About the size of the slag discharge port of Texaco gasifier
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This post was last edited by dddjie on 2010-2-25 21:19 ha1. Is there any difference between the 2.8M and 3.2M process burners of Texaco gasifier? Can you provide a drawing of its aperture, length and other dimensions? 2. Can you provide a drawing of the hole diameter, length and other dimensions of the opposed multi-nozzle gasifier burner? 3. How to determine the inner diameter of the slag discharge port? What is it closely related to? The amount of coal input? pressure? Will its size affect the gas production rate? 4. As far as I know, the actual steel shell alarm temperatures of various chemical manufacturers are different. What is the basis for determining this temperature? I am not in the chemical industry and am very knowledgeable about certain things, but I serve the coal chemical industry and make refractory materials for gasifier linings. The above knowledge needs to be used when designing lining refractory materials. Learn * This knowledge is provided to serve everyone properly. If anyone is interested in the industry I am engaged in, you can also communicate with me. :handshake This post was last edited by dddjie on 2008-1-19 17:08 ]
What you want is patented or proprietary, so it is probably difficult to achieve. Of course, I hope someone can provide it.
The issue of the size of the slag discharge port should not involve patents, right? For example, the minimum inner diameter of the 2.8M slag discharge port is mostly 525mm, and the minimum inner diameter of the 3.2M gasifier is mostly 737mm, and some are 838mm. 3.4M multi-nozzle gasifier 800mm, what is the basis for this? What is the relationship between the amount of coal input, the pressure in the furnace, and the slag discharge speed? As far as I understand, if the coal input amount is constant, the larger the slag discharge port, the smaller the pressure difference, and the slag discharge speed will also be smaller. I hope you can give me some advice. Of course, as long as patents and leaks are not involved: handshake This post was last edited by dddjie on 2008-1-17 19:40 ]
Can you give me some guidance on the outer diameter of the burner and the length it goes into the furnace?:$
The burner of the GE gasifier is basically flush with the inner wall of the refractory material when it is cold. The burner of the four-nozzle gasifier is about 200~240mm away from the inner wall of the fire-facing brick when it is cold.
The inner diameter of the gasifier is large, which requires a large slag port diameter, which is basically proportional to the relationship. Is the slag port diameter related to the slag discharge speed?