CN107349635A - Liquid extract of liquorice extraction element with batcher and drying machine - Google Patents

Abstract

The invention discloses a kind of liquid extract of liquorice extraction element with batcher and drying machine, 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, and the blow tank of elevator connects drying machine through screw extrusion dewaterer, slag bucket；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

Liquid extract of liquorice extraction element with batcher and drying machine

Technical field

The present invention relates to a kind of liquid extract of liquorice extraction element with batcher and drying machine.

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：

A kind of liquid extract of liquorice extraction element with batcher and drying machine, including body, it is characterised in that：It is provided with above body Batcher, internal body are provided with three-level to turning SPL roller, are continuous spline surface to turning SPL roller surface, often For level to turning to be equipped with radix glycyrrhizae guide groove below SPL roller, afterbody guide groove connects the hopper of radix glycyrrhizae elevator, elevator Blow tank through screw extrusion dewaterer, slag bucket connect drying machine；Elevator is provided with liquid feed valve, and body upper is provided with filter And drain pipe, the inlet communication of the filtered liquid feed valve of drain pipe and duplex strainer, the outlet of duplex strainer pass through the first filter Liquid 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, feed pipe connection climbing-falling film evaporator, climbing-falling film evaporator connects vapour liquid separator by pipeline, on vapour liquid separator The indirect steam outlet at end connects steamdrum through secondary steam pipe, and steamdrum is evenly arranged in the suitable position of body；In body Provided with SPL lacquer disk(-sc) pulse gas explosion device, SPL lacquer disk(-sc) pulse gas explosion device is by SPL lacquer disk(-sc), cylinder, flexible Bar, compressed air hose, baffle ring and pot shape spherical faced pan composition, SPL lacquer disk(-sc) section thick middle thin edge, are shaped as batten song Line, SPL lacquer disk(-sc) lower section are provided with pot shape spherical faced pan, and SPL lacquer disk(-sc) connects extra-organismal cylinder, cylinder energy through expansion link Expansion link is driven to drive SPL lacquer disk(-sc) to move up and down, expansion link front hollow simultaneously connects compressed air hose and also connects batten song Line 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 The structure of wave excitation device is spherical cap shape, and spherical cap edge is smooth splined curve, have from spherical cap center to edge crest, The feature that trough progressively expands and continuously dissipated；Body side automatically controls steam valve and manual steam by jet chimney connection Valve, steam valve and manual steam valve is automatically controlled by jet chimney parallel connection, temperature sensor, which is installed in filter, submerges leaching Go out in liquid, 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.

Conveyer is provided with the drying machine, steam fin heats device, steam fin heats device upper end are provided with drying machine Steam valve is connected, lower end connects drain valve, the side lower part connecting fan import of drying machine one, and a upper lateral part is provided with gas outlet.

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, by the dehydration of screw extrusion dewaterer again through slag bucket, dry Dry machine is dried, and the dried dregs of a decoction are discharged from discharging opening and carry out subsequent treatment, and the denseer radix glycyrrhizae effective ingredient liquid of counter-current extraction leads to Cross filter tentatively to filter, primary filtrate enters duplex strainer through drain pipe, filtering liquid feed valve and carries out in-depth filtration processing, filtering Filtrate afterwards enters storage in the presence of filtrate pump through the first filtrate pipe, filtrate valve, filtrate pump, pump discharge valve, the second filtrate pipe Flow container is stored, and outlet valve of the filtrate through receiver lower end, filtrate delivery pipe, feed pipe enter climbing-falling film evaporator, elevating membrane Formula evaporator 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 steam is through steam inlet Into climbing-falling film evaporator shell side, heating steam transfers heat to feed liquid in pipe outside a liter membrane tube, film supplying tube, caused cold Condensate is discharged through the drain valve of bottom first, and filtrate is introduced into liter membrane tube through bottom feed pipe and heated, explosive evaporation, liquid-vapor mixture Film forming is stretched in pipe, rises to top, is then transferred to the heating of second half film supplying tube, then carry out falling film evaporation, liquid-vapor mixture Enter vapour liquid separator from bottom, after separation, indirect steam is exported from separator top through indirect steam, secondary steam pipe is discharged into Steamdrum carries out Heat preservation to body, and concentrate is discharged from bottom concentrated solution outlet, 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；22nd, slag bucket；23rd, sieve aperture turnover panel conveys；24th, drying machine；27th, recovered liquid valve；28th, liquid pump is reclaimed；29th, valve；30th, reclaim Liquid pipe；41st, steam valve；42nd, steam fin heats device；43rd, drain valve；44th, blower fan；60th, steam valve is automatically controlled；61st, manually Steam valve；62nd, jet chimney；63rd, signal wire；64th, temperature sensor；70th, duplex strainer；71st, liquid feed valve is filtered；72nd, filter Liquid delivery pipe；73rd, the first filtrate pipe；74th, filtrate valve；75th, filtrate pump；76th, pump discharge valve；77th, the second filtrate pipe；78th, reservoir Tank；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； 95th, feed pipe；96th, indirect steam exports；97th, concentrated solution outlet；98th, secondary steam pipe；99th, steamdrum；100th, vapor-liquid separation Device.

Embodiment

In conjunction with accompanying drawing, the present invention is further elaborated with.

Liquid extract of liquorice extraction element with batcher and drying machine as Figure 1-Figure 8, including body 1, its feature exist In：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 SPL roller A Surface is continuous spline surface, and every grade is equipped with radix glycyrrhizae guide groove 5 to turning below SPL roller A, afterbody guide groove 5 connects The hopper 6 of radix glycyrrhizae elevator 8, the blow tank 15 of elevator 8 connect drying machine 24 through screw extrusion dewaterer 21, slag bucket 22；Carry Rise machine 8 and be provided with 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 The inlet communication of filter 70, the outlet of duplex strainer 70 by the first filtrate pipe 73, filtrate valve 74, filtrate pump 75, pump out Mouth valve 76, the second filtrate pipe 77 connect with the inlet of receiver 78, and the lower end of receiver 78 is through outlet valve 79, filtrate delivery pipe 72nd, feed pipe 95 connects climbing-falling film evaporator 90, and climbing-falling film evaporator 90 connects vapour liquid separator 100, vapour by pipeline The indirect steam outlet 96 of the upper end of liquid/gas separator 100 connects steamdrum 99 through secondary steam pipe 98, and steamdrum 99 is evenly arranged in The suitable position of body 1；SPL lacquer disk(-sc) pulse gas explosion device, SPL lacquer disk(-sc) pulse gas explosion device are provided with body 1 It is made up of SPL lacquer disk(-sc) B, cylinder 9, expansion link 10, compressed air hose 11, baffle ring 12 and pot shape spherical faced pan 13, SPL Lacquer disk(-sc) B-section thick middle thin edge, SPL is shaped as, pot shape spherical faced pan 13 is provided with below SPL lacquer disk(-sc) B, batten is bent Line lacquer disk(-sc) B connects the cylinder 9 outside body 1 through expansion link 10, and cylinder 9 can drive expansion link 10 to drive above and below SPL lacquer disk(-sc) B Motion, the front hollow of expansion link 10 simultaneously connect compressed air hose 11 and also connect SPL lacquer disk(-sc) B inner chamber bodies；The lower left corner of body 1 Provided with mechanical ultrasonic vibrator C, rotated at a high speed by the kinetic energy of actuating unit 14, mechanical ultrasonic vibrator C structure 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；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 manual steam valve 61 are in parallel by jet chimney 62, and temperature sensor 64, which is installed in filter 2, submerges leaching In liquid, temperature sensor 64 automatically controls steam valve 60 by the connection of signal wire 63, and the high temperature position of body 1 is thermally shielded at insulation Reason.

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.

Conveyer is provided with the drying machine 24, steam fin heats device 42, steam fin heats are provided with drying machine 24 The upper end of device 42 connects steam valve 41, lower end connection drain valve 43, the import of 24 1 side lower part connecting fan of drying machine 44, a upper lateral part Provided with gas outlet.

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 again through slag bucket by screw extrusion dewaterer 21 22nd, drying machine 24 is dried, and the dried dregs of a decoction are discharged from discharging opening carries out subsequent treatment, the denseer radix glycyrrhizae of counter-current extraction effectively into Part liquid is tentatively filtered by filter 2, and primary filtrate enters duplex strainer 70 through drain pipe 3, filtering liquid feed valve 71 and carries out deep layer Filtration treatment, filtrate after filtering in the presence of filtrate pump 75 through the first filtrate pipe 73, filtrate valve 74, filtrate pump 75, pump out Mouth valve 76, the second filtrate pipe 77 are stored into receiver 78, outlet valve 79 of the filtrate through the lower end of receiver 78, filtrate delivery pipe 72nd, feed pipe 95 enters climbing-falling film evaporator 90, and climbing-falling film evaporator 90 is that two groups of heating tubes, left side are installed in shell side For a liter membrane type, right side is falling film type, and heating steam enters the shell side of climbing-falling film evaporator 90 through steam inlet 93, and heating steam exists Rise membrane tube 91, film supplying tube 92 and transfer heat to feed liquid in pipe outside, caused condensed water is discharged through the first drain valve of bottom 94, filter Liquid is introduced into liter membrane tube 91 through bottom feed pipe 95 and heated, and explosive evaporation, liquid-vapor mixture stretches film forming in pipe, rises to top Portion, then it is transferred to second half film supplying tube 92 and heats, then carry out falling film evaporation, liquid-vapor mixture enters vapour liquid separator from bottom 100, after separation, indirect steam is discharged into steamdrum 99 to machine from separator top through indirect steam outlet 96, secondary steam pipe 98 Body 1 carries out Heat preservation, and concentrate is discharged from bottom concentrated solution outlet 97, 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 (6)

1. a kind of liquid extract of liquorice extraction element with batcher and drying machine, including body, it is characterised in that：Set above body There is batcher, internal body is provided with three-level to turning SPL roller, is continuous spline surface to turning SPL roller surface, Every grade is equipped with radix glycyrrhizae guide groove to turning below SPL roller, afterbody guide groove connects the hopper of radix glycyrrhizae elevator, lifting The blow tank of machine connects drying machine through screw extrusion dewaterer, slag bucket；Elevator is provided with liquid feed valve, and body upper is provided with filtering The inlet communication of device and drain pipe, the filtered liquid feed valve of drain pipe and duplex strainer, the outlet of duplex strainer passes through 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, feed pipe connection climbing-falling film evaporator, climbing-falling film evaporator connects vapour liquid separator by pipeline, on vapour liquid separator The indirect steam outlet at end connects steamdrum through secondary steam pipe, and steamdrum is evenly arranged in the suitable position of body；In body Provided with SPL lacquer disk(-sc) pulse gas explosion device, SPL lacquer disk(-sc) pulse gas explosion device is by SPL lacquer disk(-sc), cylinder, flexible Bar, compressed air hose, baffle ring and pot shape spherical faced pan composition, SPL lacquer disk(-sc) section thick middle thin edge, are shaped as batten song Line, SPL lacquer disk(-sc) lower section are provided with pot shape spherical faced pan, and SPL lacquer disk(-sc) connects extra-organismal cylinder, cylinder energy through expansion link Expansion link is driven to drive SPL lacquer disk(-sc) to move up and down, expansion link front hollow simultaneously connects compressed air hose and also connects batten song Line 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 The structure of wave excitation device is spherical cap shape, and spherical cap edge is smooth splined curve, have from spherical cap center to edge crest, The feature that trough progressively expands and continuously dissipated；Body side automatically controls steam valve and manual steam by jet chimney connection Valve, steam valve and manual steam valve is automatically controlled by jet chimney parallel connection, temperature sensor, which is installed in filter, submerges leaching Go out in liquid, 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 drying machine according to claim 1, it is characterised in that：The machine The shell at body roller position is spline surface, in Pear-Shaped.

3. the liquid extract of liquorice extraction element with batcher and drying machine according to claim 2, it is characterised in that：The machine Clean-up port is provided with below body.

4. the liquid extract of liquorice extraction element with batcher and drying machine according to claim 3, it is characterised in that：The pot Baffle ring is provided with above shape spherical faced pan.

5. the liquid extract of liquorice extraction element with batcher and drying machine according to claim 4, it is characterised in that：The machine Body is connected as one with elevator by flange, is sealing structure and easy to disassemble.

6. the liquid extract of liquorice extraction element with batcher and drying machine according to claim 1, it is characterised in that：The spiral shell The recovered liquid valve of rotation extruding-desiccation machine lower end leakage fluid dram, recovery liquid pump, valve, recovery liquid pipe connect with underpart；It is described dry Conveyer is provided with dry machine, steam fin heats device, steam fin heats device upper end connection steam valve, lower end are provided with drying machine Drain valve, the side lower part connecting fan import of drying machine one are connected, a upper lateral part is provided with gas outlet.