Hatta number

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Template:Short description The Hatta number (Ha) was developed by Shirôji Hatta (1895-1973 [1]) in 1932,[2][3] who taught at Tohoku University from 1925 to 1958.[1][2] It is a dimensionless parameter that compares the rate of reaction in a liquid film to the rate of diffusion through the film.[4] It is related to one of the many Damköhler numbers, Hatta being the square root of such a Damköhler number of the second type. Conceptually the Hatta number bears strong resemblance to the Thiele modulus for diffusion limitations in porous catalysts, which also is the square root of a Damköhler number. For a second order reaction (rA = k2CBCAScript error: No such module "Check for unknown parameters".) Hatta is defined via:

Ha2=k2CA,iCB,bulkδLDAδL CA,i=k2CB,bulkDA(DAδL)2=k2CB,bulkDAkL2


For a reaction mthScript error: No such module "Check for unknown parameters". order in AScript error: No such module "Check for unknown parameters". and nthScript error: No such module "Check for unknown parameters". order in BScript error: No such module "Check for unknown parameters".:


Ha=2m+1km,nCA,im1CB,bulknDAkL

For gas-liquid absorption with chemical reactions, a high Hatta number indicates the reaction is much faster than diffusion, usually referred to as the "fast reaction" or "chemically enhanced" regime. In this case, the reaction occurs within a thin (hypothetical) film, and the surface area and the Hatta number itself limit the overall rate.[5]

For Ha>2, with a large excess of B, the maximum rate of reaction assumes that the liquid film is saturated with gas at the interfacial (CA,i)Script error: No such module "Check for unknown parameters". and that the bulk concentration of A remains zero; the flux and hence the rate of reaction becomes proportional to the mass transfer coefficient kLScript error: No such module "Check for unknown parameters". and the Hatta number: kLCA,iHaScript error: No such module "Check for unknown parameters"..


Conversely, a Hatta number smaller than unity suggests the reaction is the limiting factor, and the reaction takes place in the bulk fluid; the concentration of A needs to be calculated taking the mass transfer limitation - without enhancement - into account.[5]

References

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  1. a b Script error: No such module "citation/CS1".
  2. a b S. Hatta, Technological Reports of Tôhoku University, 10, 613-622 (1932).
  3. Script error: No such module "citation/CS1".
  4. R.B. Bird, W.E. Stewart, E.N. Lightfoot, Transport Phenomena, 2nd ed. John Wiley & Sons, 2002
  5. a b Script error: No such module "citation/CS1".

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See also


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