Liquid-cryogen injection cooling devices and methods for using same
Heat exchange devices ( 30 ) and methods of using same are provided. In a general embodiment, the present disclosure provides for heat exchange devices ( 30 ) that are cooling devices having a double helical coil ( 32 ) in a phase-mixing-cooling section, a helical coil ( 36 ) in a phase-separation-cooling section, and a back-pressure valve ( 34 ) intermediate the two coils ( 32,36 ). The cooling devices provide maximum extraction of the heat content from a heated food product using a direct-injected liquid cryogen, and complete separation of the gaseous cryogen phase from the cooled product, while avoiding the formation of a stable foam. Hybrid direct-indirect cooling devices are also provided, as well as methods for using same.
1. A method for direct liquid-cryogen injection cooling, the method comprising:
injecting a heated product and a liquid cryogen into a double-helical pipe to form a two-phase mixture therein;
causing the two-phase mixture to traverse the double-helical pipe and a backpressure valve located downstream of the double-helical pipe;
causing the two-phase mixture to traverse a helical pipe located downstream of the backpressure valve, the two-phase mixture is separated within the helical pipe into a cooled product and a gaseous cryogen phase; and
dispensing the cooled product and the gaseous cryogen phase from the helical pipe.
2. The method of claim 1 , wherein the double-helical pipe comprises a phase-mixing-cooling section of the device.
3. The method of claim 2 , wherein the double-helical pipe causes the heated product and the liquid cryogen to mix to form the two-phase mixture and to exchange a maximum amount of heat between the two phases.
4. The method of claim 1 , wherein the helical pipe comprises a phase-separation-cooling section of the device.
5. The method of claim 4 , wherein the helical pipe is configured to induce a two-phase flow between the cooled product and the gaseous cryogen phase, the cooled product flows at an outer portion of an interior of the helical pipe and wherein the gaseous cryogen phase flows at an inner portion of the interior of the helical pipe.
6. The method of claim 1 , wherein the heated product and the liquid cryogen are injected into the double-helical pipe through first and second inlet valves, respectively.
7. The method of claim 1 , wherein the backpressure valve is configured to increase a residence time of the two-phase mixture within the double-helical pipe.