Compact integrated gas phase separator and subcooler and process

Claim 2

A compact integrated gas phase separator and subcooler for removing gas phases from a liquid gas and subcooling the liquid gas, comprising subcooler means for subcooling a liquid gas, said subcooler means including a subcooler container having a cold bath of liquid gas, gas separator means for removing gas phases from a liquid gas, said separator means including a separator container positioned inside the subcooler container in the cold bath, means for passing a liquid gas from a liquid gas supply line into the phase separator container, heat exchanger means for subcooling the liquid gas including coils extending from the phase separator through the cold bath in the subcooler container, transfer means for passing the gas phases and liquid gas from the separator including a float valve extending from the separator container into the subcooler container with a float floating on the surface of the cold bath in the subcooler, said heat exchanger means also being adapted for opening the float valve by heating the liquid gas in the subcooler bath to evaporate some of it and lower the level of the surface of the subcooler bath, said transfer means also being adapted for closing the float valve by passing liquid gas from the separator container into the subcooler to raise the level of the surface of the subcooler bath.

Claim 3

A compact integrated subcooler-gas phase separator unit, for cryogenic fluids such as subcooled liquid nitrogen, which is compact in size to enable the user to install the unit on or near equipment which uses the subcooled nitrogen comprising an outer subcooler container which is vacuum insulated against the passage of heat, a heat exchanger hollow copper coil positioned in the outer container and immersed in an ambient bath of liquid gas, said coil having an upstream end and a downstream end, a gas phase separator container positioned inside the subcooler container and immersed in the ambient bath of liquid nitrogen, a bath of use liquid gas maintained at a selected level in said inner container, the upstream end of the coil emanating from the bottom of said inner container and the downstream end of the coil exiting from the top of the outer container through an outlet tube, a use liquid inlet tube extending through the outer container into the inner container, a vapor vent positioned in the outer container above the level of the ambient bath, float valve means positioned in the outer container for maintaining the level of the liquid in the outer and inner containers, a takeoff tube extending from the selected liquid level of the use bath through the inner container to a float valve inside the outer container, a spout extending from the float valve into the outer container above the ambient bath, a float connected to the valve by an arm, and the float resting on top of the ambient bath, whereby the use liquid to be phase separated and subcooled is delivered through the inlet tube to the use bath in the inner container where it is phase separated and is delivered to the upstream end of the coil and is subcooled in the coil and delivered from the coil through the downstream end of the coil and the outlet tube.

Claim 4

A compact integrated subcooler-gas phase separator unit, for cryogenic fluids such as subcooled liquid nitrogen, which is compact in size to enable the user to install the unit on or near equipment which uses the subcooled nitrogen comprising an outer subcooler container which is vacuum insulated against the passage of heat, a heat exchanger hollow copper coil positioned in the outer container and immersed in an ambient bath of liquid gas, said coil having an upstream end and a downstream end, a gas phase separator container positioned inside the subcooler container and immersed in the ambient bath of liquid nitrogen, a bath of use liquid gas maintained at a selected level in said inner container, the upstream end of the coil emanating from the bottom of said inner container and the downstream end of the coil exiting from the top of the outer container through an outlet tube, a use liquid inlet tube extending through the outer container into the inner container, a vapor vent positioned in the outer container above the level of the ambient bath, float valve means positioned in the outer container for maintaining the level of the liquid in the outer and inner containers, a takeoff tube extending from the selected liquid level of the use bath through the inner container to a float valve inside the outer container, a spout extending from the float valve into the outer container above the ambient bath, a float connected to the valve by an arm, and the float resting on top of the ambient bath, whereby the use liquid to be phase separated and subcooled is delivered through the inlet tube to the use bath in the inner container where it is phase separated and is delivered to the upstream end of the coil and is subcooled in the coil and delivered from the coil through the downstream end of the coil and the outlet tube.

Claim 5

A process for removing gas phases from a liquid gas and subcooling the liquid gas, comprising the steps of passing a liquid gas from a supply line into a bath of liquid gas in a gas phase separator container, separating out gas phases and collecting the gas phases in the top portion of the separator container and passing the liquid to the bottom portion of the separator container, subcooling the liquid gas by passing it from the bottom portion of the separator container through heat exchanger coils which extend from the separator container through a colder bath of liquid gas in a subcooler container, delivering the subcooled liquid gas from the heat exchanger coils and the subcooler container to the supply line, passing the gas phases from the separator container into the subcooler container through a float valve, opening the float valve by lowering the level of the liquid gas in the subcooler container by heating the subcooler liquid gas and evaporating some of it, heating and evaporating said subcooler liquid gas by applying heat from the liquid gas being subcooled in the coils, closing the float valve by replenishing the subcooler liquid gas by passing liquid gas into it from the separator container through the float valve, and passing the gas phases out of the subcooler.

Claim 6

A process for removing gas phases from a liquid gas and subcooling the liquid gas, comprising the steps of passing a liquid gas from a supply line into a bath of liquid gas in a gas phase separator container, separating out gas phases and collecting the gas phases in the top portion of the separator container and passing the liquid to the bottom portion of the separator container, subcooling the liquid gas by passing it from the bottom portion of the separator container through heat exchanger coils which extend from the separator container through a colder bath of liquid gas in a subcooler container, delivering the subcooled liquid gas from the heat exchanger coils and the subcooler container to the supply line, passing the gas phases from the separator container into the subcooler container through a float valve, opening the float valve by lowering the level of the liquid gas in the subcooler container by heating the subcooler liquid gas and evaporating some of it, heating and evaporating said subcooler liquid gas by applying heat from the liquid gas being subcooled in the coils, closing the float valve by replenishing the subcooler liquid gas by passing liquid gas into it from the separator container through the float valve, and passing the gas phases out of the subcooler.

Claim 7

The process of claim 3, the liquid gas being liquid nitrogen and being passed into the gas phase separator at a temperature of about -289° F. at 60 psi.

Claim 8

The process of claim 3, the subcooled liquid gas passing from the subcooler being liquid nitrogen at about -320° F. at 60 psi.

Claim 9

A process for subcooling liquid gas and removing gas phases from liquid gas supply lines, comprising the steps of introducing liquid gas into a liquid bath in a gas phase separator, separating the gas phases from the liquid, cooling the liquid by passing it from said separator through heat exchanger coils which are located outside the separator and are submerged in a cold variable-pressure bath within a vacuum insulated subcooler container, said liquid in the heat exchanger heating the liquid bath in the subcooler container to vaporize it and lower the liquid level in the subcooler container, said lowering of the level of the subcooler bath operating to open a float valve to remove gas phases accumulated inside the gas phase separator and to raise the liquid level in the gas phase separator and, after drawing off the gas phases, drawing off liquid to replenish liquid in the subcooler container to raise its liquid level to close the float valve, removing the gas phase from the subcooler through a vent in the subcooler container, and removing the subcooled liquid gas from the heat exchanger and the subcooler container through an exit tube at a desired subcooled temperature and returning it to the supply lines.

Claim 10

A process for subcooling liquid gas and removing gas phases from liquid gas supply lines, comprising the steps of introducing liquid gas into a liquid bath in a gas phase separator, separating the gas phases from the liquid, cooling the liquid by passing it from said separator through heat exchanger coils which are located outside the separator and are submerged in a cold variable-pressure bath within a vacuum insulated subcooler container, said liquid in the heat exchanger heating the liquid bath in the subcooler container to vaporize it and lower the liquid level in the subcooler container, said lowering of the level of the subcooler bath operating to open a float valve to remove gas phases accumulated inside the gas phase separator and to raise the liquid level in the gas phase separator and, after drawing off the gas phases, drawing off liquid to replenish liquid in the subcooler container to raise its liquid level to close the float valve, removing the gas phase from the subcooler through a vent in the subcooler container, and removing the subcooled liquid gas from the heat exchanger and the subcooler container through an exit tube at a desired subcooled temperature and returning it to the supply lines.

Claim 11

The process of claim 6, said liquid gas being liquid nitrogen.

Claim 12

The process of claim 6, said liquid gas being liquid nitrogen which is introduced to the separator at about -289° F. and 60 psi, and the subcooler bath is liquid nitrogen at a temperature of about -320° F. at 14.7 psi.