Oxy/fuel combustion system having combined convective section and radiant section

a combustion system and convective section technology, applied in indirect heat exchangers, fire-box steam boilers, lighting and heating apparatus, etc., can solve the problems of unprotected steam tubes exposed to high heat fluxes, inability to accept heat fluxes, and known systems that do not provide protection for superheat tubes, etc., to achieve the effect of reducing the overall cos

Inactive Publication Date: 2010-04-01
AIR PROD & CHEM INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0008]This disclosure provides a boiler design that does not require flue gas recycle to achieve the correct heat distribution to superheat and reheat steam, achieves lower overall cost, permits superheating of at least a portion of the steam in the radiant section of an oxy / solid fuel boiler, and / or adequately protects the superheat tubes from the high heat fluxes prevailing in the radiant section.

Problems solved by technology

Superheat steam tubes are important in efficient boiler operation but are not able to accept heat fluxes as high as water tubes due to decreased thermal heat capacity per unit volume.
Known systems do not provide protection for superheat tubes from the high heat fluxes prevailing in the radiant section.
Unprotected steam tubes exposed to high heat fluxes are subject to damage and / or failure.
Using FGR to transfer heat increases the complexity of the flue gas handling system, the size of the convection section and boiler and therefore increases the overall capital and operating cost of the system.
Another challenge for oxy / coal combustion is the furnace exit gas temperature.
In an oxy / coal combustion arrangement utilizing a convective heat exchange section, less heat is available for superheating the steam, due, in part, to a constraint on the temperature of the gases exiting the radiant section of the boiler, causing an imbalance in the heat available for transfer to feedwater, steam generation, and superheating.
Recycling the flue gas adds overall capital and operating cost of the overall process.

Method used

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  • Oxy/fuel combustion system having combined convective section and radiant section
  • Oxy/fuel combustion system having combined convective section and radiant section
  • Oxy/fuel combustion system having combined convective section and radiant section

Examples

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examples

[0056]An example of the current disclosure was studied using computational fluid dynamics (CFD) simulating temperature distribution and heat transfer. The simulation region consists of a 2D rectangular area. One wall boundary was assumed to be at 3140° F. (2000 K) to mimic hot furnace gases. This boundary temperature was chosen to ensure that the maximum heat flux to the water tube was less than the critical heat flux for water. A mixed boundary condition (convection plus radiation) was applied at the opposite boundary which was assumed to be made of a 1 ft thick refractory brick. A periodic boundary condition was applied at the adjacent sides of the simulation area (see e.g., FIG. 15). The water tubes (i.e. the thermal shield 110) and steam tubes (i.e., the first heat exchanger 112) were 2 inches in outer diameter with a wall thickness of 0.375 inches (0.95 cm). The conductivity of the metal tubes varied with temperature and was assumed to be the same as stainless steel. Both the w...

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Abstract

A heat transfer system having a a radiant source, a first heat exchanger configured to permit a first fluid to flow therethrough, and a thermal shield configured to provide controlled radiative heat from the radiant source to the first exchanger. The radiant source is a flame. The thermal shield is a second heat exchanger configured to permit a second fluid to flow therethrough or a non-contact thermal shield fabricated from a material arranged to provide controlled radiative heat exposure from the radiant source to the first exchanger. Oxy/coal combustion systems are also disclosed.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS[0001]This Application is related to application Ser. No. ______, entitled “OXY / FUEL COMBUSTION SYSTEM WITH LITTLE OR NO EXCESS OXYGEN”, Attorney Docket No. 07228 USA, filed contemporaneously with this application on Sep. 26, 2008, assigned to the assignee of the present disclosure and which is herein incorporated by reference in its entirety, application Ser. No. ______, entitled “COMBUSTION SYSTEM WITH STEAM OR WATER INJECTION”, Attorney Docket No. 07238 USA, filed contemporaneously with this application on Sep. 26, 2008, assigned to the assignee of the present disclosure and which is herein incorporated by reference in its entirety, application Ser. No. ______, entitled “COMBUSTION SYSTEM WITH PRECOMBUSTOR”, Attorney Docket No. 07255 USA, filed contemporaneously with this Application on Sep. 26, 2008, assigned to the assignee of the present disclosure and which is herein incorporated by reference in its entirety, application Ser. No. ______,...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): F22B37/12F28D15/00F22B23/00F23L7/00F23B101/00F22B13/00
CPCF23L7/007Y02E20/344F23M9/00F23M5/08Y02E20/34
Inventor HENDERSHOT, REED JACOBHE, XIAOYIKLOOSTERMAN, JEFFREY WILLIAMHIBAY, MICHAEL JOSEPHSLAVEJKOV, ALEKSANDAR GEORGI
Owner AIR PROD & CHEM INC
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