CN107485887A - Liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer - Google Patents
Liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer Download PDFInfo
- Publication number
- CN107485887A CN107485887A CN201710789718.7A CN201710789718A CN107485887A CN 107485887 A CN107485887 A CN 107485887A CN 201710789718 A CN201710789718 A CN 201710789718A CN 107485887 A CN107485887 A CN 107485887A
- Authority
- CN
- China
- Prior art keywords
- spl
- valve
- liquid
- lacquer disk
- screw extrusion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61J—CONTAINERS SPECIALLY ADAPTED FOR MEDICAL OR PHARMACEUTICAL PURPOSES; DEVICES OR METHODS SPECIALLY ADAPTED FOR BRINGING PHARMACEUTICAL PRODUCTS INTO PARTICULAR PHYSICAL OR ADMINISTERING FORMS; DEVICES FOR ADMINISTERING FOOD OR MEDICINES ORALLY; BABY COMFORTERS; DEVICES FOR RECEIVING SPITTLE
- A61J3/00—Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61J—CONTAINERS SPECIALLY ADAPTED FOR MEDICAL OR PHARMACEUTICAL PURPOSES; DEVICES OR METHODS SPECIALLY ADAPTED FOR BRINGING PHARMACEUTICAL PRODUCTS INTO PARTICULAR PHYSICAL OR ADMINISTERING FORMS; DEVICES FOR ADMINISTERING FOOD OR MEDICINES ORALLY; BABY COMFORTERS; DEVICES FOR RECEIVING SPITTLE
- A61J3/00—Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms
- A61J3/04—Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms into the form of ointments
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K36/00—Medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicines
- A61K36/18—Magnoliophyta (angiosperms)
- A61K36/185—Magnoliopsida (dicotyledons)
- A61K36/48—Fabaceae or Leguminosae (Pea or Legume family); Caesalpiniaceae; Mimosaceae; Papilionaceae
- A61K36/484—Glycyrrhiza (licorice)
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
- B01D1/065—Evaporators with vertical tubes by film evaporating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/22—Evaporating by bringing a thin layer of the liquid into contact with a heated surface
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
- B01D1/305—Demister (vapour-liquid separation)
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0207—Control systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0261—Solvent extraction of solids comprising vibrating mechanisms, e.g. mechanical, acoustical
- B01D11/0265—Applying ultrasound
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/028—Flow sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/003—Filters in combination with devices for the removal of liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D2011/002—Counter-current extraction
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Natural Medicines & Medicinal Plants (AREA)
- Life Sciences & Earth Sciences (AREA)
- Medicinal Chemistry (AREA)
- Pharmacology & Pharmacy (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Physics & Mathematics (AREA)
- Acoustics & Sound (AREA)
- Mechanical Engineering (AREA)
- Automation & Control Theory (AREA)
- Alternative & Traditional Medicine (AREA)
- Biotechnology (AREA)
- Botany (AREA)
- Medical Informatics (AREA)
- Microbiology (AREA)
- Mycology (AREA)
- Epidemiology (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention discloses a kind of liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer, batcher is provided with above body, internal body is provided with three-level to turning SPL roller, every grade is equipped with radix glycyrrhizae guide groove to turning below SPL roller, afterbody guide groove connects the hopper of radix glycyrrhizae elevator, the blow tank connection screw extrusion dewaterer of elevator；Elevator is provided with liquid feed valve, and body upper is provided with filter and drain pipe, drain pipe connection climbing-falling film evaporator；SPL lacquer disk(-sc) pulse gas explosion device is provided with body, the body lower left corner is provided with mechanical ultrasonic vibrator, body side automatically controls steam valve and manual steam valve by jet chimney connection, the three-level of the present invention all has distinguishing feature to turning SPL roller, SPL lacquer disk(-sc) pulse gas explosion device and mechanical ultrasonic vibrator, the leaching extraction for promoting radix glycyrrhizae effective ingredient can be cooperateed with, possesses stronger actual application value.
Description
Technical field
The present invention relates to a kind of liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer.
Background technology
Extract of licorice root is treatment chronic adrenocortical hypofunction traditional Chinese patent medicine, and traditional processing mode is by radix glycyrrhizae
Section is boiled merging concentration three times with decocting and formed, and manufactured energy consumption is big, and time length, extraction efficiency is low, and can not realize scale
Production, and high-efficiency and continuous rubs crowded adverse current extraction innovative design with the hands and effectively realizes serialization high efficiency extraction extract of licorice root, substantially reduces life
Cost is produced, improves the performance of enterprises.
The content of the invention
The technical problem to be solved in the present invention is exactly overcome the deficiencies in the prior art, there is provided a kind of simple and practical, energy
Enough extraction elements for extracting effective ingredient in radix glycyrrhizae to greatest extent.
For overcome the deficiencies in the prior art, the present invention takes following technical scheme：
A kind of liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer, including body, it is characterised in that：Body
Top is provided with batcher, and internal body is provided with three-level to turning SPL roller, is continuous sample to turning SPL roller surface
Bar curved surface, every grade is equipped with radix glycyrrhizae guide groove to turning below SPL roller, and afterbody guide groove connects the material of radix glycyrrhizae elevator
Bucket, the blow tank connection screw extrusion dewaterer of elevator；Elevator is provided with liquid feed valve, and body upper is provided with filter and gone out
The inlet communication of liquid pipe, the filtered liquid feed valve of drain pipe and duplex strainer, the outlet of duplex strainer by the first filtrate pipe,
Filtrate valve, filtrate pump, pump discharge valve, the second filtrate pipe connect with the inlet of receiver, and receiver lower end is through outlet valve, charging
Pipe connect climbing-falling film evaporator, climbing-falling film evaporator by pipeline connect vapour liquid separator, the two of vapour liquid separator upper end
Secondary steam (vapor) outlet connects steamdrum through secondary steam pipe, and steamdrum is evenly arranged in the suitable position of body；Sample is provided with body
Bar curve lacquer disk(-sc) pulse gas explosion device, SPL lacquer disk(-sc) pulse gas explosion device is by SPL lacquer disk(-sc), cylinder, expansion link, pressure
Contracting air hose, baffle ring and pot shape spherical faced pan composition, SPL lacquer disk(-sc) section thick middle thin edge, are shaped as SPL, sample
Pot shape spherical faced pan is provided with below bar curve lacquer disk(-sc), SPL lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive
Expansion link drives SPL lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compressed air hose and also connects SPL glue
Disk inner chamber body；The body lower left corner is provided with mechanical ultrasonic vibrator, is rotated at a high speed by actuating unit kinetic energy, mechanical ultrasonic swashs
The structure of device of shaking is spherical cap shape, and spherical cap edge is smooth splined curve, there is crest, trough from spherical cap center to edge
The feature for progressively expanding and continuously dissipating；Body side automatically controls steam valve and manual steam valve by jet chimney connection,
It is in parallel by jet chimney to automatically control steam valve and manual steam valve, temperature sensor, which is installed in filter, submerges leachate
In, temperature sensor automatically controls steam valve by signal wire connection, and body high temperature position is thermally shielded isothermal holding.
The shell at the body roller position is spline surface, in Pear-Shaped.
Clean-up port is provided with below the body.
Baffle ring is provided with above the pot shape spherical faced pan.
The body is connected as one with elevator by flange, is sealing structure and easy to disassemble.
Under the recovered liquid valve of the screw extrusion dewaterer lower end leakage fluid dram, recovery liquid pump, valve, recovery liquid pipe and body
Portion connects, and is advantageous to recycle the residual water in the dregs of a decoction.
The steam valve that automatically controls automatically controls opening for steam valve according to the temperature height control of temperature sensor feedback
The amount of closing, adjust the intake of steam so that in body leachate temperature keep leaching need temperature, manual steam valve with
The handling of heat temperature raising can be strengthened by automatically controlling steam valve and being installed in parallel.
The radix glycyrrhizae of chopping is fallen into body through batcher, and the radix glycyrrhizae of chopping is extruded turning SPL roller by three-level,
Exported afterwards by elevator.Body is integrally connected with elevator by flange, and demolition and maintenance are also allowed for for sealing structure；Steam
Through automatically controlling steam valve, jet chimney enters in body, and leachate is heated into the temperature that leaching needs, dress is maintained during work
The certain position of liquid level is put, device replenisher is filled into by liquid feed valve control, overflowed by drain pipe, reaches liquid phase disengaging balance,
The radix glycyrrhizae so shredded is able to realize that counter current contacting leaches with liquid phase water in the case where entering device and three-level squeezing effect, is squeezed due to strong
Pressure promotes strong imbibition, realize most penetrate by force, the radix glycyrrhizae effective ingredient of adverse current chopping permeate leaches, reach Increasing Production and Energy Saving emission reduction.
The dregs of a decoction after leaching are exported by the blow tank of elevator, are dehydrated into screw extrusion dewaterer, the water warp of recovery
The recovered liquid valve of screw extrusion dewaterer lower end leakage fluid dram, recovery liquid pump, valve, recovery liquid pipe flow back to underpart, the dregs of a decoction from
Slag-drip opening is discharged, and the denseer radix glycyrrhizae effective ingredient liquid of counter-current extraction is tentatively filtered by filter, and primary filtrate is through drain pipe, filtering
Liquid feed valve enters duplex strainer and carries out in-depth filtration processing, and the filtrate after filtering is in the presence of filtrate pump through the first filtrate
Pipe, filtrate valve, filtrate pump, pump discharge valve, the second filtrate pipe are stored into receiver, outlet valve of the filtrate through receiver lower end,
Filtrate delivery pipe, feed pipe enter climbing-falling film evaporator, and climbing-falling film evaporator is that two groups of heating tubes are installed in shell side, left
To rise membrane type, right side is falling film type for side, and heating steam enters climbing-falling film evaporator shell side through steam inlet, and heating steam is rising
Feed liquid in pipe is transferred heat to outside membrane tube, film supplying tube, caused condensed water is discharged through the drain valve of bottom first, and filtrate is through bottom
Feed pipe is introduced into a liter membrane tube heating, and explosive evaporation, liquid-vapor mixture stretches film forming in pipe, rises to top, be then transferred to
Second half film supplying tube heats, then carries out falling film evaporation, and liquid-vapor mixture enters vapour liquid separator, after separation, secondary steaming from bottom
Vapour exports from separator top through indirect steam, secondary steam pipe be discharged into steamdrum to body carry out Heat preservation, concentrate from
Bottom concentrated solution outlet discharge, carries out subsequent treatment.
SPL roller surface is continuous spline surface, and corresponding bearing arrangement is easy to seal waterproof, adapts to strength and squeezes
Press and turn to turning and extruding differential pair, particularly advantageous extrude by force grinds crushing with stranding, promotes the counter-current extraction of the radix glycyrrhizae and water shredded sweet
Effective herbal ingredient dissolution.SPL roller bites that continuous reliable, extruding compression ratio is especially big to material, and SPL roller is bent
The differential stranding in face grinds reliable, durable, skimming over property is good, and separating twice effect is also especially good.
Core component is SPL lacquer disk(-sc), and thick edge is slightly thin among lacquer disk(-sc) section, and general shape is SPL, glue
Disk compresses pot shape spherical faced pan and forms airtight cavity, to wherein inputting compressed air, when air pressure reaches certain value, and lacquer disk(-sc) meeting
Generation is flipped up suddenly, is produced explosion type release to the compressed air wherein stored, can be produced explosion vibration shock wave, especially
It is favourable to promote material gas explosion to stir with leaching mass transfer.
Cylinder can drive expansion link to drive SPL lacquer disk(-sc) to move up and down, expansion link front hollow connection compressed air hose
Also UNICOM's lacquer disk(-sc) inner chamber body, and realized by axle sleeve and body isolate it is closed prevent leakage, and can flexibly stretch；When expansion link drives
Dynamic lacquer disk(-sc) can form airtight cavity when compressing pot shape spherical faced pan, empty at this moment by compressed air hose to wherein inputting compressed air
Atmospheric pressure rises, until SPL lacquer disk(-sc) rim pressure transfinites triggering, produces and is flipped up under lacquer disk(-sc) integral pressure acts on pair
The compressed air of interior storage produces explosion type release, and at this moment expansion link bounces back again, and just the reply of energy automatic elastic is flipped back to original to lacquer disk(-sc)
Carry out initial state, may be repeated do action, baffle ring can assist the upset of SPL lacquer disk(-sc) in case of need
Reset.
Mechanical ultrasonic vibrator rotates at a high speed in the lower left corner of device, by actuating unit kinetic energy, and axle sleeve can realize liquid
Mutually simultaneously favourable vibrator rotates at a high speed for sealing.
The structure of mechanical ultrasonic vibrator is spherical cap shape, and spherical cap edge is smooth splined curve, from spherical cap
Center has crest, trough progressively to expand continuous diverging feature to edge.Such structure has good bulk strength, when machinery is super
Sound wave vibrator is driven by actuating unit in the liquid phase to be rotated at a high speed, it is clear that the strong cavitation that can produce similar ultrasonic wave is imitated
Should, strength promotes the mass transport process of counterflow leaching, and collaboration promotes the dissolving of radix glycyrrhizae effective ingredient to leach.
Compared with prior art, beneficial effects of the present invention also reside in：
SPL roller material bites that continuous reliable, extruding compression ratio is especially big, differential to rub that to grind separating twice effect especially good with the hands,
Extruding realizes most perfect adaptation to three-level with counterflow leaching by force；
SPL lacquer disk(-sc) pulse gas explosion device can effectively simulate, produce macroscopical discontinuous blast, encourage the strong pulsatile impact of liquid phase；
Mechanical ultrasonic vibrator rotates at a high speed in the liquid phase, ingenious can produce high frequency and be imitated similar to the strong cavitation of ul-trasonic irradiation
Should；
Climbing-falling film evaporator can obtain higher evaporation rate, can improve the cocnentration factor of product, caused secondary using it
Steam and steamdrum carry out Heat preservation to body and enter end of line heat utilization, are advantageous to energy-saving and emission-reduction.
Above four main measures all have distinguishing feature, can cooperate with the leaching extraction for promoting radix glycyrrhizae effective ingredient, have ability
Field technique personnel are difficult to the operation principle predicted and technique effect, possess stronger actual application value.
Brief description of the drawings
Fig. 1 is the planar structure schematic diagram of the present invention.
Fig. 2 is SPL roller end face mplifying structure schematic diagram.
Fig. 3 is the partial enlargement structural representation of SPL lacquer disk(-sc) pulse gas explosion device.
Fig. 4 is the main structure diagram of mechanical ultrasonic vibrator.
Fig. 5 is the overlooking the structure diagram of mechanical ultrasonic vibrator.
Fig. 6 is the present invention looks up structural representation of mechanical ultrasonic vibrator.
Fig. 7 is the strabismus structural representation of bowing of mechanical ultrasonic vibrator.
Fig. 8 is the oblique present invention looks up structural representation of mechanical ultrasonic vibrator.
Each label represents in figure：
A, to turning SPL roller；B, SPL lacquer disk(-sc)；C, mechanical ultrasonic vibrator；1st, body；2nd, filter；3rd, go out
Liquid pipe；4th, liquid level；5th, guide groove；6th, hopper；7th, clean-up port；8th, elevator；9th, cylinder；10th, expansion link；11st, compressed air hose；
12nd, baffle ring；13rd, spherical faced pan；14th, actuating unit；15th, blow tank；16th, liquid feed valve；20th, batcher；21st, screw extrusion is dehydrated
Machine；27th, recovered liquid valve；28th, liquid pump is reclaimed；29th, valve；30th, liquid pipe is reclaimed；60th, steam valve is automatically controlled；61st, manual steam
Valve；62nd, jet chimney；63rd, signal wire；64th, temperature sensor；70th, duplex strainer；71st, liquid feed valve is filtered；72nd, filtrate is defeated
Send pipe；73rd, the first filtrate pipe；74th, filtrate valve；75th, filtrate pump；76th, pump discharge valve；77th, the second filtrate pipe；78th, receiver；
79th, outlet valve；90th, climbing-falling film evaporator；91st, membrane tube is risen；92nd, film supplying tube；93rd, steam inlet；94th, the first drain valve；95、
Feed pipe；96th, indirect steam exports；97th, concentrated solution outlet；98th, secondary steam pipe；99th, steamdrum；100th, vapour liquid separator.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
Liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer as Figure 1-Figure 8, including body 1,
It is characterized in that：The top of body 1 is provided with batcher 20, and the inside of body 1 is provided with three-level to turning SPL roller A, to turning batten
Curve roller A surfaces are continuous spline surface, and every grade is equipped with radix glycyrrhizae guide groove 5, afterbody to turning below SPL roller A
Guide groove 5 connects the hopper 6 of radix glycyrrhizae elevator 8, and the blow tank 15 of elevator 8 connects screw extrusion dewaterer 21；Set on elevator 8
There is liquid feed valve 16, the top of body 1 is provided with filter 2 and drain pipe 3, the filtered liquid feed valve 71 of drain pipe 3 and duplex strainer 70
Inlet communication, the outlet of duplex strainer 70 passes through the first filtrate pipe 73, filtrate valve 74, filtrate pump 75, pump discharge valve 76,
Two filtrate pipes 77 connect with the inlet of receiver 78, and the lower end of receiver 78 is through outlet valve 79, filtrate delivery pipe 72, feed pipe 95
Climbing-falling film evaporator 90 is connected, climbing-falling film evaporator 90 connects vapour liquid separator 100, vapour liquid separator 100 by pipeline
The indirect steam outlet 96 of upper end connects steamdrum 99 through secondary steam pipe 98, and steamdrum 99 is evenly arranged in the appropriate of body 1
Position；SPL lacquer disk(-sc) pulse gas explosion device is provided with body 1, SPL lacquer disk(-sc) pulse gas explosion device is by SPL glue
Disk B, cylinder 9, expansion link 10, compressed air hose 11, baffle ring 12 and pot shape spherical faced pan 13 form, in SPL lacquer disk(-sc) B-section
Between thick rim it is thin, be shaped as SPL, be provided with pot shape spherical faced pan 13 below SPL lacquer disk(-sc) B, SPL lacquer disk(-sc) B is through stretching
Contracting bar 10 connects the cylinder 9 outside body 1, and cylinder 9 can drive expansion link 10 to drive SPL lacquer disk(-sc) B to move up and down, expansion link
10 front hollows simultaneously connect compressed air hose 11 and also connect SPL lacquer disk(-sc) B inner chamber bodies；The lower left corner of body 1 is provided with mechanical ultrasonic
Wave excitation device C, rotated at a high speed by the kinetic energy of actuating unit 14, mechanical ultrasonic vibrator C structure is spherical cap shape, and spherical cap side
Edge is smooth splined curve, there is the feature that crest, trough progressively expand and continuously dissipated from spherical cap center to edge；Machine
The side of body 1 automatically controls steam valve 60 and manual steam valve 61 by the connection of jet chimney 62, automatically controls steam valve 60 and hand
Dynamic steam valve 61 is in parallel by jet chimney 62, and temperature sensor 64, which is installed in filter 2, to be submerged in leachate, TEMP
Device 64 automatically controls steam valve 60 by the connection of signal wire 63, and the high temperature position of body 1 is thermally shielded isothermal holding.
The shell at the roller position of body 1 is spline surface, in Pear-Shaped.
The lower section of body 1 is provided with clean-up port 7.
The top of pot shape spherical faced pan 13 is provided with baffle ring 12.
The body 1 is connected as one with elevator 8 by flange, is sealing structure and easy to disassemble.
The recovered liquid valve 27 of the lower end leakage fluid dram of screw extrusion dewaterer 21, recovery liquid pump 28, valve 29, recovery liquid pipe
30 connect with the bottom of body 1, are advantageous to carry out recycling to the Liquid Residue in the dregs of a decoction.
It is described to automatically control the temperature height control that steam valve 60 feeds back according to temperature sensor 64 and automatically control steam valve
60 opening and closing amount, the intake of steam is adjusted, so that the temperature of leachate keeps the temperature that leaching needs in body 1, manually
Steam valve 61 can strengthen the handling of heat temperature raising with automatically controlling steam valve 60 and being installed in parallel.
Radix glycyrrhizae after chopping is fallen into body 1 through batcher, and the radix glycyrrhizae of chopping is squeezed by three-level to turning SPL roller A
Pressure, is exported by elevator 8 afterwards.Body 1 is integrally connected with elevator 8 by flange, and dismounting dimension is also allowed for for sealing structure
Shield；Steam is through automatically controlling steam valve 60, jet chimney 62 enters in body 1, and leachate is heated to the temperature of leaching needs,
Device liquid level 4 certain position is maintained during work, device replenisher is filled into by liquid feed valve control, overflowed, reached by drain pipe
Liquid phase disengaging balance, the radix glycyrrhizae so shredded are able to realize counter current contacting with liquid phase water in the case where entering device and three-level squeezing effect
Leach, because strong extruding promotes strong imbibition, realize most penetrate by force, the radix glycyrrhizae effective ingredient of adverse current chopping permeate leaches, reach
Increasing Production and Energy Saving emission reduction.
The dregs of a decoction after leaching are exported by the blow tank of elevator 8, are dehydrated into screw extrusion dewaterer 21, the water of recovery
From the lower end leakage fluid dram discharge of screw extrusion dewaterer 21, recovered liquid valve, recovery liquid pump 28, valve 29, recovery liquid pipe 30 flow back to
Underpart, the dregs of a decoction are discharged from slag-drip opening, and the denseer radix glycyrrhizae effective ingredient liquid of counter-current extraction is tentatively filtered by filter 2, just
Filtrate enters duplex strainer 70 through drain pipe 3, filtering liquid feed valve 71 and carries out in-depth filtration processing, and the filtrate after filtering is in filtrate
Enter reservoir through the first filtrate pipe 73, filtrate valve 74, filtrate pump 75, pump discharge valve 76, the second filtrate pipe 77 in the presence of pump 75
Tank 78 is stored, and outlet valve 79 of the filtrate through the lower end of receiver 78, filtrate delivery pipe 72, feed pipe 95 enter climbing-falling film evaporator
90, climbing-falling film evaporator 90 is that two groups of heating tubes are installed in shell side, and to rise membrane type, right side is falling film type in left side, and heating is steamed
Vapour enters the shell side of climbing-falling film evaporator 90 through steam inlet 93, and heating steam passes heat outside liter membrane tube 91, film supplying tube 92
Feed liquid in pipe is passed, caused condensed water is discharged through the first drain valve of bottom 94, and filtrate is introduced into a liter film through bottom feed pipe 95
Pipe 91 heats, and explosive evaporation, liquid-vapor mixture stretches film forming in pipe, rises to top, is then transferred to second half film supplying tube 92
Heating, then carries out falling film evaporation, and liquid-vapor mixture enters vapour liquid separator 100 from bottom, and after separation, indirect steam is from separator
Top is discharged into steamdrum 99 through indirect steam outlet 96, secondary steam pipe 98 and carries out Heat preservation to body 1, and concentrate is from bottom
Concentrated solution outlet 97 is discharged, and carries out subsequent treatment.
SPL roller A surfaces are continuous spline surface, and corresponding bearing arrangement is easy to seal waterproof, adapts to strength and squeezes
Press and turn to turning and extruding differential pair, particularly advantageous extrude by force grinds crushing with stranding, promotes the counter-current extraction of the radix glycyrrhizae and water shredded sweet
Effective herbal ingredient dissolution.SPL roller A bites that continuous reliable, extruding compression ratio is especially big, SPL roller A to material
The differential stranding of curved surface grinds reliable, durable, skimming over property is good, and separating twice effect is also especially good.
Core component is SPL lacquer disk(-sc) B, and the thick edge in lacquer disk(-sc) section centre is slightly thin, and general shape is SPL,
Lacquer disk(-sc) compresses pot shape spherical faced pan and forms airtight cavity, to wherein inputting compressed air, when air pressure reaches certain value, and lacquer disk(-sc)
It can produce and be flipped up suddenly, explosion type release is produced to the compressed air wherein stored, explosion vibration shock wave can be produced, it is special
Not favorably material gas explosion is not promoted to stir with leaching mass transfer.
Cylinder 9 can drive expansion link 10 to drive SPL lacquer disk(-sc) B to move up and down, the connection compression of the front hollow of expansion link 10
The also UNICOM's lacquer disk(-sc) B inner chamber bodies of air hose 11, and realized with body by axle sleeve isolate it is closed prevent leakage, and can flexibly stretch；
Airtight cavity can be formed when expansion link 10 drives lacquer disk(-sc) B compression pot shape spherical faced pans 13, at this moment by compressed air hose 11 to it
Middle input compressed air, air pressure rise, the triggering until SPL lacquer disk(-sc) B rim pressures transfinite, and produce lacquer disk(-sc) and integrally press
The compressed air for being flipped up internally storing under power effect produces explosion type release, and at this moment expansion link 10 bounces back again, and lacquer disk(-sc) is with regard to energy
Automatic elastic is replied and is flipped back to original initial state, may be repeated do action, baffle ring 12 can be in case of need
SPL lacquer disk(-sc) B upset is assisted to reset.
Mechanical ultrasonic vibrator C rotates at a high speed in the lower left corner of device, by the kinetic energy of actuating unit 14, and axle sleeve can be realized
Liquid phase sealing and the rotation at a high speed of favourable vibrator.
Mechanical ultrasonic vibrator C structure is spherical cap shape, and spherical cap edge is smooth splined curve, from spherical cap
Center has crest, trough progressively to expand continuous diverging feature to edge.
Such structure has good bulk strength, when mechanical ultrasonic vibrator C passes through actuating unit 14 in the liquid phase
Drive and rotate at a high speed, it is clear that the strong cavitation effect of similar ultrasonic wave can be produced, strength promotes the mass transport process of counterflow leaching, association
Leached with the dissolving of radix glycyrrhizae effective ingredient is promoted.
Above-mentioned simply presently preferred embodiments of the present invention, not makees any formal limitation to the present invention.It is any to be familiar with sheet
The technical staff in field, in the case where not departing from technical solution of the present invention scope, all using the technology contents of the disclosure above
Many possible changes and modifications are made to technical solution of the present invention, or are revised as the equivalent embodiment of equivalent variations.Therefore, it is all
It is the content without departing from technical solution of the present invention, any is simply repaiied to made for any of the above embodiments according to the technology of the present invention essence
Change, equivalent variations and modification, all should fall in the range of technical solution of the present invention protection.
Claims (5)
1. a kind of liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer, including body, it is characterised in that：Machine
Batcher is provided with above body, internal body is provided with three-level to turning SPL roller, is continuous to turning SPL roller surface
Spline surface, every grade is equipped with radix glycyrrhizae guide groove to turning below SPL roller, afterbody guide groove connection radix glycyrrhizae elevator
Hopper, the blow tank connection screw extrusion dewaterer of elevator, the recovered liquid valve of screw extrusion dewaterer lower end leakage fluid dram, recovery
Liquid pump, valve, recovery liquid pipe connect with underpart；Elevator is provided with liquid feed valve, and body upper is provided with filter and goes out liquid
The inlet communication of pipe, the filtered liquid feed valve of drain pipe and duplex strainer, the outlet of duplex strainer pass through the first filtrate pipe, filter
Liquid valve, filtrate pump, pump discharge valve, the second filtrate pipe connect with the inlet of receiver, and receiver lower end is through outlet valve, feed pipe
Connect climbing-falling film evaporator, climbing-falling film evaporator by pipeline connect vapour liquid separator, vapour liquid separator upper end it is secondary
Steam (vapor) outlet connects steamdrum through secondary steam pipe, and steamdrum is evenly arranged in the suitable position of body；Batten is provided with body
Curve lacquer disk(-sc) pulse gas explosion device, SPL lacquer disk(-sc) pulse gas explosion device is by SPL lacquer disk(-sc), cylinder, expansion link, compression
Air hose, baffle ring and pot shape spherical faced pan composition, SPL lacquer disk(-sc) section thick middle thin edge, are shaped as SPL, batten
Pot shape spherical faced pan is provided with below curve lacquer disk(-sc), SPL lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder, which can drive, to be stretched
Contracting bar drives SPL lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compressed air hose and also connects SPL lacquer disk(-sc)
Inner chamber body；The body lower left corner is provided with mechanical ultrasonic vibrator, is rotated at a high speed by actuating unit kinetic energy, mechanical ultrasonic wave excitation
The structure of device is spherical cap shape, and spherical cap edge is smooth splined curve, have from spherical cap center to edge crest, trough by
The feature that step expands and continuously dissipated；Body side automatically controls steam valve and manual steam valve by jet chimney connection, from
Dynamic control steam valve and manual steam valve are in parallel by jet chimney, and temperature sensor, which is installed in filter, submerges leachate
In, temperature sensor automatically controls steam valve by signal wire connection, and body high temperature position is thermally shielded isothermal holding.
2. the liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer, its feature exist according to claim 1
In：The shell at the body roller position is spline surface, in Pear-Shaped.
3. the liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer, its feature exist according to claim 2
In：Clean-up port is provided with below the body.
4. the liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer, its feature exist according to claim 3
In：Baffle ring is provided with above the pot shape spherical faced pan.
5. the liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer, its feature exist according to claim 4
In：The body is connected as one with elevator by flange, is sealing structure and easy to disassemble.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710789718.7A CN107485887A (en) | 2017-09-05 | 2017-09-05 | Liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710789718.7A CN107485887A (en) | 2017-09-05 | 2017-09-05 | Liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107485887A true CN107485887A (en) | 2017-12-19 |
Family
ID=60651611
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710789718.7A Withdrawn CN107485887A (en) | 2017-09-05 | 2017-09-05 | Liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107485887A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113813640A (en) * | 2021-10-14 | 2021-12-21 | 丽江英煌集生物工程有限公司 | Purified macamide activity refining device and method |
-
2017
- 2017-09-05 CN CN201710789718.7A patent/CN107485887A/en not_active Withdrawn
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113813640A (en) * | 2021-10-14 | 2021-12-21 | 丽江英煌集生物工程有限公司 | Purified macamide activity refining device and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107485886A (en) | Liquid extract of liquorice extraction element with shredding machine and screw extrusion dewaterer | |
| CN107485887A (en) | Liquid extract of liquorice extraction element with batcher and screw extrusion dewaterer | |
| CN107321003A (en) | With batcher and extruding-desiccation machine to transfer roller cartridge type huperzine leaching device | |
| CN107376413A (en) | With shredding machine and drying machine to transfer roller cartridge type liquid extract of liquorice extraction element | |
| CN107349634A (en) | Liquid extract of liquorice extraction element with shredding machine and charcoal processing forming machine | |
| CN107469393A (en) | With cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element | |
| CN107496495A (en) | Liquid extract of liquorice extraction element with cleaning machine and charcoal processing forming machine | |
| CN107362582A (en) | With batcher and extruding-desiccation machine to transfer roller cartridge type liquid extract of liquorice extraction element | |
| CN107349635A (en) | Liquid extract of liquorice extraction element with batcher and drying machine | |
| CN107485885A (en) | With shredding machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element | |
| CN107362577A (en) | With batcher and charcoal processing forming machine to transfer roller cartridge type huperzine leaching device | |
| CN107469394A (en) | With batcher and drying machine to transfer roller cartridge type liquid extract of liquorice extraction element | |
| CN107362584A (en) | Liquid extract of liquorice extraction element with shredding machine and drying machine | |
| CN107349631A (en) | SPL pulley type liquid extract of liquorice extraction element with batcher and dewaterer | |
| CN107376416A (en) | Liquid extract of liquorice extraction element with cleaning machine and extruding-desiccation machine | |
| CN107376414A (en) | With cleaning machine and extruding-desiccation machine to transfer roller cartridge type liquid extract of liquorice extraction element | |
| CN107468749A (en) | Liquid extract of liquorice extraction element with batcher and charcoal processing forming machine | |
| CN107456778A (en) | Mechanical ultrasonic formula liquid extract of liquorice extraction element with shredding machine and drying machine | |
| CN107441761A (en) | Liquid extract of liquorice extraction element with cleaning machine and screw extrusion dewaterer | |
| CN107485888A (en) | Liquid extract of liquorice extraction element with cleaning machine and drying machine | |
| CN107469388A (en) | SPL pulley type liquid extract of liquorice extraction element with batcher and drying machine | |
| CN107362581A (en) | SPL pulley type liquid extract of liquorice extraction element with cleaning machine and filter | |
| CN107469397A (en) | With batcher and charcoal processing forming machine to transfer roller cartridge type liquid extract of liquorice extraction element | |
| CN107469395A (en) | With cleaning machine and drying machine to transfer roller cartridge type liquid extract of liquorice extraction element | |
| CN107362580A (en) | SPL pulley type liquid extract of liquorice extraction element with shredding machine and dewaterer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20171219 |
|
| WW01 | Invention patent application withdrawn after publication |