Heat transfer surface for efficient boiling of liquid R-11 and its equivalents

• US 4,354,550 A
• Filed: 05/07/1981
• Issued: 10/19/1982
• Est. Priority Date: 05/07/1981
• Status: Expired due to Term

• Current Assignee: American Standard Companies Incorporated (Ideal Standard International Topco SCA)
• Original Assignee: Trane Company (Trane Technologies plc)
• Inventors: Modahl, Robert J., Luckeroth, Virgil C.
• Primary Examiner(s): BECK, SHRIVE
• Application Number:
  US06/261,342
• Time in Patent Office: 530 Days
• Field of Search: 427/422, 427/423, 165/133, 62/527
• US Class Current: 165/133
• CPC Class Codes: C23C 4/06 Metallic material
• CPC Class Codes: C23C 4/129 Flame spraying
• CPC Class Codes: F28F 13/187 especially adapted for evaporator surfaces or condenser surfaces, e.g. with nucleation sites

Abstract

A heat transfer surface for boiling liquid refrigerant 11 and its equivalents and method for producing the surface. The surface comprises a porous, open-cell coating at least 15 mils thick, of oxidized metallic particles which are flame-sprayed onto a metal substrate. This surface includes a substantial number of nucleate boiling cavities having an equivalent radius in the range of 1.5 to 4 mils, which are the result of one or more of the following conditions in the flame-spraying process: (1) The flame-spraying nozzle is oriented so that the metallic particles impact the metal substrate at an angle in the range of 30° to 75°; (2) The metal substrate is preheated to a temperature which is at least 600° F., but below the melting point of the substrate; and (3) The flame-spraying apparatus is positioned such that the metallic particles travel from 3 to 6 inches before impacting the substrate. These conditions create a porous coating with substantially more nucleate boiling cavities of the required size for boiling liquid R-11 than the flame-spraying process disclosed in the prior art.

Claims

1. A heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, produced by a process in which a flame-spraying apparatus is used, said process comprising the steps of:

flame-spraying a metal substrate with metallic particles which are at least partly oxidized by heat and excess oxygen provided in the flame, the flame-spraying apparatus being oriented such that the metallic particles impact the metal substrate at an angle in the range of 45°

to 60°

, depositing on the substrate an open-cell, porous coating at least 15 mils thick, said coating comprising oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of 1.5 to 4 mils.

6. The heat transfer surface of claim 1 or 3 wherein the metallic particles impact the metal substrate at about a 45°

angle.

7. The heat transfer surface of claims 1, 2, or 3 wherein the steps of flame-spraying includes depositing the coating of metallic particles in two or more passes.

8. The heat transfer surface of claims 1, 2, 3, 4, or 5 wherein the flame-spraying apparatus is positioned during the process so that the distance the metallic particles travel from the flame-spraying apparatus to their point of impact on the metal substrate is within the range of 3 to 6 inches.

11. The heat transfer surface of claim 1, 2, 3, 4, or 5 wherein the metal substrate is copper or an alloy of copper, and the metallic particles are aluminum or an alloy thereof.

2. A heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, produced by a process in which a flame-spraying apparatus is used, said process comprising the steps of:

a. preheating a metal substrate to a temperature in the range 650°

F. to 800°

F.;

b. flame-spraying the preheated metal substrate with metallic particles which are oxidized by heat and excess oxygen provided in the flame; and

c. depositing on the substrate an open-cell, porous coating at least 15 mils thick, said coating comprising oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of from 1.5 to 4 mils.

9. The heat transfer surface of claim 2, 3, or 5 wherein the metal substrate is heated so that the temperature at the surface of the metal substrate is about 730°

F. where the metallic particles impact thereon.

3. A heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, produced by a process in which a flame-spraying apparatus is used, said process comprising the steps of:

a. preheating a metal substrate to a temperature in excess of 650°

F.;

b. flame-spraying the metal substrate with metallic particles which are at least partly oxidized by heat and excess oxygen provided in the flame, the flame-spraying apparatus being oriented such that the metallic particles impact the metal substrate at an angle in the range of 45°

to 60°

; and

c. depositing on the substrate an open-cell, porous coating at least 15 mils thick, said coating comprising oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of from 1.5 to 4 mils.

12. The heat transfer surface of claim 3 or 5 wherein the flame-spraying apparatus is oriented at an angle to the metal substrate and passes sufficiently slow in relation thereto that its flame preheats the metal substrate ahead of where the metallic particles impact.

4. A heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, produced by a process in which a flame-spraying apparatus is used, said process comprising the steps of:

flame-spraying a metal substrate with metallic particles which are at least partly oxidized by heat and excess oxygen provided in the flame, the flame-spraying apparatus being oriented such that the metallic particles impact the metal substrate at an angle in the range of 30°

to 60° and

in addition, at an angle in the range 120°

to 150°

;

depositing on the substrate an open-cell, porous coating at least 15 mils thick;

said coating comprising oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of 1.5 to 4 mils.

10. The heat transfer surface of claim 4 or 5 wherein the metallic particles impact the metal substrate at about a 45°

angle in one or more passes, and in additional one or more passes, impact the metal substrate and the coating already deposited thereon at about a 135°

angle, both angles being measured relative to the metal substrate.

5. A heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, produced by a process in which a flame-spraying apparatus is used, said process comprising the steps of:

a. preheating a metal substrate to a temperature in excess of 650°

F.;

b. flame-spraying the metal substrate with metallic particles which are at least partly oxidized by heat and excess oxygen provided in the flame, the flame-spraying apparatus being oriented such that the metallic angle in the range of 30°

to 60° and

in addition, at an angle in the range 120°

to 150°

; and

c. depositing on the substrate an open-cell, porous coating at least 15 mils thick, said coating comprising oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of from 1.5 to 4 mils.

13. A method for producing a heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, using a flame-spraying apparatus, comprising the steps of:

flame-spraying a metal substrate with metallic particles which are at least partly oxidized by heat and excess oxygen provided in the flame, the flame-spraying apparatus being oriented such that the metallic particles impact the metal substrate at an angle in the range 45°

to 60°

thereby depositing on the substrate an open-cell, porous coating at least 15 mils thick, said coating comprising oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of 1.5 to 4 mils.

18. The method of claims 13, 14, 15, 16, or 17 including the step of positioning the flame-spraying apparatus so that the distance the metallic particles travel from the flame-spraying apparatus to their point of impact on the metal substrate is within the range of 3 to 6 inches.

14. A method for producing a heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, using a flame-spraying apparatus, comprising the steps of:

a. heating a metal substrate to a temperature in the range 650°

F. to 800°

F.;

b. flame-spraying the heated metal substrate with metallic particles which are oxidized by heat and excess oxygen provided in the flame; and

c. depositing on the substrate an open-cell, porous coating at least 15 mils thick, comprising the oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of from 1.5 to 4 mils.

15. A method for producing a heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, using a flame-spraying apparatus, comprising the steps of:

a. preheating a metal substrate to a temperature in excess of 650°

F.;

b. flame-spraying the metal substrate with metallic particles which are at least partly oxidized by heat and excess oxygen provided in the flame, the flame-spraying apparatus being oriented such that the metallic particles impact the metal substrate at an angle in the range of 45°

to 60°

; and

c. depositing on the substrate an open-cell, porous coating at least 15 mils thick, comprising the oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of from 1.5 to 4 mils.

16. A method for producing a heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, using a flame-spraying apparatus, comprising the steps of:

flame-spraying a metal substrate with metallic particles which are at least partly oxidized by heat and excess oxygen provided in the flame, the flame-spraying apparatus being oriented such that the metallic particles impact the metal substrate at an angle in the range of 30°

to 60° and

in addition, at an angle in the range 120°

to 150°

, thereby depositing on the substrate an open-cell, porous coating at least 15 mils thick;

said coating comprising oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of 1.5 to 4 mils.

17. A method for producing a heat transfer surface, especially efficient in boiling liquid refrigerant-11 and its equivalents, using a flame-spraying apparatus, comprising the steps of:

a. preheating a metal substrate to a temperature in excess of 650°

F.;

b. flame-spraying the metal substrate with metallic particles which are at least partly oxidized by heat and excess oxygen provided in the flame, the flame-spraying apparatus being oriented such that the metallic particles impact the metal substrate at an angle in the range of 30°

to 60° and

in addition, at an angle in the range 120°

to 150°

; and

c. depositing on the substrate an open-cell, porous coating at least 15 mils thick, comprising the oxidized metallic particles, parts of which are fused to the substrate and to each other, the open cells of said coating forming a substantial quantity of nucleate boiling cavities having an equivalent radius of from 1.5 to 4 mils.