Anesthetic gas reclamation system and method

• US 7,596,965 B2
• Filed: 05/11/2006
• Issued: 10/06/2009
• Est. Priority Date: 05/13/2005
• Status: Active Grant

• Current Assignee: Anesthetic Gas Reclamation LLC
• Original Assignee: Anesthetic Gas Reclamation LLC
• Inventors: Berry, James M., Morris, Steve
• Primary Examiner(s): DOERRLER, WILLIAM CHARLES
• Application Number:
  US11/432,189
• Publication Number:
  US 20060254587A1
• Time in Patent Office: 1,244 Days
• Field of Search: 626/37, 626/17, 625/32, 128/200.24, 128/204.16, 128/203.25, 128/205.12, 423/235
• US Class Current: 62/532
• CPC Class Codes: A61M 16/009 Removing used or expired gases or anaesthetic vapours filtering, sterilising or disinfecting the exhaust air in drainage systems A61M1/784; bacterial filters in the expiratory path A61M16/1065
• CPC Class Codes: A61M 2202/0007 introduced into the body
• CPC Class Codes: A61M 2202/0208 Oxygen
• CPC Class Codes: A61M 2202/03 Gases in liquid phase, e.g. cryogenic liquids
• CPC Class Codes: Y02C 20/10 of nitrous oxide (N2O)

Abstract

A method and system for the fractionation and removal of nitrous oxide and other volatile halocarbon gas components from waste anesthetic gases using liquid oxygen are disclosed. Liquid oxygen is warmed for use in a healthcare facility by cooling and condensing waste anesthetic gases. A cold trap/fractionator is provided wherein selective components of the waste anesthetic gas are collected as a frost on the coils of the cold trap/fractionator by desublimation/deposition and/or condensation/solidification. In a periodic batch process, the collected frost is first thawed and the melted liquids or gases are then collected at various increasing temperatures, thereby separating the nitrous oxide and other halocarbon gas components by their varying melting points. The thawed anesthetic components are collected in separate tanks based on their melting points. Warmed by the waste anesthetic gases in the cold trap/fractionator, the oxygen is supplied to the healthcare facility for its normal uses.

Claims

1. A method for removing and separating a plurality of gaseous components from a waste anesthetic gas mixture comprising nitrogen, oxygen, and a plurality of halocarbons, the method comprising the steps of,

cooling said waste anesthetic gas mixture by passing said gas mixture over a cooling surface (36) contained within a single enclosure, said cooling surface characterized by a surface temperature gradient such that said gas mixture passes thereover in a direction from a warmer temperature to a colder temperature,

depositing by desublimation a gaseous first halocarbon component from said waste anesthetic gas mixture as a solid onto a first portion (60, 62) of said cooling surface (36), said gaseous first halocarbon component characterized by a first halocarbon melting point, said first portion (60, 62) characterized by a first temperature which is colder than said first halocarbon melting point,

depositing by desublimation a gaseous second halocarbon component from said waste anesthetic gas mixture as a solid onto a second portion (63, 64) of said cooling surface (36), said gaseous second halocarbon component characterized by a second halocarbon melting point, said second portion (63, 64) characterized by a second temperature which is colder than said second halocarbon melting point and colder than said first temperature, then

heating said cooling surface (36),

melting said deposited second halocarbon component from said second portion (63, 64) of said cooling surface (36) into a liquid phase, then

collecting said liquid second halocarbon component into a container (24A, 24B), then

melting said deposited first halocarbon component from said first portion (60, 62) of said cooling surface (36) into a liquid phase, and then

collecting said liquid first halocarbon component.

2. The method of claim 1 wherein,

said gaseous first halocarbon component is sevoflurane and said first halocarbon melting point is a melting point of sevoflurane.

3. The method of claim 1, wherein,

said gaseous second halocarbon component is isoflurane and said second halocarbon melting point is a melting point of isoflurane.

4. The method of claim 1, wherein,

said gaseous second halocarbon component is desflurane and said second halocarbon melting point is a melting point of desflurane.

5. The method of claim 1 wherein,

said waste anesthetic gas mixture further comprises nitrous oxide, and said method further comprises the steps of,

depositing by desublimation gaseous nitrous oxide from said waste anesthetic gas mixture as a solid onto a third portion (62, 63) of said cooling surface (36), said gaseous nitrous oxide characterized by a nitrous oxide melting point, said third portion (62, 63) characterized by a third temperature which is colder than said nitrous oxide melting point,

melting said deposited nitrous oxide from said third portion (62, 63) of said cooling surface (36) into a liquid phase, and

collecting said liquid nitrous oxide into said container (24A, 24B).

6. The method of claim 1, further comprising the steps of,

sublimating at least one halocarbon component deposited by desublimation as a solid onto said cooling surface (36) from said cooling surface (36) into a vapor phase, and then

collecting said sublimed at least one halocarbon component into another container (24C).

7. The method of claim 1 further comprising the steps of,

cooling said cooling surface (36) by heat transfer to and warming of a volume of liquid oxygen, then

using said warmed volume of liquid oxygen in a healthcare facility (10).

8. A method for removing and separating a plurality of gaseous components from a waste anesthetic gas mixture comprising nitrogen, oxygen, and a plurality of halocarbons, the method comprising the steps of,

cooling said waste anesthetic gas mixture by passing said gas mixture over a cooling surface (36) contained within a single enclosure, said cooling surface characterized by a surface temperature gradient such that said gas mixture passes thereover in a direction from a warmer temperature to a colder temperature,

solidifying a gaseous first halocarbon component of said waste anesthetic gas mixture onto a first portion (60, 62) of said cooling surface (36), said gaseous first halocarbon component characterized by a first halocarbon melting point, said first portion (60, 62) characterized by a first temperature which is colder than said first halocarbon melting point,

condensing a gaseous second halocarbon component of said waste anesthetic gas mixture onto a second portion (63, 64) of said cooling surface (36), said second portion (63, 64) characterized by a second temperature which is colder than said first temperature,

heating said cooling surface (36),

collecting said second halocarbon component as a liquid into a container (24A, 24B),

melting said solidified first halocarbon component from said first portion (60, 62) of said cooling surface (36) into a liquid phase, and

collecting said liquid first halocarbon component.

9. The method of claim 8, wherein, said gaseous first halocarbon component is sevoflurane and said first halocarbon melting point is a melting point of sevoflurane.

10. The method of claim 8, wherein,

said gaseous second halocarbon component is isoflurane.

11. The method of claim 8, wherein,

said gaseous second halocarbon component is desflurane.

12. The method of claim 8 wherein,

said waste anesthetic gas mixture further comprises nitrous oxide, and said method further comprises the steps of,

solidifying gaseous nitrous oxide from said waste anesthetic gas mixture onto a third portion (62, 63) of said cooling surface (36), said gaseous nitrous oxide characterized by a nitrous oxide melting point, said third portion (62, 63) characterized by a third temperature which is colder than said nitrous oxide melting point,

melting said solidified nitrous oxide from said third portion (62, 63) of said cooling surface (36) into said liquid phase, and

collecting said liquid nitrous oxide into said container (24A, 24B).

13. The method of claim 8 wherein,

said waste anesthetic gas mixture further comprises a gaseous third anesthetic component, and said method further comprises the steps of,

solidifying said gaseous third anesthetic component of said waste anesthetic gas mixture onto a third portion (62, 63, 64) of said cooling surface (36), said gaseous third anesthetic component characterized by an anesthetic melting point, said third portion (62, 63, 64) characterized by a third temperature which is colder than said anesthetic melting point, then

sublimating said solidified third anesthetic component from said third portion (62, 63, 64) of said cooling surface (36) into a vapor phase, and then

collecting said gaseous third anesthetic component into another container (24C).

14. The method of claim 8 further comprising the steps of,

cooling said cooling surface (36) by heat transfer to and warming of a volume of liquid oxygen, then

using said warmed volume of liquid oxygen in a healthcare facility (10).

15. A system for reclamation of anesthetic gas components present in waste anesthetic gas collected from an healthcare facility (10), said system comprising,

a heat exchanger (25, 25A) having an inlet (31) fluidly coupled to a waste gas flow line (39), said waste gas flow line providing said waste anesthetic gas collected from said healthcare facility, said heat exchanger arranged and designed to separate anesthetic gas components from said waste anesthetic gas as said waste anesthetic gas flows through said heat exchanger between said inlet and an outlet (37) of said heat exchanger,

a cooling coil (36) having an inlet and an outlet, said cooling coil positioned within said heat exchanger and having a cooling surface characterized by a surface temperature gradient such that said waste anesthetic gas passes thereover in a direction from a warmer temperature to a colder temperature,

said cooling coil (36) having a first portion (60, 62) characterized by a first temperature which is colder than a first melting point of a first anesthetic component of said waste anesthetic gas, said first portion arranged and designed to desublimate said first anesthetic component of said waste anesthetic gas thereon,

said cooling coil (36) also having a second portion (63, 64) characterized by a second temperature which is colder than said first temperature, said second portion arranged and designed to condense said second anesthetic component of said waste anesthetic gas thereon,

containers (23, 24A, 24B, 24C) fluidly coupled to said heat exchanger, said containers arranged and designed to collect said first anesthetic component thawed from said first portion of said cooling coil and to collect said second anesthetic component condensed onto said second portion of said cooling coil, and

an atmospheric discharge vent (46) fluidly coupled to said outlet of said heat exchanger, said atmospheric discharge vent discharging said waste anesthetic gas without said first and second anesthetic components to atmosphere.

16. The system of claim 15 further comprising,

another heat exchanger (25B) having an inlet (31) fluidly coupled to said waste gas flow line (39), said waste gas flow line providing said waste anesthetic gas collected from said healthcare facility, said another heat exchanger arranged and designed to separate anesthetic gas components from said waste anesthetic gas as said waste anesthetic gas flows through said another heat exchanger between said inlet and an outlet (37) of said another heat exchanger,

another cooling coil (36) having an inlet and an outlet, said another cooling coil positioned within said another heat exchanger and having a cooling surface characterized by a surface temperature gradient such that said waste anesthetic gas passes thereover in a direction from a warmer temperature to a colder temperature,

said another cooling coil (36) having a first portion (60, 62) characterized by a first temperature which is colder than said first melting point of said first anesthetic component of said waste anesthetic gas, said first portion arranged and designed to desublimate said first anesthetic component of said waste anesthetic gas thereon,

said another cooling coil (36) also having a second portion (63, 64) characterized by a second temperature which is colder than said first temperature, said second portion arranged and designed to condense said second anesthetic component of said waste anesthetic gas thereon, and wherein,

said containers are fluidly coupled to said another heat exchanger, said containers arranged and designed to collect said first anesthetic component thawed from said first portion of said another cooling coil and to collect said second anesthetic component condensed onto said second portion of said another cooling coil, and

said atmospheric discharge vent is fluidly coupled to said outlet of said another heat exchanger, whereby

when said waste anesthetic gas flows through said heat exchanger, said another cooling coil of said another heat exchanger is thawed and when said waste anesthetic gas flows through said another heat exchanger, said cooling coil of said heat exchanger is thawed.

17. The system of claim 15 further comprising,

a source (20) of liquid oxygen fluidly coupled to said inlet of said cooling coil, said source arranged and designed to pass liquid oxygen through said cooling coil from said inlet to said outlet.

18. The system of claim 15 further comprising,

a source (20) of liquid nitrogen fluidly coupled to said inlet of said cooling coil, said source arranged and designed to pass liquid nitrogen through said cooling coil from said inlet to said outlet.

19. The system of claim 15 further comprising,

a vacuum pump (92) in fluid communication with said outlet of said heat exchanger, said vacuum pump arranged and designed to draw any sublimed gas from said heat exchanger into one of said containers.

20. The system of claim 15 further comprising,

a source (89) of nitrogen gas fluidly coupled to said heat exchanger, said source arranged and designed to pass nitrogen through said heat exchanger to force any sublimed anesthetic components into one of said containers.