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Product Details:
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| Capacity: | 3m3/h,4m3/h,6m3/h,8m3/h. Can Be Designed According To Customer's Requirements | Waste Acid: | Fe2+<140g/L HCL 3-5% |
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| Regenerating Acid: | Fe2+<5g/L HCL 190-220g/L | Iron Powder: | Fe2O3>99% CL-<0.01% |
| Exhaust Gas: | Fe2O3<10mg/Nm3 HCL<20mg/Nm3 | Effluent: | Fe2+0-120g/L Hcl 0-20% (discontinuously Discharge) |
| Efficiency: | >99.5% | Energy Consumption: | <750Kcal/L |
| Energy: | Electricity, Water, Compressed Air | ||
| High Light: | arp Acid Regeneration Plant,acid regeneration plant 4m3/h,sulphuric acid hcl regeneration plant |
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Valued acid regeneration plant 4m3/h (energy electricity) with perfect quality
JJRS assembles excellent technology research team, high qualified management personnel, perfect management system and powerful engineering design and complete project capability. As an integrated solution provider, we are willing to provide iron and steel enterprises of all over the world with highest quality products and services, from general engineering contracting, integrated production lines, to single equipment, even components and spare parts.
Waste acid from acid pickling unit being collected into waste acid tank shall be sent into preconcentrator by waste acid pump through waste acid filter (volume is automatically adjusted by regulative valve). Waste acid shall be sent to the top of preconcentrator for spraying through preconcentrator circulating pump. They will carry out direct heat exchange with burner gas (400℃) from calcinator, thus partial water will be evaporated and the waste acid solution has been concentrated. Condensed waste acid will be sent to the top of calcinatory by its feeding pump through condensed acid filter, and then enters into calcinatory for spraying by spray lance and nozzle. In calcinatory there are 2 spray guns each with 5 nozzles installed. The spaying gun can be automatically inserted into the calcinatory.
Calcinatory housing is made from steel lined with refractory and acid resistant bricks, two burners are in tangent layout for heating, which dries precondensed acid solution drops from the burners. In the hot area of calcinatory ( from 500℃ to 800℃) , FeCL2 and FeCL3 decompose as the following chemical reaction equations show:
| Calcinator material supply flow meter | 5 | sensor | |
| Absorbing tower spraying flow | 5 | sensor | |
| Total flow of primary and secondary absorbing tower | 5 | sensor | |
| Desalted water spraying flow meter | 5 | sensor | |
| Precondensation acid inlet flow meter | 5 | sensor |
Part of the equipment
Contact Person: Mrs. Minnie Meng
Tel: 18811619513
Fax: 86-010-67887136
