A kind of method extracting athomin in horseradish
Technical field
The present invention relates to the extracting method of athomin, be specially a kind of method extracting athomin in horseradish.
Background technology
Athomin be from Cruciferae Armoracia per nnial herb horseradish (
armoracialapathifoliagilib.) the class secondary metabolite extracted in, has the liquid of volatility, oily at normal temperatures.Athomin, containing-N=C=S group in chemical structure, is isosulfocyanate compound.There is the effects such as antitumor, sterilization, desinsection.At present, the method for extraction and isolation athomin mainly contains steam distillation, ultrasonic extraction, supercritical fluid extraction and macroporous resin column chromatography etc.
Steam distillation refers to the vegetable material containing volatile component and water condistillation, and volatile component is steamed in the lump with water vapour, divides the leach extraction method getting volatile component through condensation.This method is applicable to have volatility, can be destroyed with wet distillation, stablizes and the extraction of indissoluble or water-fast active components of plants in water.Steam distillation is the method that extraction athomin is commonly used the most, find in previous experiments process, the method has certain limitation, need follow-up purifying, athomin in distillate may have part volatilization in long still-process, cause extraction yield to decline, extraction time is long in addition.
Ultrasonic extraction utilizes hyperacoustic cavatition, mechanical effect and heat effect etc. to accelerate the release of active substance in born of the same parents, diffusion and dissolving, significantly improves the extracting method of extraction efficiency.Previous experiments finds, it is low that the method extracts athomin efficiency, and along with the increase of ultrasonic time, the content of athomin reduces, and may be that in supersound extraction process, water temp raises, part athomin is volatilized.In addition, there will be the phenomenon that in extracting solution, athomin is saturated.
Supercritical liquid extraction technique is lower to water soluble component dissolving power comparatively by force to fat-soluble component dissolving power; Equipment manufacturing cost is higher and cause the depreciation of equipment ratio in product cost excessive; Will under high pressure carry out in operating process, process specifications is high; During replacing product, cleaning equipment is more difficult.
Adopt macroporous resin to the athomin in horseradish, carry out extraction purification.Macroporous resin needs pre-treatment, wash-out need be carried out respectively with bronsted lowry acids and bases bronsted lowry solution, complex operation, in residual macroporous resin, unconverted monomer, perforating agent, initiator and the oil-soluble impurities such as resolvent, dispersion agent thereof may affect the extraction purification of athomin, are unfavorable for large-scale industrial production.
Summary of the invention
Technical problem solved by the invention is to provide a kind of method extracting athomin in horseradish, to solve the shortcoming in above-mentioned background technology.
Technical problem solved by the invention realizes by the following technical solutions: a kind of method extracting athomin in horseradish, comprises following three steps;
1) described horseradish pre-treatment: horseradish is placed on 35-45
ocarry out drying in the low temperature environment of C, then undertaken being ground into meal by pulverizer by dried horseradish, described meal can all by 10 mesh sieves, but not by 50 mesh sieves;
2) preparation of described Extraction solvent: by ethyl acetate-water in proportion 1:10-1:20 carry out being mixed with solution, then in described solution, add sodium-chlor, the sodium-chlor added accounts for the 1-2% of whole described liquor capacity;
3) distillation extraction step: by the meal in step 1) made by horseradish and step 2) described in solvent according to the ratio of solid-liquid ratio 1:10-1:30, join in matrass, distillation temperature is 85-95
oc, under normal atmospheric pressure, distillation 1-2 hour, collects the distillate in matrass, obtains purity and can reach more than 95% athomin (area normalization method), be illustrated in fig. 1 shown below.
Beneficial effect of the present invention: adopt ethyl acetate-water-sodium-chlor to be Extraction solvent, carry out wet distillation extraction.The boiling point of ethyl acetate is lower, extracts, greatly can shorten extraction time, by the 3-4 hour of simple steam distillation, shorten to 1-2 hour with traditional by the wet distillation that water is solvent.In addition, steam distillation needs to carry out chromatographic separation or solvent extraction to distillate, carry out purifying, and adopt ethyl acetate-water-sodium-chlor distillation and extraction method a step can complete the process of extraction purification, and distillate is stable under the parcel of ethyl acetate.In addition, present method is easy and simple to handle, technique is simple, cost is low, be applicable to large-scale technology produces.
Accompanying drawing explanation
fig. 1 isthe color atlas of horseradish extracting solution;
Fig. 2 is dichloromethane extraction efficiency comparison color atlas;
Fig. 3 is extraction into ethyl acetate efficiency comparison color atlas;
Fig. 4 is the color atlas that wet distillation extraction method compares with ultrasonic extraction.
Embodiment
The technique means realized to make the present invention, creation characteristic, reaching object and effect is easy to understand, setting forth the present invention further below.
Embodiment: by horseradish after cleaning, removal of impurities, at 35-45
oc cryodrying, is ground into meal, and all by No. 1 sieve, but can not cross No. 3 sieves, No. 1 sieve is 10 orders, and No. 3 sieves are 50 orders.
The preparation of Extraction solvent: the ratio of ethyl acetate-water is 1:10-1:20, the weight of adding sodium-chlor is the 1-2% of liquor capacity.
Be transferred in matrass by horseradish and Extraction solvent, distillation extraction, temperature controls at 85-95
oc, under atmospheric pressure, distillation 1-2 hour, collects distillate, obtains upper strata ethyl acetate portion, obtains athomin purity and can reach more than 95% (area normalization method).
The preparation of said extracted solvent: normal hexane, methylene dichloride, ethyl acetate, ethanol are screened, found that the extraction efficiency of ethyl acetate to athomin is the highest, for methylene dichloride and ethyl acetate, Fig. 2 and Fig. 3 is the color atlas that methylene dichloride compares with the extraction efficiency of ethyl acetate.In addition, screening is optimized to the ratio of ethyl acetate-water, finds to extract athomin completely between 1:10-1:20, add the solution that sodium-chlor prevents ethyl acetate and water, in leaching process, produce emulsion.
The screening of extracting mode, compares steam distillation and ultrasonic extraction.Wet distillation extraction method, gets horseradish meal 5g, accurately weighed, and put in matrass, precision adds water 150mL, and temperature controls 95
oabout C, under atmospheric pressure, distillation 3-4 hour, collects distillate, namely obtains the extracting solution of athomin.Ultrasonic extraction: get horseradish meal 5g, accurately weighed, put in tool plug Erlenmeyer flask, precision adds water 150mL, and under 150W power, supersound process 3-4 hour, temperature controls 30
oabout C, extracting liquid filtering, namely obtains the extracting solution of athomin.Found by the extraction efficiency comparing two kinds of extracting method, wet distillation extraction method extraction efficiency comparatively ultrasonic extraction is high about 2 times, and in ultrasonic extraction extracting solution, foreign matter content is relatively high, as shown in Figure 4.
More than show and describe ultimate principle of the present invention and principal character and advantage of the present invention; the technician of the industry should understand; the present invention is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications; these changes and improvements all fall in the claimed scope of the invention, and application claims protection domain is defined by appending claims and equivalent thereof.