CN104588401A - Forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method - Google Patents
Forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method Download PDFInfo
- Publication number
- CN104588401A CN104588401A CN201510025340.4A CN201510025340A CN104588401A CN 104588401 A CN104588401 A CN 104588401A CN 201510025340 A CN201510025340 A CN 201510025340A CN 104588401 A CN104588401 A CN 104588401A
- Authority
- CN
- China
- Prior art keywords
- agriculture
- cylinder
- organic waste
- separation
- forestry organic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 50
- 238000000926 separation method Methods 0.000 title claims abstract description 40
- 238000000354 decomposition reaction Methods 0.000 title claims abstract description 24
- 239000000463 material Substances 0.000 claims abstract description 173
- 230000008569 process Effects 0.000 claims abstract description 36
- 238000010438 heat treatment Methods 0.000 claims abstract description 30
- 239000007788 liquid Substances 0.000 claims abstract description 26
- 229920005610 lignin Polymers 0.000 claims abstract description 22
- 229920002678 cellulose Polymers 0.000 claims abstract description 21
- 239000001913 cellulose Substances 0.000 claims abstract description 21
- 239000007787 solid Substances 0.000 claims abstract description 16
- 229920002488 Hemicellulose Polymers 0.000 claims abstract description 15
- 150000001720 carbohydrates Chemical class 0.000 claims abstract description 7
- 235000014633 carbohydrates Nutrition 0.000 claims abstract description 7
- 239000010815 organic waste Substances 0.000 claims description 33
- 239000000203 mixture Substances 0.000 claims description 30
- 125000003003 spiro group Chemical group 0.000 claims description 21
- 230000007246 mechanism Effects 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 14
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 14
- 230000000694 effects Effects 0.000 claims description 12
- 238000013467 fragmentation Methods 0.000 claims description 10
- 238000006062 fragmentation reaction Methods 0.000 claims description 10
- 238000000527 sonication Methods 0.000 claims description 10
- 238000010298 pulverizing process Methods 0.000 claims description 8
- 230000009471 action Effects 0.000 claims description 7
- 238000005520 cutting process Methods 0.000 claims description 7
- 239000004744 fabric Substances 0.000 claims description 7
- 239000000835 fiber Substances 0.000 claims description 7
- 235000014655 lactic acid Nutrition 0.000 claims description 7
- 239000004310 lactic acid Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 238000009413 insulation Methods 0.000 claims description 6
- 239000007921 spray Substances 0.000 claims description 5
- 108090000790 Enzymes Proteins 0.000 claims description 4
- 102000004190 Enzymes Human genes 0.000 claims description 4
- 241000505673 Scintilla Species 0.000 claims description 4
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 4
- 239000003830 anthracite Substances 0.000 claims description 4
- 238000010009 beating Methods 0.000 claims description 4
- 239000003054 catalyst Substances 0.000 claims description 4
- 229940088598 enzyme Drugs 0.000 claims description 4
- 239000000945 filler Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- 239000000853 adhesive Substances 0.000 claims description 3
- 230000001070 adhesive effect Effects 0.000 claims description 3
- 230000009286 beneficial effect Effects 0.000 claims description 3
- 230000008859 change Effects 0.000 claims description 3
- 238000006477 desulfuration reaction Methods 0.000 claims description 3
- 230000023556 desulfurization Effects 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 229910052698 phosphorus Inorganic materials 0.000 claims description 3
- 229920000052 poly(p-xylylene) Polymers 0.000 claims description 3
- 239000002861 polymer material Substances 0.000 claims description 3
- 229910052700 potassium Inorganic materials 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000004449 solid propellant Substances 0.000 claims description 3
- 108010059892 Cellulase Proteins 0.000 claims description 2
- 229940106157 cellulase Drugs 0.000 claims description 2
- 238000001192 hot extrusion Methods 0.000 claims description 2
- 239000005416 organic matter Substances 0.000 abstract description 4
- 238000001125 extrusion Methods 0.000 abstract description 3
- 239000002028 Biomass Substances 0.000 abstract description 2
- 239000002737 fuel gas Substances 0.000 abstract 1
- 238000000197 pyrolysis Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 3
- 239000002689 soil Substances 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000002224 dissection Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 239000004484 Briquette Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 239000003627 allelochemical Substances 0.000 description 1
- 239000012491 analyte Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000000994 depressogenic effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000002362 mulch Substances 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000007781 pre-processing Methods 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 230000001007 puffing effect Effects 0.000 description 1
- 238000010223 real-time analysis Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000002525 ultrasonication Methods 0.000 description 1
- 238000009333 weeding Methods 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B16/00—Regeneration of cellulose
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01G—PRELIMINARY TREATMENT OF FIBRES, e.g. FOR SPINNING
- D01G11/00—Disintegrating fibre-containing articles to obtain fibres for re-use
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/66—Disintegrating fibre-containing textile articles to obtain fibres for re-use
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Textile Engineering (AREA)
- Biochemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method. The equipment comprises a primary material crushing device which is connected by a pipeline and is in a cylindrical structure, a material heating expanding tearing device, a material microwave crushing device and a material separation device, wherein the devices are used for carrying out crushing, hammering, ultrasonic crushing, cylindrical spiral high-temperature and high-pressure extrusion tearing and cylindrical spiral microwave pyrolysis processes, and a cylindrical spiral biological enzymolysis separation technical process is also realized; a plurality of spiral extruding conveying processes are carried out in one device so that decomposition and separation of forestry and agricultural organic matter components can be realized once; finally, decomposed high-concentration liquid carbohydrates and hemicellulose and solid cellulose and lignin are obtained; the high-concentration liquid carbohydrates and hemicellulose are used for efficiently preparing biomass fuel gas, and the solid cellulose and lignin are used for preparing a clean energy source material and a liquid mulching film by adopting a formula; and the efficient utilization of the organic matter components is realized.
Description
Technical field
The invention belongs to agriculture and forestry organic waste material processing technology field, particularly a kind of agriculture and forestry organic waste material skid modular composition decomposition and separation equipment and method.
Background technology
A large amount of stalk etc. can be produced in agricultural production process and need agriculture and forestry organic waste material to be processed, along with the aggravation of energy crisis, biological flue gas highlights day by day at the great potential in the energy and refuse process two fields, existing Land use systems mainly contains following several, but all there is corresponding drawback: agriculture and forestry organic waste material is used for household biogas and large-sized biogas, raw material usually cannot by abundant efficiency utilization, natural pond liquid is mishandling flows to farmland in a large number, form pollution of area source, flow into the hidden danger that rivers and lakes become body eutrophication; Straw-returning, pathogen not only may be made to exist but also stalk itself cannot decompose rapidly, material accumulates in underground for a long time, the methane isothermal chamber gas produced in putrefaction process cannot be collected and directly enter air, cause atmosphere pollution on a large scale, and the cellulosic organic matter can not disposed in time in soil and some allelochemicals that lower first phase also can be caused to plant is influenced, as the winter wheat conservation phase needs closely knit soil environment and straw-returning makes soil aperture increase, affect Wheat Development; Stalk briquette, although the rural energy clean utilization mode being country advocates, but makes cost ratio fire coal per ton exceed about 300 yuan due to high processing cost, makes it be difficult to promote in rural area.
The important step that govern the existing utilization obstacle of agriculture and forestry organic waste material is just front end preprocessing process, if the maximum decomposition and separation of various compositions of all kinds of downstream product production can will be used in agriculture and forestry organic waste material in the process, make the lignin in plant, cellulose, hemicellulose soluble in water separately and be used respectively, to replace the processing mode of this " lumping together " at present, to make to make the best use of everything, just the problem run in current agriculture and forestry organic waste material process can be solved.And at present diversification agriculture and forestry organic waste material is difficult to accomplish that efficient composition decomposes in common process, let alone efficiency utilization, while can the treatment process of Efficient Conversion and equipment high because of operation cost, cannot agriculturally be widely used again.
Therefore, the organic composition in agriculture and forestry organic waste material how is realized to decompose completely, tremendous breakthrough will be played for diversification agriculture and forestry organic waste material high-efficiency comprehensive utilization, be conducive to agricultural wastes resource complete utilization in the world, even substitute petroleum chemicals, to reduce utilization to oil non-renewable resources, help minimizing that state leader realizes making the whole world in the APC session to the promise of the dependence of fossil energy.
Summary of the invention
The present invention for solve in known technology the technical problem that exists and provide a kind of and can realize that composition in agriculture and forestry organic waste material decomposes, the agriculture and forestry organic waste material skid modular composition decomposition and separation equipment that is separated and agriculture and forestry organic waste material composition decomposition method.
The technical scheme that the present invention takes for the technical problem existed in solution known technology is:
A kind of agriculture and forestry organic waste material skid modular composition decomposition and separation equipment, the material primary breakup device, the expanded tear device of heating material, material broken microwave device and the material separation device that comprise control panel and linked together by pipeline,
Described material primary breakup device comprises " L " shape cylinder, its vertical cylinder lateral wall is provided with radial feed hopper, vertical inner barrel is provided with disintegrating mechanism, inclination flitch is provided with below described disintegrating mechanism, Hammer is provided with in the terminal horizontal cylindrical shell of described inclination flitch, the horizontal barrel at described Hammer place is provided with the baffle plate vertical with barrel, be provided with material flow between the lower end of described baffle plate and barrel to export, this flow export place is communicated with sonication chamber inwall being provided with ultrasonic generator by screen cloth, the feeding spiro rod A be connected with reductor is provided with in described sonication chamber,
The expanded tear device of described heating material comprises " one " font cylinder be made up of the heat-insulation layer set gradually from outside to inside, high temperature heating tape and explosion-proof layer, is provided with safety explosion-proof valve and feeding spiro rod B in this cylinder in arranging;
Described material broken microwave device comprises " one " font broken microwave cylinder, and this barrel outer wall is provided with one deck microwave application of anti-leakage layers, and this inwall is provided with multiple magnetron, is also provided with feeding spiro rod C in this cylinder;
Described material separation device comprises " one " font cylinder, this barrel is provided with filler and catalyst interpolation mouth, is provided with extruding screw, this barrel is also provided with liquid outlet and discharging opening in this cylinder.
Described disintegrating mechanism comprises the ridge that reductor, rotating shaft, a 3-5 set of blades and vertical cylinder inboard wall are arranged, described set of blades is axially arranged along rotating shaft, the inclined wheel hammer leaf that each set of blades is fixed by the mooching knife be connected in rotating shaft and blade end single-point forms, in described multiple set of blades, the length of each set of blades is equal, and path length 1mm in being formed than ridge inner face.
Described set of blades is set to three, and wherein the length of blade shortens from top to bottom successively, and the length of wheel hammer leaf is elongated successively from top to bottom partially.
Described Hammer comprises a line shaft, described line shaft is vertical with disintegrating machine rotating shaft antarafacial, described line shaft is provided with an eccentric hammer, described eccentric hammer outer surface is provided with the double wedge of " recessed " character form structure, described horizontal cylinder inwall with baffle plate is provided with consistent with eccentric hammer outer surface double wedge shape and be not engaged each other " recessed " font double wedge.
Described supersonic generator is arranged on the barrel of screw rod transmission section, in material advance process, carry out ultrasonication simultaneously.
Described broken microwave pipeline and other parts different, overall make for nonmetal structure, on barrel, device has magnetron, and cylinder device anti-microwave leakage layer outward.
Described extruding is torn in cylinder and is provided with safety explosion-proof valve, and pressure exceedes setting value, and safety valve opens released vapour automatically.
The pitch numerical value of described extruding screw is unequal, and each pitch presses arithmetic series rule gradual change arrangement.
One section of guiding gutter is provided with at extruding screw back segment tight pitch place along the every 50cm in spiro rod length direction bottom " one " font cylinder of described material separation device, the middle part of described guiding gutter is provided with the tank deepened that broadens gradually from front to back, and the end of described tank arranges a liquid outlet.
A kind of agriculture and forestry organic waste material composition decomposition and separation method, comprises the steps:
1) material primary breakup process, enter pulverizing chamber through simple material radial direction of cutting to be pulverized by disintegrating mechanism, this crushing process is completed jointly by the ridge in set of blades and vertical cylinder inboard wall, then the material sinking inclined-plane arrived bottom pulverizing chamber enters and beats room, complete the further fragmentation of material, material is constantly by beating, extruding, fragmentation diminishes, then exit baffle plate is poured into, screen cloth, until be less than screen size just discharge hammering room, enter sonication chamber, ultrasonic vibration makes material fine structure loosen, also make material send to discharging opening by screw conveyer simultaneously, then screw in the expanded tear device of heating material,
2) heating material is expanded tears process, and the material through primary breakup is heated by Variable pitch screw extruding, rubbing action and high temperature heating tape, and in system, temperature constantly rises, pressure constantly raises, and volume of material is constantly compressed, and is screwing out the moment of pulp cutlet with screw rod, because pressure is die-offed, material instantaneous expansion, its fine structure is torn, in pressure process, when pressure exceedes preset value, safety explosion-proof valve is opened, and steam sprays, and ensures security of operation.
3) material broken microwave process, through adding the material that hot extrusion is torn, screw in microwave pipe-line, microwave is accelerated molecular motion and is destroyed further material micro-structural, and the scintilla of material fiber is destructurized, and then material screws in material separation device;
4) material composition separation process, under the effect at water of the material of broken microwave, make decomposed hemicellulose in material water-soluble and be separated with cellulose with lignin, add as required cellulase then cellulose be decomposed under the effect of biology enzyme and be beneficial to lactic acid fermented short-chain carbohydrates and stripping, realization is separated with solid lignin, solid lignin enters solid collection device from the discharging opening of end under the promotion of screw rod, and cellulose and water-soluble hemicellulose are from liquid outlet influent gathering-device.
Described solid lignin mixes with a certain proportion of high heat adhesive adhesion-molded after desulfurization removing nitric denitration with high-quality anthracite powder, or need dry to be directly compressed into block according to calorific value, form the renewable solid fuel of high heating value, pollution-free, low cost.
Described cellulose can be used for the manufacture raw material of lactic acid.
For the preparation of degradable liquid agricultural film after described cellulose, lignin mix with water-soluble Green Polymer Material, in described liquid agricultural film, N, P, K element can be added.
The advantage that the present invention has and good effect are: the present invention is by shattering diversification agriculture and forestry organic waste material and beating, by tubular screw extrusion and method for releasing, high-temperature high-pressure swelling tearing technology, microwave-heating principle, the technical process such as biological enzymolysis, in particular, diversification agriculture and forestry organic waste material is (breaking method that siccative is different with fresh material) after machinery is tentatively pulverized, technique is torn through tubular spiral high-temperature high-pressure swelling, tubular spiral microwave-heating technique, the processes such as biological enzymolysis, dexterously by N group tubular screw extrusion carrying method in a device, realize the decomposition and separation of agricultural organic matter fraction once, final carbohydrate and the hemicellulose obtaining the high concentration liquid after decomposing, the cellulose of solid and lignin.The carbohydrate of high concentration liquid and hemicellulose can be used for preparing biogas and lactic acid, the cellulose of solid and lignin can prepare clean energy resource material and liquid ground film and (this mulch film possesses weeding, Slow release organic fertilizer effect) through formula, achieve the efficiency utilization to each organic composition of agriculture and forestry organic waste material.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 is guiding gutter distributed architecture schematic diagram bottom " one " font cylinder.
In Fig. 1 and Fig. 2, 1. " L " shape cylinder, 2. ridge, 3. set of blades, 4. feed hopper, 5. Hammer, 6. " recessed " font double wedge, 7. eccentric hammer, 8. baffle plate, 9. heat-insulation layer, 10. high temperature heating tape, 11. explosion-proof layers, 12. screen clothes, 13. feeding spiro rod A, 14. ultrasonators, 15. feeding spiro rod B, 16. feeding spiro rod C, 17. microwave application of anti-leakage layers, 18. magnetrons, 19. guiding gutters, 20. catalyst add mouth, 21. filler, 22. liquid outlets, 23. liquid headers, 24. discharging openings, 25. solid collectors, 26. water tanks, 27. control panels, 28. inclination flitch, 29. " one " font cylinders, 30. extruding screws.
Detailed description of the invention:
For summary of the invention of the present invention, Characteristic can be understood further, hereby exemplify following examples, and coordinate accompanying drawing to be described in detail as follows:
A kind of agriculture and forestry organic waste material skid modular composition decomposition and separation equipment, the material primary breakup device, the expanded tear device of heating material, material broken microwave device and the material separation device that comprise control panel 27 and linked together by pipeline,
Material primary breakup device comprises " L " shape cylinder 1, the sidewall upper of vertical cylinder is provided with radial feed hopper 4, material enters disintegrating mechanism under the pressure effect of manpower or feeding mechanism, to ensure that surplus material also can charging smoothly, its vertical inner barrel is provided with disintegrating mechanism, this disintegrating mechanism comprises the servomotor being arranged at vertical cartridge inlet place, servomotor is connected with the rotating shaft be arranged in vertical cylindrical shell, rotating shaft is perpendicular to the ground, axially 3-5 set of blades 3 is provided with along rotating shaft, the inclined wheel hammer leaf that each set of blades 3 is fixed by the mooching knife be connected in rotating shaft and blade end single-point forms, blade in first set of blades 3 is cutting main body, inclined wheel hammer leaf knocks material, because it is based on the dissection to the surplus material just entered, it is auxiliary for knocking, therefore the mooching knife of first set of blades 3 is longer, inclined wheel hammer leaf is shorter, and the cutting of second set of blades is laid equal stress on knocking, therefore the mooching knife of two set of blades is slightly shorter than the mooching knife of group, and wheel hammer leaf is slightly long partially, the mooching knife of the 3rd set of blades is mainly to beat, and wheel hammer leaf is then the longest in three groups partially, and mooching knife is then the shortest, mooching knife is trapezoidal on the whole, and partially take turns hammer leaf and become inverted trapezoidal, but when three set of blades stretch, total length is equal, and path length 1mm in being formed than ridge 2 inner face.Ridge 2 is connected with screw with vertical barrel, and screw is depressed in the inner face of ridge 2, agrees with outside ridge with barrel, and inner face is a plane.
The crushing process of disintegrating mechanism is, jointly completed to shear by the set of blades 3 in rotating shaft and the ridge 2 on vertical barrel and pulverize, special insert design is when set of blades High Rotation Speed, inclined wheel hammer leaf and ridge 2 collide, not only auxiliary blade can smash outer rim material but also blade can be avoided and pulverize material between locular wall stagnating, the material entered drops to blade action plane, wedge shape swivel starts to cut to cutting position, when the fiber cut off because centrifugal force flies away from outside mooching knife sphere of action, can with partially take turns hammer leaf and collide, along with the material that carries out of working angles exists mainly with short fiber form, dissection weakens, material is now also because Action of Gravity Field sinks from upper group of set of blades to middle bottom knife group, the effect of beaing starts remarkable gradually, eventually pass this cutting and beat common crushing process, material sinks to arriving bottom pulverizing chamber by Action of Gravity Field, bottom is an inclination flitch 28, inclination flitch 28 is tilted to and is positioned at bottom, with the discharging opening of charging aperture opposite flank, material after pulverizing and knocking is done to skid off discharging opening along inclination flitch 28 by pushing,
Hammer 5 is provided with in the terminal horizontal cylindrical shell of inclination flitch 28, the horizontal barrel at Hammer 5 place is provided with the baffle plate 8 vertical with barrel, be provided with material flow between the lower end of baffle plate 8 and barrel to export, this flow export place is communicated with sonication chamber inwall being provided with ultrasonic generator 14 by screen cloth 12, the feeding spiro rod A13 be connected with reductor is provided with in sonication chamber, the line shaft of Hammer 5 is vertical with disintegrating machine rotating shaft antarafacial, line shaft is provided with an eccentric hammer 7, eccentric hammer 7 outer surface is provided with " recessed " font double wedge 6, horizontal cylinder inwall with baffle plate is provided with consistent with eccentric hammer outer surface double wedge shape and be not engaged each other " recessed " font double wedge 6.Hammering process completes the further fragmentation of material by impact energy, under the drive of motor, eccentric hammer 7 is rotated counterclockwise, the friction that the material evenly entered constantly is subject to tup hammering and shaggy tooth is chewed, the continuous fragmentation of material diminishes, rely on centrifugal action, pour into exit baffle plate 28 and screen cloth 12, until be less than screen size be just discharged hammering room, enter sonication chamber, ultrasonic generator 14 produces ultrasonic vibration makes material fine structure loosen, also transmitted by feeding spiro rod A simultaneously, the direction of feeding spiro rod A is vertical with disintegrating mechanism rotating shaft coplanar, the reductor be connected with feeding spiro rod A is positioned at transmission shaft terminal, material is made to send to the discharging opening of this horizontal cylinder end, material screws in the expanded tear device of heating material.
The expanded tear device of heating material comprises the expanded broken cylinder of " one " font, this barrel sets gradually heat-insulation layer 9 from outside to inside, high temperature heating tape 10 and explosion-proof layer 11, heat-insulation layer 9 is that ceramic wool insulation is cotton, feeding spiro rod B15 is provided with in this cylinder, feeding spiro rod B15 is that combined variable is apart from turbine screw rod, feeding spiro rod B15 is connected with reductor, material to enter after this cylinder by high temperature heating tape 10 to heating material, barrel is provided with safety explosion-proof valve, when the fault such as there is blocking in reductor, material can by long-time heating, reactor pressure increases to a certain degree, safety explosion-proof valve can be opened, material steam sprays, material is in extruding in the process, tear, friction, under shearing the effect of grade, its internal pressure constantly raises, temperature constantly rises, its institutional framework changes, the scintilla structural deterioration of fiber.One " relevant position of the expanded broken cylinder of font is provided with the device such as temperature sensor, pressure transmitter, and can accurately control material treatment temperature, pressure detecting etc., material is after treatment discharged by automatic pressure-relief port, sprays in material broken microwave device.
Material broken microwave device comprises " one " font broken microwave cylinder, this material is match steel, this barrel outer wall is provided with one deck microwave application of anti-leakage layers 17, this inwall is provided with multiple magnetron 18, is also provided with the feeding spiro rod C16 that reducing motor connects in this.The microwave that magnetron 18 produces accelerates the molecular motion of material, material micro-structural is destroyed further, in material comprise lignin, fiber Xu, hemicellulose key component be easy to be separated, material screws in material separation device under the effect of feeding spiro rod C16.
Material separation device comprises " one " font cylinder 29, this barrel is provided with filler 21 and catalyst interpolation mouth 20, extruding screw 30 is provided with in this cylinder, reductor is connected with extruding screw 30, extruding screw 30 is combined type turbine screw rod, pitch numerical value is unequal, each pitch presses arithmetic series rule gradual change arrangement, the leading portion pitch of screw rod 30 is loose, be mainly used in adding water, biology enzyme process fully mixes material, back segment pitch is tight, mainly material is extruded, realize the Separation of Solid and Liquid of lignocellulosic and cellulose and hemicellulose, one section of guiding gutter is provided with at extruding screw back segment tight pitch place along the every 50cm in spiro rod length direction bottom this barrel, the middle part of guiding gutter is provided with the tank deepened that broadens gradually from front to back, the end of tank arranges a liquid outlet 22, liquid is by liquid outlet 22 influent collector 23, dry lignocellulosic is wound around screw rod and continues on to discharging opening 24, discharging opening 24 is arranged at the tight pitch end of extruding screw 30 back segment, discharge lignocellulosic in solid collector or screw in next link.
Therefore, material can being separated hemicellulose and the realization soluble in water of other lyotropes and lignin after material separation device process, and different according to material variety, material separation device can be set to one or more groups.In addition, in above-mentioned four processing links, corresponding site installs relevant parameter checkout gear, and detect relevant parameter according to processing requirements, real-time analysis treatment state, compares optimization.
A kind of agriculture and forestry organic waste material composition decomposition and separation method, comprises the steps:
1) material primary breakup process, enter pulverizing chamber through simple material radial direction of cutting to be pulverized by disintegrating mechanism, this crushing process is completed jointly by the ridge in set of blades and vertical cylinder inboard wall, then the material sinking inclined-plane arrived bottom pulverizing chamber enters and beats room, complete the further fragmentation of material, material is constantly by beating, extruding, fragmentation diminishes, then exit baffle plate is poured into, screen cloth, until be less than screen size just discharge hammering room, enter sonication chamber, ultrasonic vibration makes material fine structure loosen, also make material send to discharging opening by screw conveyer simultaneously, then screw in the expanded tear device of heating material,
2) the expanded shattering process of heating material, the material through primary breakup is heated by high temperature heating tape, and pressure increase is to a certain extent, safety explosion-proof valve is opened, material steam sprays, and further by expanded for material fragmentation, is then discharged by automatic pressure-relief port and enters in material broken microwave device;
3) material broken microwave process, through the material of heating while puffing fragmentation by screw extruding, tear, rub, shear, its internal pressure constantly raises, temperature constantly rises, microwave is accelerated molecular motion and is destroyed further material micro-structural, the scintilla of material fiber is destructurized, and then material screws in material separation device;
4) material composition separation process, under the effect of the material water of broken microwave, make the hemicellulose that contains in material water-soluble and be separated with cellulose with lignin, cellulose is decomposed into and is beneficial to lactic acid fermented short-chain carbohydrates and stripping under the effect of biology enzyme, realization is separated with lignin, lignin enters solid collection device from the discharging opening of end under the promotion of screw rod, and cellulose and water-soluble hemicellulose are from liquid outlet influent gathering-device.
Lignin mixes with high-quality anthracite powder or direct briquetting after desulfurization removing nitric denitration, mix with a small amount of high-quality anthracite powder, adhesion-molded with a certain proportion of high heat adhesive, or need dry to be directly compressed into block according to calorific value, form the renewable solid fuel of high heating value, pollution-free, low cost.
Cellulose can be used for the manufacture raw material of lactic acid.
For the preparation of degradable liquid agricultural film after cellulose, lignin mix with water-soluble Green Polymer Material, in described liquid agricultural film, N, P, K element can be added.
Isolated hemicellulose analyte can be used as high gravity fermentation matrix and produces biogas.
The present invention once can complete stalk agriculture and forestry organic waste material and be converted into the process in early stage and process of producing the product such as industrial chemicals, biomass energy precursor, realize the decomposition and separation of the organic each component of agricultural, make diversification agriculture and forestry organic waste material be able to easy, efficiently, directly utilize.
Above embodiment is only in order to illustrate that technical scheme of the present invention is not intended to limit, and those of ordinary skill in the field should be appreciated that and still can modify to the detailed description of the invention of invention or portion of techniques feature be carried out to equivalent replacement; And not departing from the spirit of technical solution of the present invention, it all should be encompassed in the technology of request of the present invention protection.
Claims (10)
1. an agriculture and forestry organic waste material skid modular composition decomposition and separation equipment, is characterized in that, the material primary breakup device, the expanded tear device of heating material, material broken microwave device and the material separation device that comprise control panel and linked together by pipeline,
Described material primary breakup device comprises " L " shape cylinder, its vertical cylinder lateral wall is provided with radial feed hopper, vertical inner barrel is provided with disintegrating mechanism, inclination flitch is provided with below described disintegrating mechanism, Hammer is provided with in the terminal horizontal cylindrical shell of described inclination flitch, the horizontal barrel at described Hammer place is provided with the baffle plate vertical with barrel, be provided with material flow between the lower end of described baffle plate and barrel to export, this flow export place is communicated with sonication chamber inwall being provided with ultrasonic generator by screen cloth, the feeding spiro rod A be connected with reductor is provided with in described sonication chamber,
The expanded tear device of described heating material comprises " one " font cylinder be made up of the heat-insulation layer set gradually from outside to inside, high temperature heating tape and explosion-proof layer, is provided with safety explosion-proof valve and feeding spiro rod B in this cylinder in arranging;
Described material broken microwave device comprises " one " font broken microwave cylinder, and this barrel outer wall is provided with one deck microwave application of anti-leakage layers, and this inwall is provided with multiple magnetron, is also provided with feeding spiro rod C in this cylinder;
Described material separation device comprises " one " font cylinder, this barrel is provided with filler and catalyst interpolation mouth, is provided with extruding screw, this barrel is also provided with liquid outlet and discharging opening in this cylinder.
2. agriculture and forestry organic waste material skid modular composition decomposition and separation equipment according to claim 1, it is characterized in that, described disintegrating mechanism comprises the ridge that reductor, rotating shaft, a 3-5 set of blades and vertical cylinder inboard wall are arranged, described set of blades is axially arranged along rotating shaft, the inclined wheel hammer leaf that each set of blades is fixed by the mooching knife be connected in rotating shaft and blade end single-point forms, in described multiple set of blades, the length of each set of blades is equal, and path length 1mm in being formed than ridge inner face.
3. agriculture and forestry organic waste material skid modular composition decomposition and separation equipment according to claim 2, it is characterized in that, described set of blades is set to three, and wherein the length of blade shortens from top to bottom successively, and the length of wheel hammer leaf is elongated successively from top to bottom partially.
4. agriculture and forestry organic waste material skid modular composition decomposition and separation equipment according to claim 1, it is characterized in that, described Hammer comprises a line shaft, described line shaft is vertical with disintegrating machine rotating shaft antarafacial, described line shaft is provided with an eccentric hammer, described eccentric hammer outer surface is provided with the double wedge of " recessed " character form structure, described horizontal cylinder inwall with baffle plate is provided with consistent with eccentric hammer outer surface double wedge shape and be not engaged each other " recessed " font double wedge.
5. agriculture and forestry organic waste material skid modular composition decomposition and separation equipment according to claim 1, it is characterized in that, the pitch numerical value of described extruding screw is unequal, and each pitch presses arithmetic series rule gradual change arrangement.
6. agriculture and forestry organic waste material skid modular composition decomposition and separation equipment according to claim 1, it is characterized in that, one section of guiding gutter is provided with at extruding screw back segment tight pitch place along the every 50cm in spiro rod length direction bottom " one " font cylinder of described material separation device, the middle part of described guiding gutter is provided with the tank deepened that broadens gradually from front to back, and the end of described tank arranges a liquid outlet.
7. an agriculture and forestry organic waste material composition decomposition and separation method for device according to claim 1, is characterized in that, comprise the steps:
1) material primary breakup process, enter pulverizing chamber through simple material radial direction of cutting to be pulverized by disintegrating mechanism, this crushing process is completed jointly by the ridge in set of blades and vertical cylinder inboard wall, then the material sinking inclined-plane arrived bottom pulverizing chamber enters and beats room, complete the further fragmentation of material, material is constantly by beating, extruding, fragmentation diminishes, then exit baffle plate is poured into, screen cloth, until be less than screen size just discharge hammering room, enter sonication chamber, ultrasonic vibration makes material fine structure loosen, also make material send to discharging opening by screw conveyer simultaneously, then screw in the expanded tear device of heating material,
2) heating material is expanded tears process, and the material through primary breakup is heated by Variable pitch screw extruding, rubbing action and high temperature heating tape, and in system, temperature constantly rises, pressure constantly raises, and volume of material is constantly compressed, and is screwing out the moment of pulp cutlet with screw rod, because pressure is die-offed, material instantaneous expansion, its fine structure is torn, in pressure process, when pressure exceedes preset value, safety explosion-proof valve is opened, and steam sprays, and ensures security of operation.
3) material broken microwave process, through adding the material that hot extrusion is torn, screw in microwave pipe-line, microwave is accelerated molecular motion and is destroyed further material micro-structural, and the scintilla of material fiber is destructurized, and then material screws in material separation device;
4) material composition separation process, under the effect at water of the material of broken microwave, make decomposed hemicellulose in material water-soluble and be separated with cellulose with lignin, add as required cellulase then cellulose be decomposed under the effect of biology enzyme and be beneficial to lactic acid fermented short-chain carbohydrates and stripping, realization is separated with solid lignin, solid lignin enters solid collection device from the discharging opening of end under the promotion of screw rod, and cellulose and water-soluble hemicellulose are from liquid outlet influent gathering-device.
8. agriculture and forestry organic waste material composition decomposition method according to claim 7, it is characterized in that, described solid lignin mixes with a certain proportion of high heat adhesive adhesion-molded after desulfurization removing nitric denitration with high-quality anthracite powder, or need dry to be directly compressed into block according to calorific value, form the renewable solid fuel of high heating value, pollution-free, low cost.
9. agriculture and forestry organic waste material composition decomposition method according to claim 7, is characterized in that, described cellulose can be used for the manufacture raw material of lactic acid.
10. agriculture and forestry organic waste material composition decomposition method according to claim 7, it is characterized in that, for the preparation of degradable liquid agricultural film after described cellulose, lignin mix with water-soluble Green Polymer Material, in described liquid agricultural film, N, P, K element can be added.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510025340.4A CN104588401A (en) | 2015-01-19 | 2015-01-19 | Forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method |
CN201510359550.7A CN104959362B (en) | 2015-01-19 | 2015-06-25 | A kind of skid module formula plant component decomposes enriching apparatus and method |
PCT/CN2015/082505 WO2016206096A1 (en) | 2015-01-19 | 2015-06-26 | Modular skid mounted equipment for degradation and concentration of plant material and method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510025340.4A CN104588401A (en) | 2015-01-19 | 2015-01-19 | Forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN104588401A true CN104588401A (en) | 2015-05-06 |
Family
ID=53114652
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510025340.4A Pending CN104588401A (en) | 2015-01-19 | 2015-01-19 | Forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method |
CN201510359550.7A Active CN104959362B (en) | 2015-01-19 | 2015-06-25 | A kind of skid module formula plant component decomposes enriching apparatus and method |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510359550.7A Active CN104959362B (en) | 2015-01-19 | 2015-06-25 | A kind of skid module formula plant component decomposes enriching apparatus and method |
Country Status (2)
Country | Link |
---|---|
CN (2) | CN104588401A (en) |
WO (1) | WO2016206096A1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104959362A (en) * | 2015-01-19 | 2015-10-07 | 天津市天人世纪科技有限公司 | Skid-mounted module type plant component decomposing and gathering device and method |
CN105170289A (en) * | 2015-10-20 | 2015-12-23 | 富阳鸿祥技术服务有限公司 | Integrated crushing disposal method of industrial timber wastes |
CN110886122A (en) * | 2019-11-19 | 2020-03-17 | 湖南工业大学 | Plant fiber cellulose purification device |
CN112108217A (en) * | 2020-08-25 | 2020-12-22 | 赵虎珍 | Anti-blocking crushing equipment |
CN112588381A (en) * | 2020-12-23 | 2021-04-02 | 李云飞 | But feed grinder based on spiral transmission regrinding |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112568423A (en) * | 2020-12-10 | 2021-03-30 | 黑龙江省冠辰投资管理有限公司 | Preparation method of modified crystal corn degermed pearl powder |
CN114832746A (en) * | 2022-04-06 | 2022-08-02 | 贾关荣 | High-pressure batch autoclave is prevented to regulation and control formula |
CN115140564B (en) * | 2022-05-13 | 2024-06-18 | 南京杰亚挤出装备有限公司 | Continuous production line for separating polyester cotton by alcoholysis method |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3802325B2 (en) * | 2000-08-23 | 2006-07-26 | 信行 林 | Pressurized hydrothermal decomposition method and system for plant biomass |
JP2009091599A (en) * | 2007-10-04 | 2009-04-30 | Daitoku:Kk | Method for recovering rare metals contained in transparent electrode |
CN201613130U (en) * | 2010-01-18 | 2010-10-27 | 江苏金太阳油脂有限责任公司 | Ultrasonic hydrolysis reactor |
CN104584959B (en) * | 2015-01-19 | 2017-01-18 | 天津市天人世纪科技有限公司 | Method for producing liquid agricultural film by using forestry and agricultural residues |
CN104588181B (en) * | 2015-01-19 | 2017-02-01 | 天津市天人世纪科技有限公司 | Primary crushing device for decomposing components of forestry and agricultural residues |
CN104673846B (en) * | 2015-01-19 | 2019-02-22 | 天津市天人世纪科技有限公司 | A method of lactic acid is produced using agriculture and forestry organic waste material |
CN104588401A (en) * | 2015-01-19 | 2015-05-06 | 天津市天人世纪科技有限公司 | Forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method |
CN104611084B (en) * | 2015-01-19 | 2016-11-02 | 天津市天人世纪科技有限公司 | A kind of method utilizing agriculture and forestry organic waste material to produce clean energy resource material |
-
2015
- 2015-01-19 CN CN201510025340.4A patent/CN104588401A/en active Pending
- 2015-06-25 CN CN201510359550.7A patent/CN104959362B/en active Active
- 2015-06-26 WO PCT/CN2015/082505 patent/WO2016206096A1/en active Application Filing
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104959362A (en) * | 2015-01-19 | 2015-10-07 | 天津市天人世纪科技有限公司 | Skid-mounted module type plant component decomposing and gathering device and method |
WO2016206096A1 (en) * | 2015-01-19 | 2016-12-29 | 崔勇 | Modular skid mounted equipment for degradation and concentration of plant material and method thereof |
CN105170289A (en) * | 2015-10-20 | 2015-12-23 | 富阳鸿祥技术服务有限公司 | Integrated crushing disposal method of industrial timber wastes |
CN105170289B (en) * | 2015-10-20 | 2017-06-09 | 涂瑞强 | A kind of integrated form break process method of industrial wood rubbish |
CN110886122A (en) * | 2019-11-19 | 2020-03-17 | 湖南工业大学 | Plant fiber cellulose purification device |
CN112108217A (en) * | 2020-08-25 | 2020-12-22 | 赵虎珍 | Anti-blocking crushing equipment |
CN112588381A (en) * | 2020-12-23 | 2021-04-02 | 李云飞 | But feed grinder based on spiral transmission regrinding |
CN112588381B (en) * | 2020-12-23 | 2022-05-03 | 常德湘大骆驼饲料有限公司 | But feed grinder based on spiral transmission regrinding |
Also Published As
Publication number | Publication date |
---|---|
CN104959362A (en) | 2015-10-07 |
CN104959362B (en) | 2017-10-10 |
WO2016206096A1 (en) | 2016-12-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104588401A (en) | Forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method | |
CN104611084B (en) | A kind of method utilizing agriculture and forestry organic waste material to produce clean energy resource material | |
Ma et al. | Enhanced biomethane production from corn straw by a novel anaerobic digestion strategy with mechanochemical pretreatment | |
CN103480627A (en) | Novel recycling comprehensive utilization technology for agricultural and forestry waste | |
CN100506812C (en) | Method for producing furol by extruding plant stalk | |
CN106047680A (en) | System for preparing biogas by utilizing straw | |
CN108913259B (en) | Multi-effect utilization and manufacturing method of straw biomass fuel | |
CN101775412A (en) | Method for preparing biogas by using lignocellulose | |
CN106906126A (en) | A kind of discarded fruits and vegetables anaerobic digestion and the system and method for marsh gas purifying purification | |
CN101497893A (en) | Pure stalk fermentation biogas preparation process and apparatus based on composite strain degradation | |
CN204564733U (en) | Agriculture and forestry organic waste material skid modular composition decomposition and separation equipment | |
CN104584959A (en) | Method for producing liquid agricultural film by using forestry and agricultural residues | |
CN101314551B (en) | Apparatus and method for producing sludge gas with organic castoff | |
CN102212582A (en) | Method for preparing cellulose from straws by using biological method | |
CN101805777A (en) | Poly-generation method for steam-exploded primary refining of dioscorea raw materials | |
CN102321674B (en) | Two-phase reaction method for raising efficiency of energy grass to prepare bio-gas | |
CN203212923U (en) | Cellulosic biomass ethanol horizontal tube continuous digester steam explosion device | |
CN104673846A (en) | Method for producing lactic acid by using forestry and agricultural residues | |
CN206916131U (en) | A kind of discarded fruits and vegetables anaerobic digestion and the system of marsh gas purifying purification | |
CN204661714U (en) | The stalk with efficient straw preprocessing function produces Methane Resources system | |
CN204661711U (en) | Stalk produces biogas facility | |
CN103131498B (en) | Hot compression plasticizing molding straw carbon and manufacturing method thereof | |
CN205152227U (en) | Broken shell mould straw biogas fermentation device of machinery | |
CN103266135B (en) | Integrated utilization method of banana stalk | |
CN207276622U (en) | A kind of biogas electricity generation apparatus |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C05 | Deemed withdrawal (patent law before 1993) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20150506 |