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ACID RECOVERY TECHNOLOGY (ACT)
 

Acid Recovery Technology (ACT) basically involves recovery and purification of various process, spent, and waste acid solutions. It is a cost effective, value addition technology that is effective for pickling applications, with respect to:-

  • Acid Purification and Recovery
  • Dissolved Solids Removal
  • Reduce Acid Purchases
  • Simplified Waste Disposal
  • Process and Acid Bath Optimization
  • Guaranteed Return/Benefits on Investment
 
ACID RECOVERY FROM SPENT ACID IN PICKLING INDUSTRY

In pickling of steel, to remove rust or iron oxide scale from iron or steel before subsequent processing, such as extrusion, rolling, galvanizing, and other techniques. Technical quality HCl at typically 15 to 18% concentration is the most commonly used pickling agent for the pickling of carbon steel grades.

Pickling is the chemical removal of surface oxides (scale) and other contaminants such as dirt from metal by immersion in aqueous acid solution.    Acid reacts with the oxides and base metal to produce dissolved metal salts, thereby neutralizing the acid.

The pickling process generates considerable quantity of spent pickle liquor (SPL) containing the dissolved metal salts as well as residual free acid.   This SPL must be disposed of by chemical neutralization with alkali which consumes large chemical requirement or regenerated which is the safest way of economics and environment care.

Although carbon steel can be pickled in either sulphuric or hydrochloric acid, for quite  some  time  hydrochloric  has  been  the  acid  of  choice,  particularly  for  large, continuous, strip lines.

Hydrochloric acid offers a number of potential advantages over sulphuric acid, including the following:
• It consistently produces a uniform light gray surface on high-carbon steel
• Less chance of over-pickling    
• Iron concentrations can be as high as 13%
• Rinsing is facilitated because of the high solubility of iron chloride
• Safer to handle • Lower operating temperatures can be employed

Hydrochloric acid regeneration refers to a chemical process for the reclamation of bound and unbound HCl from metal chloride solutions such as ferrous chloride. Regenerated acid has no adverse effect on metal cleaning efficiency compared to virgin acid.  It pickles as efficiently as virgin acid.

 
METHOD OF RECOVERY
 
THE  REGENERATION PROCESS

The basic process is  well designed and   it is applicable to any size pickling operation. 

Steel is continuously fed through a series of pickling tanks.  SPL exits from the pickling line at typically about 10 to 12% iron and 3 to 5 % free hydrochloric acid. The temperature of the acid is approximately 80-90°C for a continuous pickle line but may be less for a batch pickling operation. This higher temperature accelerates the rate of reaction of iron scales with acid.

Using  a  cross-flow  heat  exchanger,  the  exiting  SPL  exchanges  heat  with  the   Regenerated Pickle Liquor (RPL) returning to the pickling line.

 The spent acid to be regenerated then flows into a reactor where it is contacted with concentrated sulphuric acid. The sulphuric acid reacts with the ferrous chloride  thereby liberating free hydrochloric acid in solution.  The resulting iron sulphate is separated by crystallization.

The mother liquor, now fortified with hydrochloric acid, but containing a residual of sulphuric acid is then separated from the crystals by vacuum filtration or centrifugation and recycled to the pickling process.

 A small amount of water is used to wash the residual mother liquor from the crystals.   This water compensates for the water of hydration that is combined with the ferrous sulphate 
 The level of residual sulphuric acid in the regenerated HCl is dependent on the concentration of iron and the temperature.

 
Advantage of this process

The process has a number of potential advantages compared to the other  alternatives.

  • The process operates at low temperatures, thereby minimizing corrosion and allowing the use of inexpensive plastics for piping and other equipment.
  • Energy expenditures for cooling and crystallization are inherently less than Evaporation and can be minimized by reclaiming heat from the SPL with heat Exchangers.
  • The ferrous sulphate  hepta-hydrate  is  a readily marketable material.    
  • The capital investment for the system is considerably less than other alternatives and it is physically much smaller.  This is fortunate, since an on-site regeneration plant is probably the best approach for such a system.
  • The process is more forgiving towards contamination with other metals such as zinc.
 
Pickling performance of the Regenerated acid
  • The addition of sulfuric acid to hydrochloric acid will increase, not decrease the pickling rate.  This may offer production gains through reduction in pickling time.
  • Inhibitors used to avoid attack of the base metal in HCl pickling remain effective with mixed acids.  In fact, unlike with competitive regeneration processes, with this system, inhibitors are recovered for recycle with the regenerated acid.
  • Accelerants used to decrease pickling times are effective with mixed acid.
  • The regenerated acid is  as efficient as VIRGIN  hydrochloric acid for
  • many applications
 
Uses of ferrous sulphate

There  are  a  number  of markets for this material including water treatment coagulants as well as sewagede-odorization.it is also used as phosphorous precipitate by publically owned treatment work for phosphate removal.

 

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