Method for protecting storage tank safety by using sulfur recovery tail gas
A sulfur recovery and tail gas technology, which is applied in combustion methods, separation methods, chemical instruments and methods, etc., can solve problems such as the safe use of sulfur-containing oily sewage tanks or sulfur-containing oil tanks, and the effective removal of hydrocarbons. To achieve the effect of low operating cost, comprehensive utilization and low cost
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Embodiment 1
[0016] A company has an acid water (sulphur-containing and ammonia-containing sewage) storage tank. According to the operating conditions, the maximum amount of "small breath" is 30Nm 3 / h, its maximum feed rate is 70Nm 3 / h, the maximum output rate is 40Nm 3 / h. Use the SCOT tail gas of the sulfur recovery unit as the positive pressure protective gas, and the gas composition is: H 2 S 0.03% (V), COS50μL / L, CS 2 10 μL / L, CO 2 34% (V), H 2 0.6% (V), H 2 O 7.0% (V), the rest is N 2 . The protective gas flow into the tank is 200 Nm 3 / h, the flow rate of positive pressure protection gas discharged from the tank is 130~300Nm 3 / h, the content of benzene and toluene in the exhaust gas is as high as (0.5~3.0)×10 4 mg / m 3 , the total hydrocarbon concentration is as high as (0.5~5.0)×10 5 mg / m 3 , H 2 S 0.01~0.05% (V), dimethyl disulfide 20~60mg / m 3 , other components such as COS, CS 2 , CO 2 , H 2 , H 2 O, N 2 It is slightly lower than the intake concentration....
Embodiment 2
[0018] A company has a delayed coking sulfur-containing sewage storage tank. According to the operating conditions, the maximum amount of "small breath" is 50Nm 3 / h, the maximum feed rate is 50Nm 3 / h, the maximum output rate is 50Nm 3 / h. Use the SCOT tail gas of the sulfur recovery unit as the positive pressure protective gas, and the gas composition is: H 2 S 0.03% (V), COS 50μL / L, CS 2 10 μL / L, CO 2 34% (V), H 2 0.6% (V), H 2 O 7.0% (V), the rest is N 2 . The protective gas flow into the tank is 200 Nm 3 / h, the flow rate of positive pressure protection gas discharged from the tank is 100-300 Nm 3 / h, the total hydrocarbon concentration in the exhaust gas is as high as (2~6)×10 5 mg / m 3 , H 2 S 0.01~0.04% (V), dimethyl disulfide 20~60mg / m 3. Exhaust gas is incinerated in the tail gas incinerator of the existing sulfur recovery unit. In the presence of an appropriate amount of fuel gas and air, the temperature of the incineration furnace is 550-650°C, and ...
Embodiment 3
[0020] According to the conditions and methods described in Example 2, the exhaust gas enters the tail gas catalytic incinerator of the existing sulfur recovery device for incineration, and adopts SiO 2 As a supported V / Fe / Ag catalyst, containing V by weight 2 o 5 4.5%, Fe 2 o 3 4.0%, Ag 1.0%, bed space velocity 5000~10000h -1 , the bed temperature is 350-430°C, the SO in the incineration flue gas 2 Less than 0.03% (V), in line with national emission standards.
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