I would appreciate it if experts could provide guidance on the physical properties of the slurry obtained and used in flue gas wet desulfurization.
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The physical properties of gypsum slurry (CaSO4), calcium sulfite slurry (CaSO3), and calcium hydroxide slurry – should the properties of slurries be different from those of solid powders?
What use are you? In conventional wet flue gas desulfurization, the calculation of the slurry is done under ideal conditions; it is of a practical nature and does not focus on the microscopic properties of the slurry, but rather on macroscopic characteristics such as density and viscosity, with other aspects being ignored
We are mainly considering using new equipment to replace some of the components in traditional desulfurization systems, and we believe that the physical properties of the slurry will be affected to some extent.
Thank you to the original poster for sharing; I’ll learn from it