Abstract A gas condenser apparatus and method is described employing two heat exchanger stages for condensing water vapor and other contaminates, such as organic solvents, out of hot air or other treated gas by means of a cooling gas which is provided by feeding back the treated gas through the cooling passages of such heat exchanger stages after removal of the water and solvents. The heat exchangers are of the counterflow type so that the treated gas and the cooling gas flow in opposite directions therethrough. Preferably, water vapor is removed from the treated gas by condensing it in the first stage and the solvents are removed by condensing them in the second stage thereby separating the condensed water and solvents. Auxiliary cooling coils are provided at the input of the first stage and at the output of the second stage for further cooling of the treated gas. A temperature sensor at the output of the first stage controls the input cooling coil in order to maintain the temperature of the treated gas at the output of the first steps above the freezing temperature of water. The treated gas is used as cooling gas and is fed back first through the output heat exchanger stage and then through the input stage in a sequence opposite to that of the flow of the treated gas. This results in a very efficient operation in which the temperature difference between the treated gas input and the cooling gas output is small, typically only about 20° F.
A method for treating gas to remove water vapor and solvent vapor having different condensation temperatures, comprising the steps of: transmitting an input gas containing water vapor and organic solvent vapor through first passages in a first heat exchanger; transmitting a cooling gas through cooling passages in said first heat exchanger to cool said input gas to a temperature below the condensation temperature of water to cause at least a portion of water vapor therein to condense as a liquid on the walls of said first passages so that a dried input gas containing solvent vapor is provided at the output of said first passages; transmitting said dried input gas through second passages in a second heat exchanger; transmitting a cooling gas through cooling passages in said second heat exchanger to cool said dried input gas to a temperature in said second passages below the condensation temperature of said solvent to cause a portion at least of the solvent vapor therein to condense as a liquid on the walls of said second passages to provide a treated gas at the output of said second passages; removing the condensed solvent from said second heat exchanger; cooling said treated gas to a temperature below the condensation temperature of the input gas component condensed in said second heat exchanger to form said cooling gas; and feeding back said cooling gas through said cooling passages of said second heat exchanger and said first heat exchanger in the order named.
Claim 2
Independent Claim
245 words
A method for treating gas to remove water vapor and solvent vapor having different condensation temperatures, comprising the steps of: transmitting an input gas containing water vapor and organic solvent vapor through first passages in a first heat exchanger; transmitting a cooling gas through cooling passages in said first heat exchanger to cool said input gas to a temperature below the condensation temperature of water to cause at least a portion of water vapor therein to condense as a liquid on the walls of said first passages so that a dried input gas containing solvent vapor is provided at the output of said first passages; transmitting said dried input gas through second passages in a second heat exchanger; transmitting a cooling gas through cooling passages in said second heat exchanger to cool said dried input gas to a temperature in said second passages below the condensation temperature of said solvent to cause a portion at least of the solvent vapor therein to condense as a liquid on the walls of said second passages to provide a treated gas at the output of said second passages; removing the condensed solvent from said second heat exchanger; cooling said treated gas to a temperature below the condensation temperature of the input gas component condensed in said second heat exchanger to form said cooling gas; and feeding back said cooling gas through said cooling passages of said second heat exchanger and said first heat exchanger in the order named.
Claim 3
Dependent Claim
73 words
A method in accordance with claim 1 in which the cooling gas is transmitted from the output of the cooling passages of the first heat exchanger with a system temperature difference with respect to the input gas at the input of the first passages which is less than the temperature difference between the input gas at the output of the first passages and the treated gas at the output of the second passages.
Claim 4
Dependent Claim
65 words
A method in accordance with claim 2 in which said system temperature difference is less than the first heat exchanger temperature difference between the input gas and the dried input gas at the input and output of said first passages and the second heat exchanger temperature difference between the dried input gas and the treated gas at the input and output of said second passages.
Claim 5
Dependent Claim
28 words
A method in accordance with claim 1 in which the temperature of the input gas flowing through said first passages is maintained above the freezing temperature of water.
Claim 6
Dependent Claim
30 words
A method in accordance with claim 1 in which at least the major portion of said water vapor is condensed out of the input gas in said first heat exchanger.