Methods and systems for maintaining cargo at an ultra-low temperature over an extended period of time

1. A transport climate control system configured to maintain an ultra-low temperature over an extended period of time, the transport climate control system comprising:

a primary climate control system including a first compressor, a first condenser, a first expander, and a main evaporator that is configured to thermally communicate with a climate controlled space; and

a secondary climate control system including an ultra-low temperature phase changing medium packaged inside or outside of an enclosure for a cargo,

wherein the secondary climate control system is configured to thermally communicate with the climate controlled space, the primary climate control system, and the cargo to provide additional or back-up climate control capacity at the ultra-low temperature,

wherein the ultra-low temperature is between −40° C. to −80° C., and

wherein the ultra-low temperature phase changing medium is packaged such that the ultra-low temperature phase changing medium is arranged to dissipate in the climate controlled space.

2. The transport climate control system of claim 1 , wherein the primary climate control system includes a liquid receiver that:

is configured to fluidly communicate with a working fluid passing through the main evaporator,

is disposed on a working fluid flow path between the first condenser and the first expander, and

is configured to contain the working fluid and manage demand fluctuations of the main evaporator.

3. The transport climate control system of claim 1 , wherein the primary climate control system includes a suction-liquid heat exchanger that

is configured to fluidly communicate with a working fluid passing through the main evaporator,

is configured to be in thermal communication with the working fluid at a working fluid flow path between the main evaporator and the compressor, and

is disposed on the working fluid flow path between the first condenser and the first expander.

4. The transport climate control system of claim 1 , wherein the primary climate control system includes an economizer that

is configured to fluidly communicate with a working fluid passing through the main evaporator, and

is configured to be in thermal communication with the working fluid at a working fluid flow path upstream from the main evaporator.

5. The transport climate control system of claim 1 , wherein the primary climate control system includes a sub-cooling heat exchanger that

is configured to fluidly communicate with a working fluid passing through the main evaporator, and

is configured to be in thermal communication with the first condenser.

6. The transport climate control system of claim 1 , wherein in the primary climate control system includes a second compressor, a second expander, and a cascade heat exchanger, wherein

the second compressor, the cascade heat exchanger, and the second expander are configured to fluidly communicate with a working fluid passing through the main evaporator,

the cascade heat exchange is configured to be in thermal communication with the working fluid passing through the first compressor, and

the first compressor, the first expander, and the first condenser are configured to fluidly communicate with the working fluid passing through the first compressor.

7. The transport climate control system of claim 1 , wherein the ultra-low temperature phase changing medium is at least one of liquid nitrogen and dry ice.

8. The transport climate control system of claim 1 , wherein the ultra-low temperature phase changing medium is packaged such that the ultra-low temperature phase changing medium is arranged to provide cooling capacity externally of the climate controlled space.

9. The transport climate control system of claim 1 , wherein the ultra-low temperature phase changing medium is packaged such that the ultra-low temperature phase changing medium is arranged to provide cooling capacity by evaporation or sublimation.

10. The transport climate control system of claim 1 , wherein

the primary climate control system includes a climate control circuit configured to provide climate control within the climate controlled space, and

the ultra-low temperature phase changing medium is arranged fluidly separate from the climate control circuit.

11. A method for maintaining climate control of a climate controlled space over an extended period of time at an ultra-low temperature, the method comprising:

running a primary climate control system that includes a first compressor, a first condenser, a first expander, and a main evaporator that is configured to thermally communicate with the climate controlled space in order to provide cooling capacity to the climate controlled space;

running a secondary climate control system that includes an ultra-low temperature phase changing medium packaged inside or outside of an enclosure for housing a cargo in order to provide additional or back-up cooling capacity to the climate controlled space at the ultra-low temperature; and

packaging the ultra-low temperature phase changing medium such that the ultra-low temperature phase changing medium is arranged to dissipate in the climate controlled space,

wherein the primary climate control system and the secondary climate control system are configured to thermally communicate with the climate controlled space, and

wherein the ultra-low temperature is between −40° C. to −80° C.

12. The method of claim 11 , further comprising:

dampening fluctuating pressures affecting the first compressor by storing, in a first liquid receiver, a portion of a working fluid passing through the main evaporator, the first liquid being disposed on a flow path between the first condenser and the first expander.

13. The method of claim 11 , further comprising:

removing thermal energy from a working fluid upstream from the main evaporator by thermally communicating the working fluid upstream from the main evaporator with the working fluid downstream from the main evaporator via a suction-liquid refrigerant heat exchanger.

14. The method of claim 11 , further comprising:

removing thermal energy upstream of the first expander by:

diverging a first portion of a working fluid upstream of the first expander to obtain a first diverged portion of the working fluid,

expanding the first diverged portion of the working fluid to obtained a first cooled diverged portion of the working fluid,

cooling a remaining portion of the working fluid upstream of the first expander using the first cooled diverged portion of the working fluid via a first economizer; or

removing thermal energy upstream of a second expander by:

diverging a second portion of the working fluid upstream of the second expander to obtain a second diverged portion of the working fluid,

expanding the second diverged portion of the working fluid to obtained a second cooled diverged portion of the working fluid,

cooling a remaining portion of the working fluid upstream of the second expander using the second cooled diverged portion of the working fluid via a second economizer.

15. The method of claim 11 , further comprising:

stabilizing pressure and temperature during a start-up operation by closing a first buffer control valve directing a portion of a working fluid into a buffer system tank; and

bypassing the buffer system after the start-up operation by opening the first buffer control valve and closing a second buffer control valve.

16. The method of claim 11 , wherein the ultra-low temperature phase changing medium is at least one of liquid nitrogen and dry ice.

17. The method of claim 11 , further comprising:

the ultra-low temperature phase changing medium providing cooling capacity externally of the climate controlled space.

18. The method of claim 11 , further comprising:

the ultra-low temperature phase changing medium providing cooling capacity by evaporation or sublimation.