CN204891976U - Plant material selectivity is smashed and splitter - Google Patents
Plant material selectivity is smashed and splitter Download PDFInfo
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- CN204891976U CN204891976U CN201520546869.6U CN201520546869U CN204891976U CN 204891976 U CN204891976 U CN 204891976U CN 201520546869 U CN201520546869 U CN 201520546869U CN 204891976 U CN204891976 U CN 204891976U
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Abstract
The utility model discloses an equipment with the separation is smashed to plant material selectivity, and this selectivity is smashed and is included with the splitter: the feeder hopper for hold pending material, lax equipment, the release of cohesion power between material granule tissue is realized to lax equipment, crushing apparatus, the separation of different cohesion power tissue in the crushing apparatus realization material granule, the whirlwind splitter, whole collection of thickness powder mixtures after the whirlwind splitter will aforesaidly be smashed gets into temporary storage bin, screening plant, thickness powder mixtures screening after screening plant will aforementionedly smash is different particle size range's result and saves respectively. The utility model discloses the mesh that the pure phm mode of plant material, selectivity were smashed and was separated has been realized to the apparatus and method for, the utility model discloses a apparatus and method for can be used for all organizational structure nature to be similar to the plant material including skin red date pulp granule, wheat bran, separation purity, material utilization ratio and the work efficiency of this type of raw materials of promotion that will be very big.
Description
Technical field
The utility model belongs to materiel machining technical field, particularly relates to plant material selective molecular attraction and separation equipment.
Background technology
The physiological function of the different tissues of plant part is all different from contained component.When these setup action foods or medicine are by human intake, they are for the effect also corresponding difference of human body.When people are in order to absorb predetermined substance, when needing the particular organization position of plant, often encounter and be difficult to the plant tissue needed is extracted targetedly and can only accept to mix the situation of other unwanted plant tissues a large amount of, thus occur the situation of " purity low but can only so "; Simultaneously, people are at processed food raw material or make in the process of food, sometimes in order to a certain object can be abandoned as waste material using containing other compositions being of value to human body in a large number again, thus cause the situation of " purity meets but waste resource ", What is more, there will be its effect of composition abandoned greatly to be underestimated, cause the situation of " purity is up to standard but lose more than gain ".
Such as, red date is rich in the nutritional labelings such as protein, fat, carbohydrate, carrotene, B family vitamin, vitamin C, citrin and calcium, phosphorus, iron and CAMP, it is food and medicine consangunity raw material, its function as food or medicine is accepted extensively by China resident, but the material composition that the pericarp of red date and pulp contain differs widely, its effect and purposes are also different.Red date skin is rare traditional Chinese medicine simply, extracting method general is at present all boil rear squeezing to remove jujube paste (pulp), again processing is continued to remaining fructus corni and jujube core, there is the shortcomings such as waste is large, wholesomeness is low, active ingredient is lost in a large number in this original processing method, and the red date powder that red date pulp is processed into is as a kind of making drinks food, there is certain health care and deeply like by consumer, but current red date powder production method is all red date entirety to be pulverized, and there is the shortcomings such as energy consumption is high, fructus corni is not easily pulverized, coarse mouthfeel.
Again such as, wheat bran is the byproduct of flour milling industry, and China's annual production exceedes 2,000 ten thousand tons, and only have minimum ratio to be applied to food at present, the overwhelming majority is used as feed.But it is the great wasting of resources that wheat bran uses as feed, from the angle of Food Science, the aleurone being attached to wheat bran internal layer is a kind of material that is significant to health, that have actual health-care effect, its essence is the large raw-food material having actual health care that can eat as staple food grain, if in addition Appropriate application, the national grain and the raw-food material that have health care that increase by 6,000,000 tons will be given every year.The difficulty extracting wheat aleurone layer is just that aleurone combines with wheat exosper, and be difficult to effective separation, so in Flour production process, aleurone is just along with wheat bran enters feed.Industrial circle meets by the precision constantly promoting flour the life requirement that people improve day by day, but incident, and this material being enriched most nutritional benefit composition in wheat of aleurone has been abandoned.
Therefore, if have a kind of physical processing method and equipment, selective, highly purified separation and pulverizing can be done containing the plant material containing different tissues, different value that skin pulp particle, wheat bran are similar from red date, make different structural constituents in origin separately, just can realize resource effectively and reasonably, the utilization of science.This processing technology will improve the product quality level of relevant industries, industry scientific and technological level and economic benefit, better, the more economical demand meeting people greatly.
Summary of the invention
First object of the present utility model is to provide a kind of plant material selective molecular attraction and separation equipment.
In order to realize above-mentioned first object, the utility model provides a kind of plant material selective molecular attraction and separation equipment, and it comprises:
Feed hopper, for holding pending material;
Lax equipment, the charging aperture of described lax equipment is connected by conveying worm with described feed hopper; Described lax equipment realizes the release of material particles inner tissue interlayer cohesive force;
Disintegrating apparatus, the charging aperture of described disintegrating apparatus is connected with the discharging opening of lax equipment; Described disintegrating apparatus realizes the separation of different cohesive force tissue in material particles, and less cohesive force tissue is pulverized after departing from disintegrating apparatus, and larger cohesive force is organized and substantially remained unchanged; Material after pulverizing is the fine powder component of granularity between 1.4 ~ 150 μm and the mixture of the meal component of granularity more than 150 μm;
Cyclonic separating apparatus, described Cyclonic separating apparatus is communicated with disintegrating apparatus discharging opening; Cyclone separator discharging opening is communicated with temporary storing bin;
Screening plant, above-mentioned material thickness powder mixture enters described screening plant from above-mentioned temporary storing bin discharging opening through conveying worm, is the product of different-grain diameter scope at described screening plant Inside sifter; And the product of different-grain diameter scope enters different storage silo respectively.
The utility model plant material selective molecular attraction as above and separation equipment, further, conveying worm comprises induction system and kinetic control system, and described kinetic control system controls and drives conveyor screw to rotate.
The utility model plant material selective molecular attraction as above and separation equipment, further, described lax equipment comprises: lax equipment charging aperture, lax equipment discharging opening, lax equipment body, vibration rod and kinetic control system; Kinetic control system drives lax equipment body and vibration rod vibrations.
The utility model plant material selective molecular attraction as above and separation equipment, further, described disintegrating apparatus comprises pulverizes body and kinetic control system; Pulverize body to comprise cavity, fixing grating disk, rotate grating disk; Fixing grating disk and inside, cavity side are connected as a single entity, and rotate grating disk and are arranged in described cavity; The rotating shaft of the motor controlled by kinetic control system is connected with rotation grating disk, drives and rotates grating disk operation.
The utility model plant material selective molecular attraction as above and separation equipment, further, fixing grating disk and rotation grating disk are all circular, be respectively arranged with the pulverizing post vertical with card, the diameter pulverizing post is Φ 6 ~ 12, length 40 ~ 90mm, the pulverizing post that pulverizing post and the rotation of fixing grating disk are pulverized is crisscross arranged, and the gap between adjacent two pulverizing posts is 0.2 ~ 1.5mm.
The utility model plant material selective molecular attraction as above and separation equipment, further, crusher cavity is oblate column, the inwall of cylinder is processed as the semicircle column type that the diameter be arranged in parallel is Φ 6 ~ 12, the axial line of semicolumn and the axis parallel pulverizing post, the gap that the most outer shroud rotating grating disk is pulverized between post and described semicolumn is 0.5 ~ 1.5mm.
The utility model plant material selective molecular attraction as above and separation equipment, further, described Cyclonic separating apparatus comprises cyclone separator, high-pressure suction fan and kinetic control system, and high-pressure suction fan is connected to the top of cyclone separator.
The utility model plant material selective molecular attraction as above and separation equipment, further, described screening setting comprises kinetic control system and three-D screening plant; Three-D screening plant is made up of sieve nest and compass screen surface; Compass screen surface tool haves three layers, and from top to bottom arranges successively.
The beneficial effects of the utility model are:
The utility model equipment is physical process equipment, material particles medium and small cohesive force structure sheaf first clashes into and release portion cohesive force through vibrations and radial direction in lax equipment, after in disintegrating apparatus through collide, rub, rub and percussion and continue release cohesive force, reach tissue depart from and pulverize object, and the kinetic energy provided due to equipment is not enough to thoroughly discharge the cohesive force of organizing of large cohesive force structure sheaf inside, in material particles, large cohesive force structure sheaf will remain unchanged or only have small part to produce phenomenon of rupture substantially.Like this, just achieve the goal of the invention of pure Physical Processing mode, selective molecular attraction, and confirm that the program is feasible by test.In addition, apparatus and method for of the present utility model, may be used for all institutional framework character and be similar to plant granule containing skin red date pulp, wheat bran, promote the use of in relevant industries, the performance of raw material, purity and utilization rate will be promoted greatly, thus promote industrial value and scientific and technological content, also there is extremely strong Economic Value Added effect.
Accompanying drawing explanation
By detailed description done in conjunction with the following drawings, above-mentioned and/or other aspects of the present utility model and advantage will become clearer and be easier to understand, and these accompanying drawings just schematically, do not limit the utility model, wherein:
Fig. 1 is the use schematic flow sheet of the material selective molecular attraction separation equipment of a kind of embodiment of the utility model;
Fig. 2 is the overall schematic of the selective crushing material separation equipment of a kind of embodiment of the utility model;
Fig. 3 is feed hopper and the conveying worm schematic diagram of a kind of embodiment of the utility model.
Detailed description of the invention
Hereinafter, the embodiment of plant material selective molecular attraction of the present utility model and separator is described with reference to the accompanying drawings.
The embodiment recorded at this is specific detailed description of the invention of the present utility model, for illustration of design of the present utility model, is all explanatory and exemplary, should not be construed as the restriction to the utility model embodiment and the utility model scope.Except the embodiment recorded at this, those skilled in the art can also adopt other technical scheme apparent based on the content disclosed in the application's claims and description, and these technical schemes comprise the technical scheme making any apparent substitutions and modifications adopted the embodiment recorded at this.
The accompanying drawing of this description is schematic diagram, and aid illustration design of the present utility model schematically shows shape and the correlation thereof of each several part.Note that the structure of each parts for the ease of clearly showing the utility model embodiment, not according to identical scale between each accompanying drawing.Identical reference marker is for representing identical part.
A kind of plant material selective molecular attraction and separation equipment, it comprises:
Feed hopper 1000, for holding pending material; The bottom of described feed hopper is back taper in one embodiment, is convenient to material by being gravitationally fallen to feeding funnel bottom part.
Lax equipment 3000, the charging aperture of described lax equipment is connected by conveying worm 2000 with described feed hopper 1000; Described lax equipment realizes the release of material cohesive force;
Disintegrating apparatus 4000, the charging aperture of described disintegrating apparatus is connected with the discharging opening of lax equipment; Described disintegrating apparatus realizes the pulverizing of material; Material after pulverizing comprises the fine powder component of grain graininess between 1.4 ~ 150 μm and the meal component of grain graininess more than 150 μm;
Cyclonic separating apparatus 5000, the thickness powder mixture after pulverizing is collected by described Cyclonic separating apparatus, and enters temporary storing bin;
Screening plant 7000, the charging aperture of described screening plant is connected by conveying worm 6000 with the temporary storing bin discharging opening of described Cyclonic separating apparatus, and the screening of described thickness powder mixture is the product of different-grain diameter scope by described screening plant; And the product of different-grain diameter scope enters different storage silo respectively.
In the plant material selective molecular attraction and separation equipment of the utility model above-described embodiment, described feed hopper comprises discharging control valve 1001, and material flows out through discharging control valve 1001.
In the plant material selective molecular attraction and separation equipment of the utility model above-described embodiment, conveying worm 2000 is for being delivered to lax equipment by material by feed hopper.Described conveying worm 2000 comprises urceolus 2021, conveyor screw 2022, kinetic control system 2030; After material enters, under the conveying thrust of conveyor screw 2022, enter conveying worm discharging opening 2011, and flow into lax equipment 3000.The movement velocity of conveyor screw 2022 determines the flow of material, this movement velocity is controlled by kinetic control system 2030, kinetic control system 2030 is combinations of a three phase electric machine and appliance controller, by man-machine interface to three phase electric machine with work order, realize the accurate control of mass flow, actual flow numerical value is determined by production throughput requirements and functions of the equipments.
In the plant material selective molecular attraction and separation equipment of the utility model above-described embodiment, lax equipment 3000 realizes the cohesive force release of material.Lax equipment 3000 comprises lax equipment charging aperture, lax equipment discharging opening, vibration rod, vibrations body and kinetic control system; Kinetic control system drives vibration rod and the vibrations of vibrations body.Kinetic control system by vibration motor and controller, shake transmission mechanism and form, implementation provides instruction in man-machine interface, vibration motor provides certain amplitude and shake vibroseis frequently, the vibrations that this vibroseis sends are delivered on vibration rod and vibrations body through the effect of vibrations transmission mechanism, vibration rod and vibrations body just work under this amplitude and shake frequently, reach technique object.Actual vibration frequency is set to 150 ~ 300Hz, and amplitude, by the setting of checking material treatment effect, is generally 2 ~ 5mm.
In the plant material selective molecular attraction and separation equipment of the utility model above-described embodiment, the pulverizing of material completes in the pulverizing body of disintegrating apparatus, and pulverizing power is provided by motor and control system; Pulverize body to comprise fixing grating disk, rotate grating disk and cavity, motor-driven rotation grating disk runs.
It is circular for rotating grating disk, and 4 rings arranging diameter different pulverize post, and the diameter that each root pulverizes post is Φ 8, length 80mm, and the gap between adjacent two pulverizing posts of same ring is 0.2 ~ 1.5mm, and rotation grating disk is fixed on and rotates Your Majesty.Fixing grating disk is circular, and 4 rings arranging diameter different pulverize post, and the diameter that each root pulverizes post is Φ 8, length 80mm, and the gap between adjacent two pulverizing posts of same ring is 0.2 ~ 1.5mm, and fixing grating disk and cavity are integrated.Fixing grating disk and rotate grating disk with the use of, the pulverizing post of the annular spread arranged separately is crisscross arranged, and the gap of adjacent two rings is 0.2 ~ 1.5mm.
In order to realize effective pulverizing of material, the inwall of cavity is processed into the semicolumn that the diameter discharged side by side is Φ 8, and the axis direction of semicolumn is parallel with the axis direction pulverizing post, plays the effect of pulverizing post.The rotating speed rotating grating disk is 3500 ~ 6500rad/min, this power rotated is provided by motor and kinetic control system, specifically provide movement instruction to motor by man-machine interface, motor is started working, drive transmission main shaft high-speed rotation, simultaneously, the rotation grating disk be arranged on transmission main shaft starts High Rotation Speed with same rotating speed, flow into the material of crushing chamber by all pulverizing posts, rotate grating disk, random turbulent motion is done in the confined space that fixing grating disk and cavity are formed, and constantly clashed into, friction, the effect of rubbing, can constantly separate through lax material little cohesive force mechanism layer, and pulverized by continuation, reach technique object.Meanwhile, under the effect of the rotation grating disk of High Rotation Speed, inside cavity forms blast, drives material to flow out from discharging opening and enters Cyclonic separating apparatus 5000.
In the plant material selective molecular attraction and separation equipment of the utility model above-described embodiment, Cyclonic separating apparatus 5000 comprises cyclone separator and high-pressure suction fan, and the airduct of high-pressure suction fan is connected to the top of cyclone separator.High negative pressure wind-force is produced by high-pressure suction fan, and its work order is given to id-motor by man-machine interface, and the running of id-motor energizes high-pressure blower fan produces the air quantity and the blast that meet technological requirement.The air quantity of high-pressure suction fan is 3500 ~ 6500m
3/ h, total head is 6000 ~ 16000Pa.Thickness powder mixture material is entered by the top charging aperture of cyclone separator to be received in whirlwind storage, under the effect of wind-force and self gravitation, shape sedimentation of spinning is flowed out from discharging opening, tail wind is discharged by sack cleaner, fine particle material in tail wind is through the filtration of cloth bag, be deposited in cyclone separator, after assembly, under self gravitation effect, sedimentation is flowed out from discharging opening in the lump, and the mixtures of materials flowed out from cyclone separator discharging opening enters temporary storing bin under self gravitation effect.
In the plant material selective molecular attraction and separation equipment of the utility model above-described embodiment, conveying worm 6000 is for being delivered to screening plant by material by temporary storing bin.Described conveying worm 6000 comprises urceolus, conveyor screw, kinetic control system; After material enters, under the conveying thrust of conveyor screw, enter discharging opening, and flow into lax equipment 7000.The movement velocity of conveyor screw determines the flow of material, this movement velocity is controlled by kinetic control system, kinetic control system is the combination of a three phase electric machine and appliance controller, by man-machine interface to three phase electric machine with work order, realize the accurate control of mass flow, actual flow numerical value is determined by production throughput requirements and functions of the equipments.
In the plant material selective molecular attraction separation equipment of the utility model above-described embodiment, three-D screening plant 7000 comprises sieve nest, compass screen surface and vibroseis.Thickness powder mixture material is delivered to the charging aperture of screening plant 7000 by conveying worm 6000, the ground floor of compass screen surface is fallen into through charging aperture, by man-machine interface, work order is given to vibration motor, vibration motor is started working, drive the most three-D motion of overall sieve nest, material by the ground floor of compass screen surface, successively through three layers of compass screen surface, the material of variable grain degree is retained and flows out on different compass screen surfaces, enters respective holder.
As shown in Figure 1, be the use schematic flow sheet of above-mentioned plant material selective molecular attraction and separation equipment, comprise the following steps:
Step 1, sends material into feed hopper, and raw meal particle size is between 1mm ~ 4mm, and moisture content of material scope is 8 ~ 15wt%; Preferably, described material is red date or wheat bran.More preferably, red date moisture is at below 9.5wt%, and the moisture of wheat bran is at below 14.5wt%.
Step 2, sends the material in feed hopper into lax equipment, and equipment shake is 150 ~ 300Hz frequently, and the processing time is 5 ~ 10 seconds; Realize the lax of cohesive force between the inner different tissues layer of material particles by the mode of vibrations, the adhesion between the organized layer making cohesive force little and the large organized layer of cohesive force significantly reduces;
Step 3, material flows into disintegrating apparatus from lax equipment, equipment rotating speed 3000 ~ 6000rad/min; Disintegrating apparatus realizes little cohesive force organized layer particle and departs from and pulverize;
Step 4, crushing rear material collects temporary storing bin by pulsed Cyclonic separating apparatus;
Step 5, in temporary storing bin, material flows into screening plant, by the screening of three-D rectangular mesh screen, makes the feed separation of different grain size scope, and enters different storage warehouses.
The concrete technology flow process utilizing the utility model equipment to realize material selective molecular attraction separation method is:
1, prepare the plant small particles material of satisfactory quality, granularity is between 1mm ~ 4mm, and moisture is 8% ~ 15%, other foreign matters that follow-up equipment damages may not be caused, material is poured in feed hopper 1000, flow out through discharging control valve 1001, enter conveying worm 2000.
2, the first conveying worm 2000 mainly realizes the conveying of material, after material enters, under the conveying thrust of conveyor screw 2022, by discharging opening 2011, and flows into lax equipment 3000.The movement velocity of conveyor screw 2022 determines the flow of material, this movement velocity is controlled by the first kinetic control system 2030, first kinetic control system 2030 is combinations of a three phase electric machine and appliance controller, by man-machine interface to three phase electric machine with work order, realize the accurate control of mass flow, actual flow numerical value is determined by production throughput requirements and functions of the equipments.
3, lax equipment 3000 mainly realizes the cohesive force release of material, material is entered by charging aperture, through the certain frequency of built-in multi-level vibration rod and the repeatedly radial compression of amplitude and collision, realize the adhesion release of the medium and small cohesive force structure sheaf of material, then flowed out by discharging opening, enter disintegrating apparatus 4000.The vibrations of vibration rod, realized by the second kinetic control system, second kinetic control system by vibration motor and controller, shake transmission mechanism and form, implementation provides instruction in man-machine interface, vibration motor provides certain amplitude and shake vibroseis frequently, the vibrations that this vibroseis sends are delivered on vibrations cavity and vibration rod through the effect of vibrations transmission mechanism, and vibrations cavity and vibration rod just work under this amplitude and shake frequently, reach technique object.Actual vibration frequency is set to 150 ~ 300Hz, and amplitude, by the setting of checking material treatment effect, is generally 2 ~ 5mm.
4, material is entered by the charging aperture of disintegrating apparatus 4000, through pulverizing body, is flowed out by discharging opening.The pulverizing of material completes in pulverizing body, and pulverizing power is provided by the 3rd kinetic control system.The main composition pulverizing body is fixing grating disk, rotates grating disk and cavity.It is circular for rotating grating disk, and 4 rings arranging diameter different pulverize post, and the diameter that each root pulverizes post is Φ 8, length 80mm, and the gap between adjacent two pulverizing posts of same ring is 0.2 ~ 1.5mm, rotate grating disk and are fixed on rotating spindle.Fixing grating disk is circular, and 4 rings arranging diameter different pulverize post, and the diameter that each root pulverizes post is Φ 8, length 80mm, and the gap between adjacent two pulverizing posts of same ring is 0.2 ~ 1.5mm, and the side of fixing grating disk and cavity is integrated.Fixing grating disk and rotate grating disk with the use of, the pulverizing post interlaced arrangement of the annular spread arranged separately, the gap of adjacent two rings is 0.2 ~ 1.5mm.In order to realize effective pulverizing of material, the inwall of the ring-shaped shell of cavity is also processed into the semicircle column type that the diameter placed side by side is Φ 8, and the axis direction of semicircle column type is parallel with the axis direction pulverizing post, plays the effect of pulverizing post.The rotating speed rotating grating disk is 3500 ~ 6500rad/min, this power rotated is provided by the 3rd kinetic control system, specifically provide movement instruction to motor by man-machine interface, motor is started working, drive transmission main shaft high-speed rotation, simultaneously, the rotation grating disk be arranged on transmission main shaft starts High Rotation Speed with same rotating speed, flow into the material of crushing chamber by all pulverizing posts, rotate grating disk, random turbulent motion is done in the confined space that fixing grating disk and cavity are formed, and constantly clashed into, friction, the effect of rubbing, there is provided certain kinetic energy that little cohesive force layer is relaxed gradually to material particles, can constantly separate through the lax little cohesive force constituting layer of material, and pulverized by continuation, reach technique object.Meanwhile, under the effect of the rotation grating disk of High Rotation Speed, inside cavity forms blast, drives material to flow out from discharging opening and enters Cyclonic separating apparatus 5000.
5, the crushing rear material of Cyclonic separating apparatus 5000 is entered, under the effect of the negative-pressure air power of high-pressure suction fan generation, in inflow cyclone separator, enter the material of cyclone separator, due under the effect of self gravity and wind-force, by also sedimentation downwards in the shape of a spiral, discharging opening through bottom flows out, the dust-like material that part proportion is less flows with wind-force, through filter cloth bag, be filtered, dust-like material will be stayed in cyclone separator, mix with material main body and sedimentation downwards, and wind is after filtering discharged through air-introduced machine.The effect of the closed processing of this pulsed Cyclonic separating apparatus had both reduced the possibility that product is subject to secondary pollution, and the leakage of minimizing material and impurity fly upward to greatest extent again, avoid environmental pollution.High negative pressure wind-force in process is produced by high-pressure suction fan, work order is sent by the 4th kinetic control system, its specific works instruction is given to id-motor by man-machine interface, id-motor brings into operation and the running of energizes high-pressure blower fan, thus produces the air quantity and the blast that meet technological requirement.Mixtures of materials through cyclone separator discharging opening enters temporary storing bin under self gravitation effect.The air quantity of high-pressure suction fan is 3500 ~ 6000m
3/ h, total head is 6000 ~ 16000Pa.
6, the second conveying worm 6000 mainly realizes the conveying of material, after material enters, under the conveying thrust of conveyor screw, by discharging opening, and flows into screening plant 7000.The movement velocity of conveyor screw determines the flow of material, this movement velocity is controlled by the 5th kinetic control system, 5th kinetic control system is the combination of a three phase electric machine and appliance controller, by man-machine interface to three phase electric machine with work order, realize the accurate control of mass flow, actual flow numerical value is determined by production throughput requirements and functions of the equipments.
7, material is flowed out by the discharging opening of the second conveying worm 6000, the ground floor of the compass screen surface of screening plant is entered through the charging aperture of three-D screening plant, screening function is by the 6th kinetic control system vibration motor, sieve nest, compass screen surface completes, the course of work sends work order to the 6th kinetic control system vibration motor by man-machine interface, vibration motor setting in motion, drive sieve nest moves, the setting in motion while that material being on compass screen surface, under own wt effect, varigrained particle is successively by the compass screen surface of different meshes, material not by corresponding order number sieve face flows out from respective discharging opening, enter respective storage silo, screening function completes.
The principle of the utility model said method is as follows:
Cohesive force and the adhesion at the different tissues position of plant part are different, sometimes also widely different.Such as, the pericarp of red date and pulp, the exosper of wheat bran and aleurone, two kinds of materials have the general character on structural capacity: the strong cohesive force of one deck and adhesion tissue, with long strand, the plant cellulose that between molecule, adhesion is very large, lignin is main composition material, its external manifestation is difficult to pulverize for using physical method, and the other weak cohesive force of one deck and adhesion tissue, with protein, the large molecule such as starch is main composition material, relative just much lower of adhesion between its molecule, its external manifestation just can make this cohesive force discharge for providing certain kinetic energy.Therefore, as long as to find on technique and equipment between these two biological structure layers at the discrepancy of cohesive force and Appropriate application, physical method just can be used to realize little cohesive force to organize disengaging to come, reach the object of high-purity, Selective Separation.
In the utility model, material medium and small cohesive force structure sheaf first clashes into and release portion cohesive force through radial direction in lax equipment, after at disintegrating apparatus through collide, rub, to rub and percussion continues to discharge cohesive force, reach and be separated and the object pulverized, and large cohesive force structure sheaf is not enough to the cohesive force of releasing structure layer inside due to kinetic energy that equipment provides, may there is portion fractures but can not be pulverized in material, so material will remain unchanged substantially.Like this, just achieve the goal of the invention of pure Physical Processing mode, selective molecular attraction, and confirm that the program is feasible by test.
In addition, apparatus and method for of the present utility model, may be used for all institutional framework character and be similar to plant material containing skin red date pulp particle, wheat bran, promote the use of in relevant industries, the performance of plant material, purity and utilization rate will be promoted greatly, thus promote industrial value and scientific and technological content, also there is extremely strong Economic Value Added effect.
Each technical characteristic of above-mentioned disclosure is not limited to that disclosed with combination that is further feature, other combination that those skilled in the art also can carry out between each technical characteristic according to the object of invention, is as the criterion with the object realizing the utility model.
Claims (8)
1. plant material selective molecular attraction and a separation equipment, is characterized in that, comprising:
Feed hopper, for holding pending material;
Lax equipment, the charging aperture of described lax equipment is connected by conveying worm with described feed hopper; Described lax equipment realizes the release of material particles inner tissue interlayer cohesive force;
Disintegrating apparatus, the charging aperture of described disintegrating apparatus is connected with the discharging opening of lax equipment; Described disintegrating apparatus realizes the separation of different cohesive force tissue in material particles, and less cohesive force tissue is pulverized after departing from disintegrating apparatus, and larger cohesive force is organized and substantially remained unchanged; Material after pulverizing is the fine powder component of granularity between 1.4 ~ 150 μm and the mixture of the meal component of granularity more than 150 μm;
Cyclonic separating apparatus, described Cyclonic separating apparatus is communicated with disintegrating apparatus discharging opening; Cyclone separator discharging opening is communicated with temporary storing bin;
Screening plant, above-mentioned material thickness powder mixture enters described screening plant from above-mentioned temporary storing bin discharging opening through conveying worm, is the product of different-grain diameter scope at described screening plant Inside sifter; And the product of different-grain diameter scope enters different storage silo respectively.
2. plant material selective molecular attraction according to claim 1 and separation equipment, is characterized in that, conveying worm comprises induction system and kinetic control system, and described kinetic control system controls and drives induction system to rotate.
3. plant material selective molecular attraction according to claim 1 and separation equipment, is characterized in that, described lax equipment comprises: lax equipment charging aperture, lax equipment discharging opening, lax equipment body, vibration rod and kinetic control system; Kinetic control system drives lax equipment body and vibration rod vibrations.
4. plant material selective molecular attraction according to claim 1 and separation equipment, is characterized in that, described disintegrating apparatus comprises pulverizes body and motor; Pulverize body to comprise cavity, fixing grating disk, rotate grating disk; Fixing grating disk and inside, cavity side are connected as a single entity, and rotate grating disk and are arranged in described cavity; Machine shaft is connected with rotation grating disk, drives and rotates grating disk operation.
5. plant material selective molecular attraction according to claim 4 and separation equipment, it is characterized in that, fixing grating disk and rotation grating disk are all circular, be respectively arranged with the pulverizing post vertical with card, the diameter pulverizing post is Φ 6 ~ 12, length 40 ~ 90mm, the pulverizing post that pulverizing post and the rotation of fixing grating disk are pulverized is crisscross arranged, and the gap between adjacent two pulverizing posts is 0.2 ~ 1.5mm.
6. plant material selective molecular attraction according to claim 4 and separation equipment, it is characterized in that, crusher cavity is oblate column, the inwall of cylinder is processed as the semicircle column type that the diameter be arranged in parallel is Φ 6 ~ 12, the axial line of semicolumn and the axis parallel pulverizing post, the gap that the most outer shroud rotating grating disk is pulverized between post and described semicolumn is 0.5 ~ 1.5mm.
7. plant material selective molecular attraction according to claim 1 and separation equipment, is characterized in that, described Cyclonic separating apparatus comprises cyclone separator and high-pressure suction fan, and high-pressure suction fan airduct is connected to the top of cyclone separator.
8. plant material selective molecular attraction according to claim 1 and separation equipment, is characterized in that, described screening plant comprises kinetic control system and three-D screening plant; Three-D screening plant is made up of sieve nest and compass screen surface; Compass screen surface tool haves three layers, and from top to bottom arranges successively.
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| CN201520546869.6U CN204891976U (en) | 2015-07-24 | 2015-07-24 | Plant material selectivity is smashed and splitter |
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| CN201520546869.6U CN204891976U (en) | 2015-07-24 | 2015-07-24 | Plant material selectivity is smashed and splitter |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105233922A (en) * | 2015-07-24 | 2016-01-13 | 连云港鼎康食品科技有限公司 | Plant material selective smashing and separating device and method |
-
2015
- 2015-07-24 CN CN201520546869.6U patent/CN204891976U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105233922A (en) * | 2015-07-24 | 2016-01-13 | 连云港鼎康食品科技有限公司 | Plant material selective smashing and separating device and method |
| CN105233922B (en) * | 2015-07-24 | 2017-11-10 | 连云港鼎康食品科技有限公司 | Plant material selective molecular attraction and separation equipment and method |
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Granted publication date: 20151223 Termination date: 20190724 |