Novel technology for preparing biodiesel by virtue of low-temperature enzyme fermentation method
A biodiesel and low-temperature technology, applied in the field of oil chemistry, can solve the problems of high cost of separation and purification and enzyme immobilization, low conversion rate of biodiesel, and difference in high temperature resistance of lipase, and achieve low cost, short production cycle and excellent reaction conditions mild effect
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Embodiment 1
[0017] Example 1: A new process for preparing biodiesel by low-temperature enzymatic fermentation, which includes the following steps:
[0018] S1. Put the solidified hogwash oil with an oil content of 95% in the drying room, and use a hot air stove to quickly increase the temperature of the drying room to 145°C, so that the hogwash oil becomes a flowing liquid;
[0019] S2. Put the liquid hogwash oil into the No. 1 reactor with an oil pump, add 1.5% No. 1 biological enzyme composite catalyst in the No. 1 reactor, and the weight ratio of the liquid hogwash oil to the No. 1 biological composite catalyst is 48:1 , reacted for 50min to obtain liquid A, wherein No. 1 biological enzyme composite catalyst was a mixture of lipase and iron sulfate, and its weight ratio was 0.8:1, and the lipase was a lipase produced by bacteria;
[0020] S3. Separating liquid A with a high-speed centrifuge, the rotating speed of the centrifuge is 11000rmp, and the centrifugation time is 30min to remo...
Embodiment 2
[0024] Example 2: A new process for preparing biodiesel by low-temperature enzymatic fermentation, which includes the following steps:
[0025] S1. Put the solidified acidified oil with an oil content of 98% in the drying room, and use a hot air stove to quickly increase the temperature of the drying room to 155°C, so that the acidified oil becomes a flowing liquid;
[0026] S2. Pump the liquid acidified oil into the No. 1 reactor, add 2.5% No. 1 biological enzyme composite catalyst to the No. 1 reactor, and the weight ratio of the liquid acidified oil to the No. 1 biological composite catalyst is 55:1 , reacted for 80min to obtain liquid A, wherein No. 1 biological enzyme composite catalyst was a mixture of lipase and iron sulfate, and its weight ratio was 1.2:1, and the lipase was produced by animal pancreas;
[0027] S3. Liquid A is separated with a high-speed centrifuge, the rotating speed of the centrifuge is 13000rmp, the centrifugation time is 40min, and the residue a...
Embodiment 3
[0031] Example 3:A new process for preparing biodiesel by low-temperature enzymatic fermentation, which includes the following steps:
[0032] S1. Put the solidified waste oil with an oil content of 97% in the drying room, and use a hot air stove to quickly increase the temperature of the drying room to 150°C, so that the waste oil becomes a flowing liquid;
[0033] S2. Put the liquid waste oil into the No. 1 reactor with an oil pump, add 2% No. 1 biological enzyme composite catalyst in the No. 1 reactor, and the weight ratio of the liquid waste oil to the No. 1 biological composite catalyst is 50:1 , and reacted for 60min to obtain liquid A, wherein No. 1 biological enzyme composite catalyst is a mixture of lipase and iron sulfate, and its weight ratio is 1:1, and the lipase is a compound produced by bacteria, fungi and animal pancreas. immobilized enzyme;
[0034] S3. Liquid A is separated with a high-speed centrifuge, the rotating speed of the centrifuge is 12000rmp, the...
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