A method for extracting capsaicin and capsanthin from capsicum oleoresin
A technology of capsicum oleoresin and capsanthin, applied in chemical instruments and methods, natural dyes, azo dyes, etc., can solve problems such as environmental pollution, high labor intensity, incomplete extraction, etc., to eliminate environmental pollution and improve labor efficiency. Efficiency, the effect of reducing energy consumption
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Publication Date
- 2015-10-21
Smart Images
Figure 1
Abstract
Description
technical field
[0001] The invention relates to a method for extracting capsaicin and capsanthin from capsicum oleoresin. Background technique
[0002] The prior art mostly uses single-phase or two-phase solvent extraction to separate capsaicin and capsanthin products in capsicum oleoresin. This extraction method has low efficiency and incomplete extraction, and the obtained products often contain various impurities. From the perspective of production efficiency, this method is inefficient, time-consuming and labor-intensive, and the labor intensity of workers is high. The organic solvent used in the production process is easy to leak, which will cause environmental pollution when the production safety is seriously endangered. The capsanthin product produced in the prior art may partially decompose, and the produced capsaicin product and capsanthin product are unstable in dissolved quality.
[0003] Therefore, in order to solve the above technical problems, it is necessary ...
Examples
Embodiment Construction
[0013] The present invention is described in further detail now in conjunction with accompanying drawing. Accompanying drawing is a simplified process flow chart, only schematically illustrates the basic process flow of the present invention.
[0014] Specific implementation one: please refer to figure 1 , a method for extracting capsaicin and capsanthin from capsicum oleoresin, the steps comprising:
[0015] (1), capsicum oleoresin 11 is made into preliminary dilution solution with diluent n-hexane in batching tank-1, wherein the volume ratio of capsicum oleoresin and diluent n-hexane is 1: 5;
[0016] (2), adding extractant methanol aqueous solution in batching tank two 2, the initial dilution solution prepared in step 1 and extractant methanol aqueous solution are transported in the cooler 3 according to the volume ratio 1:5;
[0017] (3), control the temperature of the cooling solution coming out of the cooling machine 3 between 25°C, send the cooling solution coming out...