Device and process for producing liquid hydrocarbon products from biomass
A technology for liquid hydrocarbons and biomass, which is applied in the field of Fischer-Tropsch synthesis to produce liquid hydrocarbon products, can solve the problems of increasing the tail gas discharge of the second-stage device, the complicated water-gas shift process, and reducing the system economy. The effect of reducing energy consumption and reducing investment
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Embodiment 1
[0040]The composition of crude syngas produced from biomass fuel is shown in Table 1, H 2 / CO volume ratio is 0.8:
[0041] Table 1 Composition of crude syngas produced from biomass
[0042] composition Volume content v% H 2
34 CO 42 CO 2
19 CH 4
2 N 2
3
[0043] The main process operating conditions are set as follows:
[0044] 1. The mixing volume ratio of recycle gas and crude synthesis gas is 3.5:1;
[0045] 2. The operating temperature of the Fischer-Tropsch synthesis reactor (gas synthesis unit 3) is 250°C;
[0046] 3. The operating pressure of the Fischer-Tropsch synthesis reactor is 2.5Mpa.
[0047] H in the refined synthesis gas required by gas synthesis unit 3 2 With a volume ratio of 1.2 to CO, the effective syngas H in the refined syngas 2 and CO(H 2 +CO) accounts for 50% of the total gas volume of the refined synthesis gas;
[0048] Each ton of biomass fuel can produce 53kg of liquid hydrocarbon pro...
Embodiment 2
[0050] The composition of crude syngas produced by biomass fuel is shown in Table 2, H 2 / CO volume ratio is 0.9:
[0051] Table 2 Composition of crude syngas produced from biomass
[0052] composition Volume content v% H 2
36 CO 40 CO 2
20 CH 4
2 N 2
2
[0053] The main process operating conditions are set as follows:
[0054] 1. The mixing volume ratio of recycle gas and crude synthesis gas is 2.5:1;
[0055] 2. The operating temperature of the Fischer-Tropsch synthesis reactor (gas synthesis unit 3) is 270°C;
[0056] 3. The operating pressure of the Fischer-Tropsch synthesis reactor is 3.5Mpa;
[0057] H in the refined synthesis gas required by gas synthesis unit 3 2 With a volume ratio of 1.1 to CO, the effective syngas H in the refined syngas 2 and CO(H 2 +CO) accounts for 45% of the total gas volume of the refined synthesis gas;
[0058] The liquid hydrocarbon product that can be produced per ton of bioma...
Embodiment 3
[0060] The composition of crude syngas produced by biomass fuel is shown in Table 3, H 2 / CO volume ratio is 1.0:
[0061] Table 3 Composition of crude syngas produced from biomass
[0062] composition Volume content v% H 2
37 CO 37
[0063] CO 2
20 CH 4
2 N 2
4
[0064] The main process operating conditions are set as follows:
[0065] 1. The mixing volume ratio of recycle gas and crude synthesis gas is 2.8:1;
[0066] 2. The operating temperature of the Fischer-Tropsch synthesis reactor (gas synthesis unit 3) is 280°C;
[0067] 3. The operating pressure of the Fischer-Tropsch synthesis reactor is 3.0Mpa.
[0068] H in the refined synthesis gas required by gas synthesis unit 3 2 With a volume ratio of 1.4 to CO, the effective syngas H in the refined syngas 2 and CO(H 2 +CO) accounts for 55% of the total gas volume of the refined synthesis gas;
[0069] The liquid hydrocarbon product that can be produc...
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