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Furnace controller and method of operating furnace

A furnace and charge technology, applied in the direction of furnace control device, program control, furnace feeding, etc., can solve the problems of high variability of furnace operation efficiency and productivity, loss amplification, etc.

Pending Publication Date: 2022-01-25
AIR PROD & CHEM INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This can lead to high variability in the furnace's operating efficiency and production rate
Losses due to process variability can be magnified when operators operate multiple furnaces simultaneously

Method used

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  • Furnace controller and method of operating furnace
  • Furnace controller and method of operating furnace
  • Furnace controller and method of operating furnace

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0115] image 3 A graph showing a cycle is shown in which the required energy calculation is corrected due to divergence using an embodiment of our method implemented in an exemplary embodiment of the controller 3 . Burner gas flow rate, furnace rotation speed, furnace door position, required energy calculation and flue temperature at image 3 shown in . Initially, the furnace door is open (100%) for charging, with the burners off (0%), the furnace is not spinning (0%), and it can be seen that the flue temperature decreases as it moves to equilibrium with ambient conditions . At time 77, the furnace door is closed and the burners are then opened to 80% firing rate and the furnace is set to 40% rotation speed. Over time, at about 435 time units, the required energy calculation can steadily increase to about 65% of the total required energy (percent complete). At this point, the controller 3 has identified significant deviations from the reference or desired performance. Si...

example 2

[0117] Figure 4 This example shown in shows how the controller 3 can be used to correct for aluminum oxidation (yield) losses when the furnace 2 is used to melt aluminum. In this example, the controller defines a regression equation that relates production loss (y variable) to a data parameter (x variable) to mitigate production loss during a given cycle of the furnace. Generally, due to the nature of the melting process, it is expected that the aluminum will always oxidize to some extent during cycling. A regression model was defined to be used by the controller 3 to compare the performance of the field cycle to a reference case to determine the extent to which aluminum oxidation occurred throughout the cycle. In this exemplary case, the reference cycle was considered to experience minimal aluminum oxidation. When significant aluminum oxidation is identified, corrective measures are taken where typically the firing rate of the burners and / or the rotational speed of the furna...

example 3

[0121] To help further demonstrate the improved performance that embodiments of the controller 3 can provide, refer to Figure 6 to Figure 8 A sample from nearly 700 cycles of an aluminum tilting rotary furnace is discussed as an example. In the third step S3 of this method in the present example, the materials were characterized into 9 different material groups. The expected aluminum content range for these material groups is between 20 and 80% aluminum. The number of cycles in each material group ranged from 25 to 86 cycles, and the percentage of aluminum in each material did not vary by more than + / - 5% of the average aluminum content.

[0122] The y-variable selected in step S6 of the embodiment of the method of the present example was the aluminum oxidation (yield) loss, and the resulting statistical model showed that there were multiple x-variable parameters that significantly affected the yield loss, including that of the salt used. Ratio, aluminum and oxide content i...

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PUM

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Abstract

A control scheme for a furnace can use real-time and historical data to model performance and determine relationships between different data and performance parameters for use in correcting suboptimal performance of the furnace in real-time. Operational parameters can be logged throughout the cycle for all cycles for a period of time in order to establish a baseline. This data can then be used to calculate the performance of the process. A regression analysis can be carried out in order to determine which parameters affect different aspects of performance. These relationships can then be used to predict performance during a single cycle in real-time and provide closed or open loop feedback to control furnace operation to result in enhanced performance.

Description

technical field [0001] The present invention relates to controllers configured to facilitate controlling the operation of furnaces for melting metal-bearing materials and methods of making and using the same. Background technique [0002] Secondary metal recycling and reprocessing processes may involve the melting of metal scrap from different sources and upstream processes. Recycled waste often varies widely in shape, size and composition. This high degree of inconsistency in the input scrap material must be resolved during the melting process. Consequently, the energy requirements of furnaces for metal recovery or reprocessing may often vary frequently from melt to melt. This can lead to high variability in the furnace's operating efficiency and production rate. Losses due to process variability can be magnified when operators operate multiple furnaces simultaneously. [0003] Examples of secondary metal recovery processes are known from US Patent No. 4,484,947 and US ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F27B14/20C22B7/00C22B13/02C22B15/00C22B21/00G05B19/418
CPCF27B7/42C22B7/00F27D2019/0003F27B14/20G05B19/41875C22B7/001C22B15/003C22B21/00C22B13/025F27D19/00F27D21/00F27B9/28Y02P10/20F27B3/28F27D21/0028C22B1/005C22B7/003C22B21/0092C03C1/002C03B3/026C03B5/225F27D2019/0006F27D2019/0028F27D2019/0087
Inventor M·劳伦斯A·古哈R·J·亨德肖特
Owner AIR PROD & CHEM INC