Grease high-pressure hydrolysis production method and production device by recycling sweet water
A production method and technology of a production device, which are applied in the production of fatty acids, preparation/refining of fatty acids, separation of immiscible liquids, etc., can solve the problems of high COD content, high treatment costs, environmental pollution, etc., so as to protect the environment and reduce waste water discharge. , the effect of reducing production costs
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[0026] Example 1
[0027] A production device for high-pressure hydrolysis of fats and oils for recycling sweet water, comprising a hydrolysis tower 4 and a three-effect evaporator connected in sequence; the high-pressure steam 1 is input into the steam inlet of the hydrolysis tower through a pipeline and a steam flow meter 2 is provided on the pipeline Steam one-way valve 3; grease 5 is fed into the grease inlet of the hydrolysis tower through a pipeline, and the pipeline is provided with a grease high-pressure pump 6, a grease flow meter 7, and a grease one-way valve 8.
[0028] The fatty acid 9 (lower density) produced by the hydrolysis reaction is discharged from the top of the hydrolysis tower 4 and exchanges heat with the process water 21 entering the hydrolysis tower; the sweet water 10 (the mixture of glycerin and water with higher density) produced by the hydrolysis reaction is discharged from the hydrolysis tower The bottom is discharged and exchanges heat with the grease...
Example Embodiment
[0031] Example 2
[0032] A production method of high-pressure hydrolysis of fats and oils using sweet water:
[0033] The lard from the external storage tank is pressurized by the grease high-pressure pump 6 and then enters the hydrolysis tower 4 at a flow rate of 8 tons / hour. The process water 21 is pressurized by the process water high-pressure pump 22 and then enters the hydrolysis tower at a flow rate of 5.5 tons / hour. The 6.0MPa high-pressure steam 1 enters the hydrolysis tower at a rate of 1 ton / hour. The lard and process water undergo a hydrolysis reaction at a temperature of 260°C and a pressure of 6.0 MPa to generate 7.925 tons of fatty acids and 6.575 tons of sweet water ( The concentration is 13%); the fatty acid 9 produced by the hydrolysis reaction is discharged from the top of the hydrolysis tower 4 and exchanges heat with the process water 21, and the sweet water 10 produced by the hydrolysis reaction is discharged from the bottom of the hydrolysis tower and exchang...
Example Embodiment
[0035] Example 3
[0036] A production method of high-pressure hydrolysis of fats and oils using sweet water:
[0037] The palm oil from the external storage tank is pressurized by the grease high-pressure pump 6 and then enters the hydrolysis tower 4 at a rate of 10 tons / hour. The process water 21 is pressurized by the process water high-pressure pump 22 and then enters the hydrolysis tower at a flow rate of 6.2 tons / hour. The 6.0MPa high-pressure steam 1 enters the hydrolysis tower at a rate of 1.3 tons / hour. The palm oil and process water undergo a hydrolysis reaction at a temperature of 260°C and a pressure of 6.0MPa to produce 9.85 tons of fatty acids and 7.65 tons of sweet water ( The concentration is 14.3%); the fatty acid 9 produced by the hydrolysis reaction is discharged from the top of the hydrolysis tower 4 and exchanges heat with the process water 21, and the sweet water 10 produced by the hydrolysis reaction is discharged from the bottom of the hydrolysis tower and ex...
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