Methods and apparatus for determining sorption isotherms

Claim 3

The method according to claim 1 wherein said mobile phase includes a carrier gas.

Claim 4

The method according to claim 1 wherein said mobile phase is a carrier gas selected from the group consisting of helium, nitrogen, carbon dioxide, oxygen, air and mixtures thereof.

Claim 5

The method according to claim 1 wherein the known solute concentration is provided by flowing said mobile phase containing said solute through a tube maintained at a constant temperature containing pre-column tubing whereby the solute pressure in said mobile phase is a constant saturated pressure.

Claim 6

The method according to claim 4 wherein said constant temperature is a temperature wherein at least some of said solute in said mobile phase is condensed on said pre-column tubing.

Claim 7

The method according to claim 1 wherein said known temperature is a temperature below the boiling point of said solute.

Claim 8

The method according to claim 1 wherein said solute is selected from the group consisting of water, 2-normal-propanol, 2-isopropanol, acetone, methyl ethyl ketone, methyl acetate, hexane and toluene.

Claim 9

The method according to claim 7 wherein said solute is water.

Claim 10

The method according to claim 6 wherein said known temperature is a temperature below about 100° C.

Claim 11

The method according to claim 1 wherein said food is selected from the group consisting of carbohydrates, proteins, fats, salts and mixtures thereof.

Claim 12

The method according to claim 1 wherein said solute is measured with a thermal conductivity detector or a flame ionization detector.

Claim 13

The method according to claim 1 further including the step of providing a calibration factor for converting said measurement of said concentration of said solute in said mobile phase passing downstream from said mass of said food to said amount of said solute in said mobile phase comprising the steps of (a) passing a mobile phase having a known amount of solute through a substantially empty column at a known temperature; and (b) measuring the concentration of said solute in said mobile phase passing downstream of said empty column; and (c) determining the magnitude of the detector response in said measurements of said concentration of said solute in said mobile phase which has passed downstream from said empty column during said passing step; and (d) determining said calibration factor from the amounts in steps (a) and (c).

Claim 14

Apparatus for determining sorption isotherms of food by inverse chromatography comprising: (a) means for passing a mobile phase having a known solute concentration at a known flow rate in a downstream direction through a stationary phase comprising a known mass of a food while maintaining the mass of food at a known temperature, whereby the mobile phase will pass downstream from the mass of food; (b) means for measuring the concentration of said solute in the mobile phase passing downstream from the stationary phase; (c) means for determining the amount of said solute which has passed into the mass of food at selected time intervals during operation of said passing means from said known solute concentration, said known flow rate and the time elapsed since the beginning of passage of said mobile phase having known solute concentration into the mass of food; (d) means for determining the amount of said solute in said mobile phase which has passed downstream from the mass of food at each of said selected time intervals from said measurements of said concentration of said solute in said mobile phase; and (e) means for determining the amount of solute taken up by said food at each of said selected time intervals by determining the difference between the amount of solute which has passed into the mass of food and the amount of solute which has passed downstream from the mass of food.

Claim 15

Apparatus for determining sorption isotherms of food by inverse chromatography comprising: (a) means for passing a mobile phase having a known solute concentration at a known flow rate in a downstream direction through a stationary phase comprising a known mass of a food while maintaining the mass of food at a known temperature, whereby the mobile phase will pass downstream from the mass of food; (b) means for measuring the concentration of said solute in the mobile phase passing downstream from the stationary phase; (c) means for determining the amount of said solute which has passed into the mass of food at selected time intervals during operation of said passing means from said known solute concentration, said known flow rate and the time elapsed since the beginning of passage of said mobile phase having known solute concentration into the mass of food; (d) means for determining the amount of said solute in said mobile phase which has passed downstream from the mass of food at each of said selected time intervals from said measurements of said concentration of said solute in said mobile phase; and (e) means for determining the amount of solute taken up by said food at each of said selected time intervals by determining the difference between the amount of solute which has passed into the mass of food and the amount of solute which has passed downstream from the mass of food.

Claim 16

The apparatus as claimed in claim 13 wherein said means for passing includes a source of mobile phase, a chromatograph chamber, means for maintaining said chromatograph chamber at a known temperature, a pre-column tubing disposed in said chromatograph chamber, conduit means for conducting mobile phase from said source to said pre-column tubing, an injection port for introducing a known amount of a solute into said mobile phase upstream of said pre-column tubing, and a column completed to said pre-column tubing and disposed in said chromatograph chamber for containing a stationary phase comprising food.

Claim 17

The apparatus according to claim 14 wherein said source of mobile phase is a source of a carrier gas.

Claim 18

The apparatus according to claim 15 wherein said source of mobile phase is a source of helium, nitrogen, carbon dioxide, oxygen, air and mixtures thereof.

Claim 19

The apparatus according to claim 14 wherein said temperature maintaining means is operative to maintain said chromatograph chamber at a temperature below the boiling point of said solute.

Claim 20

The apparatus according to claim 13 wherein the means for measuring concentration includes a thermal conductivity detector or a flame ionization detector.

Claim 21

The apparatus according to claim 14 further including an empty column disposed in said chromatograph chamber for calibration purposes.