coke oven gas into syngas (CO H2). The transformation is the transformation of pure oxygen burner furnace is one of the key equipment.

Burner with Jinan with intellectual innovation technology Co., Ltd. R & D patent technology, semi pre mixed turbulent mixing gas mixing combustion technology, through special structure design, so that the oxygen through the circular jet and coke oven gas jet formed strong shear, tensile, stirring, within the export ~ 200mm distance on mixing was very uniform, so complete combustion, can realize high combustion intensity, flame outlet jet high speed, strong rigidity of the flame. Combustion stability, will not temper.

Especially in the furnace burner in part by radiation and convection of a large number of imported aerospace superalloys;

The burner designed a water cooling system with forced cooling, can prolong the service life;

The design of steam burner protection, effectively prevent overfiring;

The burner with a layer of refractory ceramic fiber protective layer on the outer cylindrical surface.

The technical performance of metal burner:

By changing the material enters the reformer pressure can achieve 50% ~ ~ 120% of the operating flexibility of burner can well in a wide range of operation.

Service life of the nozzle is guaranteed to be greater than 24 months;

Use of advanced energy-saving, pure oxygen burner, safe and reliable operation, reducing process gas side pressure drop, short flame, backward catalyst bed layer combustion gas temperature and composition uniform distribution.

Optimization of burner structure, the realization of the airflow distribution in the regulation and control, the coke oven gas evenly into the combustion reaction zone, ensure a good degree of flame molding, uniform temperature field in the furnace; not to take off the fire, tempering.

Burner oxygen side pressure drop is less than or equal to 2barA and process side resistance drop as low as possible, but the process gas distribution is uniform; at the same time mixing of oxygen and the process gas must be uniform;

The catalyst bed entrance process gas plane temperature difference is less than or equal to 8 DEG c;

The combustion section of a burner of radiation to the refractory surface temperature are less than 1300.