Process and apparatus for re-cycling engine coolant

• US 4,946,595 A
• Filed: 09/09/1988
• Issued: 08/07/1990
• Est. Priority Date: 09/09/1988
• Status: Expired due to Term

• Current Assignee: Century Manufacturing Co. (Pentair Plc (Ireland))
• Original Assignee: FPPF Chemical Corporation Incorporated
• Inventors: Miller, Robert C. Jr.
• Primary Examiner(s): Lieberman, Paul
• Assistant Examiner(s): MCNALLY, JOHN
• Application Number:
  US07/243,319
• Time in Patent Office: 697 Days
• Field of Search: 210/767, 210/758, 210/759, 210/651
• US Class Current: 210/651
• CPC Class Codes: C09K 5/20 Antifreeze additives therefor, e.g. for radiator liquids for application to surfaces C09K3/18; inhibiting corrosion by liquids C23F11/00
• CPC Class Codes: F01P 11/06 Cleaning in general B08B; Combating corrosion in general C23F
• CPC Class Codes: F01P 2011/068 chemically

Abstract

A process for physically and chemically treating a used engine coolant containing one or more glycol and/or alcohol-based antifreeze components. The process includes the steps of oxidation with one or more known oxidizing agents, precipitation with one or more known salt forming agents and filtration through any suitable filtration membrane or other separation means.

A chemical additive has been developed for use in carrying out the process of the present invention which initiates and maximizes the amount of oxidation and precipitation occurring within the coolant composition, adds one or more suitable corrosion inhibitors and one or more known buffering agents in a sufficient amount to adjust the pH of the final solution to between about 9.5 and 10.5.

An apparatus for use in accordance with the process of the present invention for recycling the engine coolant is also described herein.

Claims

1. A process for physically and chemically treating a used coolant composition of the type used within an internal combustion engine cooling system, after removal from said system, to remove unwanted impurities and degradation by-products including dissolved metals, dirt, silt, salts and other unwanted suspended particulate matter contained therein, said coolant composition containing one or more glycol and/or alcohol-based antifreeze components, said process comprising:

contacting said coolant composition with one or more known oxidizing agents in an amount sufficient to form metallic oxides from any unwanted dissolved metals present in said composition thereby forming particulate metallic oxide precipitates;

contacting said coolant composition with one or more known salt forming agents in an amount sufficient to react with any unwanted organic acids present in said composition thereby forming particulate salt precipitates;

filtering said coolant composition through any suitable filtration membrane or other separation means capable of removing particulate precipitates therefrom;

adding to said coolant composition one or more suitable corrosion inhibiting agents selected from the group consisting of phosphates, phosphonates, silicates, borates, nitrites, nitrates, azols, modified acrylates and molybdates; and

introducing into said coolant composition one or more known buffering agents in an amount sufficient to adjust the pH of the final solution to between about 9.5 and 10.5 thereby providing a recycled coolant composition having corrosion capabilities equal or superior to that of the original coolant composition prior to removal.

2. The process of claim 1, wherein said process further comprises the step of:

mixing with said recycled coolant composition one or more additional antifreeze components selected from the group consisting of glycols and alcohols in an amount sufficient to provide freeze protection for said recycled coolant down to the range of about -10°

F. to about -34°

F.

3. The process of claim 2, wherein said glycol is ethylene glycol.

4. The process of claim 1, wherein said process further comprises contacting said recycled coolant composition with an ion exchange resin to substantially remove any remaining divalent metals in dissolved form.

5. The process of claim 4, wherein said ion exchange resin is a chelate forming cation exchange resin specific for the selective removal of divalent metal ions.

6. The process of claim 1, wherein said oxidizing agent is selected from the group consisting of gaseous oxygen, atmospheric oxygen and hydrogen peroxide.

7. The process of claim 1, wherein said oxidizing agent is atmospheric oxygen.

8. The process of claim 7 wherein the atmospheric oxygen is introduced into said coolant by the process of aeration.

9. The process of claim 1, wherein said salt forming agent is selected from the group consisting of alkali metal hydroxides, alkaline earth metal hydroxides, ammonium hydroxide and alkyl amines or a combination thereof.

10. The process of claim 9, wherein said alkali metal hydroxides are selected from the group consisting of sodium hydroxide and potassium hydroxide or a combination thereof.

11. The process of claim 1, wherein said separation means includes at least 2 chemically inert filters.

12. The process of claim 11, wherein said filters are arranged in series.

13. The process of claim 12, wherein said filters are capable of removing particulate matter of a size greater than 1 micron.

14. The process of claim 1, wherein said corrosion inhibitors are selected from the group consisting of azols, molybdates and nitrites or a combination thereof.

15. The process of claim 14, wherein said azoles are selected from the group of thiazoles, triazoles, salts thereof and any combination thereof.

16. The process of claim 15, wherein said azols are selected from the group consisting of tolytriazole, mercaptobenzothiazole or benzothiazole, alkali metal salts thereof, and any combination thereof.

17. The process of claim 14, wherein said molybdate is an alkali metal salt form thereof.

18. The process of claim 14, wherein said nitrites are selected from the group consisting of sodium nitrite, and potassium nitrite.

19. The process of claim 1, wherein said buffering agent is selected from the group consisting of borates, alkali metal and alkaline earth metal hydroxides or combinations thereof.

20. The process of claim 19, wherein said borate is sodium tetraborate.

21. The process of claim 1 wherein said oxidyzing agents, salt forming agents, corrosion inhibiting agents, and buffering agents are first combined into a single chemical additive and thereafter added to said coolant for the chemical treatment thereof.

22. The process of claim 21, wherein said chemical additive comprises by weight:

a. from about 0.5 to about 15 percent of one or more known salt forming agents;

b. from about 0.1 to about 15 percent of one or more known corrosion inhibiting agents;

c. a buffer compound in an amount sufficient to maintain the pH of the coolant solution in the range of about 9.5 to about 10.5; and

d. balance aqueous solvent.