Ionic liquid CO2 scrubber for spacecraft
An environmental control system includes an air conditioning subsystem; a mix manifold downstream of the air conditioning subsystem and upstream of an environment to be conditioned; and a contaminant removal subsystem downstream of the environment to be conditioned. The contaminant removal subsystem includes a first gas-liquid contactor-separator. The first gas-liquid contactor-separator includes a first packed, stationary bed that provides a heat/mass transfer surface for contact between a contaminated air from the environment and a liquid absorbent.
1. An environmental control system, comprising:
an air conditioning subsystem;
a mix manifold downstream of the air conditioning subsystem and upstream of an environment to be conditioned;
a contaminant removal subsystem downstream of the environment to be conditioned;
wherein the contaminant removal subsystem includes:
a first gas-liquid contactor-separator that includes a housing and a first packed bed that is stationary relative to the housing, wherein the first gas-liquid contactor-separator is configured to provide a heat/mass transfer surface for contact between a contaminated air from the environment and a dean liquid absorbent, and wherein the first gas-liquid contactor-separator is further configured to discharge dean air and a used liquid absorbent;
a second gas-liquid contactor-separator downstream, with respect to the used liquid absorbent, of the first gas-liquid contactor separator, wherein the second gas-liquid contactor-separator is configured to desorb gas contaminant from the used liquid absorbent to produce a regenerated liquid absorbent;
a heat exchanger between the first gas-liquid contactor-separator and the second gas-liquid contactor-separator; and
a heater directly downstream, with respect to the used liquid absorbent, of the heat exchanger and directly upstream, with respect to the used liquid absorbent, of the second gas-liquid contactor-separator, wherein the heater is configured to heat used liquid absorbent without employing another heater for heat exchange.
2. The system of claim 1 , wherein the first contactor-separator includes a first centrifugal separator.
3. The system of claim 2 , wherein the first centrifugal separator is downstream, with respect to the used liquid absorbent, of the first packed bed.
4. The system of claim 1 , wherein the first contactor-separator is further configured to direct a first flow of contaminated air co-current with a second flow of droplets of liquid absorbent.
5. The system of claim 1 , wherein the first contactor-separator further includes a nozzle that discharges droplets of liquid absorbent towards the first packed bed.