Calcium carbide furnace tail gas dry dedusting, waste heat recovery and synthesis gas production device
A technology for recovering exhaust gas and waste heat from a calcium carbide furnace, which is applied to combined devices, furnaces, waste heat treatment, etc., can solve the problems of high water and energy consumption, difficult sewage, and difficulty in ensuring the stable operation of the system and meeting the purification requirements. The effect of advanced technology, high temperature calcium carbide furnace tail gas energy and resource recovery efficiency maximization
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specific Embodiment 1
[0053] A 200,000-ton / year calcium carbide production line in a certain factory is equipped with two 48,000KVA sealed calcium carbide furnaces, and the total normal flow rate of the calcium carbide furnace tail gas is 11,000Nm 3 / h, the temperature is normally 400-600°C, and the exhaust gas composition and dust characteristics are shown in Table 1, Table 2, and Table 3:
[0054] Table 1. Composition of calcium carbide furnace exhaust gas
[0055] name
CO
H 2
CO 2
N 2
O 2
other
dust
Content (V%)
70~90
2~6
1~3
2~5
0.2~1
~1
120g / Nm 3
[0056] Table 2. Composition of dust carried by the tail gas of calcium carbide furnace
[0057] Dust composition
CaO
C
SiO 2
Fe 2 o 3
Al 2 o 3
other
Percentage (W%)
37.2
34.1
15.8
0.96
7.1
~4.84
[0058] Table 3. Particle size distribution of dust carried by calcium carbide furnace ta...
specific Embodiment 2
[0067] A 200,000-ton / year calcium carbide production line in a certain factory is equipped with a complete set of equipment for regenerative calcium carbide production. This device produces H 2 ≈8700Nm 3 / h, the matching of the closed calcium carbide furnace is similar to that of Example 1, and the output and composition properties of the calcium carbide tail gas are also similar to those of Example 1. In this example, the ratio of CO gas recovered from the calcium carbide furnace tail gas and the ratio of by-product hydrogen to carry out methanation reaction The production of LNG is 22,000 tons / year.
[0068] The production scheme of this example is similar to that of Example 1, the difference is that this example does not have a calcium carbide tail gas composition reforming system 3 after the high-temperature calcium carbide tail gas dedusting system, and all effective CO gases pass through the high-temperature calcium carbide tail gas waste heat recovery system 4 and low-t...
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