Corrosion resistant tubular air preheater

• US 4,034,803 A
• Filed: 07/24/1975
• Issued: 07/12/1977
• Est. Priority Date: 07/24/1975
• Status: Expired due to Term

• Current Assignee: Koch Engineering Co., Inc. (KOCH Industries Incorporated)
• Original Assignee: John ZINK Company LLC (KOCH Industries Incorporated)
• Inventors: Reed, Robert D., Hart, Wallace F.
• Primary Examiner(s): Davis, Jr., Albert W.
• Application Number:
  US05/598,782
• Time in Patent Office: 719 Days
• Field of Search: 165/103, 165/134, 165/135, 165/157, 165/DIG. 2, 165/160, 165/161, 126/110 R, 126/117, 126/109, 126/106, 126/103, 237/12.3 A
• US Class Current: 165/103
• CPC Class Codes: F23L 15/04 Arrangements of recuperators
• CPC Class Codes: Y02E 20/34 Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
• CPC Class Codes: Y10S 165/122 U heat exchange flow path and linear bypass
• CPC Class Codes: Y10S 165/901 Heat savers

Abstract

A corrosion resistant tubular air preheater in which combustion air is heated by heat transfer from flue gases from a furnace. The heat exchanger is of a longitudinal type having a central enclosure of rectangular cross-section in which a plurality of tubular heat transfer elements are mounted. Surrounding the central enclosure is an outer plenum. Cold combustion air enters at the bottom of the outer plenum and circulates around and up the plenum to a series of openings on top of the heat transfer elements. The partially heated combustion air then passes downwardly through metal tubes in the heat transfer elements and then passes outwardly to the furnace. The minimum temperature in metal structure enclosing the combustion gases is controlled by two means. One is the use of insulation in selected areas to limit heat transfer rate to cold air impinging upon metal surfaces. The second method is by control of cold air flow incidence on or along heat transfer surfaces so as to minimize rapid heat transfer from any metal surface, which might chill the surface below the dew point.

Claims

1. A corrosion resistant tubular air preheater for transfer of heat from hot flue gases carrying corrosive vapors, without condensing said corrosive vapors, comprising:

a. an inner vertical cylindrical metal conduit or wall, for the upward flow of hot flue gas;

b. an outer vertical cylindrical metal wall of the same cross-section shape as said inner wall spaced outwardly from said inner wall forming an annular air inlet plenum;

c. a plurality of heat transfer elements and surfaces, including elements of narrow cross-section and including a plurality of vertical thin wall metal tubes connected between upper and lower plena;

d. said heat transfer elements inserted inside said inner wall with said upper plena connected to the top of said inlet plenum through said inner wall to an outlet plenum surrounding said inner wall below said inlet plenum;

e. inlet air conduit means connected to the bottom of said inlet plenum;

f. outlet air conduit means connected to said outlet plenum;

g. bypass means to control the flow velocity of cold air through said air preheater; and

h. thermal insulation covering selected portions of the heat transfer surfaces where condensation and corrosion is likely to occur;

whereby the cooling of said flue gases below the dew point of said corrosive vapors in the presence of water vapor is prevented.

2. The air preheater as in claim 1 in which said thermal insulation cover at least the lower portion of said inner wall inside said air inlet plenum in the region of said inlet air conduit.

3. The air preheater as in claim 2 in which said thermal insulation covers at least portions of the walls of said upper plena subject to direct impingement of cool air.

4. The air preheater as in claim 1 in which said bypass means comprises bypass conduit means between said inlet air conduit and said outlet air conduit, and control means to control the flow of air through said by-pass conduit means.

5. The air preheater as in claim 1 including means to introduce cold inlet air into the lower end of said inlet air plenum tangential to one wall of said inner wall.

6. The air preheater as in claim 1 in which said corrosive vapors comprise sulfur oxides in the presence of water vapor.

7. The air preheater as in claim 1 in which the cross-sectional shape of said inner and outer walls is rectangular, and said elements are of rectangular cross-section, and said cold air inflow in tangent to one wall of said inner wall.

8. The air preheater as in claim 1 in which said air inlet plenum has a cross-sectional area approximately four times that of said inlet air conduit.

9. The air preheater as in claim 1 in which said inlet air flow in said inlet plenum is co-directional, and in said heat transfer elements is counter-directional to the flow of said hot flue gases.

10. A corrosion tubular air preheater for transfer of heat from hot flue gases carrying corrosive sulfur oxides in the presence of water vapor without condensing said sulfur oxides, comprising:

a. an inner vertical cylindrical metal conduit or wall of the upward flow of hot flue gas;

b. an outer vertical cylindrical metal wall spaced outwardly from said inner wall forming an annular air inlet plenum;

c. a plurality of cylindrical heat transfer elements, each having a plurality of vertical thin wall metal tubes connected between upper and lower plena;

d. said heat transfer elements inserted inside said inner wall with said upper plena connected to the top of said inlet plenum through said inner wall, and said lower plena connecting through said inner wall to an outlet plenum surrounding said inner wall below said inlet plenum;

e. inlet air conduit means connected to the bottom of said inlet plenum;

f. outlet air conduit means connected to said outlet plenum;

g. bypass means to control the flow velocity of cold air through said air preheater; and

h. thermal insulation covering selected portions of the heat transfer surfaces subject to direct impingement of cold air;

whereby the cooling of said flue gases on the inner surfaces of said heat transfer surfaces, below the dew point of said sulfur oxides and water vapor is prevented.