Integrated desiccant-based cooling and dehumidification
Integrated systems comprising both i) heat and mass exchange systems and ii) electrolysis stacks are disclosed, together with related methods of use. The disclosed systems cool and/or dehumidify air using two streams of salt solutions as liquid desiccants.
1. A method of dehumidifying air, comprising:
absorbing water from a process air stream into a first liquid desiccant, dehumidifying the process air stream;
desorbing water from a second liquid desiccant into a purge air stream;
following the absorbing step, converting the first liquid desiccant into the second liquid desiccant by diluting the first liquid desiccant using the second liquid desiccant; and
following the desorbing step, converting the second liquid desiccant into the first liquid desiccant by concentrating the second liquid desiccant using the first liquid desiccant;
repeating the process, wherein:
the converted first liquid desiccant is utilized for the desorbing step and the converted second liquid desiccant is utilized for the absorbing step.
2. The method of claim 1 , further comprising:
purging heat from the first liquid desiccant into the second liquid desiccant, thus cooling the dehumidified process air stream.
3. The method of claim 1 , wherein:
the first liquid desiccant and the second liquid desiccant comprise the same salt solution selected from sodium chloride, potassium chloride, potassium iodide, lithium chloride, copper(II) chloride, silver chloride, chlorine fluoride, bromomethane, iodoform, hydrogen chloride, lithium bromide, hydrogen bromide, potassium acetate, 1-ethyl-3-methylimidazolium acetate, and combinations thereof.
4. The method of claim 3 , wherein the salt solution is selected from lithium chloride and calcium chloride.
5. The method of claim 3 , wherein the salt solution is lithium chloride.
6. The method of claim 1 , wherein:
when absorbing water from the process air stream into the first liquid desiccant and desorbing water from the second liquid desiccant, the difference in a salt ion concentration between the first liquid desiccant and the second liquid desiccant is less than about 20% by weight (wt %).
7. The method of claim 1 , wherein:
when initiating a rejection of salt ions from the first liquid desiccant to the second liquid desiccant and when initiating an acceptance of salt ions from the first liquid desiccant into the second liquid desiccant the difference in a salt ion concentration between the first liquid desiccant and the second liquid desiccant is about 10 wt %.
8. The method of claim 1 , wherein:
when absorbing water from the process air stream, the first liquid desiccant has a salt ion concentration of about 20 wt % to about 45 wt %.
9. The method of claim 1 , wherein:
when desorbing water into the purge air stream, the second liquid desiccant has a salt ion concentration of about 3 wt % to about 30 wt %.