Inferential pulverized fuel flow sensing and manipulation within a coal mill
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
B02C-004/32
B02C-007/14
출원번호
UP-0726149
(2007-03-21)
등록번호
US-7850104
(2011-02-10)
발명자
/ 주소
Havlena, Vladimir
Pekar, Jaroslav
Pachner, Daniel
출원인 / 주소
Honeywell International Inc.
대리인 / 주소
Schwegman, Lundberg, & Woessner, P.A.
인용정보
피인용 횟수 :
12인용 특허 :
7
초록▼
The subject matter herein relates to coal mills and, more particularly, inferential pulverized fuel flow sensing and manipulation within a coal mill. Various embodiments provide systems, methods, and software to manipulate a primary air flow rate and a coal feed rate into a coal mill to produce a ta
The subject matter herein relates to coal mills and, more particularly, inferential pulverized fuel flow sensing and manipulation within a coal mill. Various embodiments provide systems, methods, and software to manipulate a primary air flow rate and a coal feed rate into a coal mill to produce a target pulverized fuel flow. Some embodiments include sensing a differential pressure between two or more locations within a coal mill to estimate a recirculated load of coal at one or more stages within the coal mill.
대표청구항▼
What is claimed is: 1. A coal mill controller comprising: a primary airflow control module; a coal feed control module; differential pressure sensors to sense pressure differences between each of a plurality of sets of two locations within a fuel path of a coal mill, each differential pressure sens
What is claimed is: 1. A coal mill controller comprising: a primary airflow control module; a coal feed control module; differential pressure sensors to sense pressure differences between each of a plurality of sets of two locations within a fuel path of a coal mill, each differential pressure sensed with respect to a powder stage of coal within the fuel path of the coal mill; a mill control module including an instruction set, operable on a processing device interconnected with the primary airflow and coal feed control modules and the differential pressure sensors, to cause the coal mill controller to: receive, from the primary airflow rate control module, a primary airflow rate of a primary airflow into the coal mill; receive, from a coal feed control module, a coal feed rate of coal being fed into the coal mill; receive, from the differential pressure sensors, differential pressures each sensed with respect to a powder stage within the fuel path of the coal mill; determine a recirculated load of coal within the coal mill and a pulverized fuel flow of coal from the coal mill as a function of the differential pressure measurements, the primary airflow rate, and the coal feed rate; estimate a mass of coal powder in each powder stage within the fuel path of the coal mill; and store the determined recirculated load of coal, the estimated masses of coal powder in each powder stage, and the pulverized fuel flow of coal with the received primary airflow rate and coal feed rate. 2. The coal mill controller of claim 1, wherein the instruction set of the mill control module is further operable on the processing device to cause the mill controller to: receive a target pulverized fuel flow; determine a primary airflow rate and target coal feed rate to achieve the target pulverized fuel flow from the coal mill; send a primary air flow rate command to the primary airflow control module to cause the target primary airflow rate to be achieved within the coal mill; and send a coal feed rate command to the coal feed control module to cause the target coal feed rate to be achieved within the coal mill. 3. The coal mill controller of claim 2, wherein the coal feed rate and primary air flow rate are determined as a function of a model. 4. The coal mill controller of claim 3, wherein the model is a Kalman filter. 5. The coal mill controller of claim 4, wherein disturbance variables of the Kalman filter include a coal moisture content value and a coal calorific value. 6. The coal mill controller of claim 2, wherein the model is refined as a function of the stored determined recirculated load of coal, pulverized fuel flow of coal, and the primary airflow rate and coal feed rate. 7. The coal mill controller of claim 1, wherein the two or more locations within a fuel path of the coal mill where the differential pressure is sensed include a location prior to a pulverized coal recirculation point and a location after the pulverized coal recirculation point. 8. The coal mill controller of claim 1, wherein the instruction set of the mill control module is further operable on the processing device to cause the coal mill controller to: receive and store a target flue gas oxygen level for flue gases flowing from a combustion process fed by operation of the coal mill; receive a sensed flue gas oxygen level sensed from the combustion process fed by operation of the coal mill; and determine the primary airflow rate and target coal feed rate as a function of the stored target flue gas oxygen level to cause the flue gas oxygen level to approach and achieve the flue gas oxygen level target. 9. A method of coal mill control comprising: receiving a primary airflow rate of a primary airflow into the coal mill; receiving a coal feed rate of coal being fed into the coal mill; receiving differential pressures sensed between each of a plurality of sets of two locations within a fuel path of the coal mill, each differential pressure sensed with respect to a powder stage of coal within the fuel path of the coal mill; determining a recirculated load of coal within the coal mill and a pulverized fuel flow of coal from the coal mill as a function of the differential pressure measurements, the primary airflow rate, and the coal feed rate; and storing the determined recirculated load of coal and the pulverized fuel flow of coal with the received primary airflow rate and coal feed rate. 10. The method of coal mill control of claim 9, further comprising: receiving a target pulverized fuel flow; determining a primary airflow rate and target coal feed rate to achieve the target pulverized fuel flow from the coal mill; sending a primary air flow rate command to the primary airflow control module to cause the target primary airflow rate to be achieved within the coal mill; and sending a coal feed rate command to the coal feed control module to cause the target coal feed rate to be achieved within the coal mill. 11. The method of coal mill control of claim 10, wherein the coal feed rate and primary air flow rate are determined as a function of a model. 12. The method of coal mill control of claim 11, wherein the model is a Kalman filter. 13. The method of coal mill control of claim 12, wherein disturbance variables of the Kalman filter include a coal moisture content value and a coal calorific value. 14. The method of coal mill control of claim 9, wherein the two or more locations within a fuel path of the coal mill where the differential pressure is sensed include a location prior to a pulverized coal recirculation point and a location after the pulverized coal recirculation point. 15. The method of coal mill control of claim 9, further comprising: receiving and storing a target flue gas oxygen level for flue gases flowing from a combustion process fed by operation of the coal mill; receiving a sensed flue gas oxygen level sensed from the combustion process fed by operation of the coal mill; and determining the primary airflow rate and target coal feed rate as a function of the stored target flue gas oxygen level to cause the flue gas oxygen level to approach and achieve the flue gas oxygen level target.
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Robert M. Williams, Jr., Control logic for use in controlling grinding mill systems.
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