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US4244698A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for drying magnesium sulfate

Assignee: Dow Chemical Co
•
Filing: 1978-05-02
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Granted: 1981-01-13
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Expires: 1998-05-02
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Abstract

Abstract A method of drying hydrated crystalline magnesium sulfate to reduce its surface moisture content is disclosed. The method comprises: (a) fluidizing a bed of hydrated crystalline magnesium sulfate particles by continuously passing a heated gaseous medium in a generally upwardly direction through the particles at a superficial velocity at least sufficient to maintain turbulent fluidization and mixing of the particles throughout the bed; (b) transferring a dispersed form of hydrated crystalline magnesium sulfate to be dried into the fluidized bed; (c) maintaining the amount of crystalline magnesium sulfate within the fluidized bed at a constant depth; (d) controlling the temperature and relative humidity of the heated gaseous medium to maintain a bed temperature and humidity sufficient to vaporize at least a portion of the surface moisture from the hydrated crystalline magnesium sulfate without removing waters of hydration; and (e) removing dried hydrated crystalline magnesium sulfate from the bed.

Inventors

  • 👤 Robert J. King
  • 👤 Herbert A. Johnson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 14:53
CPC Classifications
C; C01; C01F; C01F5/00; C01F5/40; F; F26; F26B; F26B3/00; F26B3/02; F26B3/06; F26B3/08

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 159 words
A method of drying hydrated crystalline magnesium sulfate to reduce its surface moisture content comprising: (a) fluidizing a bed of hydrated crystalline magnesium sulfate particles by continuously passing a heated gaseous medium in a generally upwardly direction through the particles at a superficial velocity at least sufficient to maintain turbulent fluidization and mixing of the particles throughout the bed; (b) transferring hydrated crystalline magnesium sulfate to be dried into the bed of particles from a crystal feeding means, said magnesium sulfate to be dried being in a dispersed form; (c) controlling the amount of hydrated crystalline magnesium sulfate within the bed to maintain a constant bed depth; (d) controlling the temperature and relative humidity of the heated gaseous medium to maintain a bed temperature and humidity sufficient to vaporize at least a portion of the surface moisture from the hydrated crystalline magnesium sulfate without removing waters of hydration; and (e) removing dried hydrated crystalline magnesium sulfate from the bed.
Claim 2
Independent Claim 159 words
A method of drying hydrated crystalline magnesium sulfate to reduce its surface moisture content comprising: (a) fluidizing a bed of hydrated crystalline magnesium sulfate particles by continuously passing a heated gaseous medium in a generally upwardly direction through the particles at a superficial velocity at least sufficient to maintain turbulent fluidization and mixing of the particles throughout the bed; (b) transferring hydrated crystalline magnesium sulfate to be dried into the bed of particles from a crystal feeding means, said magnesium sulfate to be dried being in a dispersed form; (c) controlling the amount of hydrated crystalline magnesium sulfate within the bed to maintain a constant bed depth; (d) controlling the temperature and relative humidity of the heated gaseous medium to maintain a bed temperature and humidity sufficient to vaporize at least a portion of the surface moisture from the hydrated crystalline magnesium sulfate without removing waters of hydration; and (e) removing dried hydrated crystalline magnesium sulfate from the bed.
Claim 3
Dependent Claim 47 words
The method of claim 1 wherein the temperature and relative humidity of the gaseous medium are controlled to maintain a partial water vapor pressure in the gaseous medium less than the water vapor pressure present at the surface of the hydrated crystalline magnesium sulfate within the bed.
Claim 4
Dependent Claim 11 words
The method of claim 1 wherein the gaseous medium is air.
Claim 5
Dependent Claim 16 words
The method of claim 1 wherein the superficial velocity is at least 2 foot per second.
Claim 6
Dependent Claim 19 words
The method of claim 1 wherein the superficial velocity is from about 3 to about 5 feet per second.
Claim 7
Dependent Claim 19 words
The method of claim 1 wherein the superficial velocity is from about 3 to about 4 feet per second.
Claim 8
Dependent Claim 18 words
The method of claim 1 wherein substantially all the surface moisture is vaporized without removing waters of hydration.
Claim 9
Dependent Claim 26 words
The method of claim 1 wherein the temperature of the heated gaseous medium is controlled to maintain a bed temperature of less than about 48° C.
Claim 10
Dependent Claim 28 words
The method of claim 1 wherein the temperature of the heated gaseous medium is controlled to maintain a bed temperature of from about 20° to about 45° C.
Claim 11
Dependent Claim 28 words
The method of claim 1 wherein the temperature of the heated gaseous medium is controlled to maintain a bed temperature of from about 40° to about 45° C.
Claim 12
Dependent Claim 28 words
The method of claim 1 wherein the hydrated crystalline magnesium sulfate to be dried has a surface moisture content of less than about 10 percent by weight water.
Claim 13
Dependent Claim 30 words
The method of claim 11 wherein the hydrated crystalline magnesium sulfate to be dried has a surface moisture content of from about 3 to about 6 percent by weight water.
Claim 14
Dependent Claim 23 words
The method of claim 1 wherein the magnesium sulfate to be dried has a particle size of about 3 to about 70 mesh.
Claim 15
Dependent Claim 19 words
The method of claim 13 wherein the hydrated crystalline magnesium sulfate removed from the bed is substantially uniformly dried.
Claim 16
Dependent Claim 13 words
The method of claim 1 wherein the magnesium sulfate is magnesium sulfate heptahydrate.
Claim 17
Dependent Claim 13 words
The method of claim 8 wherein the magnesium sulfate is magnesium sulfate heptahydrate.
Claim 18
Dependent Claim 13 words
The method of claim 13 wherein the magnesium sulfate is magnesium sulfate heptahydrate.

References Cited (Backward Citations)

US3401216A Cited
US3638328A Cited
US3748103A Cited
US4005987A Cited
US4083198A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-01-13 1984-07-14 1985-01-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-01-13 1988-07-14 1989-01-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-01-13 1992-07-14 1993-01-13 $7700.00 Window Closed / Lapsed

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