The invention discloses a fresh
zanthoxylum oleoresin separation and purification process which comprises the following steps: after harvesting fresh
zanthoxylum, carrying out cold pressing within two hours to obtain fresh
zanthoxylum oleoresin, carrying out countercurrent extraction separation on the fresh zanthoxylum
oleoresin through a liquid substance extraction and separation unit of a supercritical CO2 fluid dynamic countercurrent extraction and
separation system, and after the countercurrent extraction separation is completed, obtaining fresh zanthoxylum resin from an extraction unit, and obtaining the fresh pepper
essential oil through the separation unit. The extraction
separation process is as follows: the feeding rate is 40kg / h, the CO2 flow rate is 600L / h, the extraction temperature is 45 DEG C, and the extraction pressure is 20MPa; the separation temperature I is 40 DEG C, the separation pressure I is 7.5 MPa, the separation temperature is 55 DEG C, and the separation pressure II is 4-6 MPa; the total yield of the fresh zanthoxylum oil resin product reaches 98.74%-99.19%, and the separation efficiency reaches 94.00%-99.24%; the volatile
oil content of the obtained fresh
zanthoxylum bungeanum essential oil can reach 101.94-128.93 ml / 100g, and the numb degree is lower than 5 mg / g; and the content of volatile oil in the obtained fresh
zanthoxylum bungeanum maxim resin is smaller than 5 ml / 100 g, the hemp degree can reach 141.12 mg / g to 182.56 mg / g, and the hemp degree is increased to 42.59% to 53.17%. According to the process disclosed by the invention, the fresh Chinese prickly ash
essential oil with high volatile
oil content and the fresh Chinese prickly ash resin with high numb degree can be obtained, and the purification effect of the two products is remarkable.