Adsorbent composites for sorption cooling process and apparatus

Claim 2

A desiccant cooling apparatus comprising: (a) a housing defining an interior, a partition dividing the interior of said housing into a first zone and a second zone, a first fluid inlet means and a first fluid outlet means in communication with said first zone and a second fluid inlet means and second fluid outlet means in communication with said second zone; (b) a plurality of zeolite-lined exchanger tubes extending longitudinally within said housing said tubes having a first end and a second end opposite, said tubes having an interior surface lined with a zeolite composition, said zeolite composition being bonded directly to said surface and defining an interior tube space containing a refrigerant, said tubes spaced to permit transverse fluid flow through said housing; and (c) means for sealing said first and second ends of said tubes.

Claim 3

The desiccant cooling apparatus of claim 1 wherein the zeolite composition comprises a low cerium mixed rare earth exchanged Y zeolite and a binder, having a uniform thickness of from 1.0 to 1.2 mm.

Claim 4

The desiccant cooling apparatus of claim 1 further comprising a plurality of fins disposed on the exterior of said zeolite-lined tubes.

Claim 5

A process for sorption cooling to refrigerate a feedstream from an initial temperature to a lower temperature comprising the following steps: (a) passing a first fluid at a first temperature to a first zone containing at least a portion of a zeolite-lined tube, said first portion of said zeolite-lined tube having a uniform lining comprising zeolite and an inner tube space containing a refrigerant, to desorb a portion of the refrigerant from said first portion of said zeolite-lined tube to produce a vaporized refrigerant stream therein, and passing said vaporized refrigerant stream to a second portion of a zeolite-lined tube; (b) simultaneously passing a second fluid at a second temperature to a second zone to condense and readsorb said vaporized refrigerant stream within said second portion of said zeolite-lined tube; (c) terminating steps (a) and (b); (d) passing said second fluid at said second temperature to said first zone to heat said second fluid to a third temperature; (e) simultaneously passing said feedstream at the initial temperature to said second zone and withdrawing said feedstream at said lower temperature; and, (f) terminating the passing of said second fluid and said feedstream and repeating steps (a) to (e) to provide a sorption cooling cycle.

Claim 6

A process for sorption cooling to refrigerate a feedstream from an initial temperature to a lower temperature comprising the following steps: (a) passing a first fluid at a first temperature to a first zone containing at least a portion of a zeolite-lined tube, said first portion of said zeolite-lined tube having a uniform lining comprising zeolite and an inner tube space containing a refrigerant, to desorb a portion of the refrigerant from said first portion of said zeolite-lined tube to produce a vaporized refrigerant stream therein, and passing said vaporized refrigerant stream to a second portion of a zeolite-lined tube; (b) simultaneously passing a second fluid at a second temperature to a second zone to condense and readsorb said vaporized refrigerant stream within said second portion of said zeolite-lined tube; (c) terminating steps (a) and (b); (d) passing said second fluid at said second temperature to said first zone to heat said second fluid to a third temperature; (e) simultaneously passing said feedstream at the initial temperature to said second zone and withdrawing said feedstream at said lower temperature; and, (f) terminating the passing of said second fluid and said feedstream and repeating steps (a) to (e) to provide a sorption cooling cycle.

Claim 7

The process of claim 4 wherein the first temperature ranges from about 80° C. to about 250° C.

Claim 8

The process of claim 4 wherein the second temperature is lower than the first temperature.

Claim 9

The process of claim 4 wherein the initial temperature ranges from about 20° C. to about 50° C.

Claim 10

The process of claim 4 wherein a single zeolite-lined tube provides said first portion of a zeolite-lined tube and said second portion of a zeolite-lined tube.

Claim 11

The process of claim 4 wherein the lower temperature of said feedstream ranges from about 20° C. to about 0° C.

Claim 12

The process of claim 4 wherein the uniform lining comprising zeolite ranges between 1.0 and 1.2 mm in thickness.

Claim 13

The process of claim 4 wherein steps (a) and (b) consume at least one-half of said sorption cooling cycle.

Claim 14

The process of claim 11 wherein said first zone and said second zone are located in a first desiccant cooling apparatus at least one other desiccant cooling apparatus operated according to the sorption cooling cycle of steps (a) through (f) and offset by at least one-half of said sorption cooling cycle is provided to continuously cool said feedstream.

Claim 15

The process of claim 12 wherein the at least one other desiccant cooling apparatus is insulated from said desiccant cooling apparatus and is contained within a common housing.

Claim 16

The process of claim 4 wherein the second fluid is a portion of said feedstream.

Claim 17

The process of claim 4 wherein said feedstream is selected from the group consisting of a light hydrocarbon stream and air.

Claim 18

The process of claim 4 wherein said first zone containing said first tube portion and said second zone containing said second portion of said zeolite-lined tube are physically separated and refrigerant flows thereinbetween.

Claim 19

The process of claim 4 wherein said sorption cooling cycle ranges from about 0.01 to about 1 hour.