High-temperature semicoke grinding system and grinding method
A high-temperature semi-coke and high-temperature technology, which is applied in the field of high-temperature semi-coke grinding systems, can solve the problems of large cooling water consumption, increase semi-coke production costs, and limit material temperature, so as to simplify the production process, improve grinding efficiency, Reduce the effect of intermediate links
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Embodiment 1
[0090] This embodiment proposes a high-temperature semi-coke grinding system and grinding method. The lignite is dried and then enters the pyrolysis furnace to generate semi-coke. After the powder enters the pulverized coal boiler for combustion, steam is sent to the steam turbine to generate electricity. The technical data of lignite are shown in Table 1:
[0091] Table 1: Technical data of lignite:
[0092]
[0093] The amount of lignite coal is designed to be 120t / h, and it enters the dryer through the feeder. After drying, the moisture Mt of the lignite is ≤ 10%, and then enters the pyrolysis furnace for pyrolysis.
[0094] Semi-coke is produced after lignite pyrolysis, the output is 65t / h, the semi-coke outlet temperature is 700°C, and the semi-coke parameters are as follows:
[0095] Table 2: High temperature semi-coke parameters
[0096]
[0097] The high-temperature semi-coke and the raw coal in the raw coal bunker enter the coal mill according to the ratio of 2...
Embodiment 2
[0104] This embodiment is the same as the system used in the above-mentioned embodiment 1, but the process conditions are different, as described below. The technical data of lignite are shown in Table 1:
[0105] Table 1: Technical data of lignite:
[0106]
[0107] The amount of lignite coal is designed to be 110t / h, and it enters the dryer through the feeder, and the moisture Mt of the dried lignite is ≤ 10%, and then enters the pyrolysis furnace for pyrolysis.
[0108] Semi-coke is produced after lignite pyrolysis, the output is 60t / h, the semi-coke outlet temperature is 900°C, and the semi-coke parameters are as follows:
[0109] Table 2: High temperature semi-coke parameters
[0110]
[0111] The high-temperature semi-coke and the raw coal in the raw coal bunker enter the coal mill at a ratio of 1:1. The raw coal parameters in the raw coal bunker are as follows:
[0112] Table 3 Basic data of raw coal in raw coal bunker
[0113]
[0114] After entering the c...
Embodiment 3
[0118] This embodiment is the same as the system used in the above-mentioned embodiment 1, but the process conditions are different, as described below. The technical data of lignite are shown in Table 1:
[0119] Table 1: Technical data of lignite:
[0120]
[0121] The amount of lignite coal is designed to be 100t / h, and it enters the dryer through the feeder, and the moisture Mt of the dried lignite is ≤ 10%, and then enters the pyrolysis furnace for pyrolysis.
[0122] Semi-coke is produced after lignite pyrolysis, the output is 60t / h, the semi-coke outlet temperature is 700°C, and the semi-coke parameters are as follows:
[0123] Table 2: High temperature semi-coke parameters
[0124]
[0125] The high-temperature semi-coke and the raw coal in the raw coal bunker enter the coal mill at a ratio of 1:2. The raw coal parameters in the raw coal bunker are as follows:
[0126] Table 3 Basic data of raw coal in raw coal bunker
[0127]
[0128] After entering the c...
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