The equipment is designed for completing the process lines for soda production. The following equipment is manufactured:
The equipment is designed for completing the process lines for soda production. The following equipment is manufactured:
If any section fails, it is possible its individual replacement.
The distillation heat exchanger erves for carbonic acid topping from distillation condenser liquid with the help of vapor and gas mixture.
| Equipment description | Components | Service | Overall, dimensions, mm | Weight, kg | |
| Diameter | Height | ||||
| Absorption column | Tank I (R-I) | For storage of weak
active liquid and ammoniated brine | 7168 | 23437 | |
| Tank II (R-II) | For storage of weak
active liquid and ammoniated brine | 2800 | 6715 | 20760 | |
| The second absorber (AB-II) | For brine absorption of ammonia and carbonic acid | 12333 | 82950 | ||
| The first absorber (AB-I) | For brine absorption of ammonia and carbonic acid, not absorbed in the second absorber | 8340 | 45100 | ||
| The second column gas washe (PGK-II) | For brine absorption of ammonia and carbonic
acid, supplied with gas from the first gas carbonation washer | 10103 | 54110 | ||
| Distillation gas cooler (HGDS) | For distillation gas cooling | 1245 | 5612 | ||
| Total absorption column | 52000 | 282500 | |||
| Distillation heat exchanger | For topping the carbonic acid from distillation condenser liquid with the help of vapor and gas mixture | 3200 | 15950 | 65845 | |
Main | Production | Production Potentialities | Quality system | Contact us