CN117617497A - Extraction process of uric acid reducing component and application of uric acid reducing component in preparation of tortoise jelly - Google Patents
Extraction process of uric acid reducing component and application of uric acid reducing component in preparation of tortoise jelly Download PDFInfo
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Abstract
The invention discloses an extraction process for reducing uric acid components and application thereof in preparing tortoise jelly, and belongs to the technical field of biology. The extraction process provided by the invention comprises the following steps: mixing radix puerariae, leaching solvent and alkaline cellulase, and leaching at 50-70 ℃; the leaching solvent is a mixture of water, alcohol and organic amine; the pH of the leaching solvent is 8-9. The extraction process for uric acid reducing components provided by the invention can effectively improve the extraction efficiency of puerarin in the kudzuvine root, is simple, and is easy to realize and popularize. The invention also provides application of the extraction process in preparation of tortoise jelly.
Description
Technical Field
The invention relates to the technical field of biology, in particular to an extraction process for reducing uric acid components and application thereof in preparation of tortoise jelly.
Background
Uric acid is the final product of the metabolism of purine substances in vivo, and is produced by hypoxanthine and xanthine under the catalysis of xanthine oxidase, and peroxide free radicals are generated. Stable uric acid levels in the body involve a balance between uric acid production, absorption, metabolism and breakdown. Increased uric acid production or decreased uric acid excretion due to disturbed purine metabolism may lead to hyperuricemia. It is believed that a blood uric acid salt level of greater than or equal to 417. Mu. Mol/L may induce hyperuricemia or a range of other symptoms such as gouty arthritis and hyperuricemia nephropathy. Modern medicine has clarified that the onset of gout is directly related to hyperuricemia, and is a serious metabolic disease which endangers human health. Gouty arthritis is a tissue lesion and inflammatory reaction caused by urate deposition in joint capsules, synovium, cartilage, kidneys, subcutaneous tissues and other tissues due to the increase of uric acid in the body, and is mainly characterized by joint swelling, repeated pain attacks and joint flexion and extension disadvantages. Elevated blood uric acid is an important feature of gouty arthritis.
The main cause of the increase in uric acid is the change of dietary structure, and the intake of sugar, protein and fat is obviously increased. At present, common medicines for Western medicine treatment comprise nonsteroidal anti-inflammatory medicines, colchicine, glucocorticoid, probenecid, benzene-australine, allopurinol and the like, and most of the medicines are anti-inflammatory and analgesic medicines, and can quickly relieve pain, stop acute onset of gout, prevent gouty arthritis and gouty kidney stones from forming, but the medicines have serious side effects, such as damage to gastrointestinal tracts with different degrees, liver and kidney dysfunction in serious cases, bone marrow suppression, hepatocyte necrosis, neurotoxic reaction and the like after long-term administration. Researchers have therefore tried to explore traditional Chinese medicine ingredients to reduce uric acid accumulation.
The kudzuvine root has sweet, pungent and cool taste and has rich pharmacological effects, such as reducing vascular resistance, improving blood circulation of heart and brain, reducing heart rate fear, reducing oxygen consumption of cardiac muscle and the like. Clinically, the traditional Chinese medicine composition is commonly used for treating diarrhea, thirst, back pain, defervescence and other diseases caused by spleen deficiency and fever. The research shows that the kudzuvine root has the functions of reducing uric acid and resisting gout, and the action mechanism of the kudzuvine root can be related to improving liver and kidney injury, reducing serum uric acid and reducing the expression of urate transporter proteins in kidney tissues. Further, researches also find that the main component with uric acid reducing effect in the kudzuvine root is puerarin; in order to avoid the burden of other components in the kudzuvine root on the body of a patient, puerarin in the kudzuvine root needs to be extracted by a design method.
Aiming at puerarin, the traditional extraction method mainly comprises a water boiling method, a solvent leaching method, a percolation method and the like. In recent years, new materials and new technologies are continuously applied to traditional Chinese medicine extraction research, such as supercritical fluid extraction, ultrasonic extraction, semi-bionic extraction, cyclone extraction, enzymatic method and the like, and the technologies are still in research and development stages. At present, in actual production, the extraction of the kudzuvine root mostly adopts water extraction and alcohol extraction process route experimental design, and most adopts methods such as single factor design, orthogonal design, uniform design and the like, and optimal process conditions are optimized. Because the kudzu root raw materials in different areas and the experimental conditions are different in each experiment, the optimal technological parameters are greatly different. However, in either method, the extraction efficiency of pueraria is low, for example, the extraction efficiency of puerarin by a conventional percolation method is less than 1.5%, and the extraction efficiency of puerarin by a conventional water boiling method and a solvent leaching method is lower.
In conclusion, how to improve the extraction efficiency of puerarin in kudzuvine root is a key factor affecting the medical exertion of the uric acid reducing effect of puerarin.
Disclosure of Invention
The present invention aims to solve at least one of the technical problems existing in the prior art. Therefore, the invention provides the extraction process for reducing uric acid content, which can effectively improve the extraction efficiency of puerarin, and is simple in extraction process and easy to realize and popularize.
The invention also provides application of the extraction process in preparing uric acid reducing products.
The invention also provides tortoise jelly, and the preparation raw materials of the tortoise jelly comprise uric acid reducing components (puerarin) extracted by the extraction process.
According to an embodiment of the first aspect of the present invention, there is provided an extraction process for uric acid lowering ingredients, the extraction process comprising: mixing radix puerariae, leaching solvent and alkaline cellulase, and leaching at 50-70 ℃;
the leaching solvent is a mixture of water, alcohol and organic amine; the pH of the leaching solvent is 8-9.
The extraction process provided by the embodiment of the invention has at least the following beneficial effects:
(1) The solubility of puerarin in water and alcohol is not very high, which is one factor limiting the extraction efficiency, and the invention adds organic amine into the leaching solvent, and the organic amine reacts with hydroxyl in puerarin to generate alcohol amine at pH of 8-9, so that the solubility of puerarin in the organic solvent is promoted, and the extraction efficiency of puerarin is further improved.
(2) Puerarin is a secondary metabolite of plants, which is present in the nuclear cell matrix inside cells, whereas the cells of pueraria are encapsulated in the cell wall, which is cellulose in composition. The alkaline cellulase adopted by the invention has higher activity under the pH condition of 8-9, and can decompose cell walls, thereby promoting puerarin in cells to be extracted; thereby improving the extraction efficiency of puerarin in the kudzuvine root.
According to some embodiments of the invention, the kudzuvine root may pass through an 80 mesh screen. Thereby increasing the contact area between the kudzuvine root and the leaching solvent and improving the leaching efficiency of uric acid reducing components (including puerarin).
According to some embodiments of the invention, the volume ratio of water to alcohol in the leaching solvent is 1:0.3-4. Considering that the types of the organic amine are different, the reaction product of the organic amine and puerarin is prone to be dissolved in water or alcohol, and the leaching solvent adopted by the invention comprises water and alcohol, so that the proportion of water to alcohol can be adjusted according to the needs in actual production, and the solubility of puerarin in the leaching solvent is improved.
According to some embodiments of the invention, the organic amine comprises at least one of methylamine, ethylamine, and triethylamine. The amount of organic amine added is determined by the pH of the leaching solvent.
According to some embodiments of the invention, a co-solvent is also included in the leaching solvent. Thereby further improving the efficiency of leaching uric acid components.
According to some embodiments of the invention, the co-solvent comprises at least one of PVP, lysine and nicotinamide.
According to some embodiments of the invention, the leaching solvent comprises 1-5 wt% of the co-solvent.
According to some embodiments of the invention, the mass to volume ratio of the kudzuvine root to the leaching solvent is 1g: 5-20 mL.
According to some embodiments of the invention, the alkaline cellulase accounts for 0.1-1% of the kudzuvine root by mass.
According to some embodiments of the invention, the number of leaches is 1-3.
According to some embodiments of the invention, the duration of a single leaching is 1-3 hours.
According to some embodiments of the invention, the leaching method comprises ultrasonic assisted reflux leaching.
According to some embodiments of the invention, the leaching uses ultrasonic waves with a power of 0.3W/cm 2 ~0.5W/cm 2 。
According to some embodiments of the invention, the ultrasonic waves used for the leaching have an ultrasonic frequency of 40kHz to 60kHz.
According to some embodiments of the invention, the extraction filtrate is obtained by sequentially filtering and standing precipitation after the extraction. The filtering can filter large-particle radix puerariae residues, and the standing precipitation can remove radix puerariae starch.
According to some embodiments of the invention, the filtering employs a mesh size of 200 mesh or more.
According to some embodiments of the invention, the length of time of the standing precipitation is 2-5 hours.
According to some embodiments of the invention, the extraction process further comprises, after the leaching, sequentially acidifying and extracting the resulting leaching filtrate.
According to some embodiments of the invention, the pH of the acidified leach liquor is in the range of 5 to 7.
According to some embodiments of the invention, the reagent used for the acidification is an aqueous acid solution. The solute of the aqueous acid solution comprises at least one of hydrochloric acid and oxalic acid. The pH of the acid aqueous solution is 2-4. The acid concentration is not very high, the puerarin and the organic amine can be promoted to form a compound which is converted into puerarin, and the puerarin performance can not be influenced by the excessive acidity.
According to some embodiments of the invention, the extractant used for the extraction comprises at least one of ethyl acetate and n-butanol. The extraction agents can selectively extract puerarin, and the separation ratio of the puerarin is high; the puerarin can be transferred from the leaching filtrate to the extractant by adopting the extractant, and the yield of the extraction step is higher.
According to some embodiments of the invention, the extracted O/a value is 1:2-4. Thereby, the uric acid lowering ingredient can be enriched in the extract phase.
According to some embodiments of the invention, the extracting comprises shaking and standing in sequence. The duration of the oscillation is 10-40 min. The standing time is 1-2 h.
According to some embodiments of the invention, the extraction process further comprises, prior to the acidification, performing a preliminary concentration of the leaching filtrate. The volume after preliminary concentration is 40-70% of the original volume. Therefore, the subsequent acidification and extraction amounts can be reduced, and the consumption of the extractant is saved; furthermore, the alcohol content in the leaching filtrate can be reduced to a certain extent, and mutual dissolution and emulsification between the leaching filtrate and the extractant in the subsequent extraction process are avoided.
According to some embodiments of the invention, the extraction process further comprises concentrating the resulting loaded organic phase after the extraction.
According to some embodiments of the invention, the concentrating comprises concentrating under reduced pressure.
According to some embodiments of the invention, the temperature of the concentration is 50-70 ℃.
According to some embodiments of the invention, the end point of the concentration is extractant-free.
According to some embodiments of the invention, the extraction process comprises the steps of:
s1, mixing kudzuvine root, leaching solvent and alkaline cellulase, and leaching;
the leaching solvent is a mixture of water, alcohol and organic amine, and the pH value is 8-9;
the leaching method comprises ultrasonic assisted reflux leaching;
s2, acidifying the leaching filtrate obtained in the step S1, and extracting an acidified product;
the extractant adopted by the extraction comprises at least one of ethyl acetate and n-butanol;
s3, concentrating the loaded organic phase obtained in the step S2; the concentrated product contains the uric acid reducing component, namely the puerarin.
According to an embodiment of the second aspect of the present invention, an application of the extraction process in preparing uric acid lowering products is provided.
The application adopts all the technical schemes of the extraction process of the embodiment, so that the method has at least all the beneficial effects brought by the technical schemes of the embodiment.
According to some embodiments of the invention, the uric acid reducing product is tortoise jelly. The tortoise jelly comprises uric acid reducing components extracted by the extraction process, so that the tortoise jelly not only has the effects of clearing heat and promoting diuresis and maintaining beauty and keeping young, but also can reduce uric acid and effectively relieve gout.
According to an embodiment of the third aspect of the present invention, there is provided tortoise jelly, wherein the raw materials for preparing the tortoise jelly include uric acid reducing components extracted by the extraction process.
The tortoise jelly adopts all the technical schemes of uric acid reducing components prepared by the extraction process of the embodiment, so that the tortoise jelly has at least all the beneficial effects brought by the technical schemes of the embodiment.
According to some embodiments of the invention, the tortoise jelly further comprises tortoise shell extract, other plant extracts and auxiliary agents.
According to some embodiments of the invention, the plant material of the other plant extract comprises at least one of cassia, hawthorn, red sage, astragalus, tuckahoe, plantain and burdock. Therefore, the other plant extracts can cooperate with uric acid reducing components extracted by the extraction process, and have better uric acid reducing effect.
According to some embodiments of the invention, the uric acid reducing component accounts for 0.1-1 wt% of the tortoise jelly.
According to some embodiments of the invention, the preparation method of the tortoise jelly comprises the following steps:
D1. decocting carapax et Plastrum Testudinis to obtain carapax et Plastrum Testudinis extract;
decocting plant materials to obtain the other plant extracts;
D2. mixing the carapax et Plastrum Testudinis extract and other plant extracts, heating and stirring to paste, and mixing with uric acid reducing component.
According to some embodiments of the invention, in step D1, the mass ratio of the tortoise shell to the plant material is 1:8-10.
According to some embodiments of the invention, in step D1, the duration of the boiling is 1-4 hours.
According to some embodiments of the invention, in step D1, the mass ratio of water to tortoise shell in the boiling is 5-10:1.
According to some embodiments of the invention, in step D1, the mass ratio of water to plant material is 8-10:1.
According to some embodiments of the invention, in step D1, the time period for the decoction is 10-40 min.
According to some embodiments of the invention, in step D2, the auxiliary agent comprises at least one of a flavouring agent and a stabilizer.
The term "about" as used herein, unless otherwise specified, means that the tolerance is within + -2%, for example, about 100 is actually 100 + -2%. Times.100.
Unless otherwise specified, the term "between … …" in the present invention includes the present number, for example "between 2 and 3" includes the end values of 2 and 3.
Additional features and advantages of the invention will be set forth in the description which follows, and in part will be obvious from the description, or may be learned by practice of the invention.
Detailed Description
The conception and the technical effects produced by the present invention will be clearly and completely described in conjunction with the embodiments below to fully understand the objects, features and effects of the present invention. It is apparent that the described embodiments are only some embodiments of the present invention, but not all embodiments, and that other embodiments obtained by those skilled in the art without inventive effort are within the scope of the present invention based on the embodiments of the present invention.
In the description of the present invention, the descriptions of the terms "one embodiment," "some embodiments," "illustrative embodiments," "examples," "specific examples," or "some examples," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the present invention. In this specification, schematic representations of the above terms do not necessarily refer to the same embodiments or examples. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The kudzuvine root used in the embodiment of the invention is collected and prepared according to Chinese pharmacopoeia (2015), and the specific collection place is selected from Shicheng.
Example 1
The example provides an extraction process for reducing uric acid components, which comprises the following specific steps:
s1, mixing kudzuvine root, leaching solvent and alkaline cellulase, and leaching; wherein,
the kudzuvine root is crushed 80 mesh screen lower material;
the leaching solvent is a mixture of water, alcohol and organic amine, and the pH value is 8.5; the volume ratio of the water to the alcohol is 1:2; the organic amine is triethylamine;
the leaching times are 3 times, after each leaching is finished, solid-liquid separation is carried out on the obtained mixed system by using a 200-mesh screen, and then the filtrate is kept stand for 4 hours, so as to obtain leaching filtrate of single leaching;
the alkaline cellulase is purchased from Beijing Soy Bao technology Co., ltd., CAS number is 9012-54-8, product number is C8270, and the dosage is 0.5% of the mass of the kudzuvine root raw material.
The leaching method is reflux leaching assisted by ultrasonic wave; the power of the ultrasonic wave used was 0.4W/cm 2 The frequency is 50kHz; the temperature is 60 ℃, and the duration of single leaching is 1h;
the leaching filtrates of the three leaches were combined and concentrated to 50% of the original volume. The concentration was carried out under reduced pressure at a temperature of 50 ℃.
S2, acidifying the concentrated leaching filtrate obtained in the step S1, and extracting an acidified product; wherein,
the reagent used for acidification is aqueous hydrochloric acid at ph=3.5.
The extractant adopted in the extraction is ethyl acetate; the O/A value is 1:3; the extraction includes shaking for 15min and then standing for 1.5h. Separating to obtain the loaded organic phase.
S3, concentrating the loaded organic phase obtained in the step S2; the obtained concentrated product contains uric acid reducing components including puerarin; wherein the concentration is reduced pressure concentration until the extractant is completely removed.
Example 2
The embodiment provides an extraction process for reducing uric acid components, which is different from embodiment 1 in specific aspects:
in the step S1, the leaching solvent also comprises a cosolvent PVP, and the addition amount of PVP is 2% of the mass of the leaching solvent.
Example 3
The embodiment provides an extraction process for reducing uric acid components, which is different from embodiment 1 in specific aspects:
ph=8 of the leaching solvent, volume ratio of water to alcohol is 1:0.5; the leaching temperature was 70 ℃.
Comparative example 1
The embodiment provides an extraction process for reducing uric acid components, which is different from embodiment 1 in specific aspects:
ph=7 of the leaching solvent.
Comparative example 2
The embodiment provides an extraction process for reducing uric acid components, which is different from embodiment 1 in specific aspects:
the temperature of leaching was 40 ℃.
Comparative example 3
The embodiment provides an extraction process for reducing uric acid components, which is different from embodiment 1 in specific aspects:
the temperature of leaching was 80 ℃.
Comparative example 4
The embodiment provides an extraction process for reducing uric acid components, which is different from embodiment 1 in specific aspects:
the pH of the leaching solvent was adjusted directly with aqueous sodium hydroxide solution at ph=12 without the addition of an organic amine.
Application example 1
The tortoise jelly is prepared by the method, wherein the preparation raw materials comprise uric acid reducing components provided by the examples and the comparative examples; the method comprises the following specific steps:
D1. mixing carapax et Plastrum Testudinis (Brazilian tortoise) and water at a mass ratio of 1:8, and decocting for 3 hr to obtain carapax et Plastrum Testudinis extract;
mixing and decocting plant materials such as fructus crataegi and water at a mass ratio of 1:9 for 30min to obtain other plant extracts;
wherein the mass ratio of the tortoise shell to the hawthorn is 1:9.
D2. Mixing carapax et Plastrum Testudinis extract and other plant extracts, heating and stirring to paste, and mixing with uric acid lowering component; uric acid reducing components account for 0.5 percent of the tortoise jelly by mass.
Application example 2
The tortoise jelly is prepared in this example, and the specific differences from the application example 1 are that:
the preparation raw materials do not comprise uric acid reducing components prepared in examples and comparative examples.
Test example 1
The content of puerarin in uric acid reducing components obtained in examples and comparative examples was tested in this example, and the extraction efficiency of puerarin was calculated. Wherein, the content of puerarin is quantitatively detected by a high performance liquid chromatograph, and the chromatographic conditions are as follows:
chromatographic column: symmetry C18, 250mm x 4.6mm,5 μm;
mobile phase: methanol+36% acetic acid+water=25+3+72 (volume ratio);
flow rate: 0.60mL/min;
detection wavelength: 247nm;
sample injection volume: 10 mu L.
Drawing a standard curve: accurately weighing 20mg puerarin standard substance (accurate to 0.1 mg), dissolving in 70% methanol, and shaking to 100mL for use. At this time, the concentration of puerarin standard use solution was 200. Mu.g/mL. Sucking the above-mentioned use solution, using 70%The methanol is diluted into the following concentrations respectively: 5. Mu.g/mL, 10. Mu.g/mL, 20. Mu.g/mL, 30. Mu.g/mL, 50. Mu.g/mL standard use solution. The high performance liquid chromatograph is adopted to draw a standard graph, R, of a standard use solution for measuring puerarin, the puerarin concentration is taken as an abscissa (X axis) and the peak area is taken as an ordinate (Y axis) 2 >99.9%。
Preparation of sample solution: accurately weighing 0.500g (accurate to 0.0001 g) of a sample (uric acid reducing component), adding 5mL of 70% methanol, performing ultrasonic treatment in an ultrasonic cleaner for 25min, taking out, cooling to room temperature, fixing the volume to 10mL with 70% methanol, uniformly mixing, standing, taking supernatant, filtering with a 0.45 μm filter membrane, and performing quantitative analysis by using a high performance liquid chromatograph.
Calculating the ratio of the mass of the kudzuvine root in uric acid reducing components and the mass of the kudzuvine root raw material, and marking the ratio as the extraction efficiency of puerarin. The results of specific extraction efficiencies are shown in table 1.
Table 1 extraction efficiency of puerarin by the examples and comparative examples extraction process
Example 1 | Example 2 | Example 3 | ||
Extraction yield% | 3.2 | 3.5 | 3.0 | |
Comparative example 1 | Comparative example 2 | Comparative example 3 | Comparative example 4 | |
Extraction yield% | 1.07 | 1.1 | 2.15 | 1.55 |
It is reported that the puerarin is extracted by ultrasonic extraction with 70% methanol aqueous solution, and the puerarin extraction rate is about 2.9% in the puerarin picked from Shicheng; compared with the traditional method, the extraction efficiency of puerarin in the kudzuvine root is obviously improved by adjusting the pH and the components of the leaching solvent and combining the synergy of alkaline cellulase.
As can be seen from comparative examples 1 and 2, if a certain amount of cosolvent is added into the leaching solvent, the leaching efficiency of puerarin can be further improved.
As can be seen from comparative examples 1 and 3, the activities of alkaline cellulases may not differ greatly at ph=8 and ph=8.5, but example 1 slightly increases the pH to facilitate the reaction of organic amine and puerarin, promote the dissolution in the leaching solvent, and further increase the leaching efficiency of puerarin in pueraria.
Comparative example 1 and comparative example 1 show that if the pH of the leaching solvent is lowered, on the one hand the activity of the alkaline cellulase is affected and on the other hand the content of organic amine used for pH adjustment is significantly lowered, thereby significantly inhibiting the reaction of organic amine and puerarin; overall, the extraction efficiency for puerarin is significantly reduced.
As is clear from comparative example 1 and comparative examples 2 to 3, lowering the temperature or raising the temperature affects the activity of alkaline cellulase; after the temperature is reduced, the reaction of the organic amine and puerarin can be influenced; but also promotes the leaching of puerarin and the reaction of puerarin and organic amine after the temperature is raised. Thus, the extraction efficiency of puerarin in comparative example 2 was significantly lowered, and the extraction efficiency of puerarin in comparative example 3 was only slightly lowered.
Comparative examples 1 and 4 show that if the organic amine is replaced with sodium hydroxide, the effect of strong base on enzyme and active ingredient in pueraria cells is unexpected, and in summary, has a negative effect on puerarin extraction efficiency.
According to the comparison and analysis, in the extraction process provided by the invention, the extraction efficiency of puerarin in the kudzuvine root is obviously improved through the synergistic effect between enzyme types and leaching solvent components.
Test example 2
The uric acid reducing effect of the tortoise jelly obtained in examples and comparative examples on uric acid was tested in this example and application examples 1 to 2 (pharmacological experiments on uric acid reducing effect of hyperuricemia mice).
1. Animal grouping and dosing program
Hypoxanthine is a precursor substance of uric acid in organism, and injection of hypoxanthine can accumulate uric acid, thereby inducing hyperuricemia; potassium oxazinate can inhibit uricase from decomposing uric acid, so that uric acid decomposition in a body is reduced, and uric acid level is continuously increased, thereby inducing hyperuricemia. The two can be combined to form a model which can obviously induce hyperuricemia and renal function injury.
SPF-grade Kunming male mice were randomly grouped into three major groups of 18 subgroups of 10 animals each. The three large groups are an experimental group, a control group and a blank group respectively, wherein 15 small groups are arranged in the experimental group, 2 small groups are arranged in the control group, and 1 small group is arranged in the blank group. After 4 days of adaptive feeding, the experiment is started after confirming that the animal has good health condition.
2. Grouping and experimental method
The blank control group is not treated and is fed normally. Except for blank groups, the other groups are subjected to continuous molding by adding hypoxanthine at a dosage of 500mg/kg, the corresponding groups of test drugs and positive control drugs are added at intervals of 30min in the first six days, the uric acid reducing components are extracted from each example or comparative example in the experimental group and are correspondingly named, and the injection is carried out according to an administration volume of 10mg (puerarin)/kg/d (the mass of tortoise jelly given by application example 2 is equal to that of tortoise jelly given by application example 1).
The control components are positive control group and negative control group, wherein the drug used as positive control drug is allopurinol. Allopurinol tablets were administered by gavage at a dose of 10 mg/kg/d. The negative control group was not treated except for feeding.
All mice fasted in the evening on the sixth day, and after the last administration of hypoxanthine for 30min on the seventh day, the corresponding group of drugs (reagents) were administered by intragastric administration at intervals of 20min with the exception of the blank control group and the negative control group, which were each of 300mg/kg of potassium oxazinate injected intraperitoneally.
1h after the intraperitoneal injection of the potassium oxazinate is finished, the orbit is used for taking blood, the blood is placed in a clean centrifuge tube, the blood is kept stand for 2h at room temperature, the blood is obtained after centrifugation for 10min at 3000rpm, and the blood is packaged in a 200 mu L centrifuge tube. Serum was assayed for blood uric acid content using uric acid kit and the results are shown in table 2. Results are all expressed as mean ± standard deviation. The mean and standard deviation of each group were calculated and t-tested using SPSS16.0 statistical software, respectively.
The results of the above tests are shown in table 2.
Table 2 uric acid reducing effects (part of) of uric acid reducing compositions obtained in examples and comparative examples and tortoise jelly obtained in application examples 1 to 2
Note that: *** represents p compared with the negative control group<0.001, # Representative is compared with blank group, p<0.1, ## Representative is compared with blank group, p<0.05。
Since the serum uric acid levels differ slightly between the examples, between the comparative examples, and between the corresponding application examples, only a few representative sets of results are listed in table 2.
Comparing the control group with the blank group, the animal modeling of the present invention was successful.
As is clear from comparison of the results of example 1 and comparative example 4, the effect of example 1 on reducing uric acid was better than that of comparative example 4, although the same puerarin equivalent was given, because the effect of reducing serum uric acid was better because the effect of reducing serum uric acid was smaller because the impurity content of the uric acid-reducing component obtained in example 1 was smaller, and the toxic and side effects on mice were also smaller, and the dosage was more accurate.
The comparison of the results of the example 1, the example 1-the application example 1 and the application example 2 shows that the tortoise jelly provided by the invention has a synergistic effect between other plant extracts and uric acid reducing components, and has obvious effect of reducing uric acid content in blood.
In summary, in the extraction process provided by the invention, a synergistic effect occurs between the steps and the parameters, so that the extraction efficiency and purity of puerarin in the obtained uric acid lowering ingredient are improved; furthermore, the uric acid reducing components and other preparation raw materials of the tortoise jelly have synergistic effect, so that the uric acid reducing effect is further improved.
While the embodiments of the present invention have been described in detail, the present invention is not limited to the above embodiments, and various changes can be made without departing from the spirit of the present invention within the knowledge of those skilled in the art. Furthermore, embodiments of the invention and features of the embodiments may be combined with each other without conflict.
Claims (10)
1. An extraction process for reducing uric acid components is characterized by comprising the following steps: mixing radix puerariae, leaching solvent and alkaline cellulase, and leaching at 50-70 ℃;
the leaching solvent is a mixture of water, alcohol and organic amine; the pH of the leaching solvent is 8-9.
2. The extraction process according to claim 1, wherein the volume ratio of water to alcohol in the leaching solvent is 1:0.3-4.
3. The extraction process according to claim 1, wherein the mass to volume ratio of the kudzuvine root to the leaching solvent is 1g: 5-20 mL.
4. The extraction process according to claim 1, wherein the alkaline cellulase accounts for 0.1-1% of the kudzuvine root by mass.
5. The extraction process according to claim 1, wherein the number of leaches is 1-3; and/or, the duration of a single leaching is 1-3 h.
6. The extraction process of claim 1, wherein the method of leaching comprises ultrasonic assisted reflux leaching.
7. The extraction process according to any one of claims 1 to 6, further comprising, after said leaching, sequentially acidifying and extracting the obtained leaching filtrate; and/or the extractant used for the extraction comprises at least one of ethyl acetate and n-butanol.
8. Use of an extraction process according to any one of claims 1 to 7 for the preparation of uric acid lowering products.
9. The use according to claim 8, wherein the uric acid lowering product is tortoise jelly.
10. A tortoise jelly characterized in that the raw materials for preparing the tortoise jelly comprise uric acid reducing components extracted by the extraction process according to any one of claims 1 to 7.
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