Engine collant recycling apparatus and process

• US 5,167,826 A
• Filed: 07/03/1991
• Issued: 12/01/1992
• Est. Priority Date: 07/03/1991
• Status: Expired due to Fees

• Current Assignee: Stanadyne Automotive Holding Corporation (Stanadyne Holdings Incorporated)
• Original Assignee: Stanadyne Automotive Holding Corporation (Stanadyne Holdings Incorporated)
• Inventors: Eaton, Edward R.
• Primary Examiner(s): Sever, Frank
• Application Number:
  US07/725,351
• Time in Patent Office: 517 Days
• Field of Search: 210/651, 210/195.2, 210/634, 210/644, 210/652, 210/195.2, 210/257.2, 210/321.6, 210/321.72, 210/167, 210/171
• US Class Current: 210/651
• CPC Class Codes: B01D 61/025 Reverse osmosis; Hyperfiltration
• CPC Class Codes: F01P 11/06 Cleaning in general B08B; Combating corrosion in general C23F

Abstract

An apparatus and a process for recycling used engine coolant employs a reverse osmosis process for separating ethylene glycol from a concentrate coolant solution. The engine coolant concentrate is pre-filtered through a series of filters and pressurized prior to being passed through a semi-permeable membrane. The membrane separates the feed stream into a permeate solution of ethylene glycol and water and concentrate solution. The concentrate solution is returned to a concentrate tank for continuous circulation through the apparatus. A heat exchanger maintains the temperature of the concentrate solution below a pre-established threshold.

Claims

1. Apparatus for recycling engine coolant comprising:

concentrate container means for retaining engine coolant to be recycled, said concentrate container means having an inlet and an outlet;

permeate container means for retaining recovered engine coolant, said permeate container means having an inlet;

flow path means for defining a fluid flow path extending from said concentrate outlet to said permeate inlet and said concentrate container inlet;

circulation means for circulating fluid along said flow path;

filtration means interposed in said flow path for filtering particulate matter from said coolant to form a filtered coolant solution;

pressurizing means for pressurizing said filtered coolant solution to form a feed stream;

separator means comprising a semi-permeable membrane interposed in said flow path for separating glycols from said feed stream filtered coolant solution by a reverse osmosis process to form a first stream of glycol and water permeate solution and a second stream of separated concentrate coolant solution;

conduit means for directing said permeate solution to said permeate inlet; and

return means for returning said separated concentrate coolant solution to said concentrate inlet.

2. The apparatus of claim 1 wherein said pressurizing means further comprises means for pressurizing the coolant to a pressure in excess of 50 psi.

3. The apparatus of claim 1 wherein said separator means comprises a housing and a generally cylindrical semi-permeable membrane mounted in said housing and defining a first outer side and a second inner side, wherein filtered pressurized coolant is fed along the first side and the permeate solution is separated for flow along said second side.

4. The apparatus of claim 1 wherein said filtration means comprises a plurality of filter stages having progressive filter elements with decreasing filter porosity diameters.

5. The filtration system of claim 1 wherein said filtration means comprises three filters having 50, 20 and 5 microns respective porosity ratings.

6. The apparatus of claim 1 further comprising a heat exchanger means for maintaining the concentrate temperature at less than 120°

F.

7. The apparatus of claim 1 further comprising pressure control means for terminating operation of said apparatus in the event that the pressure of the system does not exceed a pre-established threshold.

8. The apparatus of claim 1 further comprising dampening means for dampening the turbulence of said pressurized filtered coolant.

9. The apparatus of claim 1 further comprising temperature control means for terminating operation of said system in the event that the temperature of said coolant exceeds 120°

F.

10. The apparatus of claim 1 wherein the semi-permeable membrane is composed of fluoridated hydrocarbon material.

11. The apparatus of claim 1 wherein the semi-permeable membrane has a spiral configuration and spacer means are interposed between spiral layers of said membrane.

12. The apparatus of claim 1 wherein said first stream is approximately 2-4% by volume of said feed stream.

13. The apparatus of claim 1 wherein the flux rate of solution passing through said membrane to form said first stream is approximately 5 gallons per square feet of membrane surface per 24 hours.

14. The apparatus of claim 1 wherein the rate of flow of said separated concentrated coolant solution in said return means is at least 10 times the rate of flow of permeate solution in the conduit means.

15. The apparatus of claim 1 wherein the feed stream has a pressure in the range of 100 to 400 psi.

16. Apparatus for recycling engine coolant comprising:

concentrate container means for retaining engine coolant to be recycled;

permeate container means for retaining recovered engine coolant;

flow path means for defining a fluid flow path extending from said concentrate container means to said permeate container means;

circulation means for circulating coolant along said flow path;

pressurizing means for pressurizing said coolant to form a feed stream;

separator means comprising a semi-permeable membrane interposed in said flow path for separating glycol and water from said feed stream solution by a reverse osmosis process to form a first stream of glycol and water permeate solution and a second stream of separated concentrate coolant solution;

conduit means for directing said permeate solution to said permeate container means; and

return means for returning said separated concentrate coolant solution for recirculation in said feed stream.

17. The apparatus of claim 16 wherein said pressurizing means pressurizes said feed stream to a pressure between 100 and 400 psi.

18. The apparatus of claim 16 wherein said separator means comprises a housing and a generally cylindrical semi-permeable membrane mounted in said housing and defining an outer channel and an inner channel, wherein said feed stream pressurized coolant is fed along the outer channel and the permeate solution is separated for flow along said inner channel.

19. The apparatus of claim 16 further comprising filtration means upstream from said separator means and comprising a plurality of filter stages having progressive filter elements with decreasing filter porosity ratings.

20. The apparatus of claim 16 wherein the semi-permeable membrane is composed of fluoridated hydrocarbon material.

21. The apparatus of claim 16 wherein the semi-permeable membrane has a spiral configuration and spacer means are interposed between spiral layers of said membrane.

22. The apparatus of claim 16 wherein said first stream is approximately 2-4% by volume of said feed stream.

23. The apparatus of claim 16 further comprising heat exchanger means for maintaining the temperature of the concentrate below a pre-established threshold.

24. The apparatus of claim 16 further comprising temperature control means for terminating operation of the apparatus if the temperature exceeds a pre-established threshold.

25. The apparatus of claim 16 further comprising pressure control means for terminating operation of the apparatus if the pressure exceeds a pre-established threshold.

26. A process for recycling engine coolant comprising:

continuously circulating engine coolant along a flow path;

filtering particulate matter from the coolant in said flow path;

pressurizing the coolant to form a feed stream;

passing said feed stream along a semi-permeable membrane to separate glycol and water from said feed stream by reverse osmosis to form a first stream of glycol and water permeate solution and a second stream of separated concentrated solution; and

returning said separated concentrate coolant to said flow path.

27. The process of claim 26 further comprising pressurizing the feed stream to a pressure in the range of 100 to 400 psi.

28. The process of claim 26 further comprising maintaining the temperature of said feed stream at a temperature less than 120°

F.

29. The process of claim 26 further comprising the steps of adding pure glycol solution to said permeate to form a solution by having a pre-established glycol concentration.

30. The process of claim 29 further comprising adding corrosion inhibitors to said solution and mixing same.

31. The process of claim 30 further comprising adding stabilizers to prevent the precipitation of inhibitors.

32. The process of claim 26 further comprising controlling the rate of flow through said membrane so that said first stream is approximately 2-4% by volume of the feed stream.

33. The process of claim 26 further comprising diverting the feed stream from said membrane if the pressure of said feed stream exceeds a pre-established threshold.