Method for removing kitchen grease by using calcium stearate generated through phase-split anaerase hydrolysis
A technology of calcium stearate and anaerobic enzyme, applied in fermentation and other directions, can solve the problems of complicated steps, harsh requirements, increased processing cost, etc., to improve the efficiency of anaerobic digestion, reduce the inhibitory effect, and realize the recycling of resources. Effect
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Embodiment 1
[0033] A. The kitchen waste used in the experiment was taken from the canteen of Beijing University of Chemical Technology. After manual sorting, the kitchen waste was crushed with a pulverizer and stored in a refrigerator at 4°C for later use.
[0034] The basic properties of the raw materials were determined, and the specific results are shown in Table 1.
[0035] Table 1
[0036] Determination index
TS%
VS%
pH
TCOD mg / L
SCOD mg / L
Grease %
Ca 2+ mg / kg
18.60
17.01
5.34
172.93
88.26
23.5
3356.1
9.21%
5.23%
7.60
119.17
-
-
-
[0037] B. Put the food waste into the acidification reactor for anaerobic digestion according to the organic load of 30gVS / L. The acidification reactor is a 5L CSTR. (VS) / inoculum (VS) =2 Add anaerobic mud, acclimate for 5 days in a water bath at a temperature of 35°C,
[0038] C. Fee...
Embodiment 2
[0041] Steps A and B are the same as in Example 1.
[0042] C. From the 6th day onwards, feed and discharge once a day, according to the organic load of 4gVS / L d, 6gVS / L d, 8gVS / L d, 10gVS / L d, run twice under each load condition hydraulic retention time. Finally, the long-term operation is maintained at 10gVS / L·d. At this time, the daily food waste feeding amount of the acidification reactor is 200-250g.
[0043] D. The methane item reactor is a 10L CSTR reactor. The above-mentioned output is added to the reactor, the initial feed load is 2.0gVS / L·d, and the water retention time is 20 days, and then the load is respectively raised to 3.0gVS / L. L d, 4.0gVS / L d, 5.0gVS / L d, run 20 hydraulic retention times under each load condition to keep it consistent with the operating load of the acidification phase reactor, and run at 5.0gVS / L d Long-term operation under high load.
[0044] During the whole process, the volumetric gas production of the methane phase increased from 1.0L / ...
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