Catalytic incineration system

• US 5,291,859 A
• Filed: 01/29/1993
• Issued: 03/08/1994
• Est. Priority Date: 01/29/1993
• Status: Expired due to Fees

• Current Assignee: Joseph A. Brinck
• Original Assignee: Joseph A. Brinck
• Inventors: Reis, Stephen L., Brinck, Joseph A.
• Primary Examiner(s): Favors, Edward G.
• Application Number:
  US08/011,286
• Time in Patent Office: 403 Days
• Field of Search: 431/5, 422/173, 122/7 R, 165/81, 110/212, 110/214, 110/344, 110/345, 110/233, 110/234
• US Class Current: 122/7.00R
• CPC Class Codes: F23G 7/066 preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator
• CPC Class Codes: F23G 7/07 in which combustion takes place in the presence of catalytic material

Abstract

A catalytic incinerator system for oxidation/combustion of volatile organic compounds (VOCs). The system is relatively compact, is designed to accommodate the thermal stresses within the system without adversely affecting the system components, and to provide substantially uniform temperature distribution in the VOCs and combustion air. The system includes a dual shell housing having an inner shell and an outer shell, wherein the inner shell is capable of thermal expansion and movement relative to the outer shell. Also included is a multi-pass tube-type heat exchanger suspended or otherwise mounted within a heat exchange chamber. The heat exchanger is mounted within the heat exchange chamber so that one end is unfixed and thus the heat exchanger can freely expand and contract due to temperature fluctuations within the heat exchange chamber. Additionally, a unique baffle system is disposed in the flow path of the VOCs and combustion air within the combustion chamber to provide a uniform temperature distribution, resulting in substantially complete oxidation of the VOCs.

Claims

1. A system for catalytically incinerating volatile organic compounds, comprising:

a dual shell housing having an outer shell and an inner shell, said inner shell capable of expansion and movement relative to said outer shell, and said inner shell defining a heat exchange chamber and a combustion chamber;

a blower for conveying the volatile organics first through said heat exchange chamber and then through said combustion chamber;

a multi-pass, tube-type heat exchanger in said heat exchange chamber, said heat exchanger comprising first and second tube sheets and a plurality of tubes through which the volatile organics pass, affixed at their respective ends to said first and second tube sheets, said heat exchanger suspended within said heat exchange chamber and fixed to said inner shell at one end only so that said heat exchanger can freely expand and contract due to temperature changes within said heat exchange chamber, thereby reducing thermal stresses on said heat exchanger and said housing;

a high pressure blower for supplying combustion air to said combustion chamber and mixing with the volatile organics;

a burner for heating the volatile organics to incineration temperature;

at least one flow baffle disposed within said combustion chamber in the flow path of the heated volatile organics and combustion air to provide a substantially uniform temperature distribution therein; and

an oxidation catalyst in said combustion chamber through which the heated volatile organics and combustion air pass, said catalyst initiating incineration of the volatile organics, thereby producing hot exhaust vapors.

2. The system of claim 1,

said tubes of said heat exchanger being disposed substantially vertically within said heat exchange chamber.

3. The system of claim 2,

said hot exhaust vapors being directed to and flowing through said heat exchange chamber on the shell side of said tubes to preheat the volatile organics flowing through said tubes.

4. The system of claim 1, further comprising:

a flexible joint in the flow path of the volatile organics downstream of said heat exchanger and upstream of said combustion chamber, said flexible joint accommodating expansion of said inner shell.

5. The system of claim 1, further comprising:

a perforated plate in the flow path of the volatile organics downstream of said heat exchanger and upstream of said burner, said perforated plate providing uniform flow of the volatile organics across said burner to reduce localized heating thereof.

6. The system of claim 5, further comprising:

a filter in the flow path of the volatile organics downstream of said heat exchanger and upstream of said perforated plate.

7. The system of claim 1, further comprising:

at least one access port in said housing which penetrates said outer shell and enables the measurement of one or more physical parameters within said system.