Traditional Chinese medicine compound product co-production equipment for wine
By using a combined production equipment for Chinese herbal medicines in alcoholic beverages, the problems of high loss and high energy consumption in Chinese herbal medicine extraction equipment have been solved, achieving stable conversion and efficient utilization of the effective components of Chinese herbal medicines, and improving production efficiency and product stability.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-04-21
- Publication Date
- 2026-03-24
AI Technical Summary
Existing Chinese medicine extraction equipment suffers from high residual equipment wear and tear, high energy consumption, long production cycles, unstable material quality, and large batch-to-batch fluctuations in composition, which affect production efficiency and product uniformity.
The equipment for the co-production of compound Chinese medicine products for winemaking includes a compound Chinese medicine extract separation unit, an extract preparation unit, and an extract preparation unit. It uses low-precision and high-precision filter bag filters and inorganic ceramic membrane filters to remove solid particles. Combined with MVR concentrators, spray dryers, and other equipment, it realizes solid-liquid separation and aging processes, thereby improving the conversion rate and comprehensive utilization rate of the effective components of Chinese medicinal materials.
It maximizes the uniformity of functional components, reduces equipment energy consumption and cleaning costs, improves production efficiency, reduces material loss, and enhances product stability and the comprehensive utilization rate of Chinese medicinal materials.
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Figure CN224024316U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model relates to health wine production equipment technical field, especially a kind of wine with traditional Chinese medicine compound product cogeneration equipment. BACKGROUND
[0002] At present, the impurity removal of solid particles of medicinal material extraction liquid in traditional Chinese medicine extraction industry is all carried out using butterfly centrifuge, horizontal screw centrifuge, plate and frame filter and diatomite filter, which is complicated in operation, has large equipment residual loss, and some devices need to be matched with high-energy auxiliary facilities to use, which not only increases the cost of equipment energy consumption and labor cost, but also prolongs the production cycle of single batch of medicinal materials.
[0003] Traditional impurity removal of traditional Chinese medicine extraction liquid is carried out by solid-liquid separation or liquid-solid separation and solid-liquid-solid method, and the impurity removal needs to be continuously carried out due to the large amount of traditional Chinese medicine extraction liquid in production, and the filter element needs to be replaced or the residue needs to be discharged at intervals during equipment operation, and the separation method has large loss of material liquid ratio in production process, which easily leads to unstable batch material quality, large material balance difference and prolonged production cycle of single variety, and affects the content of effective components of product in downstream process, and is not conducive to the improvement of production efficiency and the uniformity of effective components between batches. SUMMARY
[0004] In order to overcome the shortcomings of the prior art, the utility model provides an energy-saving and consumption-reducing wine with traditional Chinese medicine compound product continuous production and impurity removal filter equipment, which can maximize the uniformity of functional components, effectively protect the conversion of effective components of medicinal materials, and is beneficial to the improvement of product stability. At the same time, the by-products are produced by impurity removal again during aging stage, and the comprehensive utilization rate of medicinal materials is improved.
[0005] The utility model provides the following technical scheme: a kind of wine with traditional Chinese medicine compound product cogeneration equipment, including traditional Chinese medicine compound extraction liquid separation unit, and with traditional Chinese medicine compound extraction liquid separation unit through pipeline connection extraction preparation unit and extraction liquid preparation unit respectively;
[0006] The traditional Chinese medicine compound extraction liquid separation unit includes extraction liquid storage tank, and the extraction liquid storage tank is connected with low-precision filter bag filter and high-precision filter bag filter respectively through pipeline, and the outlet of low-precision filter bag filter and high-precision filter bag filter is connected with inorganic ceramic membrane filter through pipeline, and the inorganic ceramic membrane filter is connected with extraction preparation unit and extraction liquid preparation unit respectively.
[0007] As a preferred technical scheme of the utility model, the precision specification of the low-precision filter bag filter is 1000 meshes, and the precision specification of the high-precision filter bag filter is 10000 meshes.
[0008] As a preferred technical scheme of the utility model, the extract preparation unit comprises an MVR concentrator, a spray dryer, a smashing mixer and a packaging machine connected with the inorganic ceramic membrane filter in sequence.
[0009] As a preferred technical scheme of the utility model, the extract preparation unit comprises an MVR concentrator, a spray dryer, a smashing mixer and a packaging machine connected with the inorganic ceramic membrane filter in sequence.
[0010] As a preferred technical scheme of the utility model, the extract preparation unit comprises an MVR concentrator, a spray dryer, a smashing mixer and a packaging machine connected with the inorganic ceramic membrane filter in sequence.
[0011] As a preferred technical scheme of the utility model, the precision of the inorganic ceramic membrane filter is 50 nm, the material thereof is SUS316, the pore size is 50 um, and the equipment structure part can withstand the corrosion of high-concentration nitric acid, sodium hydroxide and sodium hypochlorite under high-temperature conditions.
[0012] Compared with the prior art, the utility model has the beneficial effects that:
[0013] The wine traditional Chinese medicinal material compound extract is separated by the filter bag, solid particles are removed, the uniformity of functional components is maximally retained, the conversion of effective components of traditional Chinese medicinal materials is effectively ensured, and the product stability is improved. Secondly, byproduct is produced by removing impurities again in the aging stage, and the comprehensive utilization rate of traditional Chinese medicinal materials is improved. In terms of energy consumption and cleaning, high equipment investment and cleaning cost are saved, energy consumption can be continuously saved, production efficiency is improved, and sewage discharge amount is reduced. The filter bag impurity removal retains the material liquid zero loss to a large extent in the production process, material balance between batches is ensured, large equipment maintenance and reagent cleaning cost are not needed, and the filter bag can be reused after being directly used, cleaned and flushed. BRIEF DESCRIPTION OF DRAWINGS
[0014] Figure 1 It is a traditional Chinese medicinal material compound extract separation unit structural relationship schematic view of the utility model;
[0015] Figure 2 It is a co-production equipment connection relationship schematic view of the utility model;
[0016] Among them: 1-extract storage tank, 2-conveying pipeline, 3-conveying pump, 4-first electromagnetic valve, 5-low-precision filter bag filter, 6-second electromagnetic valve, 7-high-precision filter bag filter, 8-liquid pipeline, 9-inorganic ceramic membrane filter. DETAILED DESCRIPTION
[0017] To make the technical means, creative features, and achieved objectives and effects of this utility model easier to understand, the present utility model is further described below with reference to specific embodiments. However, the following embodiments are merely preferred embodiments of this utility model and not all of them. Other embodiments obtained by those skilled in the art based on the embodiments described herein without creative effort are all within the protection scope of this utility model. Unless otherwise specified, the experimental methods in the following embodiments are conventional methods, and the materials and reagents used in the following embodiments are commercially available unless otherwise specified.
[0018] Example 1
[0019] This embodiment provides a co-production device for traditional Chinese medicine compound products for winemaking, including a traditional Chinese medicine compound extract separation unit, and an extract preparation unit and an extract preparation unit respectively connected to the traditional Chinese medicine compound extract separation unit through pipelines.
[0020] like Figure 1 As shown, the traditional Chinese medicine compound extract separation unit includes an extract storage tank 1. The extract storage tank 1 is connected to a low-precision filter bag 5 and a high-precision filter bag 7 through a conveying pipe 2. The outlets of the low-precision filter bag 5 and the high-precision filter bag 7 are connected to an inorganic ceramic membrane filter 9 through a feed pipe 8. The inorganic ceramic membrane filter 9 is connected to the extract preparation unit and the extract preparation unit.
[0021] The low-precision filter bag filter 5 has a precision specification of 1000 mesh, while the high-precision filter bag filter 7 has a precision specification of 10000 mesh.
[0022] In actual production, an online turbidity detector (not shown in the figure) can be installed on the conveying pipeline 2. The opening and closing of the first solenoid valve 4 and the second solenoid valve 6 are controlled by setting a threshold. When the turbidity is below the threshold, the first solenoid valve 4 opens and the second solenoid valve 6 closes, allowing the extract to enter the low-precision filter bag 5. When the turbidity is above the threshold, the first solenoid valve 4 closes and the second solenoid valve 6 opens, allowing the extract to enter the high-precision filter bag 7. This setup ensures the clarity and filtration effect of the feed solution transferred to the inorganic ceramic membrane filter 9, which is beneficial to the stability of the effective components of the extract between batches.
[0023] Example 2
[0024] This embodiment provides a co-production device for traditional Chinese medicine compound products for winemaking, including a traditional Chinese medicine compound extract separation unit, and an extract preparation unit and an extract preparation unit respectively connected to the traditional Chinese medicine compound extract separation unit through pipelines.
[0025] like Figure 1As shown, the traditional Chinese medicine compound extract separation unit includes an extract storage tank 1. The extract storage tank 1 is connected to a low-precision filter bag 5 and a high-precision filter bag 7 through a conveying pipe 2. The outlets of the low-precision filter bag 5 and the high-precision filter bag 7 are connected to an inorganic ceramic membrane filter 9 through a feed pipe 8. The inorganic ceramic membrane filter 9 is connected to the extract preparation unit and the extract preparation unit.
[0026] The low-precision filter bag filter 5 has a precision specification of 1000 mesh, while the high-precision filter bag filter 7 has a precision specification of 10000 mesh.
[0027] In actual production, the extract can be transferred to the extract storage tank in stages according to the process flow, and then impurity removal is carried out. Based on the properties of Chinese medicinal materials, fruits and seeds are filtered using low-precision filter bag filter 5, while leaves and rhizomes are filtered using high-precision filter bag filter 7. The on-site filter bag equipment meets the requirements of "different high and low precision" material-liquid separation effect, and meets the impurity removal process of different Chinese medicinal material production processes. This not only improves the production efficiency of single products, but also achieves the effect of continuous production of multiple varieties.
[0028] Example 3
[0029] This embodiment provides a co-production device for traditional Chinese medicine compound products for winemaking, including a traditional Chinese medicine compound extract separation unit, and an extract preparation unit and an extract preparation unit respectively connected to the traditional Chinese medicine compound extract separation unit through pipelines.
[0030] like Figure 1 As shown, the traditional Chinese medicine compound extract separation unit includes an extract storage tank 1. The extract storage tank 1 is connected to a low-precision filter bag 5 and a high-precision filter bag 7 via a conveying pipe 2. The outlets of the low-precision filter bag 5 and the high-precision filter bag 7 are connected to an inorganic ceramic membrane filter 9 via a feed pipe 8. The inorganic ceramic membrane filter 9 is connected to both the extract preparation unit and the extract preparation unit. The low-precision filter bag 5 has a precision specification of 1000 mesh, and the high-precision filter bag 7 has a precision specification of 10000 mesh.
[0031] like Figure 2 As shown, the extract preparation unit includes an MVR concentrator, a spray dryer, a pulverizing mixer, and a packaging machine, all connected in sequence to the inorganic ceramic membrane filter. The extract preparation unit includes a blending tank, an aging tank, a filling machine, and a packaging machine, all connected in sequence to the inorganic ceramic membrane filter.
[0032] In actual production, taking the simultaneous extraction of tartary buckwheat extract and concentrated liquid as an example, the tartary buckwheat raw medicinal material is cleaned, and then is fed into an extraction tank through a feeding pipeline for warming and decoction. After the extraction process is completed, the extraction liquid is sent into an extraction liquid storage tank 1. The extraction liquid can be filtered by using the low-precision filter bag filter 5 and the high-precision filter bag filter 7 in the manner of the embodiment 1 or the embodiment 2, and then is filtered by using the inorganic ceramic membrane filter 9 for large molecule screening. According to the customer demand, the product output is as follows: the inorganic ceramic membrane filtrate is used for wine body blending and aging, and then is filled and packaged; the supernatant is obtained by filling to obtain wine concentrated liquid; and the subnatant is further filtered by using the high-precision filter bag filter 7 to remove impurities, and then is fed into the inorganic ceramic membrane separator 9, concentrated by using the MVR concentrator to obtain high-viscosity material, and then is dried, crushed and mixed by using the spray dryer to obtain tartary buckwheat extract.
[0033] The production system realizes the simultaneous extraction and separation of tartary buckwheat extract and concentrated liquid, realizes the systematic production of two products and different specifications of effective components, reduces the purchase cost of medicinal material raw materials and the use amount of organic solvents, promotes the "exhaustive extraction" of medicinal material effective components, reduces the production energy consumption, and reduces the production cost of products.
[0034] Meanwhile, the filter bag impurity removal manner of the embodiment can effectively reduce the loss rate of the material liquid when a large amount of material liquid is treated, the material liquid separation rate can reach 100%, the loss of the material liquid is 0, and the material loss is greatly reduced. When the disc centrifuge is separated, the device structure needs small and large discharges, for example, in conventional production, one batch of material needs 60-100 times of small discharges and 10-20 times of large discharges, and the solid adhesion and the material liquid are discharged together through the discharge in the warehouse body, which affects the separation rate of the single batch of material and causes the instability of the material components between batches. The continuous production of the filter bag greatly reduces the industrial production and manufacturing cost, and the filter bag has high reusability, and the water amount of CIP cleaning and the pollution discharge amount are reduced in industrial production.
[0035] The basic principle, main features and advantages of the utility model are shown and described. It should be understood by those skilled in the art that the utility model is not limited by the above embodiments, the above embodiments and the description in the specification are only preferred examples of the utility model, and are not used to limit the utility model, various changes and improvements of the utility model can be made without departing from the spirit and scope of the utility model, and these changes and improvements all fall within the scope of the utility model claimed. The protection scope of the utility model is defined by the appended claims and equivalents thereof.
Claims
1. A co-production equipment for compound products of traditional Chinese medicine used in winemaking, characterized in that: The Chinese medicine compound extraction solution separation unit, an extract preparation unit, and an extraction solution preparation unit are connected by pipelines; The Chinese medicine compound extraction solution separation unit includes an extraction solution storage tank, which is connected with a low-precision filter bag filter and a high-precision filter bag filter by pipelines, and the outlets of the low-precision filter bag filter and the high-precision filter bag filter are connected with an inorganic ceramic membrane filter by pipelines, and the inorganic ceramic membrane filter is connected with the extract preparation unit and the extraction solution preparation unit.
2. The apparatus of claim 1, wherein: The precision specification of the low-precision filter bag filter is 1000 meshes, and the precision specification of the high-precision filter bag filter is 10000 meshes.
3. The apparatus of claim 1, wherein: The extract preparation unit includes an MVR concentrator, a spray dryer, a smashing mixer, and a packaging machine connected with the inorganic ceramic membrane filter in sequence.
4. The apparatus of claim 1, wherein: The extraction solution preparation unit includes a blending tank, an aging device, a filling machine, and a packaging machine connected with the inorganic ceramic membrane filter in sequence.
5. The apparatus of claim 4, wherein: The aging device is also connected with the high-precision filter bag filter by a reflux pipeline.
6. The apparatus of claim 1, wherein: The precision of the inorganic ceramic membrane filter is 50 nm, the material is SUS316, and the pore size is 50 um.