CN113575898A - Method for removing foreign matters in royal jelly slurry residue based on crystallization technology - Google Patents
Method for removing foreign matters in royal jelly slurry residue based on crystallization technology Download PDFInfo
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- CN113575898A CN113575898A CN202110918255.6A CN202110918255A CN113575898A CN 113575898 A CN113575898 A CN 113575898A CN 202110918255 A CN202110918255 A CN 202110918255A CN 113575898 A CN113575898 A CN 113575898A
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- 229940109850 royal jelly Drugs 0.000 title claims abstract description 54
- 238000000034 method Methods 0.000 title claims abstract description 24
- 238000005516 engineering process Methods 0.000 title claims abstract description 11
- 238000002425 crystallisation Methods 0.000 title claims abstract description 10
- 230000008025 crystallization Effects 0.000 title claims abstract description 9
- 239000002002 slurry Substances 0.000 title claims description 17
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 62
- 238000007873 sieving Methods 0.000 claims abstract description 19
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 238000007790 scraping Methods 0.000 claims abstract description 11
- 238000001704 evaporation Methods 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 34
- QHBZHVUGQROELI-SOFGYWHQSA-N (E)-10-hydroxydec-2-enoic acid Chemical compound OCCCCCCC\C=C\C(O)=O QHBZHVUGQROELI-SOFGYWHQSA-N 0.000 claims description 25
- QHBZHVUGQROELI-UHFFFAOYSA-N Royal Jelly acid Natural products OCCCCCCCC=CC(O)=O QHBZHVUGQROELI-UHFFFAOYSA-N 0.000 claims description 25
- 239000008213 purified water Substances 0.000 claims description 18
- 239000000706 filtrate Substances 0.000 claims description 17
- 238000003756 stirring Methods 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 16
- 239000004677 Nylon Substances 0.000 claims description 14
- 229920001778 nylon Polymers 0.000 claims description 14
- 238000005406 washing Methods 0.000 claims description 9
- 238000002156 mixing Methods 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 4
- 238000005057 refrigeration Methods 0.000 claims description 4
- 238000002390 rotary evaporation Methods 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 3
- 238000002386 leaching Methods 0.000 claims description 2
- 239000002893 slag Substances 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 239000000047 product Substances 0.000 description 9
- 238000010586 diagram Methods 0.000 description 6
- 230000014759 maintenance of location Effects 0.000 description 5
- 239000010802 sludge Substances 0.000 description 5
- 238000005303 weighing Methods 0.000 description 5
- 239000012535 impurity Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- -1 10-HDA and the like Chemical class 0.000 description 1
- 206010027146 Melanoderma Diseases 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000003550 marker Substances 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Images
Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L21/00—Marmalades, jams, jellies or the like; Products from apiculture; Preparation or treatment thereof
- A23L21/20—Products from apiculture, e.g. royal jelly or pollen; Substitutes therefor
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/08—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in rotating vessels; Atomisation on rotating discs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/30—Combinations with other devices, not otherwise provided for
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Mycology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Jellies, Jams, And Syrups (AREA)
Abstract
The invention provides a method for removing foreign matters in royal jelly pulp residue based on crystallization technology, which comprises the steps of adding 95 percent edible alcohol into the royal jelly pulp residue, scraping and filtering, magnetically holding and adsorbing, evaporating and concentrating, sieving by a 400-mesh sieve and the like to obtain refined pulp residue; the method can greatly improve the purity of the pulp slag, reduces foreign matters in the pulp slag to the maximum extent, does not increase foreign components, thereby improving the product quality, simultaneously avoids the labor cost caused by manually selecting the pulp slag and the instability of the pulp slag selection quality, and is worthy of being implemented in the actual production.
Description
Technical Field
The invention belongs to the field of royal jelly health-care products, and particularly relates to a method for removing foreign matters in royal jelly residues.
Background
The royal jelly residue is residue of royal jelly filtered by 100 mesh screen, as shown in figure 1, and contains about 20-40% of royal jelly acid-10-HDA, which is natural effective substance existing in royal jelly only in nature and is quality index and marker component index of royal jelly.
As the royal jelly slurry residue is rich in 10-HDA, the royal jelly slurry residue must be returned to the raw materials in the processing process, so as to meet the requirements of customers or national standards on the 10-HDA quality index. The royal jelly residue contains a large amount of impurities including wax scraps and other foreign matters (metal foreign matters and small black spots) besides effective components such as organic acids such as 10-HDA and the like, proteins and the like, and the royal jelly residue needs to be purified, otherwise the quality of products is influenced. The impurity content of filtered pulp residue of royal jelly produced in different producing areas and seasons has great difference.
Practice proves that foreign matters in the royal jelly pulp residue cannot be completely removed by the absorption of the magnetic rod, and particularly, the non-metal foreign matters are difficult to remove by the absorption of the magnetic rod. The conventional treatment means for impurities in the pulp residue in the prior art is to wash the pulp residue with water, sieve the pulp residue with a thicker 10-20-mesh sieve, wherein the sieve is residue, the main component is wax scraps, the lower part is a usable part and contains 10-HDA (royal jelly efficacy substance), meanwhile, smaller foreign matters also pass through the sieve, and the lower part of the royal jelly pulp residue is placed on a 120-mesh sieve to be squeezed by hands to obtain the washed pulp residue which needs to be further manually selected to be foreign matters visible to the naked eyes, so that purified pulp residue is obtained and then used for production. The production of the pulp slag can undoubtedly increase the labor cost, the pulp slag purification effect is unstable, the non-metallic foreign matters in the pulp slag, mainly small black spots, cannot be removed and are brought into the product, and the quality problem is caused.
Disclosure of Invention
Aiming at the defects in the prior art, the invention provides a method for removing foreign matters in royal jelly pulp residue based on a crystallization technology, which is simple and quick, and the pulp residue is pure and light yellow in crystal, and has no ethanol or foreign matters.
In order to realize the purpose of the invention, the invention adopts the following technical scheme:
a method for removing foreign matters in royal jelly slurry residue based on crystallization technology comprises the following steps:
1) adding 95% edible alcohol into Lac Regis Apis slurry residue, stirring for dissolving, adding purified water, stirring for dissolving, sieving with 120 mesh nylon sieve, sieving with 200 mesh nylon sieve, and sieving with magnetic rod to adsorb foreign matter to obtain filtrate;
2) adding purified water into the obtained filtrate, mixing, rotary evaporating for concentration until the distilled liquid has no ethanol, pouring out the material, washing the inner wall with water, mixing with the material, placing in 0-5 deg.C refrigerator, storing overnight, taking out the material, sieving with 400 mesh sieve, and collecting the purified slurry residue on the upper part of the sieve;
or the like, or, alternatively,
2') adding purified water into the obtained filtrate, stirring and mixing, placing in a refrigeration house at 0-5 ℃, storing overnight, passing through a 400-mesh nylon screen with available pulp residue on the upper part of the screen, collecting the available pulp residue, adding water and leaching until no ethanol smell exists, thus obtaining refined pulp residue;
the mass ratio of the royal jelly residues, the 95% edible alcohol and the purified water in the step 1) is 1:1: 0.667-1.
Further, in the step 1), the mass ratio of the royal jelly residues, the 95% edible alcohol and the purified water is 1:1-3: 1.
Furthermore, the royal jelly residue is residue obtained by filtering royal jelly raw material, is rich in royal jelly acid 10-HDA which is peculiar to royal jelly, and has the water content of 40-60%.
Furthermore, the number of the magnetic rods in the step 1) is 6, and the magnetic force of the magnetic rods is more than or equal to 7000 gausses.
Further, the step 2) is carried out rotary evaporation concentration under the conditions of 45-50 ℃ and 0.09 MPa.
The invention relates to selection of mesh number of a screen:
the foreign matters in the royal jelly dregs have different properties and sizes. 10-HDA is insoluble in water and can be dissolved in ethanol, 95% edible alcohol can quickly dissolve 10-HAD, and 10-HDA is dissolved into transparent solution for absolutely removing foreign matters, and then filtered by a screen with a certain mesh number. Considering that the requirements of customers for metal foreign matters in the product are less than 0.2mm, and the aperture size of the 100-mesh screen is 0.109mm, the requirements of the production process are completely met, and tests show that the operation of filtering by using the 100-mesh screen is feasible. The slurry residue solution can be filtered by adopting a 120-mesh → 200-mesh procedure, and the obtained product has less foreign matters.
Although the process for removing the metal foreign matters in the royal jelly production process is carried out for 3-5 times, the royal jelly needs to be adjusted by using the pulp residue to adjust the content of 10-HDA, and the pulp residue is a main source of small black spot foreign matters in the royal jelly product. The small black spots are one of indexes of foreign matters in the product, and each 100g of the small black spots is required to be less than 30, and the small black spots visible to naked eyes can be completely removed by filtering through a 200-mesh screen.
Meanwhile, in the existing pulp slag treatment process, a large amount of manpower is needed to select small black spots and other foreign matters in the pulp slag, the selection operation is very manual, the selection effect is different from person to person, and the method has the advantage that the manpower can not be replaced.
Determination of the sludge solvent:
the pulp residue contains 10-HDA as main component, wax bits, and small amount of protein and other impurities. The solubility of 10-HDA in ethanol of different concentrations is shown in Table 2
TABLE 1 10-HDA solubilization in ethanol of different concentrations
| Concentration of ethanol | Processing method | 10-HDA，％ | Residue, g |
| 0％ | 10g of pulp residue | 22.1 | 10 |
| 20％ | 10g of pulp residue → 20g of water → 80g of ethanol | 0.47 | 4.5 |
| 30％ | 10g of pulp → 30g of water → 70g of ethanol | 1.59 | 3.3 |
| 40％ | 10g of pulp → 40g of water → 60g of ethanol | 2.09 | 2.6 |
| 50％ | 10g of pulp → 50g of water → 50g of ethanol | 2.07 | 2.2 |
Therefore, more than 40% of ethanol can completely dissolve 10-HDA, and the optimal yield can be obtained by dissolving the pulp residue with 50% of ethanol. Considering that 40% is the critical ethanol concentration with high solubility of 10-HDA, and the concentration difference may cause the loss due to the too low solubility of 10-HAD in the production and preparation processes, the research adopts 50% ethanol to dissolve the pulp residue, so that the high solubility of 10-HAD can be ensured, and the yield is higher.
The method for removing the foreign matters in the royal jelly pulp residue can greatly improve the purity of the pulp residue, furthest reduce the foreign matters in the pulp residue, and does not increase external components, thereby improving the product quality, simultaneously avoiding the labor cost and the instability of the pulp residue selection quality caused by manually selecting the pulp residue, and being worthy of being promoted in the actual production.
Drawings
FIG. 1 is a diagram of untreated royal jelly sludge;
FIG. 2 is a graph of royal jelly dregs obtained by the treatment of example 1;
FIG. 3 is a picture of royal jelly dregs obtained by the treatment of example 3;
FIG. 4 is a diagram of royal jelly sludge obtained by the treatment of comparative example;
FIG. 5 is a diagram showing foreign matters in the sludge obtained in example 1, wherein black matters in the diagram are foreign matters;
FIG. 6 is a diagram showing foreign matters in the sludge obtained in the comparative example, wherein black matters in the diagram are foreign matters.
Detailed Description
The technical scheme of the invention is further described in detail by the following specific embodiments in combination with the attached drawings:
example 1
Weighing 10kg of royal jelly pulp, adding 10kg (95%) of edible alcohol, stirring for dissolving, adding 6.67kg of purified water, stirring for dissolving, sieving with a 120-mesh nylon sieve, performing scraping filtration by using 6 magnetic rods to adsorb foreign matters (the magnetic force of the magnetic rods is more than or equal to 7000 gauss), continuously sieving the obtained filtrate with a 200-mesh nylon sieve, performing scraping filtration by using 6 magnetic rods to adsorb foreign matters (the magnetic force of the magnetic rods is more than or equal to 7000 gauss) to obtain filtrate, adding 10kg of purified water into the filtrate, performing rotary evaporation concentration at 45 ℃ and 0.09MPa until the distilled liquid is free of ethanol, pouring out the material, washing the inner wall with water, adding the filtrate into the material, placing the material in a 0-5 ℃ refrigeration house, storing overnight, taking out the material, sieving with a 400-mesh sieve, collecting 8.88kg of pulp on the upper part of the sieve, and showing in figure 3.
Example 2
Weighing 10kg of royal jelly pulp, adding 10kg (95%) of edible alcohol, stirring for dissolving, adding 10kg of purified water, stirring for dissolving, sieving with a 120-mesh nylon sieve, performing scraping filtration by using 6 magnetic rods to adsorb foreign matters (the magnetic force of the magnetic rods is more than or equal to 7000 gauss), continuously sieving the obtained filtrate with a 200-mesh nylon sieve, performing scraping filtration by using 6 magnetic rods to adsorb foreign matters (the magnetic force of the magnetic rods is more than or equal to 7000 gauss) to obtain filtrate, adding 10kg of purified water into the filtrate, performing rotary evaporation concentration at 45 ℃ and 0.09MPa until the distilled liquid is free of ethanol, pouring out the material, washing the inner wall with water, putting into a 0-5 ℃ refrigeration house, storing overnight, taking out the material, sieving with a 400-mesh sieve, collecting 8.65kg of pulp on the upper part of the sieve.
Example 3
Weighing 10kg of royal jelly pulp, adding 10kg (95%) of edible alcohol, stirring for dissolving, adding 8.6kg of purified water, stirring for dissolving, sieving with a 120-mesh nylon sieve, performing scraping filtration by using 6 magnetic rods to adsorb foreign matters (the magnetic force of the magnetic rods is more than or equal to 7000 Gauss), continuously sieving the obtained filtrate with a 200-mesh nylon sieve, performing scraping filtration by using 6 magnetic rods to adsorb foreign matters (the magnetic force of the magnetic rods is more than or equal to 7000 Gauss), adding 20kg of purified water into the obtained filtrate, stirring and mixing, placing in a 0-5 ℃ refrigerator, standing overnight, taking out materials, sieving with a 400-mesh sieve to obtain usable pulp on the upper part of the sieve, wherein the pulp contains a small amount of ethanol, and repeatedly washing with water until no ethanol smell exists to obtain 8.67kg of refined pulp. See fig. 4.
Example 4
Weighing 10kg of royal jelly pulp, adding 10kg (95%) of edible alcohol, stirring for dissolving, adding 10kg of purified water, stirring for dissolving, sieving with a 120-mesh nylon sieve, performing scraping filtration by using 6 magnetic rods to adsorb foreign matters (the magnetic force of the magnetic rods is more than or equal to 7000 Gauss), further sieving with a 200-mesh nylon sieve, performing scraping filtration by using 6 magnetic rods to adsorb foreign matters (the magnetic force of the magnetic rods is more than or equal to 7000 Gauss), adding 40kg of purified water into the obtained filtrate, stirring and mixing, placing in a 0-5 ℃ refrigerator, storing overnight, taking out materials, sieving with a 400-mesh sieve to obtain usable pulp on the upper part of the sieve, wherein the pulp contains a small amount of ethanol, and repeatedly washing with water until no ethanol smell to obtain 8.53kg of refined pulp.
Comparison of example 1 and example 3 with respect to 10-HDA retention:
the 10-HDA is the characteristic component of the royal jelly and has positive correlation with the commodity price, and if the 10-HDA yield is too low in the treatment process, the method has defects and has no application value. Although 10-HDA has strong heat resistance, the research is a physical crystallization method, and the total amount of 10-HDA in the slurry residue cannot be lost, in view of the importance of 10-HDA, the research still examines two different post-treatment methods, namely the retention rate and the material balance of 10-HDA, the retention rate difference of the two post-treatment methods is larger, which is related to the concentration of ethanol, and dilute ethanol has higher solubility than water. The retention cases are shown in table 2.
TABLE 2 10-HDA Retention Rate profiles for different slurry and slag treatment methods
The data in this table is problematic in that the material is now 1 and 1 (20kg) in relation to alcohol, and then the residue plus filtrate is at least 10kg, and is now less than 9kg in addition
Comparative example (prior art)
Weighing 10kg of royal jelly pulp residue, adding 50kg of purified water, stirring and dissolving, screening by using a 10-20-mesh screen, wherein the screen is provided with residues, the main component is wax scraps, the lower part is an available part, the lower part of the royal jelly pulp residue is placed on a 120-mesh screen, and squeezing is carried out by hands to obtain washing pulp residue, the washing pulp residue needs to be further manually selected to obtain macroscopic foreign matters, so that the purified pulp residue is obtained, the method cannot remove the non-metallic foreign matters (mainly small black spots) in the pulp residue and bring the foreign matters into the product, so that the quality problem is caused, and the washing and purifying pulp residue is shown in figure 2.
The royal jelly residue treated by the prior art and the royal jelly residue treated by the technique are subjected to foreign matter detection, and the results are shown in figures 5 and 6. As can be seen from the figure, the foreign matters in the royal jelly residues treated by the prior art and the royal jelly residues treated by the technology have obvious difference seen by naked eyes, and the effect of removing the foreign matters by the technology is far better than that of the common prior art.
Claims (4)
1. A method for removing foreign matters in royal jelly slurry residue based on crystallization technology is characterized by comprising the following steps:
1) adding 95% edible alcohol into Lac Regis Apis slurry residue, stirring for dissolving, adding purified water, stirring for dissolving, sieving with 120 mesh nylon sieve by scraping, filtering with magnetic rod to adsorb foreign matter, sieving with 200 mesh nylon sieve by scraping, and filtering with magnetic rod to adsorb foreign matter to obtain filtrate without foreign matter;
2) adding purified water into the obtained filtrate without foreign matters, mixing, rotary evaporating for concentration until the distilled liquid has no ethanol, pouring out the material, washing the inner wall with water, mixing with the material, placing in a 0-5 deg.C refrigerator, storing overnight, taking out the material, passing through a 400 mesh screen with purified slurry residue on the upper part;
or the like, or, alternatively,
2') adding purified water into the obtained filtrate, stirring and mixing, placing in a refrigeration house at 0-5 ℃, storing overnight, passing through a 400-mesh nylon screen with available pulp residue on the upper part of the screen, collecting the available pulp residue, adding water and leaching until no ethanol smell exists, thus obtaining refined pulp residue;
the mass ratio of the royal jelly residues, the 95% edible alcohol and the purified water in the step 1) is 1:1: 0.667-1.
2. The method for removing foreign matter in royal jelly slurry residue based on crystallization technology according to claim 1, characterized in that the royal jelly slurry residue is residue of filtered royal jelly raw material, is rich in royal jelly acid 10-HDA peculiar to royal jelly, and has a moisture content of 40% -60%.
3. The method for removing foreign matters in royal jelly slurry residue based on crystallization technology according to claim 1, wherein the number of the magnetic rods in step 1) is 6, and the magnetic forces of the magnetic rods are more than or equal to 7000 gauss.
4. The method for removing foreign matters in royal jelly slurry residue based on crystallization technology according to claim 1, wherein the rotary evaporation concentration is performed under the conditions of 45-50 ℃ and 0.09MPa in the step 2).
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115191583A (en) * | 2022-05-23 | 2022-10-18 | 浙江江山恒亮蜂产品股份有限公司 | Royal jelly raw material processing method and beverage production process thereof |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN86107034A (en) * | 1986-12-10 | 1987-07-15 | 上海冠生园食品厂 | Manufacturing process of fresh royal jelly products |
| CN1076362A (en) * | 1993-03-08 | 1993-09-22 | 王训华 | The preparation method of royal jelly oral products |
| CN1357528A (en) * | 2000-12-14 | 2002-07-10 | 四川辰龙制药有限公司 | Caproleic acid extracting process from royal jelly |
| CN103044240A (en) * | 2011-10-15 | 2013-04-17 | 山东华康蜂业有限公司 | Process for extracting 10-oxhydryl-2-caproleic acid from royal jelly |
| CN103772497A (en) * | 2014-01-10 | 2014-05-07 | 浙江大学 | Ultrafiltration membrane separation method for obtaining royal jelly major protein and active filtrate in royal jelly |
| CN105712872A (en) * | 2014-12-05 | 2016-06-29 | 刘春香 | Process for extracting 10-hydroxy-2-decenoic acid from royal jelly waste |
| CN108669509A (en) * | 2018-03-21 | 2018-10-19 | 巢氏健康生物科技股份有限公司 | A kind of novel royal jelly liquid and preparation method thereof containing 10-HDA liposomes |
| CN209205532U (en) * | 2018-11-05 | 2019-08-06 | 巢氏健康生物科技股份有限公司 | Metallic foreign body eliminating equipment in a kind of efficient fresh royal jelly |
-
2021
- 2021-08-11 CN CN202110918255.6A patent/CN113575898A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN86107034A (en) * | 1986-12-10 | 1987-07-15 | 上海冠生园食品厂 | Manufacturing process of fresh royal jelly products |
| CN1076362A (en) * | 1993-03-08 | 1993-09-22 | 王训华 | The preparation method of royal jelly oral products |
| CN1357528A (en) * | 2000-12-14 | 2002-07-10 | 四川辰龙制药有限公司 | Caproleic acid extracting process from royal jelly |
| CN103044240A (en) * | 2011-10-15 | 2013-04-17 | 山东华康蜂业有限公司 | Process for extracting 10-oxhydryl-2-caproleic acid from royal jelly |
| CN103772497A (en) * | 2014-01-10 | 2014-05-07 | 浙江大学 | Ultrafiltration membrane separation method for obtaining royal jelly major protein and active filtrate in royal jelly |
| CN105712872A (en) * | 2014-12-05 | 2016-06-29 | 刘春香 | Process for extracting 10-hydroxy-2-decenoic acid from royal jelly waste |
| CN108669509A (en) * | 2018-03-21 | 2018-10-19 | 巢氏健康生物科技股份有限公司 | A kind of novel royal jelly liquid and preparation method thereof containing 10-HDA liposomes |
| CN209205532U (en) * | 2018-11-05 | 2019-08-06 | 巢氏健康生物科技股份有限公司 | Metallic foreign body eliminating equipment in a kind of efficient fresh royal jelly |
Non-Patent Citations (1)
| Title |
|---|
| 刘媛 等: "王浆渣中提取反-10-羟基-2-癸烯酸的研究", 《天津化工》, no. 2, pages 4 - 6 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115191583A (en) * | 2022-05-23 | 2022-10-18 | 浙江江山恒亮蜂产品股份有限公司 | Royal jelly raw material processing method and beverage production process thereof |
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