CN107469393A - With cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element - Google Patents
With cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element Download PDFInfo
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- CN107469393A CN107469393A CN201710783615.XA CN201710783615A CN107469393A CN 107469393 A CN107469393 A CN 107469393A CN 201710783615 A CN201710783615 A CN 201710783615A CN 107469393 A CN107469393 A CN 107469393A
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- China
- Prior art keywords
- transfer roller
- dewaterer
- lacquer disk
- cleaning machine
- radix glycyrrhizae
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- 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
-
- 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
- B01D11/00—Solvent extraction
- B01D2011/002—Counter-current extraction
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- Acoustics & Sound (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Cleaning By Liquid Or Steam (AREA)
Abstract
The invention discloses it is a kind of with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, bubble washer is sequentially connected radix glycyrrhizae conveyer, shredding machine and body, internal body is provided with three-level to transfer roller cylinder, it is cylinder to transfer roller cylinder, every grade is equipped with radix glycyrrhizae guide groove below transfer roller cylinder, afterbody guide groove connects the hopper of radix glycyrrhizae elevator, and the blow tank of elevator is connected through screw extrusion dewaterer;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, the three-level of the present invention all has distinguishing feature to transfer roller cylinder, 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, operation principle and the technique effect for being difficult to predict with those skilled in the art, possess stronger actual application value.
Description
Technical field
The present invention relates to it is a kind of with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element.
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 leaching devices 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:
It is a kind of with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, including body, it is characterised in that:Gas
The cleaning machine discharging opening for steeping cleaning machine is connected by radix glycyrrhizae conveyer with chopping machine inlet, and machine is provided with below shredding machine discharging opening
Body, internal body are provided with three-level to transfer roller cylinder, are cylinder to transfer roller cylinder, and every grade is equipped with radix glycyrrhizae guide groove below transfer roller cylinder,
Afterbody guide groove connects the hopper of radix glycyrrhizae elevator, the blow tank connection screw extrusion dewaterer of elevator;Set on elevator
There is liquid feed valve, body upper is provided with filter and drain pipe, and drain pipe connects through receiver, liquid storage tube, reservoir pump, reservoir delivery pipe
Filtration system is connect, filtration system connects climbing-falling film through filtrate outlet pipe, filtrate tank, filtrate pipe, filtrate delivery pump, filtrate delivery pipe
Evaporator, climbing-falling film evaporator connect vapour liquid separator by pipeline, and the indirect steam of vapour liquid separator upper end is exported through two
Secondary steam pipe connects steamdrum, and steamdrum is evenly arranged in the suitable position of body;SPL lacquer disk(-sc) pulse is provided with body
Gas explosion device, SPL lacquer disk(-sc) pulse gas explosion device by SPL lacquer disk(-sc), cylinder, expansion link, compressed air hose, baffle ring and
Pot shape spherical faced pan composition, SPL lacquer disk(-sc) section thick middle thin edge, is shaped as SPL, is set below SPL lacquer disk(-sc)
There is a pot shape spherical faced pan, SPL lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive expansion link to drive batten bent
Line lacquer disk(-sc) moves up and down, and expansion link front hollow simultaneously connects compressed air hose and also connects SPL lacquer disk(-sc) inner chamber body;Body is left
Inferior horn is provided with mechanical ultrasonic vibrator, is rotated at a high speed by actuating unit kinetic energy, the structure of mechanical ultrasonic vibrator is ball
Cap-shaped, and spherical cap edge is smooth splined curve, has crest, trough progressively to expand from spherical cap center to edge simultaneously continuous
The feature of diverging;Body side automatically controls steam valve and manual steam valve by jet chimney connection, automatically controls steam valve
In parallel by jet chimney with manual steam valve, temperature sensor, which is installed in filter, to be submerged in leachate, temperature sensor
Steam valve is automatically controlled by signal wire connection, 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.
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.
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.
Wired belt conveyer is provided with the bubble washer, Bubble blowing tube is provided between the upper and lower guipure of wired belt conveyer, froths
Pipe one end connects blower export, and the other end is closed, and Bubble blowing tube stretches into part surrounding in water and is provided with aperture, wired belt conveyer middle part
Top is provided with shower, and bubble washer one end is provided with cleaning machine discharging opening, and the other end is provided with cleaning machine inlet.
Appropriate water is noted in bubbling -cleaning box body, starts air blower and bubble is produced in water by Bubble blowing tube, do not wash
The cleaned machine inlet of radix glycyrrhizae fall into casing and do tumbling state under the combination of bubble and water, and with wired belt conveyer not
Disconnected to push ahead, when going out the water surface, the high-end shower that is provided with carries out high pressure washing, the cleaned machine discharging opening of clean radix glycyrrhizae, sweet
Careless conveyer is shredded into shredding machine, and the radix glycyrrhizae of chopping is fallen into body from shredding machine discharging opening, and the radix glycyrrhizae of chopping passes through
Three-level is extruded transfer roller cylinder, is exported afterwards by elevator.Body is integrally connected with elevator by flange, is sealing structure
Maintenance easy to disassemble;Steam is through automatically controlling steam valve, jet chimney enters in body, and leachate is heated into what leaching needed
Temperature, device liquid level certain position being maintained during work, device replenisher is filled into by liquid feed valve control, overflowed by drain pipe,
Reach liquid phase disengaging balance, the radix glycyrrhizae so shredded is able to realize adverse current with liquid phase water in the case where entering device and three-level squeezing effect
Contact is leached, 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, 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 after the denseer liquorice liquid of counter-current extraction carries out initial filter by filter, is overflowed by drain pipe and is transported to receiver,
Filtrate is filtered through reservoir pump, pipeline into filtration system, and filtrate flows into filtrate tank through filtrate outlet pipe, and filtrate conveys through filtrate
Pump, pipeline enter climbing-falling film evaporator, and climbing-falling film evaporator is that two groups of heating tubes are installed in shell side, and left side is liter film
Formula, right side are falling film type, and heating steam enters climbing-falling film evaporator shell side through steam inlet, and heating steam is in a liter membrane tube, drop
Feed liquid in pipe is transferred heat to outside membrane tube, caused condensed water is discharged through the drain valve of bottom first, and filtrate is through bottom feed pipe
A liter membrane tube heating is introduced into, 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 from bottom, and after separation, indirect steam is from dividing
Exported from device top through indirect steam, secondary steam pipe is discharged into steamdrum and carries out Heat preservation to body, concentrate is dense from bottom
Contracting liquid outlet discharge, carries out subsequent treatment.
It is cylinder to transfer roller cylinder, corresponding bearing arrangement is easy to sealing waterproof, and it is poor to turning and extruding to adapt to strength extruding
Dynamic to turning, particularly advantageous extrude by force grinds crushing with rubbing with the hands, promotes the counter-current extraction radix glycyrrhizae effective ingredient dissolution of the radix glycyrrhizae and water shredded.
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:
Bite that continuous reliable, extruding compression ratio is especially big to transfer roller cylinder material, differential especially good, the three-level of grinding separating twice effect of rubbing with the hands
Strong extruding realizes most perfect adaptation with counterflow leaching;
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 the partial enlargement structural representation of SPL lacquer disk(-sc) pulse gas explosion device.
Fig. 3 is the main structure diagram of mechanical ultrasonic vibrator.
Fig. 4 is the overlooking the structure diagram of mechanical ultrasonic vibrator.
Fig. 5 is the present invention looks up structural representation of mechanical ultrasonic vibrator.
Fig. 6 is the strabismus structural representation of bowing of mechanical ultrasonic vibrator.
Fig. 7 is the oblique present invention looks up structural representation of mechanical ultrasonic vibrator.
Each label represents in figure:
A, to transfer roller cylinder;B, SPL lacquer disk(-sc);C, mechanical ultrasonic vibrator;1st, body;2nd, filter;3rd, drain pipe;4、
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, shredding machine;21st, screw extrusion dewaterer;27th, reclaim
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, steam
Pipeline;63rd, signal wire;64th, temperature sensor;66th, radix glycyrrhizae conveyer;80th, bubble washer;81st, air blower;82nd, Bubble blowing tube;
83rd, wired belt conveyer;84th, shower;85th, cleaning machine discharging opening;86th, machine inlet is cleaned;87th, sewage draining exit;90th, climbing-falling film
Evaporator;91st, membrane tube is risen;92nd, film supplying tube;93rd, steam inlet;94th, the first drain valve;95th, feed pipe;96th, indirect steam goes out
Mouthful;97th, concentrated solution outlet;98th, secondary steam pipe;99th, steamdrum;100th, vapour liquid separator;101st, receiver;102nd, reservoir
Pump;103rd, filtration system;104th, filtrate tank;105th, filtrate delivery pump;106th, liquid storage tube;107th, reservoir delivery pipe;108 filtrates go out
Pipe;109th, filtrate pipe;110th, filtrate delivery pipe.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
As shown in Fig. 1-Fig. 7 with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, including body
1, it is characterised in that:The cleaning machine discharging opening 85 of bubble washer 80 is connected by radix glycyrrhizae conveyer 66 and the charging aperture of shredding machine 20
Connecing, be provided with body 1 below the discharging opening of shredding machine 20, the inside of body 1 is provided with three-level to transfer roller cylinder A, to transfer roller cylinder A to be cylindrical,
Every grade is equipped with radix glycyrrhizae guide groove 5 below transfer roller cylinder A, and afterbody guide groove 5 connects the hopper 6 of radix glycyrrhizae elevator 8, elevator 8
Blow tank 15 connect screw extrusion dewaterer 21;Elevator 8 is provided with liquid feed valve 16, and the top of body 1 is provided with filter 2 and gone out
Liquid pipe 3, drain pipe 3 connect filtration system 103, mistake through receiver 101, liquid storage tube 106, reservoir pump 102, reservoir delivery pipe 107
Filter system 103 rises through filtrate outlet pipe 108, filtrate tank 104, filtrate pipe 109, filtrate delivery pump 105, the connection of filtrate delivery pipe 110
Downward film evaporator 90, climbing-falling film evaporator 90 connect vapour liquid separator 100 by pipeline, the upper end of vapour liquid separator 100
Indirect steam outlet 96 connects steamdrum 99 through secondary steam pipe 98, and steamdrum 99 is evenly arranged in the suitable position of body 1;Machine
SPL lacquer disk(-sc) pulse gas explosion device is provided with body 1, SPL lacquer disk(-sc) pulse gas explosion device is by SPL lacquer disk(-sc) B, gas
Cylinder 9, expansion link 10, compressed air hose 11, baffle ring 12 and pot shape spherical faced pan 13 form, webbing among SPL lacquer disk(-sc) B-section
Edge is thin, is shaped as SPL, is provided with pot shape spherical faced pan 13 below SPL lacquer disk(-sc) B, SPL lacquer disk(-sc) B is through expansion link 10
The cylinder 9 outside body 1 is connected, cylinder 9 can drive expansion link 10 to drive SPL lacquer disk(-sc) B to move up and down, and expansion link 10 is anterior
It is hollow and 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 edge is stream
Smooth splined curve, there is the feature that crest, trough progressively expand and continuously dissipated from spherical cap center to edge;Body 1 one
Side automatically controls steam valve 60 and manual steam valve 61 by the connection of jet chimney 62, automatically controls steam valve 60 and manual 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, and temperature sensor 64 is logical
Cross the connection of signal wire 63 and automatically control steam valve 60, 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.
Wired belt conveyer 83 is provided with the bubble washer 80, wired belt conveyer is provided with Bubble blowing tube between guipure about 83
82, the one end of Bubble blowing tube 82 connection air blower 81 exports, and the other end is closed, and Bubble blowing tube 82 stretches into part surrounding in water and is provided with aperture,
The middle part of wired belt conveyer 83 top is provided with shower 84, and the one end of bubble washer 80 is provided with cleaning machine discharging opening 85, and the other end is set
There is cleaning machine inlet 86.
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.
Appropriate water is noted in the casing of bubble washer 80, starts air blower 81 and gas is produced in water by Bubble blowing tube 82
Bubble, the cleaned machine inlet 86 of radix glycyrrhizae do not washed fall into casing and do tumbling state under the combination of bubble and water, and with net
Band conveyer 83 is constantly pushed ahead, and when going out the water surface, the high-end shower 84 that is provided with carries out high pressure washing, and clean radix glycyrrhizae is through clear
Washing machine discharging opening 85, radix glycyrrhizae conveyer 66 are shredded into shredding machine 20, and the radix glycyrrhizae of chopping falls into from the discharging opening of shredding machine 20
In body 1, the radix glycyrrhizae of chopping is extruded transfer roller cylinder A by three-level, is exported afterwards by elevator 8.Body 1 is logical with elevator 8
Cross flange to be integrally connected, demolition and maintenance are also allowed for for sealing structure;Steam is through automatically controlling steam valve 60, jet chimney 62 enters
In body 1, leachate is heated to the temperature that leaching needs, the certain position of device liquid level 4, device replenisher are maintained during work
Filled into by liquid feed valve control, overflowed by drain pipe, reach liquid phase disengaging balance, the radix glycyrrhizae so shredded is entering device and three
It is able to realize that counter current contacting leaches with liquid phase water under level squeezing effect, because strong extruding promotes strong imbibition, realization is most penetrated by force, oozed
The radix glycyrrhizae effective ingredient leaching of saturating adverse current chopping, reaches 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
Body is flowed back to through 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
Bottom, the dregs of a decoction are discharged from slag-drip opening, after the denseer liquorice liquid of counter-current extraction carries out initial filter by filter 2, are overflowed by drain pipe 3
Receiver 101 is transported to, filtrate is filtered through reservoir pump 102, pipeline into filtration system 103, and filtrate is through filtrate outlet pipe 108
Filtrate tank 104 is flowed into, filtrate enters climbing-falling film evaporator 90 through filtrate delivery pump 105, pipeline, and climbing-falling film evaporator 90 is
Two groups of heating tubes are installed in shell side, to rise membrane type, right side is falling film type in left side, and heating steam enters through steam inlet 93 to be lifted
The shell side of kestner long-tube evaporator 90, heating steam transfer heat to feed liquid in pipe, caused condensation outside liter membrane tube 91, film supplying tube 92
Water is discharged through the first drain valve of bottom 94, and filtrate is introduced into liter membrane tube 91 through bottom feed pipe 95 and heated, and explosive evaporation, vapour-liquid is mixed
Compound stretches film forming in pipe, rises to top, is then transferred to second half film supplying tube 92 and heats, then carry out falling film evaporation, vapour-liquid
Mixture enters vapour liquid separator 100 from bottom, and after separation, indirect steam exports 96, two from separator top through indirect steam
Secondary steam pipe 98 is discharged into steamdrum 99 and carries out Heat preservation to body 1, and concentrate is discharged from bottom concentrated solution outlet 97, after progress
Continuous processing.
It is cylinder to transfer roller cylinder A, corresponding bearing arrangement is easy to sealing waterproof, and it is poor to turning and extruding to adapt to strength extruding
Dynamic to turning, particularly advantageous extrude by force grinds crushing with rubbing with the hands, promotes the counter-current extraction radix glycyrrhizae effective ingredient dissolution of the radix glycyrrhizae and water shredded.
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 (6)
1. it is a kind of with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, including body, it is characterised in that:
The cleaning machine discharging opening of bubble washer is connected by radix glycyrrhizae conveyer with chopping machine inlet, is provided with below shredding machine discharging opening
Body, internal body are provided with three-level to transfer roller cylinder, are cylinder to transfer roller cylinder, every grade is equipped with radix glycyrrhizae below transfer roller cylinder and leads
Groove, afterbody guide groove connect the hopper of radix glycyrrhizae elevator, the blow tank connection screw extrusion dewaterer of elevator;On elevator
Provided with liquid feed valve, body upper is provided with filter and drain pipe, and drain pipe is through receiver, liquid storage tube, reservoir pump, reservoir delivery pipe
Filtration system is connected, filtration system connects elevating membrane through filtrate outlet pipe, filtrate tank, filtrate pipe, filtrate delivery pump, filtrate delivery pipe
Formula evaporator, climbing-falling film evaporator connect vapour liquid separator, the indirect steam outlet warp of vapour liquid separator upper end by pipeline
Secondary steam pipe connects steamdrum, and steamdrum is evenly arranged in the suitable position of body;SPL lacquer disk(-sc) arteries and veins is provided with body
Device of air is burst, SPL lacquer disk(-sc) pulse gas explosion device is by SPL lacquer disk(-sc), cylinder, expansion link, compressed air hose, baffle ring
Formed with pot shape spherical faced pan, SPL lacquer disk(-sc) section thick middle thin edge, be shaped as SPL, SPL lacquer disk(-sc) lower section
Provided with pot shape spherical faced pan, SPL lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive expansion link to drive batten
Curve lacquer disk(-sc) moves up and down, and expansion link front hollow simultaneously connects compressed air hose and also connects SPL lacquer disk(-sc) inner chamber body;Body
The lower left corner is provided with mechanical ultrasonic vibrator, is rotated at a high speed by actuating unit kinetic energy, the structure of mechanical ultrasonic vibrator is
Spherical cap shape, and spherical cap edge is smooth splined curve, has crest, trough progressively to expand and connect from spherical cap center to edge
The scattered feature of supervention;Body side automatically controls steam valve and manual steam valve by jet chimney connection, automatically controls steam
Valve and manual steam valve are in parallel by jet chimney, and temperature sensor, which is installed in filter, to be submerged in leachate, TEMP
Device automatically controls steam valve by signal wire connection, and body high temperature position is thermally shielded isothermal holding.
2. according to claim 1 with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, its feature
It is:The shell at the body roller position is spline surface, in Pear-Shaped.
3. according to claim 2 with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, its feature
It is:Clean-up port is provided with below the body.
4. according to claim 3 with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, its feature
It is:Baffle ring is provided with above the pot shape spherical faced pan.
5. according to claim 4 with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, its feature
It is:The body is connected as one with elevator by flange, is sealing structure and easy to disassemble.
6. according to claim 1 with cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element, its feature
It is:Screw extrusion dewaterer lower end leakage fluid dram recovered liquid valve, recovery liquid pump, valve, recovery liquid pipe and the underpart
Connection;Wired belt conveyer is provided with the bubble washer, Bubble blowing tube, Bubble blowing tube one are provided between the upper and lower guipure of wired belt conveyer
End connection blower export, the other end is closed, and Bubble blowing tube stretches into part surrounding in water and is provided with aperture, wired belt conveyer middle part top
Provided with shower, bubble washer one end is provided with cleaning machine discharging opening, and the other end is provided with cleaning machine inlet.
Priority Applications (1)
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CN201710783615.XA CN107469393A (en) | 2017-09-04 | 2017-09-04 | With cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element |
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CN201710783615.XA CN107469393A (en) | 2017-09-04 | 2017-09-04 | With cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element |
Publications (1)
Publication Number | Publication Date |
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CN107469393A true CN107469393A (en) | 2017-12-15 |
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CN201710783615.XA Withdrawn CN107469393A (en) | 2017-09-04 | 2017-09-04 | With cleaning machine and dewaterer to transfer roller cartridge type liquid extract of liquorice extraction element |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116807031A (en) * | 2023-08-28 | 2023-09-29 | 云南邦纳科技有限公司 | Preparation process of truffle extract for truffle wine |
-
2017
- 2017-09-04 CN CN201710783615.XA patent/CN107469393A/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116807031A (en) * | 2023-08-28 | 2023-09-29 | 云南邦纳科技有限公司 | Preparation process of truffle extract for truffle wine |
CN116807031B (en) * | 2023-08-28 | 2023-11-10 | 云南邦纳科技有限公司 | Preparation process of truffle extract for truffle wine |
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Application publication date: 20171215 |