Process technology and device for simultaneously recovering various gases such as hydrogen and methane gas from petrochemical exhaust gas emissions
A process technology, tail gas technology, applied in membrane technology, gas treatment, chemical instruments and methods, etc., can solve the problem of undisclosed hydrogen-pressure swing adsorption, etc., and achieve the effect of saving energy consumption and improving production efficiency
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Embodiment 1
[0099] Separating and recovering hydrogen and hydrocarbon gases from the tail gas of Sinopec C2-PSA unit, and producing gas with higher calorific value.
[0100] The exhaust gas composition of the C2-PSA unit is as follows (in actual operation, the exhaust gas composition often has a fluctuation range of 10%):
[0101]Table 1 Components of exhaust gas from C2-PSA plant
[0102]
[0103] According to the parameters listed in Table 3 and Table 4 use such as figure 1 Shown gas separation and recovery process technology of the present invention, use such as figure 2 The device shown, such as image 3 The shown CHx-VSA adsorption tower operating steps and process cycle design and Figure 4 Shown H 2 - PSA adsorption tower operation steps and process cycle design to separate the above-mentioned tail gas. Wherein, the number of adsorption towers in the CHx-VSA device is 4, and the diameter of the adsorption towers in each CHx-VSA device is 30 centimeters, and the working len...
Embodiment 2
[0106] Separation and recovery of hydrogen and hydrocarbon gases from the tail gas of Sinopec's similar C2-PSA plant system, and produce gas with higher calorific value.
[0107] The exhaust gas composition in this example is as follows (in actual operation, the exhaust gas composition often has a fluctuation range of 10%):
[0108] Table 2 Exhaust gas components emitted by similar C2-PSA devices
[0109]
[0110] According to the parameters listed in Table 3 and Table 4 use such as figure 1 Shown gas separation and recovery process technology of the present invention, such as figure 2 The device shown, such as image 3 The shown CHx-VSA adsorption tower operating steps and process cycle design and Figure 4 Shown H 2 - PSA adsorption tower operation steps and process cycle design to separate the above-mentioned tail gas. Wherein, the number of adsorption towers in the CHx-VSA device is 4, and the diameter of the adsorption towers in each CHx-VSA device is 300 centime...
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