Method for co-producing biogas-oil-carbon by coupling anaerobic fermentation of kitchen waste with straw pyrolysis
A technology for anaerobic fermentation and kitchen waste, applied in fermentation, preparation of liquid hydrocarbon mixture, petroleum industry, etc., can solve the problems of incomplete treatment of organic waste, ineffective utilization, low methane purity, etc. The effect of large-scale promotion and utilization, realization of resource utilization, and improvement of biogas yield and concentration
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Embodiment 1
[0040] Process such as figure 1 shown;
[0041] The food waste is crushed, and then sent to the anaerobic fermentation reactor for anaerobic fermentation reaction to generate biogas, biogas residue and biogas slurry; the solid mass content of the food waste is 28%; the temperature of the anaerobic fermentation reaction is 30~ 40°C for 35 days;
[0042] The biogas residue and biogas slurry are discharged from the anaerobic fermentation reactor, and after solid-liquid separation, the biogas slurry is mixed with the crushed food waste, and enter the anaerobic fermentation reactor together; the biogas slurry and the crushed food waste The mixing ratio is 1:2 by mass ratio;
[0043] Mix biogas residue and straw, crush, dry and remove water, and then put it into a pyrolysis reactor to generate synthesis gas, pyrolysis liquid and biochar through pyrolysis reaction; the mixing ratio of biogas residue and straw is 1:2 by mass ; The temperature of the pyrolysis reaction is 700°C, and...
Embodiment 2
[0050] Method is with embodiment 1, and difference is:
[0051](1) The solid mass content of kitchen waste is 39%; the anaerobic fermentation reaction time is 25 days;
[0052] (2) The mixing ratio of biogas slurry and crushed kitchen waste is 1:3 by mass ratio;
[0053] (3) The mixing ratio of biogas residue and straw is 1:3 by mass; the temperature of pyrolysis reaction is 600°C, and the time is 2h;
[0054] (4) The amount of biochar added is 15g per liter of kitchen waste in the anaerobic fermentation reactor;
[0055] (5) The amount of the small molecule solution added is 2g per liter of kitchen waste in the anaerobic fermentation reactor;
[0056] Biogas yield was 75%.
Embodiment 3
[0058] Method is with embodiment 1, and difference is:
[0059] (1) The solid mass content of kitchen waste is 22%; the anaerobic fermentation reaction time is 40 days;
[0060] (2) The mixing ratio of biogas slurry and crushed kitchen waste is 1:1 by mass ratio;
[0061] (3) The mixing ratio of biogas residue and straw is 1:1 by mass; the temperature of pyrolysis reaction is 800°C, and the time is 1h;
[0062] (4) The amount of biochar added is 20g per liter of kitchen waste in the anaerobic fermentation reactor;
[0063] (5) The amount of the small molecule solution added is 1g per liter of kitchen waste in the anaerobic fermentation reactor;
[0064] The biogas yield is 80%.
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