CA2422012A1 - Non-aqueous heat transfer fluid and use thereof - Google Patents

Non-aqueous heat transfer fluid and use thereof Download PDF

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Publication number
CA2422012A1
CA2422012A1 CA002422012A CA2422012A CA2422012A1 CA 2422012 A1 CA2422012 A1 CA 2422012A1 CA 002422012 A CA002422012 A CA 002422012A CA 2422012 A CA2422012 A CA 2422012A CA 2422012 A1 CA2422012 A1 CA 2422012A1
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CA
Canada
Prior art keywords
heat transfer
transfer fluid
percent
weight
total weight
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CA002422012A
Other languages
French (fr)
Other versions
CA2422012C (en
Inventor
John W. Evans
J. Thomas Light
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Evans Cooling Systems Inc
Original Assignee
Evans Cooling Systems, Inc.
John W. Evans
J. Thomas Light
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Evans Cooling Systems, Inc., John W. Evans, J. Thomas Light filed Critical Evans Cooling Systems, Inc.
Publication of CA2422012A1 publication Critical patent/CA2422012A1/en
Application granted granted Critical
Publication of CA2422012C publication Critical patent/CA2422012C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/20Antifreeze additives therefor, e.g. for radiator liquids
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/08Materials not undergoing a change of physical state when used
    • C09K5/10Liquid materials
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/08Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Thermal Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Lubricants (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

A non-aqueous, reduced toxicity diol based heat transfer fluid is provided comprised of at least one diol that acts as an antidote for ethylene glycol poisoning, such as for example propylene glycol. The heat transfer fluid may also include corrosion inhibitors that are soluble in the diols used for the heat transfer fluid. The heat transfer fluid may be used as a coolant in internal combustion engines such as automobile engines.

Claims (29)

1. A diol based heat transfer fluid for use in a heat exchange system, said heat transfer fluid comprising:
(a) a first diol consisting of ethylene glycol;
(b) at least one second diol, wherein the second diol acts as an antidote for ethylene glycol poisoning when it is mixed with ethylene glycol, and wherein the second diol has a boiling point above approximately 150°C; and (c) at least one corrosion inhibitor additive that is soluble in the first and second diols.
2. The heat transfer fluid of claim 1, wherein the corrosion inhibitor additive is selected from the group consisting of a molybdate salt, a nitrate salt and an azole.
3. The heat transfer fluid of claim 1, wherein the diols comprise from about percent by weight to about 99.85 percent by weight of the heat transfer fluid.
4. The heat transfer fluid of claim 1, wherein the second diol is propylene glycol.
5. The heat transfer fluid of claim 1, wherein propylene glycol comprises from about 30 percent by weight to about 100 percent by weight of the total weight of the diols, and ethylene glycol comprises from about 0 percent by weight to about 70 percent by total weight of the total weight of the diols.
6. The heat transfer fluid of claim 1, wherein the corrosion inhibitor is comprised of a molybdate salt in a concentration of between about 0.05 percent to about 5 percent by weight of the total weight of the heat transfer fluid.
7. The heat transfer fluid of claim 1, wherein the corrosion inhibitor is comprised of a nitrate salt in a concentration of between about 0.05 percent to about 5 percent by weight of the total weight of the heat transfer fluid.
8. The heat transfer fluid of claim 1, wherein the corrosion inhibitor is comprised of an azole in a concentration of between about 0.05 percent to about 5 percent by weight of the total weight of the heat transfer fluid.
9. The heat transfer fluid of claim 6, wherein the molybdate salt is sodium molybdate.
10. The heat transfer fluid of claim 7, wherein the nitrate salt is sodium nitrate.
11. The heat transfer fluid of claim 8, wherein the azole is tolyltriazole.
12. The heat transfer fluid of claim 1, wherein the corrosion inhibitor is comprised of at least one of (i) sodium molybdate in a concentration between about 0.05 percent by weight to about 5 percent by weight of the total weight of the heat transfer fluid, (ii) sodium nitrate in a concentration between about 0.05 percent by weight to about 5 percent by weight of the total weight of the heat transfer fluid, and (iii) tolyltriazole in a concentration between about 0.05 percent by weight to about 5 percent by weight of the total weight of the heat transfer fluid.
13. The heat transfer fluid of claim 1, wherein (a) ethylene glycol comprises about 70 percent by weight of the total weight of diols in the heat transfer fluid;
(b) propylene glycol comprises about 30 percent by weight of the total weight of diols in the heat transfer fluid;
(c) sodium molybdate comprises about 0.5 percent by weight of the total weight of the heat transfer fluid;
(d) sodium nitrate comprises about 0.5 percent by weight of the total weight of the heat transfer fluid; and (e) tolyltriazole comprises about 0.5 percent by weight of the total weight of the heat transfer fluid.
14. A diol based heat transfer fluid for use in a heat exchange system comprising at least one diol having a boiling point above approximately 150°C, and means for providing an antidote for ethylene glycol poisoning when it is mixed with ethylene glycol.
15. The heat transfer fluid of claim 14, wherein the antidote to ethylene glycol poisoning is propylene glycol.
16. The heat transfer fluid of claim 14, further comprising at least one corrosion inhibitor additive that is soluble in the diols in the heat transfer fluid.
17. The heat transfer fluid of claim 16, wherein the corrosion inhibitor additive is selected from the group consisting of a molybdate salt, a nitrate salt and an azole.
18. The heat transfer fluid of claim 16, wherein the diols comprise from about percent by weight to about 99.85 percent by weight of the heat transfer fluid.
19. The heat transfer fluid of claim 16, wherein the corrosion inhibitor is comprised of a molybdate salt in a concentration of between about 0.05 percent to about 5 percent by weight of the total weight of the heat transfer fluid.
20. The heat transfer fluid of claim 16, wherein the corrosion inhibitor is comprised of a nitrate salt in a concentration of between about 0.05 percent to about 5 percent by weight of the total weight of the heat transfer fluid.
21. The heat transfer fluid of claim 16, wherein the corrosion inhibitor is comprised of an azole in a concentration of between about 0.05 percent to about 5 percent by weight of the total weight of the heat transfer fluid.
22. The heat transfer fluid of claim 19, wherein the molybdate salt is sodium molybdate.
23. The heat transfer fluid of claim 20, wherein the nitrate salt is sodium nitrate.
24. The heat transfer fluid of claim 21, wherein the azole is tolyltriazole.
25. The heat transfer fluid of claim 16, wherein the corrosion inhibitor is comprised of at least one of sodium molybdate in a concentration between about 0.05 percent by weight to about 5 percent by weight of the total weight of the heat transfer fluid, sodium nitrate in a concentration between about 0.05 percent by weight to about 5 percent by weight of the total weight of the heat transfer fluid, or tolyltriazole in a concentration between about 0.05 percent by weight to about 5 percent by weight of the total weight of the heat transfer fluid.
26. The heat transfer fluid of claim 14, wherein at least one diol is ethylene glycol.
27. A method for rendering an ethylene glycol based heat transfer fluid non-toxic comprising the steps of:
(a) providing an ethylene glycol based heat transfer fluid; and (b) adding a sufficient amount of a diol that acts as an antidote for ethylene glycol poisoning to render the heat transfer fluid non-toxic.
28. The method of claim 27, wherein the diol that acts as an antidote for ethylene glycol poisoning comprises at least 30 percent by weight of the heat transfer fluid.
29. The method of claim 28, wherein the diol that acts as an antidote for ethylene glycol is propylene glycol.
CA2422012A 2000-07-19 2001-07-19 Non-aqueous heat transfer fluid and use thereof Expired - Fee Related CA2422012C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US21918900P 2000-07-19 2000-07-19
US60/219,189 2000-07-19
PCT/US2001/022859 WO2002006420A1 (en) 2000-07-19 2001-07-19 Non-aqueous heat transfer fluid and use thereof

Publications (2)

Publication Number Publication Date
CA2422012A1 true CA2422012A1 (en) 2002-01-24
CA2422012C CA2422012C (en) 2012-12-11

Family

ID=22818245

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2422012A Expired - Fee Related CA2422012C (en) 2000-07-19 2001-07-19 Non-aqueous heat transfer fluid and use thereof

Country Status (10)

Country Link
US (3) US20030136809A1 (en)
EP (1) EP1320575B1 (en)
JP (1) JP2004513982A (en)
KR (1) KR100506549B1 (en)
CN (2) CN1511187A (en)
AU (2) AU8064501A (en)
BR (1) BRPI0112642B1 (en)
CA (1) CA2422012C (en)
MX (1) MX246518B (en)
WO (1) WO2002006420A1 (en)

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Also Published As

Publication number Publication date
JP2004513982A (en) 2004-05-13
US20100176334A1 (en) 2010-07-15
CN1511187A (en) 2004-07-07
MX246518B (en) 2007-06-18
AU8064501A (en) 2002-01-30
BRPI0112642B1 (en) 2016-02-10
EP1320575B1 (en) 2013-09-04
CA2422012C (en) 2012-12-11
AU2001280645B2 (en) 2005-10-20
EP1320575A1 (en) 2003-06-25
US20030136809A1 (en) 2003-07-24
US20080061269A1 (en) 2008-03-13
MXPA03000538A (en) 2004-04-21
KR20030097775A (en) 2003-12-31
EP1320575A4 (en) 2009-08-26
CN102061147A (en) 2011-05-18
BR0112642A (en) 2004-06-22
WO2002006420A1 (en) 2002-01-24
KR100506549B1 (en) 2005-08-05
US7655154B2 (en) 2010-02-02

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