CN203467608U - Synchronous production device for producing dendrobium officinale oral solution and medicinal slice beverage - Google Patents
Synchronous production device for producing dendrobium officinale oral solution and medicinal slice beverage Download PDFInfo
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Abstract
The utility model provides a synchronous production device for producing a dendrobium officinale oral solution and a medicinal slice beverage. The synchronous production device is commonly composed of a pressurizing unit, a pressure transmitter, a tunnel type energy accumulator, a spiral jet flow spraying pipe, a central processing unit, a pressure sensing valve, a time delay, a signal conversion receiver, a control valve, an information processing device, a data acquisition unit, a power source and a node sensor, wherein the tunnel type energy accumulator is composed of three stainless pressure bearing pipes which are connected to form a door frame type; U-shaped connection pipes at one ends of a plurality of door frame pipes are connected and arrayed to form a tunnel type; under the condition of combining process conditions of the tunnel type energy accumulator with the spiral jet flow spraying pipe, dendrobium officinale plant cells are blast instantly at a liquid state at low temperature of lower than 20 DEG C and in an ultrahigh pressure of more than 500MPa; the tunnel type energy accumulator can meet the requirements of batch production and the like; the synchronous production device is a synchronous production device for a plurality of finished products with high polysaccharide content.
Description
Technical field
The present invention relates to a kind of synchronous production device of making dendrobium candidum oral liquid medicine materical crude slice beverage, belong to common technology scope Internet of Things bioengineering field, the synchronous production process unit of low temperature explosion plant cell.
Background technology
Dendrobium candidum rises establishing in large scale in the whole nation, the stem of noble dendrobium is the perennial herbaceous plant that grows nonparasitically upon another plant of the orchid family, there is unique medical value, be described as first of nine immortal grass and be used as medicine with stem, Chinese medicine is called the stem of noble dendrobium, belong to the yin tonics < < Chinese pharmacopoeia > > in tonic, according to the fast development of current growing dendrobium, the establishing in large scale of industrialization, the plantation casual household of surging forward, and exactly lack catching up with of scale deep processing industry, rest on maple and seek market on using stratagems, to there is vegetables valency in the stem of noble dendrobium price of going down for a long time, (2012 the end of the year stem of noble dendrobium price fresh goods per kilogram be 800-1500 unit, cost ratio with 2010, in 2 years, dropped 50%).
Owing at least containing 30% above heat-sensitive substance in plant, fear high temperature, and dendrobium candidum finished product technique major part rests on tender stem is twisted into helical form or spring-like, dry, commodity are the storage of maple bucket, the reprocessing of maple bucket must not have new dendrobium candidum deep processed product, fine work exploitation by high temperature, and after the collection of the formation stem of noble dendrobium, price significantly drops.
The extracting method of plant polyose is generally extracting in boiling water, cycle is long, temperature is high, liquid ratio is large, be unfavorable for suitability for industrialized production, low-temperature ultrahigh-pressure (UHP) cell blasting technique, is according to the plant cell explosion between several pressure variations and one or more circulating pressure, recovery rate by explosion cell dendrobium polysaccharide is 95% of content, draws the manufacturing technique method of oral liquid the best.
The extracting method of current existing Dendrobium officinale polysaccharide is: dendrobium candidum water is: 100ml/g; Extracting temperature is 100 ℃, and extraction time is 3-5 hour, has more than 60% WATER AS FLOW MEDIUM waste after extraction at least, and more advanced have electromagnetic oscillation, enzyme digestion reaction, ultrasonic wave extract, all industrialization cost and height because its energy is little, complex technical process.
Documents: 200810162493.3 dendrobium polysaccharide extracting method, 201210080911.0 response surface method dendrobium polysaccharide extraction processes, 201210291799.5 disposable dendrobium polysaccharide EN separating and extracting process, all exist defect, dendrobium polysaccharide peptide yield and the defect low, effects of energy saving and emission reduction is undesirable of Dendrobium Plants waste.
Superelevation isostatic cool pressing continuous sterilization process and the device of the liquid food of documents 201110148468.1, it just carries out sterile test to liquid food, although this oral liquid belongs to liquid range (liquid food) and only belongs to conventional adopted name, especially because its technological requirement of difference of plant variety is also different, more specifically be that the difference, cell elite releasing effect of Chinese herbal medicine target plant is also just different, single pressure limit only plays sterilization functions, and its process time, utilization rate was lost greatly in long power consumption.
The dendrobium polysaccharide extracting method of documents 200810162493.3,201210080911.0 response surface method dendrobium polysaccharide extraction processes, all exist the defect that dendrobium candidum resource cannot be utilized completely, the defect that also have that polysaccharide discharges that incomplete product yield is low, effects of energy saving and emission reduction cannot improve in technological process.
Dendrobium candidum contains abundant polysaccharose substance, there is the effect that strengthens immunologic function, there is no to realize the technique follow-up of scale deep processing, stem of noble dendrobium raw materials market will supply exceed demand, static UHP common technology is combined with dynamic supersonic speed water jet technique, the preliminary experiment of technological process shows, low-temperature ultrahigh-pressure can impel the ripe explosion of dendrobium polysaccharide cell, under supersonic speed water jet operating mode, void effect explosion dendrobium candidum plant cell, dendrobium polysaccharide content discharges more than 95%, (UHP) be the abbreviation of plant cell blasting technique, through looking into domestic and foreign literature, all being difficult electronic program control (UHP) general character pressure is combined with spiral jet nozzle, produce supersonic jet and swash the relevant technological report that quick-fried stem of noble dendrobium plant cell extracts polysaccharide.
The invention discloses a kind of synchronous production device of making dendrobium candidum oral liquid medicine materical crude slice beverage, belong to Chinese herbal medicine and extract innovation art field, it is the extension in industrial generic technology (UHP) innovation, tunnel type accumulator is combined down with spiral jet nozzle process conditions, with the above ultra high pressure liquid of the following low temperature 500Mpa of 20 degree moment explosion dendrobium candidum plant cell, peptidoglycan content and much higher finished product synchronous production process unit method, tunnel type accumulator can meet the requirement of medium batch production.
Summary of the invention
The innovation of this device has produced (UHP) process conditions, is technological deficiency before overcoming, and from enzyme digestion reaction, ultrasonic wave, soaks
Carry, film is separated, alcohol is analysed sums up the reform of deficiency factor with the Technology Integration such as CO 2 supercritical, fluid extraction, tunnel type holds
Can maximize reduction batch production operating cost, the overall economic efficiency of performance dendrobium candidum by device; Improve dendrobium polysaccharide purity (peptidoglycan).The greatest problem of comparing the more ultrasonic wave of current application, electromagnetic oscillation crush method is: in ultrasonic concussion process, sound wave is absorbed and produces large heat by solution, can not in time heat be shifted out, impel the temperature of cell suspending liquid sharply to raise, cause enzyme and other bioactivator deactivation, also because sound wave transmission and the heat radiation of large-rolume container are difficult, having limited the large-scale application of industrialization, is (UHP) abbreviation of ultra high pressure liquid technology.
This device can solve the problems of the technologies described above, with time, pressure and temp chain rate and the solid-liquid ratio of plant cell circulation explosion, these affect in the factor of dendrobium polysaccharide recovery rate, carry out process conditions innovation, during tunnel type accumulator release pressure, produce the conversion of positive negative energy, in spiral jet nozzle, produce 2 Mach of supersonic jets, thereby improve the yield of Dendrobium officinale polysaccharide, three kinds of finished products synchronous output in a technological process, reduces the consumption of the energy.
Peptidoglycan content is difference by the difference of the stem of noble dendrobium place of production, kind, management, due to dendrobium candidum Jing Gan tissue tight, the active ingredient condition of releasing needs the above high temperature of 130 degree, high temperature has destroyed again the heat-sensitive substance in plant cell, make poor stability and the cell wall structure of active substance of plant tightr, it is low and without the high-quality finished product of dendrobium candidum deep processing that existing technique is extracted content.
The present invention is to provide a kind of synchronous production technique and device of making stem of noble dendrobium oral liquid medicine materical crude slice beverage, with electronic program, controlling tunnel type accumulator is combined with supersonic speed water jet technique, under sensor information guiding, in spiral jet nozzle, carry out the conversion of positive negative energy, produce void effect and swash broken dendrobium candidum plant cell, discharge peptidoglycan content and high synchronous production process unit.
Concrete technical scheme of the present invention is as follows:
Make a synchronous production device for dendrobium candidum oral liquid, medicine materical crude slice beverage, by hydraulic pressure unit 1, pressure transmitter 2, tunnel type accumulator 3, spiral jet nozzle 4, central processing unit 5, pressure sensing valve 6, the time relay 7, signal conversion receiver 8, control valve 9, information processor 10, data acquisition unit 11, power source 12, node sensor 13, jointly formed.
Central processing unit 5 connection signal conversion receivers 8, information processor 10, the time relay 7, information processor 10, data acquisition unit 11, the time relay 7 connection hydraulic pressure units 1, power source 12, hydraulic pressure unit 1 pipe leads to and connects pressure transmitter 2, pressure transmitter 2 pipes lead to and connect tunnel type accumulator 3, the two ends of tunnel type accumulator 3 are provided with pressure sensing valve 6, tunnel type accumulator 3 one end are fixedly connected with pressure transmitter 2, one end pipe leads to and connects spiral jet nozzle 4, control valve 9, node sensor 13 is arranged on the tube connector of spiral jet nozzle 4 and tunnel type accumulator 3, it is characterized in that: described tunnel type accumulator 1 is that 3 stainless steel pressure-bearing pipes connect into door case type, one end U type of a plurality of doorframe pipes is taken over to connect and is arranged in tunnel type, described in be arranged in tunnel the number of permutations by the volume=internal diameter * length of designing requirement, decided.
Pressure-bearing body important technological parameters=design internal diameter of tube body d≤50 mm of described tunnel type accumulator 3; Outer diameter D≤135 mm; Length 3000 mm; Footpath is than K=2.7, and operating pressure pW=620 Mpa, burst pressure pb=46.39pW=3246.3Mpa, design pressure pd=1.7pW=1200 Mpa, design temperature are room temperature; From strengthen pressure pA=0.89pW=640 Mpa, pressure ratio 16: safe-working pressure pA=0.81pW=568.25Mpa, mechanical property of materials σ s=980 MPa; σ b=1310 Mpa, Performance Ratio >=0.6, is characterized in that U type interface adopts the seal of particular design, guarantees the capacity requirement of suitability for industrialized production.
The design's tunnel type accumulator 3 operating pressures reach 620Mpa, bearing capacity 800 MPa, but consider that pressure surpasses after 600 MPa, and simple aqueous medium will freeze, and therefore, the pressure that food liquid machining adopts is no more than 600 MPa conventionally.
The Hydraulic Station that described hydraulic pressure unit 1 is 40-50Mpa, the time relay being connected by central processing unit 5
(7) according to the dwell time periodic duty of designing requirement.
What described power source 12 adopted is novel harmonic motor, and when pressure transmitter 2 enhances pressure, motor power consumption is constant, and than conventional motor power saving, more than 30%, volume I is attached on Hydraulic Station bedframe.
Described pressure transmitter 2 consists of double cylinder double acting by high pressure cylinder and low pressure (LP) cylinder and electro-hydraulic reversal valve, and two ends are provided with sub-chamber and normal pressure through hole, sub-chamber can with the main body dismounting of pressure transmitter 2, cleaning different medium, change sealing ring.
Compared with prior art, the beneficial effect of this device is: process unit make dendrobium candidum oral liquid, medicine materical crude slice beverage can synchronous production, the first section of being broken into after cleaning with fresh goods dendrobium candidum, after entering high speed beater, with clean water, according to the slurries ratio of dendrobium candidum, require dilution, pressurize 5-15 minute release pressure under the pressure of 450～550Mpa, pressurization, decompression cycles operate 3 partial nodes and are controlled by node sensor, and technique overall process is 0.65 hour 50L; Dendrobium candidum slurries after release pressure adopt 3 groups of apertures to be respectively 1.2 μ m, 0.8 μ m, 0.6 μ m ceramic membrane filter, Dendrobium officinale polysaccharide extract (oral liquid) removes slag to obtain, the purity super existing technique far away that quantitatively records polyoses content through alcohol precipitation, slag is pressed into medicine materical crude slice by pharmaceutical tabletting machine.
A kind of synchronous production technique of making dendrobium candidum oral liquid, medicine materical crude slice beverage that the present invention also provides, following 3 variablees can be set: the liquid ratio of dendrobium candidum dry product (maple bucket) and fresh goods and water, extract pressure and dwell time, corresponding according to eucaryotic cell structure demolition effect, utilize 3 pressurizations of circulation, reduce pressure into spiral jet nozzle, precipitation, concentrated, separation obtain dendrobium polysaccharide peptide, and the raffinate after separation is beverage.
Contrast drew with the process time; (UHP) variation of temperature and feed liquid chain rate, pressurized circulation number of times and pressure, is optimized the influence factor of dendrobium polysaccharide recovery rate, and conclusion is that the temperature of optimum optimizing condition is 18.5 ℃; The pressure that circulation pressurization is 3 times is respectively: 450Mpa10 minute, 500Mpa10 minute, 550Mpa10 minute, and the process time is 0.65 hour 5L, and chain rate is 1.25 o'clock, and the yield of polysaccharide can reach the more than 95% of stem of noble dendrobium content.
This application of installation step is: the section that () is just broken into dry product dendrobium candidum (maple bucket), with clean water, according to the liquid ratio of dendrobium candidum, soak at normal temperatures again, worry removes remaining water and with clean water, according to dendrobium candidum liquid ratio, enters high speed beater again, pressurize 5-15 minute release pressure under the pressure of 450～550Mpa, pressurization, decompression cycles operation 3 times.
(2) the fresh goods stem of noble dendrobium just enters high speed beater after the section of being broken into after cleaning, then dilutes according to the slurries ratio of dendrobium candidum with clean water, 15 minutes release pressures of pressurize under the pressure of 450～550Mpa, pressurization, decompression cycles operation 3 times; It is characterized in that: with electronic program, control pressure and generate and the general character function discharging, again in conjunction with spiral jet nozzle technique, under sensor information guiding, change positive negative energy, make stem of noble dendrobium liquid material produce void effect in spiral jet pipe chamber, nozzle exit supersonic jet swashs quick-fried dendrobium candidum plant cell.
Circulating pressure and dwell time can be set; According to eucaryotic cell structure demolition effect, be pressurised into successively: 450,500.550Mpa, the dwell time is: within 15 minutes, 10 minutes, 5 minutes, carry out decompression cycles and controlled by node sensor, product precipitation is concentrated is optimized for dendrobium polysaccharide peptide, and parting liquid is beverage.
Because stainless steel can meet foodstuff sanitation-stage requirement, the dendrobium candidum slurries after release of pressure adopt 3 groups of apertures to be respectively 1.2 μ m, 0.8 μ m, 0.6 μ m ceramic membrane filter removes slag, and by conventional pharmaceutical tabletting machine, slag are pressed into medicine materical crude slice.
Accompanying drawing explanation
Fig. 1 is pressure-bearing device tunnel type accumulator,
Fig. 2 is system and device schematic diagram.
The specific embodiment
This device 2 is further described by reference to the accompanying drawings below:
The conventional Hydraulic Station that described hydraulic pressure unit 1 is 40-50Mpa, the time relay 7 in central processing unit 5 connects is according to the dwell time periodic duty of designing requirement, when power source 12 is started working hydraulic pressure unit 1, due to power source 12 employings are harmonic motors, at pressure transmitter 2, enhance pressure time-harmonic wave motor power consumption constant, the conventional motor power saving of the little ratio of volume is more than 30%.
The pressure source of Hydraulic Station enters pressure transmitter 2 by pipeline, mode with multi-stage booster becomes pressurization pressure to tunnel type accumulator 3, tunnel type accumulator 3 is connected by three stainless steel tube gate-types, in gate-type stainless steel tube one end U type, take over another gate-type stainless steel tube of connection and be arranged in series into a tunnel, required gate-type is arranged according to the calculation of capacity of designing requirement, the number of permutations decides how many stainless steel tube series windings by the volume=internal diameter * length requiring, there is an end socket tunnel type accumulator 3 one end, on end socket, have a connecting hole, the import of spiral jet nozzle 4 first face has a connecting hole, by pipe, led on the end socket connecting hole of tunnel type accumulator 3, the little intermediate drum circle in inner chamber two of described spiral jet nozzle 4, the target piece that is greater than spout aperture is installed apart from spout 50mm place, target bulk matter is hard ceramic.
When the technological design condition tunnel type accumulator that is 500L 3 one end release pressure, the time value that central processing unit 5 is set by information processor 10, data acquisition unit 11, by signal conversion receiver 8, information processor 10, sent instructions to the time relay 7, power source 12 on the time relay 7 connection hydraulic pressure units 1, the work that stops power source 12 meet the circulation of dwell time, and node sensor 13 is determined the different dwell times.
The pressure sensing valve 6 that install at tunnel type accumulator 3 two ends, by the pressure information of pressure transmitter 2, security alarm information exchange is crossed signal conversion receiver 8, information processor 10 sends to central processing unit 5, the control valve 9 of opening tunnel type accumulator 3 one end is communicated with spiral jet nozzle 4, hydraulic fluid in tunnel type accumulator 3 enters in spiral jet nozzle 4, conversion at the positive negative energy of the interior generation of spiral jet nozzle 4, hard ceramic target piece is impacted in 2 Mach of supersonic jets of release of pressure ejection, further swash the yield that quick-fried stem of noble dendrobium plant cell improves Dendrobium officinale polysaccharide, three kinds of finished products synchronous output in a technological process, reduce the consumption of the energy.
Described tunnel type accumulator 3 is that 3 stainless steel pressure-bearing pipes connect into door case type, and the U-shaped adapter in one end of a plurality of doorframe pipes connects and is arranged in tunnel type, described in be arranged in tunnel the number of permutations by the volume=internal diameter * length of designing requirement, decided.
Described pressure transmitter 2 is comprised of high pressure cylinder and low pressure (LP) cylinder and electro-hydraulic reversal valve, for double cylinder double acting, (separately having special designs) two ends are provided with sub-chamber and normal pressure through hole, sub-chamber can dismantle with the main body of pressure transmitter 2, cleaning different medium, change sealing ring, in isolated pressure transmitter 2 from oil pressure, the oil gas of Hydraulic Station.
Pressure-bearing body important technological parameters
Design internal diameter of tube body d≤50 mm; Outer diameter D≤135 mm; Length 3000 mm; Footpath is than K=2.7, and working media is water.Operating pressure pW=620 Mpa, burst pressure pb=46.39pW=3246.3Mpa, design pressure pd=1.7pW=1200 Mpa, design temperature are room temperature; From strengthen pressure pA=0.89pW=640 Mpa, pressure ratio 16: safe-working pressure pA=0.81pW=568.25Mpa, mechanical property of materials σ s >=980 MPa; σ b >=1300 Mpa, Performance Ratio >=0.6.
The design's extra-high tension unit operating pressure reaches 620Mpa, bearing capacity 800 MPa, but consider that pressure surpasses after 600 MPa, and simple aqueous medium will freeze, and therefore, the pressure that food liquid machining adopts is no more than 600MPa conventionally.
Embodiment: dendrobium candidum oral liquid is produced
One, dry product processing
1, dry product immersion is 0.5-20mm by the disconnected section of dendrobium candidum dry product, be dipped to moisture content and be greater than 60% (weight content, general 24 hours), when soaking, there is cleaning action, after considering the remaining water of de-soak, with clean water, according to the liquid ratio of 65 to 1 dendrobium candidums, mix, with the making beating of high speed beater, enter storage tank and do pressurization preparation.
2, vavuum pump sucks 500L extra high voltage system device for the slurries of dendrobium candidum, pressure generator classification cycle is pressurised into 450,500,550Mpa each once, successively the dwell time be 15,10,5min, the 3rd release pressure rear slurry is at spiral
Produce 2 Mach of supersonic jets in jet nozzle and swash quick-fried stem of noble dendrobium plant cell, then membrane filtration removes slag, and cannedly under aseptic condition becomes a kind of dendrobium candidum special efficacy oral liquid.
Two, fresh goods processing
1, cleaning making beating is 0.5-20mm by iron-sheet dendrobe fresh product cleaning, shearing section, directly with clean water, according to the liquid ratio of 50 to 1 dendrobium candidums, with high speed beater, pulls an oar, and enters the pressurization of storage tank do and prepares.
2, the slurries of fresh dendrobium candidum suck 500L extra high voltage system device with vavuum pump, pressure generator classification cycle is pressurised into 450,500,550Mpa each once, each dwell time is 10min, the 3rd time release pressure rear slurry swashs quick-fried stem of noble dendrobium plant cell with 2 Mach of supersonic jets in spiral jet nozzle, then membrane filtration removes slag, and cannedly under aseptic condition becomes a kind of dendrobium candidum special efficacy oral liquid.
Three, micro-polysaccharide drink
1, concentration extraction: iron-sheet dendrobe fresh product is cleaned, is cut into 0.5-20mm section, use clean water according to 50 to 1 iron sheet stones
The solid-liquid ratio of dry measure used in former times, directly with the making beating of high speed beater, enters storage tank and does pressurization preparation.
Slurries suck 500L extra high voltage system device with vavuum pump, with pressure generator classification cycle pressurization 450.500.550Mpa respectively once, each dwell time 10min, the 3rd time release pressure rear slurry swashs quick-fried dendrobium candidum plant cell, then filter and remove residue with 2 Mach of supersonic jets in spiral jet nozzle.
Filtered fluid floats supernatant liquor with the alcohol precipitation method, then is respectively 1.2 μ m, 0.8 μ m, the concentrated polysaccharide underflow that to obtain of 0.6 μ m nano ceramics film dehydration with 3 groups of apertures, through the yield of the benzene phenol-sulfuric acid method quantitative assay polysaccharide of improvement, is the more than 95% of stem of noble dendrobium content.
2, rinsing liquid also contains polysaccharide and other element of 0.5-1.2% after measured, and rinsing liquid is canned under aseptic condition can become a kind of drinking water that contains micro-polysaccharide, and added value is considerably beyond the beverage of class mineral water.
Four, Dendrobium officinale polysaccharide medicine materical crude slice includes at least multiple other elements such as Dendrobium officinale polysaccharide more than 0.5-1.2%, alkaloid, EN due to the recrement after filtering, when being less than 20%, mixes with the solid tablet 5% of (medicinal regulation permission to use) edible drying to moisture content, with pharmaceutical tabletting machine film-making, be a kind of healthcare decoction pieces of low content polysaccharide, finished product packing.
Tool of the present invention has the following advantages and efficiency
Apply a kind of synchronous production technique of making dendrobium candidum oral liquid, medicine materical crude slice beverage, due to power source 12 employings are harmonic motors of a kind of novelty, at pressure transmitter 2, enhance pressure time-harmonic wave motor power consumption constant, the conventional motor power saving of the little ratio of volume is more than 30%, by electronic program, controls each safety alarm device and control valve is guaranteed technical process handling safety.
When process conditions are extra high voltage system device and the spiral jet nozzle below 500L, adopt pressure-bearing device tunnel type accumulator and the jet pipe inner chamber of stainless steel, reach foodstuff sanitation-stage requirement completely, maximum pressure is 6150Mpa, temperature is lower than 20 ℃, classification is pressurised into 450.500.550Mpa and circulates after 3 times, under the conversion of slurries positive negative energy in by spiral jet nozzle cavity, produce void effect, with the sharp quick-fried stem of noble dendrobium plant cell of 2 Mach of supersonic jets, polysaccharide, discharge more than 95%.
Because pressure transmitter is double cylinder double acting, can meet the large flow of industrialization production requirements, two ends are provided with sub-chamber and normal pressure through hole, sub-chamber can dismantle with the main body of pressure transmitter 2, cleaning different medium, replacing sealing ring, in can isolated pressure transmitter, from the oil pressure oil gas of Hydraulic Station, by sub-chamber, can avoid oil gas to pass pollution oral liquid, be the necessary condition of guaranteeing stem of noble dendrobium oral liquid, beverage medicine materical crude slice production sanitary standard.
The output that is M hour 500L in the process time can reach the above industrialization of middle rank, and 95% of the rate of releasing >=stem of noble dendrobium content of polysaccharide, has shortened the production time, and production process temperature is low, and operating cost is produced in the low saving of consuming energy; Improved product efficiency; Chain rate is to have reduced energy loss at 1: 25 o'clock, water resource is without waste, production technology overall process, without zero emission, meets the production standard of national environmental protection cleaned industry, can also be applied to low temperature sterilization, for example milk, wine, the beverage of food liquid in enormous quantities.
In sum, it is the innovation of oral liquid production method that (UHP) super-pressure circulation pressurization that the present invention adopts designs a model, belong to a kind of extension of common technology, with existing technique electromagnetic oscillation, enzyme digestion reaction, supercritical ultrasonics technology is compared, its industrialization production scale and polysaccharide yield maximize (different by the polyoses content of the different cultivars stem of noble dendrobium), and resulting optimum condition is not the value of setting, but within the scope imposing a condition, tunnel type accumulator adopts (UHP) super-pressure circulation pressurization to be combined with spiral jet nozzle, what obtain is best quantification process conditions.
Application of installation technique is simple, and electronic program control operation is convenient, safety, and operating cost is cheap, is suitable for automatic industrial and produces; Product color is good, and dissolubility is good, and active component is high, and the active ingredient in oral liquid is absorbed by the body completely.
Finally; it is also to be noted that; a kind of synchronous production process unit of making dendrobium candidum oral liquid, medicine materical crude slice, beverage; because its low temperature liquid super-pressure technique is that common technology can range of application and wide; what more than enumerate is only several specific embodiments of the present invention; obviously; the invention is not restricted to above embodiment; can also there be many retrofits, products innovation, patent family application; all distortion that those of ordinary skill in the art can directly derive or associate from content disclosed by the invention, all should think protection scope of the present invention.
Claims (2)
1. make a synchronous production device for dendrobium candidum oral liquid, medicine materical crude slice beverage, by hydraulic pressure unit (1), pressure transmitter (2), tunnel type accumulator (3), spiral jet nozzle (4), central processing unit (5), pressure sensing valve (6), the time relay (7), signal conversion receiver (8), control valve (9), information processor (10), data acquisition unit (11), power source (12), node sensor (13), jointly formed, central processing unit (5) connection signal conversion receiver (8), information processor (10), the time relay (7), information processor (10), data acquisition unit (11), the time relay (7) connection hydraulic pressure unit (1), power source (12), hydraulic pressure unit (1) pipe leads to and connects pressure transmitter (2), pressure transmitter (2) pipe leads to and connects tunnel type accumulator (3), the two ends of tunnel type accumulator (3) are provided with pressure sensing valve (6), tunnel type accumulator (3) one end is fixedly connected with pressure transmitter (2), one end pipe leads to and connects spiral jet nozzle (4), control valve (9), node sensor (13) is arranged on the tube connector of spiral jet nozzle (4) and tunnel type accumulator (3), it is characterized in that: described tunnel type accumulator (3) is that 3 stainless steel pressure-bearing pipes connect into door case type, the U-shaped adapter connection in one end of a plurality of doorframe pipes is arranged in tunnel type.
2. a kind of synchronous production device of making dendrobium candidum oral liquid, medicine materical crude slice beverage according to claim 1, is characterized in that: pressure-bearing body important technological parameters=design internal diameter of tube body d≤50 mm; Outer diameter D≤135 mm; Length 3000 mm; Footpath is than K=2.7, operating pressure pW=620 Mpa, burst pressure p
b=46.39pW=3246.3Mpa, design pressure p
d=1.7pW=1200 Mpa, design temperature are room temperature; From strengthen pressure pA=0.89pW=640 Mpa, pressure ratio 16: safe-working pressure pA=0.81pW=568.25Mpa, mechanical property of materials σ s=980 MPa; σ b=1310 Mpa, Performance Ratio>=0.6.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106177492A (en) * | 2016-07-21 | 2016-12-07 | 合肥工业大学 | A kind of method improving Herba Dendrobii fresh goods effective ingredient dissolution |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106177492A (en) * | 2016-07-21 | 2016-12-07 | 合肥工业大学 | A kind of method improving Herba Dendrobii fresh goods effective ingredient dissolution |
| CN106177492B (en) * | 2016-07-21 | 2019-11-08 | 合肥工业大学 | A method of improving the dissolution of Dendrobidium huoshanness fresh goods effective component |
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