CN205182202U - Smuggle formula thin material layer microwave evaporation plant in succession secretly - Google Patents

Abstract

The utility model provides a smuggle formula thin material layer microwave evaporation plant in succession secretly adopts and a pair ofly rot. Ly go up to press from both sides the roller and press from both sides the roller down, through two filter screen areas for no reason, with the solid -liquid mixture butt clamp between the filter screen area, form the butt clamp bed of material structure of upward filtration guipure, the solid -liquid mixture bed of material and downward filtration guipure to come and go the ascending mode that transports of successive layer with the level and pass through the microwave cavity, make solid -liquid mixture feed liquid in the butt clamp bed of material, absorbing microwaves energy under even thin layer state and by heating evaporation, simultaneously, still through the nozzle cyclic loading to the segregation feed liquid, improve the evaporation capacity to and through advance, the seal structure of the ejection of compact, improve the vacuum in the evaporimeter, make feed liquid high efficient conversion under the lower temperature be the gaseous phase. In addition, because the butt clamp bed of material that adopts the multilayer to transport the state makes the increase of heat transfer specific surface, evaporation plant is compact, and area utilization rate is high, and cooperation condensation and gas -liquid separation can realize the distillation, draw the operation.

Description

A kind of strap-clamping-type thin bed of material microwave evaporation device continuously

Technical field

The utility model relates to solidliquid mixture evaporation and is separated or concentration technique field, more particularly, relates to a kind of strap-clamping-type thin bed of material microwave evaporation device continuously.

Background technology

The molecule of liquid to be escaped from liquid phase surface because molecular motion has or the tendency of volatilization, and this tendency increases along with the rising of temperature.Utilize the difference of each component volatilization degree in liquid mixture or solidliquid mixture, liquid phase volatile in liquid mixture or solidliquid mixture is heated to gasification, makes liquid become steam, be i.e. so-called evaporation.

In evaporation process, volatile components obtains enrichment in steam, and difficult volatile component (comprising solid phase) also obtains enrichment in raffinate, and this achieves the separation of different component to a certain extent.Volatility difference between component is larger, then this enrichment degree is also larger.If liquid mixture or solidliquid mixture are placed in airtight vacuum system, then fluid molecule overflows with keeping, and on liquid interface, form steam, if maintain certain vacuum by the continuous sucking of vacuum pump set, then from this vacuum systems, volatile vapor can be exported continuously.Evaporation is applicable to the techniques such as various distillation, separation, purification, concentrated, extraction, degassed, taste removal, reaction, therefore, is widely used in the industries such as pharmacy, biology, food, spices, petrochemical industry, daily use chemicals, environmental protection, agricultural chemicals, desalinization.

Because evaporation relates to mass transfer, heat transfer, also belong to heat transmission equipment, and liquid film heat transfer is one of effective ways of augmentation of heat transfer.Rete is thinner, film forming is more even, and heat transfer efficiency is higher.For making even film layer, reduce thermograde, increase specific area, shorten heated time, the kestner long-tube evaporator of exploitation, its known type comprises: rise membrane type, falling film type, mechanical agitation type thin film evaporator and centrifugal film evaporator, wherein, rises membrane type and falling film type is conventional traditional form evaporimeter.

Mechanical agitation type thin film evaporator, also known as rotary film evaporator, is adopt mechanical agitation to carry out the higher evaporimeter of the efficiency of falling film evaporation under a kind of vacuum condition.Wherein, be that the mechanical agitation type thin film evaporator of representative is also used widely with scraped film evaporator, its principle is: feed liquid is divided into multiply stream by upper end rotating liquid distributor and enters cylinder inner wall; Per share stream is stirred by corresponding scraper plate, is dispersed on evaporation cylinder heated internal wall and forms uniform liquid film; Liquid film absorbs heat medium (vapours or conduction oil) in chuck and passes to the heat of evaporating surface, and in the evaporation rapidly of its surface, rete is thinning, is swept again and scrapes, form new film, then evaporate, so repeatedly carry out by follow-up scraper plate.Its characteristic is that vacuum pressure drop is little, operating temperature is low, heated time is short, evaporation intensity is high, operating flexibility is large, is specially adapted to thermal sensitivity, viscosity, has the evaporation and concentration of raw dirty foaming tendencies feed liquid to be separated.

Centrifugal film evaporator, also known as centrifugal evaporator.Its structure is similar with disc centrifuge, but video disc has interlayer, interior logical heating steam.Due to the centrifugal action of rotating compact disc, feed liquid is distributed in the inner surface of video disc, forms film.Steam liquid film in video disc interlayer carries out heating evaporation, and concentrate then comes together in periphery liquid bath, by suction tube nationality vacuum action by its sucking-off.Indirect steam collects rising through video disc headroom, enters condenser condenses, and is extracted out by vavuum pump.Heating steam is passed into by bottom hollow rotating shaft, enters video disc interlayer through passage.Its characteristic is that heat transfer efficiency is high, and evaporation intensity is large, and feed liquid heated time is short, and the rete of formation is thin, is particularly suitable for the evaporation and concentration of heat sensitive material, but should not be used for the feed liquid of large, the easy crystallization of viscosity, easily fouling.

Usual kestner long-tube evaporator forms evaporation operation system together with its auxiliary equipment.Auxiliary equipment generally has preheater, degasser, vacuum pump set, delivery pump, rectifying flow container and concentrate batch can and corresponding heating system and cooling/condenser system etc., is widely used in the techniques such as evaporation and concentration, degassed precipitation, distilation, distillation extraction.But the kestner long-tube evaporator of existing technology mostly is vertical, the flow velocity of feed liquid in evaporimeter cylinder is very fast, easily causes volatile component to be evaporated abundant not, have impact on evaporation effect to a certain extent.

The separation being evaporated to principle based on feed liquid rete this kind of, the distillation such as concentrated are extracted or in extraction equipment, most employing be partition heating heat transfer type, namely the vapours in chuck or interlayer or heat conduction wet goods thermal medium, wall surface material is first made to be heated, feed liquid is transferred heat to again by conduction heating, period, hot-fluid passed through multiple interface, have impact on the raising of heat exchange efficiency.Another kind of heat transfer type is directly imported in evaporimeter vapours, by Convective Heating, feed liquid surface heating is evaporated, the problem brought is that water vapour is mixed in gas phase volatile matter, adds additional follow-up gas-liquid separation load, even may have influence on the quality of separator.Therefore, heat medium and the heat exchange mode with feed liquid are also the key factors affecting evaporator effectiveness.

Microwave is defined as wavelength at lm ~ 1mm, a kind of electromagnetic wave of frequency within the scope of 300 ~ 3000GHz, therefore, has straightline propagation and by characteristics such as the absorption of different medium, reflection and transmission effects.When Absorption of Medium microwave energy, namely microwave produces heat effect to medium.

Microwave heats medium mainly through two kinds of mechanism: i.e. Polarization Mechanism and ionic conduction.Wherein, dipole polarization and interfacial polarization are the dominant polarization heating mechanism of covalent compound, and medium internal cause exists the Ion transfer electric current moving freely ion and produce at elect magnetic field, and then producing heat, is then that the ionic conduction of ionic compound mainly heats mechanism.

Medium is made up of polar molecule and nonpolar molecule, wherein, and the orientation movement of polar molecule under microwave electromagnetic field action, constantly change with the frequency of billions of times per second, cause the sharp impacts friction of molecule and produce heat, visible, heating using microwave is dielectric material loss electric field energy and generates heat.Because different dielectric materials has different dielectric losses, therefore, under microwave electromagnetic field action, its fuel factor is also different.Polar molecule medium can absorb microwave energy preferably, if water is strong polar molecule, is the best medium absorbing microwave.Nonpolar molecule medium does not substantially absorb or seldom absorbs microwave, as the resin such as polytetrafluoroethylene (PTFE), polypropylene and glass, pottery etc., can not absorb microwave through microwave.Metallic conductor then microwave reflection and seldom absorb microwave energy.

The feature of heating using microwave is remarkable, and as feed liquid and electromagnetic field entirety are had an effect, produce body phase fuel factor, firing rate is fast, even and the thermal efficiency is high; Feed liquid medium dielectric constant microwave medium and the little component of dielectric loss, microwave energy absorbing is few, and wherein, the fuel factor that polarity is large is strong, and non-polar component heat effect is very little, and selective heating is remarkable; Microwave output power easily adjusts, and heating process controllability is good, and thermal inertia is little, contributes to the quality etc. improving evaporated components.Therefore, as a kind of contactless mode of heating, heating using microwave is extracted in distillation, extraction, the field such as concentrated, dry obtain applying quite widely.

The patent below quoted from relates to heating using microwave for the apparatus structure that extracts, extract and method, but this can not be interpreted as inevitably, these existing technology liquid mixture evaporation is separated or concentrated be suitable.

The Chinese patent CN94192507.2 of Achi Macs, disclose a kind of method and apparatus of solvent-free microwave extraction of natural products, comprise in container biological substance being placed on solvent is not housed and accept microwave irradiation, then from the natural prodcuts of extraction, be separated the residual biological substance of removing.In addition, also relate to when microwave irradiation to container decompression, and heat to compensate in the most of the time of at least microwave irradiation because of water evaporation and the temperature that causes declines from biological substance.

The Chinese patent CN02111457.9 of the people such as Deng Xiu, disclose a kind of extraction equipment, comprise cylindrical shape extractor, isolator, transition conduit, between cylindrical vessel and isolator, form work annular space, the height of the work annular space integral multiple that is the half-wavelength of adopted microwave field resonance mode.

The Chinese patent CN02111640.7 of the medium people of Huang Kai, disclose a kind of microwave extracting apparatus, there is the extractor of agitator, cooling and electric control gear, at the tank body circumferentially-spaced certain distance of extractor, point multilayer is equipped with multiple microwave power supply and magnetron equably, can carry out batch (-type) or continous way operation, concrete form can adopt vertical or horizontal type device.

The Chinese patent CN200410027563.6 of the people such as Zheng Bisheng, disclose a kind of microwave extracting apparatus, comprise microwave applicator and solid-liquid transmitting device, microwave applicator is a hollow cavity, and its front and back walls has hole, and solid-liquid transmitting device tiltedly stretches into cavity from antetheca tapping, stretch out from back wall aperture, the outer top of microwave applicator is provided with microwave magnetron, and solid-liquid transmitting device bottom is provided with solid material import and extract outlet, and top is provided with discharging opening and extract entrance.

The Chinese patent CN200510031458.4 of the people such as Wan Shaoping, disclose a kind of method using microwave heating extraction grease from the plant seed benevolence containing grease, by the part containing grease in plant seed benevolence or its byproduct, put after pulverizing and accept microwave irradiation in a reservoir, when rising to a timing by irradiation temperature of charge, stop irradiation, solvent penetration is extracted, be separated melt cinder, concentration and recovery solvent, thus obtain target grease.

The Chinese patent CN200510096079.3 of Li Sheng, discloses a kind of microwave counter current continuous extraction apparatus, comprises extraction cylinder, and its one end is provided with feed hopper and extract outlet, and the other end is provided with slag notch and extract import; Extraction cylinder is provided with microwave system, and the inner chamber of extraction cylinder is provided with spiral propeller, drives spiral propeller by drive unit.

The Chinese patent CN200610044442.1 of the people such as Ma Feng, discloses a kind of decompressed microwave extraction device for effective ingredients in plant extraction and method.Be made up of micro-wave oven, extractor, condenser, gas-liquid separator and decompressor.Micro-wave oven is arranged on extractor periphery, is evenly arranged microwave generator in it, and extractor is provided with electric mixer.Under decompression and microwave action, solvent evaporation becomes liquid solvent through condenser condenses.

The Chinese utility model patent CN200620136108.4 of the people such as Li Sheng, disclose a kind of ring shape microwave extraction equipment, comprise frame, extraction cylinder, transmitting device, microwave heating system, its main feature is extraction cylinder is end to end ring pipe, the outside of extraction cylinder is provided with microwave heating system, transmitting device is provided with in extraction cylinder, transmitting device is provided with conveying dividing plate, conveying dividing plate is fixed on transporting chain plate, and conveying dividing plate is provided with the aperture of solvent circulation, by transporting chain plate and conveying dividing plate, the conveying space in extraction cylinder is divided into supply unit one by one, in supply unit, material and solvent extract under microwave heating action.

The Chinese utility model patent 200620049558.X of Du Rongqing, disclose a kind of device natural plants being carried out to continuous-type microwave extraction on laboratory or industrial production, comprise vertical feeding agitating device, horizontal spiral advances extraction equipment and device for discharging, horizontal spiral advances extraction equipment to be divided into leading portion microwave abstracting section and back segment cooling section.

The Chinese patent CN200610138359.0 of the people such as Guo Weitu, discloses a kind of continuously extracting pipeline type microwave equipment, comprises two steeping tanks, Microwave Extraction device, centrifugal separator.Steeping tank is connected with frequency conversion timing screw pump each via an autocontrol valve, screw pump outlet is connected with the import of Microwave Extraction device, the outlet of Microwave Extraction device is divided into three tunnels, lead up to after an autocontrol valve and receive centrifugal separator, two-way is connected with steeping tank behind the door each via an autocontrol valve in addition.

The Chinese patent CN200810047172.9 of the people such as Chen Sheng, discloses a kind of multifunctional microwave extraction instrument extracting Chinese style essence spice for cigarette.The extraction chamber of abstraction instrument is upright tubular, is provided with serpentine coil in it, and serpentine coil is through whole extraction chamber from top to bottom, and the microwave source in extraction chamber by two microwave generators, and carries out microwave extraction to the extraction material flowed through in serpentine coil.

The Chinese patent CN200910073920.5 of the people such as Yan Zheng, discloses a kind of microwave extracting apparatus for high capacity layered radiation, comprises and be provided with rabbling mechanism, backflow mechanism, charging aperture, slag-drip opening, feed tube, discharging tube and microwave source, extractor is as microwave cavity, and its inner interval layering arranges waveguide, and the microwave end of one or more waveguide is fixed on outside tank body, microwave end arranges magnetron, and the other end of one or more waveguide to extend in tank body and arranges feedback mouth.

The Chinese patent CN200910115127.7 of the people such as Zheng Xiaofei, disclose the device of a kind of dry microwave extraction effective components in plants, by extraction parts, mixing component, microwave irradiation heater block forms, and extraction parts are combined by multiple circular cylinder body with filter screen cavity and the flat gate valve of blanking.

The Chinese patent application publication No. CN103182192A of the people such as Sun Wei, disclose a kind of microwave evaporation concentration systems, comprise climbing film evaporator, condenser, cooler, microwave applicator, flash vessel, microwave applicator connects climbing film evaporator, climbing film evaporator connects flash vessel by a high-pressure plunger pump, and flash vessel connects cooler.Microwave applicator comprises tank body, at least one microwave generator, an agitating device of a sealing, microwave generator is positioned at the top of tank interior, transmitting terminal is towards tank body bottom, agitating device is positioned at the bottom of tank interior, after stoste enters microwave applicator, while microwave heats stoste, agitating device stirs stoste.

The Chinese patent application publication No. CN103505902A of Zheng Ailin, a kind of multi-pipe type Large Copacity microwave abstracting machine and microwave assisted extraction methods thereof are disclosed, comprise transmission device, microwave tank, microwave device, aerator, rotor arrangement, drawing mechanism, control device, microwave tank tank skin is provided with several magnetrons be evenly equally spaced, aerator comprises several compressed air inlet ports be arranged on microwave tank tank skin, compressed air input channel, stirring structure, feed liquid in microwave tank is made constantly to run switch, extract can be made to be subject to electromagnetic field effect equably heated.

The Chinese patent CN201310747536.5 of the people such as Zhou Zhide, disclose a kind of Microwave Extraction device, comprise the microwave extraction tank being provided with microwave feed-in mouth, microwave extraction tank top is connected with condenser and is provided with feedback outlet, feedback outlet is equipped with spray head, the bottom of microwave extraction tank is provided with the end socket of band discharging opening, and discharging opening connects feedback outlet by pipeline through pump, forms circulation bypass.

The Chinese patent application publication No. CN103752028A of the people such as Luo Lixin, disclose a kind of there is thin film evaporator function microwave wiped film molecular evaporator and utilize it to produce the method for fatty acid methyl ester, this microwave wiped film molecular evaporator has thin film evaporator and knifing molecular clock two kinds of functions.In addition, the basis retaining the heating of heating oil heater with the addition of microwave radiation technology piece-rate system, improve separating effect, volatile low molecule material can also be separated.

The Chinese patent application publication No. CN104014158A of the people such as Wang Qiannan, disclose that a kind of Chinese medicine is ultrasonic involves Microwave Extraction system, comprise the openable closed box of upper cover, the sample solution device of openable entrance and the moveable microwave introduction device on it, also comprise and be arranged on inner the second reflux for making the sample solution of vaporization reflux of described closed box.By arranging coordinated regulation device, to importing time, the importing order of ultrasonic wave and microwave, importing power and the shut-in time strictly controls, thus reaching the optimum Match effect of ultrasonic wave and microwave.

The Chinese utility model patent CN201020592299.1 of the people such as Zheng Bisheng, disclose the solid liquid counterflow extraction device of a kind of tunnel type micro wave, comprise extraction chamber, microwave magnetron, conveyer belt, conveyer belt supporter and driving wheel, also comprise high-order groove, pump, head tank and the receiving slit of overflowing; Described extraction chamber is hollow cavity, and extraction upper end, chamber is uniformly distributed multiple microwave magnetron, and the front and back end in extraction chamber is provided with opening, conveyer belt is through the front and back end in extraction chamber, supported by driving wheel and regulating wheel, form belt conveying system, driving wheel is connected with motor by speed changer; Conveyer belt has equally distributed micropore, the conveyer belt lower end in extraction chamber is interval with conveyer belt supporter, and conveyer belt supporter is made up of the axis of rolling of two end band rolling bearings and baffle plate; A multiple high position overflow groove be spaced apart and arranged in extraction chamber in upper end, outside extraction chamber, rear end is provided with head tank, in head tank and extraction chamber, the high position of the rear end groove that overflows is communicated with, in extraction chamber, lower end is interval with receiving slit, each receiving slit is communicated with respectively by pump and the high position groove that overflows, and pump is arranged on the outside in extraction chamber.

It should be noted that, the solid liquid counterflow extraction device of tunnel type micro wave described in CN201020592299.1, solid material is at tunnel type extraction front opening place, chamber, be evenly dispersed on conveyer belt by distributor, the conveyer belt with equally distributed micropore extracts horizontally through tunnel type in the process in chamber, extract water or solvent are sprayed onto on the material of the conveyer belt of below by the high-order groove that overflows, and conveyer belt lower end be interval with two end band baffle plates send band supporter, extract falls into receiving slit through solid material and transport tape, be pumped into the excessive groove of a previous stage high position again, be sprayed to again on solid material, in process and so forth, multistage compound infiltration, microwave energy absorbing, realize so-called counter-current extraction.Visible, this patent utilizes extract cyclically through the principle of the solids bed of material, in order to make extract through there being the enough extraction mass transfer time during bed of material, the bed of material and liquid level must have certain thickness, and this thickness is that conveyer belt two end-stopping plate by arranging ensures.Simultaneously, due to employing is individual layer conveyer belt, conveyer belt upper surface can only be utilized to carry material, the conveying of material disposablely can only extract chamber by tunnel type, the area utilization of device is low, in addition, and the feed inlet and outlet of its open type, be difficult to form vacuum in tunnel type extraction chamber, and be unfavorable for that reduction vaporization extracts.

The Chinese utility model patent CN201320026540.8 of Meng Xiangjun, disclose a kind of active peptide high-frequency microwave extractor, be characterized in frame, support a kind of long and narrow tubular cracking storehouse extended in the horizontal direction, cracking storehouse is provided with feed hopper above one end, cracking storehouse is built with conveyer belt, by bracket, multi-section microwave emitter is housed above conveyer belt, cracking storehouse upper opening is connected to air intake duct, air intake duct other end access condenser.

It should be noted that, active peptide high-frequency microwave extractor described in CN201320026540.8, support a long and narrow tubular cracking storehouse extended in the horizontal direction in frame, cracking storehouse is provided with feed hopper above one end, cracking storehouse is built with conveyer belt, and conveyer belt preferably adopts nylon tape, also can adopt bamboo curtain splint, nontoxic heat resistant plastics etc., by bracket above conveyer belt, multi-section microwave emitter is housed.Active peptide raw material loads on the conveyor belt by feed hopper, and the direct irradiation of microwave is at the upper surface of active peptide stockpile lamination (body).Its Problems existing is, due to employing is individual layer conveyer belt, not only the thickness of accumulation horizon and uniformity do not control, and conveyer belt upper surface can only be utilized to carry material, the conveying of material can only be disposable by long and narrow tubular cracking storehouse, and the area utilization of device is too low, simultaneously, the feed inlet and outlet of its open type, is also difficult to form vacuum in tubular cracking storehouse, and is unfavorable for reduction vaporization.

Known by above-mentioned patent, except CN103752028A relates on the basis of scraping thin film evaporation, adopt heating using microwave molecular clock, and CN201020592299.1 and CN201320026540.8 is on conveyer belt or conveyer belt, carry out outside heating using microwave to feed liquid, other is and carries out heating using microwave to feed liquid entirety.

Summary of the invention

The technical problems to be solved in the utility model is, a kind of strap-clamping-type thin bed of material microwave evaporation device is continuously provided, it is for solidliquid mixture, what utilize upper and lower filter screen to be formed clamping structure is inverted the equal material refining layer transported continuously, with the motion mode of round rising in microwave cavity, under the bigger serface of multilayer, pass through microwave irradiation, body phase homogeneous heating is carried out to the thinner bed of material, under higher vacuum, low temperature can be carried out and rapidly and efficiently evaporate.

The utility model solves the technical scheme that its technical problem adopts: a kind of strap-clamping-type thin bed of material microwave evaporation device continuously of structure, comprise evaporator tube, stone roller is provided with in described evaporator tube, pinch upper roll, the traction conveying roller that pinch under roll and multiple layering are crisscross arranged, upper filter screen band and lower filter screen band are set between pinch upper roll and pinch under roll, solidliquid mixture to be delivered between upper filter screen band and lower filter screen band and by pinch upper roll and pinch under roll pressing by described stone roller, described traction conveying roller drives upper filter screen band and lower filter screen band to carry in evaporator tube, described evaporator tube is provided with microwave heating equipment.

In such scheme, the top of described evaporator tube is provided with separate roller and lower separate roller, upper filter screen band and lower filter screen band upper separate roller and lower separate roller place separated, the side of described upper separate roller is provided with upper scraping plate, and the side of described lower separate roller is provided with lower scraping plate.

In such scheme, described evaporator tube is connected with vacuum extractor.

In such scheme, the top of described stone roller is provided with screw conveying feeding bed.

In such scheme, top and the bottom of described cylindrical shell are respectively equipped with bend wheel.

In such scheme, described microwave heating equipment is the microwave magnetron be arranged on cylindrical shell, and described cylinder lateral wall is provided with the installing hole corresponding with the feedback mouth of described microwave magnetron.

In such scheme, described inner barrel is provided with the carrying roller supporting upper filter screen band and lower filter screen band.

In such scheme, the top of described cylindrical shell is provided with evaporimeter upper cover and boil-off gas discharge pipe, and the bottom of described cylindrical shell is provided with liquid collecting bucket and drain connection.

In such scheme, be connected in described liquid collecting bucket with pressure feed pump, arrange in described evaporator tube and organize nozzle more, described nozzle is connected with pressure feed pump.

In such scheme, the described thickness to material folding layer determined by the roll surface locating slot groove depth of pinch upper roll and pinch under roll, groove depth scope is 1 ~ 50mm, preferably, 5 ~ 15mm, described upper filter screen band and lower filter screen band are wave transparent nonmetallic materials, and the cotton as thin is weaved cotton cloth, or terylene filter cloth, terylene filter screen, nylon leaching net etc.

In such scheme, describedly come and go the transfer ways successively risen with level, by one group at a certain distance between left and right, the traction conveying roller that upwards staggered floor is arranged along plummet direction realizes, make describedly to be delivered to discharge outlet above microwave cavity to material folding layer, on pivotal at a pair separate roller and lower separate roller surface guide effect under, upper filter screen band is separated with lower filter screen band, described to the releasing of material folding Rotating fields, material comes off.In the process, because solidliquid mixture is sandwiched between upper filter screen band and lower filter screen band, and owing to drawing the tension of conveying roller, can not come off under the inversion state that solidliquid mixture can be transported continuously in left and right break-in.

In such scheme, described microwave cavity is by low electric damage value microwave reflection metallic conductor, as stainless steel, the materials such as aluminium, be configured to the rectangle housing that basic configuration is a setting, make the device that all and described upper filter screen band contacts with lower filter screen band and the solidliquid mixture bed of material, all be contained in the rectangle housing of described setting, wherein, a pair of plummet direction side in opposite directions, folding face shape can be designed to, array microwave magnetron is arranged on the outer wall in folding face, the refraction of microwave can be strengthened in these folding faces, be conducive to forming microwave resonance field, and wave field is evenly distributed, the outer wall diverse location place of described microwave cavity, is provided with multiple infrared temperature measurement device, by controlling with microwave pulse power supply pulsewidth and being coupled of arteries and veins spacing, makes heating using microwave evaporating temperature at the operated within range of setting.

In such scheme, when described to material folding layer with continuous transportation state, from pinch upper roll and pinch under roll, via one group of traction conveying roller and modified roller, supreme separate roller and lower separate roller, namely by bottom in the course of conveying of upper strata, omnidistance under the irradiation of microwave field, solidliquid mixture microwave energy absorbing, and body phase homogeneous heating, make volatility liquid-phase conversion be gas phase.

In such scheme, when pivotal described pinch upper roll and pinch under roll, logical screen belt is by solidliquid mixture to when being clipped between filter screen band, and the part feed liquid in solidliquid mixture, because being subject to portion extrusion effect during roll surface engagement, and through filter screen, segregation falls into described microwave cavity bottom liquid collecting bucket and collects, and by external pressure feed pump, organizes nozzle by arranging in described microwave cavity more, again be sprayed onto in transport process on material folding layer, carry out circulating-heating evaporation; This part feed liquid can concentrate gradually, can go out described microwave cavity by periodic exhaustion, and be used as required.

In such scheme, in the upstream of pivotal described pinch upper roll and pinch under roll, screw conveying feeding bed and stone roller are set, described screw conveying feeding bed is arranged on the top of stone roller, the projection of the feed opening axis of symmetry of screw conveying feeding bed and the dead in line of stone roller, the gap between feed opening and roll surface, the flashboard controlled by an electric pushrod adjusts, the height of the solidliquid mixture bed of material that the described lower filter screen belt surface on described stone roller roll surface is formed, controls on an Appropriate.

In such scheme, described Appropriate refers to, the solidliquid mixture bed of material is when the roll surface engagement of pinch upper roll and pinch under roll, only be subject to part, or suitable squeezing action, make the wet part contained by the bed of material can take into account the following factor of balance: when the solidliquid mixture thickness of feed layer preferable range that the roll surface locating slot groove depth of pinch upper roll and pinch under roll is formed is 5 ~ 15mm, microwave electric field intensity obviously can not decay and affect the uniformity of heating in the bed of material; Can not make described to material folding layer on being delivered to when separate roller and lower separate roller, still containing higher wet part; Can not make described to material folding layer in course of conveying, overflow from filter screen belt edge because of too high rheological characteristic; Can not make the evaporation treatment capacity to solidliquid mixture, too low compared with the power consumption of microwave, namely evaporation efficiency is too low.

In such scheme, screw conveying feeding bed passes through varying pitch, or become spiral shell gauge structure, and revolution speed of screw, make solidliquid mixture form certain material seal pressure in described screw conveying feeding bed, to produce pressure reduction at charging aperture place, make described microwave cavity interior under the swabbing action of vacuum pump set, form certain vacuum, to be conducive to the low-temperature evaporation of feed liquid; Material seal pressure in described screw conveying feeding bed, to associate with helical feed servomotor or variable-frequency motor by pressure sensor and controls.

In such scheme, described upper separate roller and lower separate roller surface, arrange material scraping plate and lower material scraping plate respectively, and upper and lower brush roll, the material that described upper filter screen band after separation and lower filter screen band are adhered to removes, these through evaporation after material, fall into described helical feed hopper.

In such scheme, helical feed hopper passes through varying pitch, or become spiral shell gauge structure, and revolution speed of screw, make material in the spiral conveying tube of described helical feed hopper, form certain material envelope effect, to produce pressure reduction at discharge gate place, make described microwave cavity interior under the swabbing action of vacuum pump set, form certain vacuum, to be conducive to the low-temperature evaporation of feed liquid.The material envelope action intensity of described spiral transferring feeding hopper, controls by helical feed motor speed.

In such scheme, the described upper filter screen band be separated by described upper separate roller, the described lower filter screen band be separated with lower separate roller, turn back to respectively by modified roller, pivotal described pinch upper roll and pinch under roll, continue circulation to clamping liquid mixture, form the even thin bed of material under continuous transportation state, and then by heating using microwave continuous evaporation.

The utility model additionally provides a kind of strap-clamping-type thin bed of material microwave evaporation device continuously, comprise: boil-off gas discharge pipe, infrared temperature measurement device, evaporimeter upper cover, carrying roller, modified roller, traction conveying roller, upper filter screen band, evaporator tube, screw conveying feeding bed, screw conveying feeding motor, pinch upper roll, pinch upper roll motor, pinch under roll, pinch under roll motor, stone roller, stone roller motor, brush roll, brushroll motor, upper separate roller, upper separate roller motor, upper scraping plate, lower separate roller, lower separate roller motor, lower scraping plate, helical feed hopper, lower filter screen band, to material folding layer, nozzle, liquid collecting bucket, circulation fluid drain connection, microwave magnetron.

In such scheme, described boil-off gas discharge pipe is arranged on the vertex of a cone center of described evaporimeter upper cover; Multiple described infrared temperature measurement device is arranged on the folding face shape sidewall of evaporimeter upper cover and evaporator tube, and it is inner to evaporimeter that infrared measurement of temperature hot spot runs through described evaporator tube through hole, the quantity of infrared temperature measurement device 5 ~ 9.

In such scheme, described carrying roller is arranged on every layer of below to material folding layer stage casing, contacts with to the lower surface of material folding layer, and the below in upper filter screen band in the horizontal direction and lower filter screen band stage casing respectively arranges a carrying roller in addition.

In such scheme, described modified roller has 2, wherein 1, is arranged on the position with pinch upper roll homonymy above evaporator tube, and modified roller location portability position in the horizontal direction, is bolted, to adjust the tension force of upper filter screen band; Another 1 in described modified roller, be arranged on below evaporator tube, with upper separate roller homonymy, modified roller has the shift amount of adjustable lower filter screen belt tension in the horizontal direction, and is bolted.

In such scheme, multiple described traction conveying roller is arranged on every layer of both sides to material folding layer, to make material folding layer changed course conveying, and load-bearing solidliquid mixture; Described traction conveying roller roll surface has the stopper slot with pinch upper roll and pinch under roll roll surface locating slot same size and structure, stopper slot is along the width of roll surface axis direction, can according to the treating capacity of evaporimeter, selected within the scope of 500 ~ 5000mm, the quantity of traction conveying roller, can determine according to evaporator specifications, larger to specification, traction electric machine can be configured, to improve the tension distribution of filter screen band in traction conveying roller.

In such scheme, described upper filter screen band and lower filter screen band, be respectively the band of filter screen for no reason that a width is slightly less than traction conveying roller roll surface stopper slot width 5 ~ 10mm, filter screen band is the nonmetallic materials of wave transparent, cotton as thin is weaved cotton cloth, or terylene filter cloth, terylene filter screen, nylon leaching net etc.

In such scheme, the basic configuration of described evaporator tube is the rectangle housing body of a setting, and outer wall is with structural steel frame structural strengthening, as microwave cavity, wherein, a pair of plummet direction side in opposite directions, can be designed to folding face shape, the angle β scope between folding face is 120 ° ~ 170 °.

In such scheme, described evaporator tube, the diverse location place of two folding face shape outer walls, be provided with several microwave magnetron and multiple infrared temperature measurement device, between microwave magnetron and infrared temperature measurement device, by controlling with being coupled of pulsewidth and arteries and veins spacing of microwave pulse power supply, make heating using microwave evaporating temperature at 25 ~ 100 DEG C of operated within range of setting; The microwave magnetron feedback mouth place of evaporator tube, closes with the polyfluortetraethylene plate of wave transparent.

In such scheme, the microwave frequency of described magnetron can select 2450MHz, or 915MHz, when solidliquid mixture electricity damage value is comparatively large or evaporation capacity is larger, can matches 915MHz, generally match 2450MHz; Microwave rated power configures: 2450MHz, 5.4 ~ 50kW; 915MH, 20 ~ 120kW, according to different solidliquid mixtures and treating capacity, actual power adjustable.

In such scheme, described pinch upper roll and pinch under roll, be arranged on the below of evaporator tube, with screw conveying feeding bed homonymy, driven in opposite directions by pinch upper roll motor and pinch under roll motor in synchrony respectively, or shunt locking phase to driving by a motor via belt wheel, rotating speed is by servo or frequency conversion adjustment; Pinch upper roll and pinch under roll roll surface offer locating slot respectively, along the groove width of roll surface axis direction, according to the treating capacity of evaporimeter, can select within the scope of 500 ~ 5000mm.

In such scheme, described stone roller is arranged on pivotal pinch upper roll and pinch under roll upstream end, and axis horizontal distance range is 200 ~ 600mm; Stone roller is driven by stone roller motor, and rotating speed is by servo or frequency conversion adjustment.

In such scheme, described screw conveying feeding bed is arranged on the top of stone roller, the projection of the feed opening axis of symmetry of screw conveying feeding bed and the dead in line of stone roller, the feed opening of screw conveying feeding bed along the width of axis, compared with the little 20 ~ 30mm of pinch upper roll roll surface locating slot groove width 500 ~ 5000mm value range; The feed opening edge of screw conveying feeding bed is 20 ~ 70mm to the width range of material folding layer throughput direction; Gap between described screw conveying feeding bed feed opening and stone roller roll surface, adjusted by the flashboard connecting electric pushrod, control range is 5 ~ 25mm.

In such scheme, described screw conveying feeding bed, pass through varying pitch, or become spiral shell gauge structure, and revolution speed of screw, make solidliquid mixture in screw conveying feeding bed, form certain material seal pressure, produce pressure reduction at charging aperture place, pressure differential range is 0.035 ~ 0.095MPa, to associate control by pressure sensor with helical feed servomotor or variable-frequency motor 1; The feed hopper of described screw conveying feeding bed is arranged on outside the microwave cavity of evaporator tube; On the sidewall of the contiguous screw conveying feeding bed of described evaporator tube, arrange the observation window that can have an X-rayed, window material is anti-microwave leakage glass.

In such scheme, described upper separate roller and lower separate roller, be arranged on the top of evaporator tube, with helical feed hopper homonymy, driven in opposite directions by upper separate roller motor and lower separate roller motor in synchrony respectively, or shunt locking phase to driving by a motor via belt wheel, rotating speed is by servo or frequency conversion adjustment.

In such scheme, described upper scraping plate and lower scraping plate are separately positioned on the surface of separate roller and lower separate roller, and contact with lower filter screen band with corresponding upper filter screen band, contact force size is adjustable; Described upper scraping plate and lower scraping plate material are polytetrafluoroethylene (PTFE).

In such scheme, described brush roll to be separately positioned on above separate roller and below lower separate roller, and the bristle of brush roll is contacted along the bandwidth direction of upper filter screen band with lower filter screen band respectively; Described brush roll is driven by brushroll motor.

In such scheme, it is characterized in that, described helical feed hopper is arranged on the top of evaporator tube, with upper separate roller homonymy, and upper scraping plate and lower scraping plate and brush roll are dissolved in wherein, what make to remove all falls into helical feed hopper to material folding layer, the conveyor screw of its underpart passes through varying pitch, or become spiral shell gauge structure, and revolution speed of screw, make material in carrier pipe, form certain material envelope effect, produce pressure reduction at discharge gate place, pressure differential range is 0.035 ~ 0.095MPa, controls by helical feed motor speed; On the sidewall of the evaporator tube corresponding with described helical feed hopper, arrange the observation access door that can have an X-rayed, window material is anti-microwave leakage glass.

In such scheme, described nozzle is stratified and set on, with upper separate roller homonymy, the top of orlop and time lower floor's traction conveying roller roll surface, the liquid mist that nozzle is formed, evenly can be sprayed at the surface to material folding layer, the feed liquid of spraying, by the compression pump of joining outward, extract from liquid collecting bucket via circulation fluid drain connection.

In such scheme, described upper separate roller, lower separate roller, traction conveying roller, pinch upper roll, the rotating speed of pinch under roll and stone roller, by PLC or industrial computer integrating control, make the tension distribution of upper filter screen band and lower filter screen band even, and make upper filter screen band and lower filter screen band, respectively from separate roller and lower separate roller, modified roller can be passed through, successfully turn back to pinch upper roll and pinch under roll, formed the clip-on circulation transport structure of solidliquid mixture.

Because clip-on solidliquid mixture thickness of feed layer is even and thinner, in the bed of material, microwave electric field strength retrogression is little, can compared with the mode of the overall heated material of microwave, and the absorption of the bed of material to microwave energy significantly improves, and heating evaporation speed is fast.

In addition, due to the mode of heating of microwave irradiation, instead of the heating steam directly imported in evaporimeter, the gas phase in evaporimeter is only feed liquid and evaporates the escaping gas produced, eliminate the incremental contribution of water vapour to gas phase in evaporimeter, be conducive to gas clean-up.

These improve the combination measure of the vacuum in microwave cavity, strongly reduce the pressure on bed of material gas-liquid interface, make volatile component acquisition high-efficiency evaporating at low temperatures, also reduce the gas-liquid separation load of escaping gas subsequent condensation simultaneously, reduce possible heat effect excessively to the impact of volatile component quality.

If will discharge the escaping gas of described microwave cavity, suction enters condensing unit and gas-liquid separation device, and the method and device can be utilized to carry out distillation operation.Condensation and gas-liquid separation can adopt high-efficiency condensation well known in the art and separator, as screw pipework condensation device, membrane separator, chromatographic column separator, macroreticular resin separator etc.

Implement continuous strap-clamping-type of the present utility model thin bed of material microwave evaporation device, there is following beneficial effect:

The utility model utilizes pivotal pinch upper roll and pinch under roll, what formed clamping structure by upper filter screen band and lower filter screen band is inverted the even thin bed of material transported continuously, come and go the transfer ways successively risen with left and right in microwave cavity, under microwave irradiation, body phase homogeneous heating is carried out to the thin bed of material, and by the nozzle CYCLIC LOADING to segregation feed liquid, improve evaporation capacity, and by the hermetically-sealed construction of charging and discharging, improve the vacuum in evaporimeter, make feed liquid at a lower temperature Efficient Conversion be gas phase.Meanwhile, due to adopt multilayer transportation state to material folding layer, heat exchange specific area is increased, and vaporising device is compact, and area utilization significantly improves, and coordinates condensation and gas-liquid separation device, can realize distillation, extraction operation.

Accompanying drawing explanation

Below in conjunction with drawings and Examples, the utility model is described in further detail, in accompanying drawing:

Fig. 1 is the main pseudosection of continuous strap-clamping-type thin bed of material microwave evaporation device;

Fig. 2 is the side cutaway view of continuous strap-clamping-type thin bed of material microwave evaporation device;

Fig. 3 is the top view of continuous strap-clamping-type thin bed of material microwave evaporation device;

Fig. 4 is the main pseudosection in feeding structure local of Fig. 1 shown device;

Fig. 5 be Fig. 1 shown device upper and lower nip rolls and to material folding Rotating fields local main pseudosection;

Fig. 6 is the main pseudosection in discharging structure local of Fig. 1 shown device.

Detailed description of the invention

In order to there be understanding clearly to technical characteristic of the present utility model, object and effect, now contrast accompanying drawing and describe detailed description of the invention of the present utility model in detail.

The continuous strap-clamping-type of the utility model thin bed of material microwave evaporation method adopts a pair pivotal pinch upper roll and pinch under roll, by two filter screen bands for no reason, by solidliquid mixture to being clipped between filter screen band, formed upper filter screen band, the solidliquid mixture bed of material and lower filter screen band to material folding Rotating fields, and come and go with level the transfer ways successively risen and pass through microwave cavity, make the solidliquid mixture feed liquid in material folding layer, microwave energy absorbing under thin uniform layer state and by heating evaporation.

Being determined by the roll surface locating slot groove depth of pinch upper roll and pinch under roll the thickness of material folding layer, groove depth scope is 1 ~ 50mm, preferably, 5 ~ 15mm, upper filter screen band and lower filter screen band are wave transparent nonmetallic materials, and the cotton as thin is weaved cotton cloth, or terylene filter cloth, terylene filter screen, nylon leaching net etc.

The transfer ways successively risen is come and gone with level, by one group at a certain distance between left and right, the traction conveying roller that upwards staggered floor is arranged along plummet direction realizes, make to be delivered to discharge outlet above microwave cavity to material folding layer, on pivotal at a pair separate roller and lower separate roller surface guide effect under, upper filter screen band is separated with lower filter screen band, and remove material folding Rotating fields, material comes off.In the process, because solidliquid mixture is sandwiched between upper filter screen band and lower filter screen band, and owing to drawing the tension of conveying roller, can not come off under the inversion state that solidliquid mixture can be transported continuously in left and right break-in.

Microwave cavity is by low electric damage value microwave reflection metallic conductor, as the material such as stainless steel, aluminium, be configured to the rectangle housing that basic configuration is a setting, make all devices contacted with lower filter screen band and the solidliquid mixture bed of material with upper filter screen band, all be contained in the rectangle housing of setting, wherein, a pair of plummet direction side in opposite directions, folding face shape can be designed to, array microwave magnetron is arranged on the outer wall in folding face, the refraction of microwave can be strengthened in these folding faces, is conducive to forming microwave resonance field, and wave field is evenly distributed; The outer wall diverse location place of microwave cavity, is provided with multiple infrared temperature measurement device, by controlling with microwave pulse power supply pulsewidth and being coupled of arteries and veins spacing, makes heating using microwave evaporating temperature at the operated within range of setting.

When to material folding layer with continuous transportation state, from pinch upper roll and pinch under roll, via one group of traction conveying roller and modified roller, supreme separate roller and lower separate roller, namely by bottom in the course of conveying of upper strata, omnidistance under the irradiation of microwave field, solidliquid mixture microwave energy absorbing, and body phase homogeneous heating, make volatility liquid-phase conversion be gas phase.

When pivotal pinch upper roll and pinch under roll, lead to screen belt by solidliquid mixture to when being clipped between filter screen band, part feed liquid in solidliquid mixture, because being subject to portion extrusion effect during roll surface engagement, and through filter screen, segregation falls into microwave cavity bottom liquid collecting bucket and collects, by external pressure feed pump, organize nozzle by arranging in microwave cavity more, be again sprayed onto in transport process on material folding layer, carry out circulating-heating evaporation; This part feed liquid can concentrate gradually, can go out microwave cavity by periodic exhaustion, and be used as required.

In the upstream of pivotal pinch upper roll and pinch under roll, screw conveying feeding bed and stone roller are set, screw conveying feeding bed is arranged on the top of stone roller, the projection of the feed opening axis of symmetry of screw conveying feeding bed and the dead in line of stone roller, gap between feed opening and roll surface, the flashboard controlled by an electric pushrod adjusts, and the height of the solidliquid mixture bed of material that the lower filter screen belt surface on stone roller roll surface is formed, controls on an Appropriate.

Appropriate refers to, the solidliquid mixture bed of material is when the roll surface engagement of pinch upper roll and pinch under roll, only be subject to part, or suitable squeezing action, make the wet part contained by the bed of material can take into account the following factor of balance: when the solidliquid mixture thickness of feed layer preferable range that the roll surface locating slot groove depth of pinch upper roll and pinch under roll is formed is 5 ~ 15mm, microwave electric field intensity obviously can not decay and affect the uniformity of heating in the bed of material; Can not make on being delivered to, when separate roller and lower separate roller, still to contain higher wet part to material folding layer; Can not make, to material folding layer in course of conveying, to overflow from filter screen belt edge because of too high rheological characteristic; Can not make the evaporation treatment capacity to solidliquid mixture, too low compared with the power consumption of microwave, namely evaporation efficiency is too low.

Screw conveying feeding bed passes through varying pitch, or become spiral shell gauge structure, and revolution speed of screw, make solidliquid mixture in screw conveying feeding bed, form certain material seal pressure, to produce pressure reduction at charging aperture place, make microwave cavity interior under the swabbing action of vacuum pump set, form certain vacuum, to be conducive to the low-temperature evaporation of feed liquid; Material seal pressure in screw conveying feeding bed, to associate with helical feed servomotor or variable-frequency motor by pressure sensor and controls.

Upper separate roller and lower separate roller surface, arrange material scraping plate and lower material scraping plate respectively, and upper and lower brush roll, and the material that the upper filter screen band after separation and lower filter screen band are adhered to removes, these through evaporation after material, fall into helical feed hopper.

Helical feed hopper passes through varying pitch, or become spiral shell gauge structure, and revolution speed of screw, make material in the spiral conveying tube of helical feed hopper, form certain material envelope effect, to produce pressure reduction at discharge gate place, make microwave cavity interior under the swabbing action of vacuum pump set, form certain vacuum, to be conducive to the low-temperature evaporation of feed liquid.The material envelope action intensity of spiral transferring feeding hopper, controls by helical feed motor speed.

The upper filter screen band be separated by upper separate roller, with the lower filter screen band that lower separate roller is separated, turns back to respectively by modified roller, pivotal pinch upper roll and pinch under roll, continue circulation to clamping liquid mixture, form the even thin bed of material under continuous transportation state, and then by heating using microwave continuous evaporation.

As Fig. 1, shown in Fig. 2 and Fig. 3, the continuous strap-clamping-type of the one that the utility model provides thin bed of material microwave evaporation device 01, its structure comprises: boil-off gas discharge pipe 0101, infrared temperature measurement device 0102, evaporimeter upper cover 0103, carrying roller 0104, modified roller 0105, traction conveying roller 0106, upper filter screen band 0107, evaporator tube 0108, screw conveying feeding bed 0109, screw conveying feeding motor 01091, pinch upper roll 0110, pinch upper roll motor 01101, pinch under roll 0111, pinch under roll motor 01111, stone roller 0112, stone roller motor 01121, brush roll 0113, brushroll motor 01131, upper separate roller 0114, upper separate roller motor 01141, upper scraping plate 0115, lower separate roller 0116, lower separate roller motor 01161, lower scraping plate 0117, helical feed hopper 0118, lower filter screen band 0119, to material folding layer 0120, nozzle 0121, liquid collecting bucket 0122, circulation fluid drain connection 0123, microwave magnetron 0124.

As shown in Figure 1, Figure 2 and Figure 3, boil-off gas discharge pipe 0101 is arranged on the vertex of a cone center of evaporimeter upper cover 0103, by sealing flange or weld connection; Multiple infrared temperature measurement device 0102 is arranged on the folding face shape sidewall of evaporimeter upper cover 0103 and evaporator tube 0108, connected by flange and bolt seal, it is inner to evaporimeter that infrared measurement of temperature hot spot runs through evaporator tube 0108 through hole, the quantity of infrared temperature measurement device 0,102 5 ~ 9, the present embodiment is 5; Carrying roller 0104 is arranged on every layer of below to material folding layer 0120 stage casing, contacts with to the lower surface of material folding layer 0120, and the upper filter screen band 0107 of another horizontal direction and the below in lower filter screen band 0119 stage casing respectively arrange a carrying roller 0104; Modified roller 0105 has 2, wherein 1, is arranged on the position with pinch upper roll 0110 homonymy above evaporator tube 0108, and modified roller 0105 location portability position in the horizontal direction, is bolted, to adjust the tension force of upper filter screen band 0107.

Multiple traction conveying roller 0106 is arranged on every layer of both sides to material folding layer 0120, carries to make to alter course to material folding layer 0120, and load-bearing solidliquid mixture; Traction conveying roller 0106 roll surface has the stopper slot with pinch upper roll 0110 and pinch under roll 0111 roll surface locating slot same size and structure, to prevent material folding layer 0120 sideslip under transportation state; Stopper slot is along the width of roll surface axis direction, can according to the treating capacity of evaporimeter, selected within the scope of 500 ~ 5000mm, the present embodiment is 1600mm, the quantity of traction conveying roller 0106, can determine according to evaporator specifications, larger to specification, traction electric machine can be configured in traction conveying roller 0106, to improve the tension distribution of filter screen band, the present embodiment, arranges 10 traction conveying rollers 0106, and the traction conveying roller 0106 of the 6th from bottom to up configures traction electric machine.

Upper filter screen band 0107 and lower filter screen band 0119, it is respectively the band of filter screen for no reason that a width is slightly less than traction conveying roller 0106 roll surface stopper slot width 5 ~ 10mm, filter screen band is the nonmetallic materials of wave transparent, cotton as thin is weaved cotton cloth, or terylene filter cloth, terylene filter screen, nylon leaching net etc., the present embodiment is that cotton is weaved cotton cloth, and tape thickness λ scope is 0.5 ~ 2mm.

The basic configuration of evaporator tube 0108 is the rectangle housing of a setting, outer wall with structural steel frame structural strengthening, as microwave cavity, wherein, a pair of plummet direction side in opposite directions, can be designed to folding face shape, the angle β scope between folding face is 120 ° ~ 170 °, in the present embodiment, β=116.15 °, the refraction of microwave can be strengthened in these folding faces, is conducive to forming microwave resonance field, and wave field is evenly distributed; Whole evaporator tube 0108 is with low electric damage value microwave reflection metallic conductor, and as the material structure such as stainless steel, aluminium, in the present embodiment, be stainless steel SUS304, cylindrical shell height is 2950mm, width 2100/2500mm, thickness 2150mm.

Evaporator tube 0108, the diverse location place of two folding face shape outer walls, be provided with several microwave magnetron 0124 and multiple infrared temperature measurement device 0102, between microwave magnetron 0124 and infrared temperature measurement device 0102, by controlling with being coupled of pulsewidth and arteries and veins spacing of microwave pulse power supply, make heating using microwave evaporating temperature at 25 ~ 100 DEG C of operated within range of setting; The microwave magnetron 0124 of evaporator tube 0108 presents mouth place, closes with the polyfluortetraethylene plate of wave transparent.

The microwave frequency of magnetron 0124 can select 2450MHz, or 915MHz, when solidliquid mixture electricity damage value is comparatively large or evaporation capacity is larger, can matches 915MHz, generally match 2450MHz; Microwave rated power configures: 2450MHz, 5.4 ~ 50kW; 915MH, 20 ~ 120kW; In the present embodiment, the microwave frequency of magnetron 0124 is the magnetron of 2450MHz, 12 0.9kW, and the maximum rated power of configuration is 10.8kW, according to different solidliquid mixtures and treating capacity, and actual power adjustable.

Pinch upper roll 0110 and pinch under roll 0111, be arranged on the below of evaporator tube 0108, with screw conveying feeding bed 0109 homonymy, respectively by pinch upper roll motor 01101 and pinch under roll motor 01111 locking phase to driving, or shunt locking phase to driving by a motor via belt wheel, rotating speed is by servo or frequency conversion adjustment; Pinch upper roll 0110 and pinch under roll 0111 roll surface offer locating slot respectively, along the groove width of roll surface axis direction, can according to the treating capacity of evaporimeter, and selected within the scope of 500 ~ 5000mm, the present embodiment is 1600mm; Groove depth δ scope is 5 ~ 15mm, and the present embodiment is 10mm.

Stone roller 0112 is arranged on pivotal pinch upper roll 0110 and pinch under roll 0111 upstream end, and axis horizontal distance range is 200 ~ 600mm, and the present embodiment is 345mm; Stone roller 0112 is driven by stone roller motor 01121, and rotating speed is by servo or frequency conversion adjustment.

Screw conveying feeding bed 0109 is arranged on the top of stone roller 0112, the projection of the feed opening axis of symmetry of screw conveying feeding bed 0109 and the dead in line of stone roller 0112, the feed opening of screw conveying feeding bed 0109 along the width of axis, compared with the little 20 ~ 30mm of pinch upper roll 0110 roll surface locating slot groove width 500 ~ 5000mm value range; The feed opening of screw conveying feeding bed 0109 is along being 20 ~ 70mm to the width range of material folding layer 0120 throughput direction, and the present embodiment is 35mm; Gap between screw conveying feeding bed 0109 feed opening and stone roller 0112 roll surface, adjusted by the flashboard connecting electric pushrod, control range is 5 ~ 25mm, and the present embodiment is 12mm.

Screw conveying feeding bed 0109, pass through varying pitch, or become spiral shell gauge structure, and revolution speed of screw, solidliquid mixture is made to form certain material seal pressure in screw conveying feeding bed 0109, produce pressure reduction at charging aperture place, pressure differential range is 0.035 ~ 0.095MPa, to associate control by pressure sensor with helical feed servomotor or variable-frequency motor 01091; The feed hopper of screw conveying feeding bed 0109 is arranged on outside the microwave cavity of evaporator tube 0108; On the sidewall of the contiguous screw conveying feeding bed 0109 of evaporator tube 0108, arrange the observation window that can have an X-rayed, window material is anti-microwave leakage glass.

Upper separate roller 0114 and lower separate roller 0116, be arranged on the top of evaporator tube 0108, with helical feed hopper 0118 homonymy, respectively by upper separate roller motor 01141 and lower separate roller motor 01161 locking phase to driving, or shunt locking phase to driving by a motor via belt wheel, rotating speed is by servo or frequency conversion adjustment.

Upper scraping plate 0115 and lower scraping plate 0117 are separately positioned on the surface of separate roller 0114 and lower separate roller 0116, and contact with lower filter screen band 0119 with corresponding upper filter screen band 0107, contact force size is adjustable; Upper scraping plate 0115 and lower scraping plate 0117 material are polytetrafluoroethylene (PTFE).

Brush roll 0113 to be separately positioned on above separate roller 0114 and below lower separate roller 0116, and the bristle of brush roll 0113 is contacted along the bandwidth direction of upper filter screen band 0107 with lower filter screen band 0119 respectively; Brush roll 0113 is driven by brushroll motor 01131.

Helical feed hopper 0118 is arranged on the top of evaporator tube 0108, with upper separate roller 0114 homonymy, and upper scraping plate 0115 and lower scraping plate 0117 and brush roll 0113 are dissolved in wherein, what make to remove all falls into helical feed hopper 0118 to material folding layer 0120, the conveyor screw of its underpart passes through varying pitch, or become spiral shell gauge structure, and revolution speed of screw, make material in carrier pipe, form certain material envelope effect, pressure reduction is produced at discharge gate place, pressure differential range is 0.035 ~ 0.095MPa, controls by helical feed motor speed; On the sidewall of the evaporator tube 0108 corresponding with helical feed hopper 0118, arrange the observation access door that can have an X-rayed, window material is anti-microwave leakage glass.

Another 1 in modified roller 0105, be arranged on below evaporator tube 0108, with upper separate roller 0114 homonymy, modified roller 0105 location portability position in the horizontal direction, is bolted, to adjust the tension force of lower filter screen band 0119.

Nozzle 0121 is stratified and set on, with upper separate roller 0114 homonymy, the top of orlop and time lower floor's traction conveying roller 0106 roll surface, the liquid mist that nozzle 0121 is formed, evenly can be sprayed at the surface to material folding layer 0120, the feed liquid sprayed, by the compression pump of joining outward, extracts from liquid collecting bucket 0122 via circulation fluid drain connection 0123.

Upper separate roller 0114, lower separate roller 0116, traction conveying roller 0106, pinch upper roll 0110, the rotating speed of pinch under roll 0111 and stone roller 0112, by PLC or industrial computer integrating control, make the tension distribution of upper filter screen band 0107 and lower filter screen band 0119 even, and make upper filter screen band 0107 and lower filter screen band 0119, can respectively from separate roller 0114 and lower separate roller 0116, by modified roller 0105, successfully turn back to pinch upper roll 0110 and pinch under roll 0111, formed the clip-on circulation transport structure of solidliquid mixture.

By reference to the accompanying drawings embodiment of the present utility model is described above; but the utility model is not limited to above-mentioned detailed description of the invention; above-mentioned detailed description of the invention is only schematic; instead of it is restrictive; those of ordinary skill in the art is under enlightenment of the present utility model; do not departing under the ambit that the utility model aim and claim protect, also can make a lot of form, these all belong within protection of the present utility model.

Claims (9)

1. a continuous strap-clamping-type thin bed of material microwave evaporation device, it is characterized in that, comprise evaporator tube, the traction conveying roller that stone roller, pinch upper roll, pinch under roll and multiple layering are crisscross arranged is provided with in described evaporator tube, upper filter screen band and lower filter screen band are set between pinch upper roll and pinch under roll, solidliquid mixture to be delivered between upper filter screen band and lower filter screen band and by pinch upper roll and pinch under roll pressing by described stone roller, described traction conveying roller drives upper filter screen band and lower filter screen band to carry in evaporator tube, and described evaporator tube is provided with microwave heating equipment.

2. continuous strap-clamping-type according to claim 1 thin bed of material microwave evaporation device, it is characterized in that, the top of described evaporator tube is provided with separate roller and lower separate roller, upper filter screen band and lower filter screen band upper separate roller and lower separate roller place separated, the side of described upper separate roller is provided with upper scraping plate, and the side of described lower separate roller is provided with lower scraping plate.

3. continuous strap-clamping-type according to claim 1 thin bed of material microwave evaporation device, it is characterized in that, described evaporator tube is connected with vacuum extractor.

4. continuous strap-clamping-type according to claim 1 thin bed of material microwave evaporation device, is characterized in that, the top of described stone roller is provided with screw conveying feeding bed.

5. continuous strap-clamping-type according to claim 1 thin bed of material microwave evaporation device, is characterized in that, top and the bottom of described cylindrical shell are respectively equipped with bend wheel.

6. continuous strap-clamping-type according to claim 1 thin bed of material microwave evaporation device, is characterized in that, described microwave heating equipment is the microwave magnetron be arranged on cylindrical shell, and described cylinder lateral wall is provided with the installing hole corresponding with the feedback mouth of described microwave magnetron.

7. continuous strap-clamping-type according to claim 1 thin bed of material microwave evaporation device, is characterized in that, described inner barrel is provided with the carrying roller supporting upper filter screen band and lower filter screen band.

8. continuous strap-clamping-type according to claim 1 thin bed of material microwave evaporation device, is characterized in that, the top of described cylindrical shell is provided with evaporimeter upper cover and boil-off gas discharge pipe, and the bottom of described cylindrical shell is provided with liquid collecting bucket and drain connection.

9. continuous strap-clamping-type according to claim 8 thin bed of material microwave evaporation device, is characterized in that, be connected in described liquid collecting bucket with pressure feed pump, and arrange in described evaporator tube and organize nozzle more, described nozzle is connected with pressure feed pump.