Apparatus for removal of volatile organic compounds from gaseous mixtures

• US 6,165,253 A
• Filed: 05/23/1994
• Issued: 12/26/2000
• Est. Priority Date: 05/23/1994
• Status: Expired due to Fees

• Current Assignee: New Jersey Institute of Technology
• Original Assignee: New Jersey Institute of Technology
• Inventors: Majumdar, Sudipto, Poddar, Tarun, Sirkar, Kamelesh K.
• Primary Examiner(s): Spitzer, Robert H.
• Application Number:
  US08/248,062
• Time in Patent Office: 2,409 Days
• Field of Search: 95/44-46, 95/50, 95/49, 95/51, 95/54, 96/4-14
• US Class Current: 96/6
• CPC Class Codes: B01D 53/14 by absorption
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: B01D 53/229 Integrated processes (Diffusion and at least one other process, e.g. adsorption, absorption)
• CPC Class Codes: Y02A 50/20 Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

A vaporizable solute transfer system for transferring a vaporizable solute from a gas feed mixture to an absorbent liquid comprises an absorption module, a porous membrane which divides the absorption module into a gas-feed chamber and an absorbent chamber, a regeneration module, and a nonporous material which divides the regeneration module into an absorbent chamber and a vacuum atmosphere chamber. The absorption module has gas feed mixture inlet and outlet ports which communicate with the gas feed chamber, and absorbent liquid inlet and outlet ports which communicate with the absorbent chamber. The regeneration module has a liquid absorbent inlet and outlet port which communicate with the liquid absorbent chamber, and a vacuum outlet port which communicates with the vacuum chamber.

Claims

1. A volatile solute-transfer system for transferring a volatile solute from a gas-feed mixture to a liquid absorbent, the solute-transfer system comprising:

(a) an absorption module;

(b)) a porous membrane located within and connected to the absorption module, the porous membrane being wettable by the liquid absorbent, the porous membrane dividing the absorption module into a gas feed chamber and a liquid absorbent chamber, the absorption module having a gas-feed mixture inlet port and a gas-feed mixture outlet port which communicate with the gas-feed chamber and a liquid absorbent inlet port and a liquid absorbent outlet port which communicate with the liquid absorbent chamber, in which the absorption module contains a pressure difference control means for maintaining a difference between a gas pressure of the gas-feed mixture in the gas feed chamber and a liquid pressure of a liquid absorbent in the liquid absorbent chamber substantially within a predetermined pressure range so that an interface between the gas-feed mixture and the liquid absorbent is substantially immobilized at the membrane, to effectively prevent the formation of a dispersion of gas-feed mixture and liquid absorbent in either chamber on opposing sides of the membrane;

(c) a regeneration module; and

(d) a nonporous membrane that is permeable to the volatile solute located within and connected to the regeneration module, the nonporous membrane dividing the regeneration module into a liquid absorbent chamber and a vacuum atmosphere or sweep vapor chamber, the regeneration module having a liquid absorbent inlet port and a liquid absorbent outlet port which communicate with the liquid absorbent chamber and a vacuum outlet port or sweep vapor outlet port which communicates with the vacuum or sweep vapor chamber.

2. The solute transfer system according to claim 1 in which the porous membrane located within the absorption module is in the shape of a hollow tube, the interior of the tube defining the gaseous feed chamber.

3. The solute transfer system according to claim 1 in which the porous membrane is composed of a hydrophobic material selected from the group consisting of porous polyethylene, porous polypropylene, porous polytetrafluoroethylene, porous polyetherketone, porous polyamides, porous polyimides, porous polyvinylidene fluoride, porous polyvinyliene fluoride, porous polysulfone, and porous polyethersulfone.

4. The solute transfer system according to claim 1 in which the porous membrane is composed of a hydrophilic material selected from the group consisting of porous regenerated cellulose, porous cellulose acetate, porous cellulose acetate-nitrate, porous cellulose triacetate, polyacrylonitrile, microporous glass, and porous porcelain.

5. The solute transfer system according to claim 1 in which the porous membrane is composed of a polymeric gel swollen by the absorbent liquid.

6. The solute transfer system according to claim 1 in which the nonporous membrane located within the regeneration module is in the shape of a hollow tube, the interior of the tube defining one vacuum atmosphere chamber.

7. The solute transfer system according to claim 1 in which the nonporous membrane located within the regeneration module is in the shape of a hollow tube, the exterior of the tube defining one vacuum atmosphere chamber.

8. The solute transfer system according to claim 1 in which the porous membrane has an ultrathin plasma polymerized nonporous layer of silicone on an outside surface.

9. The solute transfer system according to claim 1, in which the liquid absorbent is a high boiling, inert, nonvolatile, organic liquid which has a low vapor pressure.

10. The solute transfer system according to claim 9 wherein the absorbent liquid is selected from the group consisting of mineral oils, dimethyl/polymethyl siloxanes, paraffinic oils, synthetic hydrocarbon solvents, vegetable oils, heat transfer fluids, aqueous solutions of alkanolamines, hindered amines, and pure polar hydrocarbons.

11. The solute transfer system according to claim 1 in which the vacuum outlet port communicates with a condenser.

12. The solute transfer system according to claim 1 in which the volatile solute is an organic compound is selected from the group consisting of acetone, methylene chloride, methanol, ethanol, toluene, methylethylketone, carbon tetrachloride, xylene, trichloroethane, isobutanol, chlorobenzene, pentane, hexane, octane, fluorinated hydrocarbons (CFC-11, CFC-12, CFC-113, CFC114, CFC-115, etc.), HCFC (C₂ HCl₂ F₃), and perchloroethylene.

13. The solute transfer system according to claim 1 in which the solute is selected from the group consisting of carbon dioxide (CO₂), hydrogen sulfide (H₂ S), sulfur dioxide (SO₂), and oxygen (O₂).

14. A volatile solute transfer system comprising:

(a) an absorption module containing a plurality of microporous hollow fibers through the lumen of which a gas containing a volatile solute can pass and a liquid absorbent which contacts the exterior of the tubes;

(b) a regeneration module containing a plurality of nonporous hollow fibers forming hollow tubes in which a vacuum or sweep vapor is applied to one surface and the liquid absorbent containing the volatile solute extracted from the gas is on the opposite surface;

(c) pressure control means for maintaining a difference between a gas pressure of the gas and a liquid pressure of the liquid absorbent substantially within a predetermined pressure range so that an interface between the gas and the liquid absorbent is substantially immobilized at the membrane, to effectively prevent the formation of a dispersion of gas-feed mixture and liquid absorbent on opposing sides of the membrane; and

(d) means for transferring the liquid absorbent from the absorption module to the regeneration module and from the regeneration module to the absorption module.

15. The absorption module according to claim 14 in which the microporous hollow fibers are hydrophobic.

16. The absorption module according to claim 15 in which the microporous hydrophobic hollow fibers have the properties of Celgard X-10 or Celgard X-20.

17. The solute transfer system according to claim 15 in which the microporous hydrophobic hollow fibers of the liquid absorbent chamber have an ultrathin plasma polymerized nonporous layer of silicone on an outside surface.

18. The solute transfer system according to claim 14 in which the liquid absorbent is a high boiling inert, nonvolatile organic liquid with a low vapor pressure.

19. The solute transfer system according to claim 18 in which the organic liquid absorbent is selected from the group consisting of mineral oils, dimethyl/polymethyl siloxanes, paraffinic oils, synthetic hydrocarbon solvents, vegetable oils, heat transfer fluids, aqueous solutions of alkanolamines, hindered amines, and pure polar hydrocarbons.

20. The solute transfer system according to claim 14 in which the volatile solute is selected from the group consisting of acetone, methylene chloride, methanol, ethanol, toluene, methylethylketone, carbon tetrachloride, xylene, trichloroethane, isobutanol, chlorobenzene, pentane, hexane, octane, fluorinated hydrocarbons (CFC-11, CFC-12, CFC-113, CFC114, CFC-115, etc.), HCFC (C₂ HCl₂ F₃), and perchloroethylene.

21. The solute transfer system according to claim 14 in which the hollow fibers of the regeneration chamber have an ultrathin plasma polymerized nonporous silicone skin selected from the group consisting of dimethylsilicone, copolymers of silicone-polycarbonate, poly(1-trimethylsily-1-propyne), fluoroelastomers, polyurethane, and polyvinyl fluoride.

22. The solute transfer system according to claim 14 in which the solute is selected from the group consisting of carbon dioxide (CO₂), hydrogen sulfide (H₂ S), sulfur dioxide (SO₂), and oxygen (O₂).