Mobile-type tail-gas treatment device and method
A tail gas treatment, mobile technology, applied in separation methods, chemical instruments and methods, and dispersed particle separation, etc., can solve the problems of hidden dangers in the adsorption of high-concentration tail gas, unsuitable for refining and chemical enterprises, and pollutants that cannot be recycled. Achieve good industrial application prospects, solve the problem of tail gas emission control, and have the effect of simple structure
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Embodiment 1
[0073] When the aromatics extraction unit of the refinery is shut down, the tail gas is replaced by nitrogen. The tail gas is composed of light hydrocarbon components, mainly including alkanes, olefins, aromatics, ethers and halogenated hydrocarbons. Gas flow rate is 5Nm 3 / h, the operating conditions of the membrane module and low-temperature catalytic oxidation are shown in Table 1 below, and the process results are shown in Table 2.
[0074] Table 1, Device Operating Conditions
[0075] name
temperature
pressure
flow
device entry
20~60℃
Absolute pressure 105~150KPa
1~5Nm 3 / h
Membrane retentate side
30~70℃
Absolute pressure 200~500KPa
0.9~4.5Nm 3 / h
membrane permeate side
30~70℃
Absolute pressure 0.1~15KPa
0.1~0.5Nm 3 / h
Catalytic Oxidation Outlet
260~340℃
Absolute pressure 101~150KPa
1~10Nm 3 / h
[0076] Table 2, process treatment results (gas concentration in vario...
Embodiment 2
[0079] After the catalytic device and the catalytic waste oil storage tank are shut down, the exhaust gas is replaced with nitrogen, and the gas is composed of hydrocarbons produced in crude oil and after catalytic cracking, mainly including alkanes, olefins, aromatics, ethers and halogenated hydrocarbons, hydrogen sulfide, and mercaptans and other sulfur-containing components. Gas flow rate is 10Nm 3 / h, the temperature, pressure, flow and other conditions of each step of the system are shown in Table 3 below, and the results of the main components of the gas after being processed by this process are shown in Table 4.
[0080] Table 3, Device Operating Conditions
[0081] name
temperature
pressure
flow
device entry
10~80℃
Absolute pressure 105~150KPa
8~10Nm 3 / h
Membrane retentate side
30~70℃
Absolute pressure 200~500KPa
7~9.5Nm 3 / h
membrane permeate side
30~50℃
Absolute pressure 0.1~15KPa
0.5~1N...
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