The capacity to produce soda ash from melamine exhaust gases
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This post was last edited by lxq700918 on 2009-10-14 at 23:11. We invite experts in soda ash production to discuss the issue of using large amounts of melamine – such as 50,000 tons or 100,000 tons – in the production of soda ash. What capacity is necessary to ensure proper crystallization in the carbonation tower of the soda ash production facility? Should the ratio be 100,000 tons of soda ash per 10,000 tons of melamine, or 50,000 tons of soda ash per 10,000 tons of melamine? And can a facility with a ratio of 50,000 tons of soda ash per 10,000 tons of melamine operate properly?
What we use is co-production, at a ratio of 1:2 compared to alkali. The production capacity for triamines is 15,000 tons, while that for soda ash is 300,000 tons
What was mentioned upstairs is likely 1:20; currently, there are discussions about increasing the supporting capacity to achieve 1:15 (triamine:soda ash)
J: Yes, for the new triamine and alkali combination we are using, the ratio is between 1:10 and 1:15.
The ratio of triamine to base is 1:15. Our company has 180,000 tons of soda ash, along with 12,000 tons of triamine
Dear friend hcyyry: What process is used for producing your triamines? Triamine is used to produce soda ash; can the quality of the soda ash be guaranteed?
Do they all have carbonization towers, CO2 purification towers, etc.? Where can I find information on the relevant processes?
Does anyone know which melamine manufacturers use double-alkali to absorb exhaust gases? Please give me some advice