The invention relates to package water tube boilers, and more specifically, industrial water tube boilers.
One of the more common types of boilers, the water-tube boiler, uses heat from fuel burned within a combustion chamber to heat water circulating through a network of internal tubes. Water-tube boilers typically consist of two principal sections, a radiant section and a convective section. The radiant section is the heat transfer surface area of the boiler which is directly exposed to the flame in the combustion chamber. The convective section is the heat transfer surface area shielded from direct exposure to the flame. The radiant section and the convection section each comprise both riser and downcomer tubes connecting a lower water or mud drum to an upper steam drum. The greater amount of steam that is generated, the larger amount of heat energy that may be transferred or used for a desired purpose.
When designing and operating such boilers, the overall furnace volume may be dictated by the heat flux of the system, i.e., certain furnace volumes must be utilized in order to maintain a desired level of heat flux. Reducing the heat flux in the system lowers the incidence of failure of the boiler tubes.
It would, therefore, be advantageous to provide a package tube boiler which provides greater steam output while maintaining a lower heat flux, thereby prolonging the life of the boiler tubes.
The invention comprises a package water tube boiler having a novel radiant tube design which may be used in both hot water and steam applications. The novel tube design includes one or more additional tubes located within the combustion section of the boiler.
A plurality of carbon steel tubes 140 connects the lower drum 130 to the upper drum 120. In
The furnace 150 has inside and outside furnace walls which are formed by radiant tubes 170 connected to one another by welded steel fins 180, also referred to as membrane tubes. A plurality of joined membrane tubes 170, including inboard radiant riser tubes and outboard radiant tubes, form a membrane furnace wall 190 or baffle which separates the radiant section of the boiler from the convection section 160 of the boiler. It will be recognized that it is also possible to separate the two sections via the placement of tangent tubes or some other similar arrangement in lieu of membrane wall tubes.
The portion of the radiant tubes 170 which face the combustion chamber 150, i.e. essentially one side of the tubes, are radiant heating surfaces as they are exposed to direct flame. Therefore, the heating surface of a radiant tube in a standard configuration is approximately one-half of the circumference of the tube.
In the instant invention, one or more additional radiant tubes 210 are installed within the furnace section. The additional furnace tube(s) 210 is/are inserted between the standard radiant membrane tubes 170. As shown in
The embodiments set forth in the attached figures reflect additional furnace tubes on both walls of the respective furnaces but that need not be the case. Additional tubes 210 can be added to one or both of the inboard or outboard walls. Further, the number of tubes 210 may be varied along each wall.
Inserting an additional furnace tube 210, or tubes, vastly increases the effective heating surface in the furnace. The heating surface could be almost doubled, if not tripled, or increased even further, from the standard configuration. By way of example, the effective furnace area in a traditional 80,000 lb/hr boiler would be 810 sq. ft. The inclusion of additional dual tubes, i.e., on both sides of furnace, would increase the effective furnace area to 1,494 sq. ft. For the traditional 80,000 lb/hr boiler the typical heat flux is 121,870 But/hr sq. ft. compared to 66,372 But/hr sq. ft. with a dual tube configuration as set forth herein.
The increase in radiant heating surface provides numerous advantages. First, the configuration provides for a substantial increase in the amount of steam generation. Aside from increased steam capacity, the overall footprint of the boiler can be reduced while still generating an equivalent amount of steam. Second, the configuration can also be used to reduce the flue gas temperature entering the convection section and thereby reduce the heat flux of the system. Normally, gas temperature would be lowered by increasing the size of the furnace, and commensurately, the footprint of the boiler. However, increasing size increases cost, shipping difficulties, and installation issues. The configuration set forth herein is able to reduce gas temperature within the same boiler footprint since the overall heating surface is increased. The reduction in heat flux directly correlates to an increase in water-tube life.
It will be noted that just as with a more conventional device, a boiler having this configuration can typically be operated as a multiple pass boiler via the installation of baffles within the convection section. Insulation (not shown) may be present within the housing, where required, to further prevent gas leakage or thermal loss.
While the invention has been described in reference to certain preferred embodiments, it will be readily apparent to one of ordinary skill in the art that certain modifications or variations may be made to the system without departing from the scope of invention claimed below and described in the foregoing specification.
This application claims priority from U.S. Provisional Patent Application No. 62/633,531 filed on Feb. 21, 2018.
Number | Date | Country | |
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62633531 | Feb 2018 | US |