Production of dihydroxyethane in a synthetic ammonia plant with an annual output of 150,000 tons
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For a synthetic ammonia plant with an annual production capacity of 150,000 tons that also produces methanol, what type of reactor should be used in the methanol synthesis process? Since it is a small-scale synthesis, could we use just one net alcohol column to save costs? Thank you for the help! ! !
The key is to determine the purpose of using diol in your plant: is it to increase the production of methanol, or is it merely intended to eliminate copper washing and achieve purification? In terms of market share and operational stability, Hangzhou Linda’s constant-temperature towers are quite good. As for the pure alcohol towers, it is still recommended to use two, otherwise the separation effect will be too poor.
A pure alcohol tower can be used, and the efficiency of water washing is quite high.
It mainly depends on the ammonia-to-alcohol ratio you choose, which refers to the residual carbon content after conversion and decarburization. If the ammonia-to-alcohol ratio is high, one methanol synthesis tower is sufficient; if it is low, two methanol synthesis towers are needed. Efforts should be made to keep the carbon content in the methane feed as low as possible.
Here too, we produce synthetic ammonia and glycol, and one pure glycol tower is sufficient.
The synthesis tower of Nanjing Guochang is also good
I would like to know how effective the methanol high-efficiency separator produced by Xi’an Ultrafiltration is
Everyone’s analysis makes sense; we’ve learned a lot of knowledge. It’s great to discuss things more in depth.:lol
It’s possible, but it still depends on your entire process! Conduct a comprehensive assessment……