October 9, 2026
When a sulfuric acid absorption tower fails to reach its design capacity, operators often blame the packing or the gas flow first. But one of the most common and most easily overlooked causes is uneven sulfuric acid distribution. If the acid does not reach every part of the packing at the same rate, the tower cannot perform efficiently, no matter how strong the acid or how modern the packing.
Inside an absorption tower, acid is pumped to the top and must flow down across the packing as an even film. When uneven sulfuric acid distribution occurs, part of the packing is flooded while other areas run nearly dry. The dry zones offer almost no contact area, the flooded zones add resistance to gas flow, and the tower treats less gas than it was designed for. The symptoms build slowly: rising outlet SO2, a higher pressure drop across the packing, and a need to increase acid circulation just to hold the original performance.
Uneven sulfuric acid distribution usually has one of four roots.
The remedy begins with correct distributor selection and design. The number of distribution points, the weir heights, the orifice sizing and the trough spacing must all be matched to the tower diameter and the expected acid circulation rate. For concentrated sulfuric acid service, an anodic protection acid distributor is often the most reliable choice, because it holds the metal in a passive state and keeps the carefully machined flow paths dimensionally stable for years rather than months. Reviewing the full Sulfuric Acid Distributor range is a sensible first step before committing to a design.
The same problem affects drying towers as much as absorption towers. In a drying tower, poor acid spread lets moisture pass into the downstream process; in a final absorption tower it lets SO2 escape to atmosphere. Both outcomes are expensive, and both trace back to the same root cause on the acid side of the tower.
Look for rising pressure drop, falling absorption efficiency and a growing gap between design and actual acid circulation. A temperature or flow survey across the tower cross-section will usually reveal dry and flooded zones.
Only temporarily. Pumping more acid raises the bulk flow but cannot correct a pattern that already has dry and flooded zones; it usually increases energy use and acid mist without solving the imbalance.
Most operators inspect during every major shutdown, checking hole condition, levelness and any sign of corrosion or distortion. Where anodic protection is fitted, the protection potential should be logged continuously.
To recommend the right distributor for your tower, send us the tower diameter, acid concentration, operating temperature, design flow rate and a description of your existing equipment. With those five inputs we can advise on distribution point density, material and protection method.