CN106258252B - A kind of biomass straw crushes briquetting all-in-one machine and its method of work - Google Patents
A kind of biomass straw crushes briquetting all-in-one machine and its method of work Download PDFInfo
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- CN106258252B CN106258252B CN201610666704.1A CN201610666704A CN106258252B CN 106258252 B CN106258252 B CN 106258252B CN 201610666704 A CN201610666704 A CN 201610666704A CN 106258252 B CN106258252 B CN 106258252B
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Classifications
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- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01F—PROCESSING OF HARVESTED PRODUCE; HAY OR STRAW PRESSES; DEVICES FOR STORING AGRICULTURAL OR HORTICULTURAL PRODUCE
- A01F29/00—Cutting apparatus specially adapted for cutting hay, straw or the like
- A01F29/02—Cutting apparatus specially adapted for cutting hay, straw or the like having rotating knives with their cutting edges in a plane perpendicular to their rotational axis
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- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01F—PROCESSING OF HARVESTED PRODUCE; HAY OR STRAW PRESSES; DEVICES FOR STORING AGRICULTURAL OR HORTICULTURAL PRODUCE
- A01F29/00—Cutting apparatus specially adapted for cutting hay, straw or the like
- A01F29/09—Details
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01F—PROCESSING OF HARVESTED PRODUCE; HAY OR STRAW PRESSES; DEVICES FOR STORING AGRICULTURAL OR HORTICULTURAL PRODUCE
- A01F29/00—Cutting apparatus specially adapted for cutting hay, straw or the like
- A01F29/09—Details
- A01F29/12—Discharge means
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B15/00—Details of, or accessories for, presses; Auxiliary measures in connection with pressing
- B30B15/26—Programme control arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/04—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams
- B30B9/06—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams co-operating with permeable casings or strainers
- B30B9/062—Extrusion presses
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/30—Presses specially adapted for particular purposes for baling; Compression boxes therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/30—Presses specially adapted for particular purposes for baling; Compression boxes therefor
- B30B9/3003—Details
- B30B9/3007—Control arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/30—Presses specially adapted for particular purposes for baling; Compression boxes therefor
- B30B9/3003—Details
- B30B9/3035—Means for conditioning the material to be pressed, e.g. paper shredding means
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
Abstract
The invention discloses a kind of biomass straws to crush briquetting all-in-one machine and its method of work, is made of feeding port, crushing motor, pulverizing chamber, mixed liquor conveyance conduit, discharge chambe, waste solution channel, discharge port and electric control box；The sprinkling of multi-stage crushing and mixed liquor conveyance conduit of the pending stalk Jing Guo pulverizing chamber, the stalk after crushing fall into discharge chambe and are compressed packing processing, and extra waste liquid is discharged by waste solution channel；A kind of biomass straw of the present invention crushes briquetting all-in-one machine, the apparatus structure is compact, floor space is small, high degree of automation, it is vdiverse in function, adapt to the work that the crushing of comprehensive multiple types stalk and the compression of stalk are packaged, the utilization rate for conveniently, effectively raising agricultural crop straw is provided for the subsequent processing of stalk, transport and use.
Description
Technical field
The invention belongs to agricultural stalk apparatus fields, and in particular to a kind of biomass straw crushes briquetting all-in-one machine.
Background technology
For Chinese 80% population lives in rural area, the biomass energies such as stalk and fuel wood are the main life fuels in rural area, although
Use of the commercial energys such as coal in rural area increases sharply, but biomass energy still occupies an important position.Life in the countryside in 1998 is used
3.65 hundred million tons of mark coals of energy total amount, wherein stalk and fuel wood are 2.07 hundred million tons of mark coals, account for 56.7%.Therefore, biomass is developed
Special Significance can be had more to Chinese countryside.
With the raising of rural economic development and life of farmers level, rural area is increasingly urgent for the demand of high-grade fuel,
Since the crops such as stalk, fuel wood volume is big, storage is difficult, energy is low, traditional energy Land use systems, which have been difficult to meet rural area, to be showed
Generationization demand, biomass energy high quality conversion are imperative.
At present, part of the manufacturer's also just positive development ＆ production forming machine for straw, but there are it is complicated, output efficiency is low, into
The problems such as type is unstable.
In addition present rural area makes it return crop field, the place of this stalk to another processing mode of stalk using burning
Reason mode was both time-consuming, also polluted environment, is unfavorable for environmental protection or even can cause fire, it is therefore desirable to stalk be carried out secondary
Processing makes it have new purposes, it is necessary to be crushed to stalk before stalk carries out secondary operation, existing stalk crushes
Machine, it is complicated, it is of high cost, it is unfavorable for being promoted the use of in wast rural area.
The content of the invention
In order to solve the above technical problem, the present invention provides a kind of biomass straws to crush briquetting all-in-one machine, including：Feeding
Mouth 1 crushes motor 2, pulverizing chamber 3, mixed liquor conveyance conduit 4, discharge chambe 5, waste solution channel 6, discharge port 7, electric control box 8；
Wherein described discharge chambe 5 is in rectangular parallelepiped structure, and 5 upper face of discharge chambe is disposed with pulverizing chamber 3, wherein 3 top half of pulverizing chamber
Structure is wedge shaped, and the latter half structure is cylinder, and pulverizing chamber 3 is penetrated through with discharge chambe 5；3 top of pulverizing chamber, which is equipped with, to crush
Motor 2,3 one side of pulverizing chamber are equipped with feeding port 1, and 3 opposite side of pulverizing chamber is equipped with mixed liquor conveyance conduit 4, wherein feeding port 1 and mixed
Liquid conveyance conduit 4 is closed to penetrate through with pulverizing chamber 3；The waste solution channel 6 is located at 5 one side bottom of discharge chambe, and discharge port 7 is located at compression
5 another side bottom of room, wherein discharge port 7 and 5 hinge connection of discharge chambe；The electric control box 8 is placed in 5 front surface one of discharge chambe
Side, electric control box 8 are fixed with discharge chambe 5 and welded；
The crushing motor 2 is connected by conducting wire with the control of electric control box 8.
Further, the pulverizing chamber 3 includes：Reducing mechanism 3-1, mixed liquor nozzle 3-2, humidity sensor 3-3, two level
Sieve 3-4, level-one sieve 3-5；Wherein described 3 inside center of pulverizing chamber be equipped with reducing mechanism 3-1, wherein reducing mechanism 3-1 with
Crush 2 output shaft coaxial rotating of motor；The level-one sieve 3-5 and the equal levels of two level sieve 3-4 are fixed on 3 lower half of pulverizing chamber
Point cylindrical inner surface, and through reducing mechanism 3-1；The mixed liquor nozzle 3-2 is located in 3 top half inclined-plane of pulverizing chamber
Wall, mixed liquor nozzle 3-2 and 4 seamless welding of mixed liquor conveyance conduit；The 3 lower half cylindrical inner surface side wall cloth of pulverizing chamber
Humidity sensor 3-3 is equipped with, humidity sensor 3-3 is connected by conducting wire with the control of electric control box 8.
Further, the reducing mechanism 3-1 includes：Central shaft 3-1-1 aids in swing arm 3-1-2, level-one crushing knife 3-1-
3, two level crushing knife 3-1-4, three-level crushing knife 3-1-5 are pushed away and are swept swing arm 3-1-6；Central shaft 3-1-1 cloth successively from top to bottom
It is equipped with auxiliary swing arm 3-1-2, level-one crushing knife 3-1-3, two level crushing knife 3-1-4, three-level crushing knife 3-1-5 and pushes away and sweep swing arm 3-
1-6, wherein auxiliary swing arm 3-1-2 and 1 center of feeding port are in the same horizontal line, level-one crushing knife 3-1-3 is located at level-one sieve
3-5 tops, level-one crushing knife 3-1-3 and level-one sieve 3-5 spacing are 50mm~100mm, two level crushing knife 3-1-4, three-level powder
It broken knife 3-1-5 and pushes away and sweeps swing arm 3-1-6 and be located between level-one sieve 3-5 and two level sieve 3-4 and be equally spaced, spacing 40mm
~70mm.
Further, described push away is swept swing arm 3-1-6 and is included：Fill groove 3-1-6-1, filler 3-1-6-2；It is wherein described
It pushes away and sweeps swing arm 3-1-6 structures as triangular prism, push away and sweep swing arm 3-1-6 two sides and be arranged with filling groove 3-1-6-1, fill groove
3-1-6-1 is internally provided with filler 3-1-6-2, and wherein filler 3-1-6-2 is high molecular material.
Further, the discharge chambe 5 includes：Surge chamber 5-1, compression push plate 5-2 compress baffle 5-3, discharging inclined plate 5-
4, waste liquid outlet 5-5 liquid level sensors 5-6；Wherein described 5 inner tip of discharge chambe is equipped with surge chamber 5-1, surge chamber 5-1 and pressure
5 structure of contracting room is identical and upper bottom surface size is the same, and surge chamber 5-1 thickness is 80cm~100cm；The surge chamber 5-1 lower parts
Equipped with compression push plate 5-2 and compression baffle 5-3, wherein compression push plate 5-2 and compression baffle 5-3 by being fixed in discharge chambe 5
Driven by Hydraulic Cylinder on wall, compression baffle 5-3 surfaces are uniformly distributed through hole, and through-hole diameter is between 5mm~8mm；The discharging
Inclined plate 5-4 is located at 5 inner bottom of discharge chambe, and discharging inclined plate 5-4 surfaces are uniformly distributed through hole, through-hole diameter 5mm~8mm it
Between, discharging inclined plate 5-4 is shown as α with 5 bottom surface angle of discharge chambe, and α codomains are 45 °~60 °；On the 5 bottom side wall of discharge chambe
Equipped with waste liquid outlet 5-5,5 lower front wall of discharge chambe is equipped with liquid level sensor 5-6, and wherein liquid level sensor 5-6 is by leading
Line is connected with the control of electric control box 8.
Further, the filler 3-1-6-2 is molded by high molecular material pressing mold, the composition of filler 3-1-6-2 into
Divide and manufacturing process is as follows：
First, filler 3-1-6-2 constituents：
It counts in parts by weight, 30~65 parts of methene cyclopropane -2,2- diethyl dicarboxylate, 1- cyano cyclopropane -1- carboxylics
12~45 parts of acetoacetic ester, trans- 41~89 parts of 4- propyl-cyclohexyls alkane carboxylic acid -4- ethyoxyls phenyl ester, 4- cyclopropyl (hydroxyl) methylene
52~130 parts of base -3,5- diketone cyclohexanecarboxylate, 3- methyl -3- [4- (2- methyl-propyls) phenyl] oxirane carboxylic acid
85~212 parts of ethyl ester, trans -4- ethyl cyclohexanes formic acid 4- [2- (trans -4- propylcyclohexyls) ethyl] phenylester 43~98
Part, double (1, the 1- dimethyl of double (1,1- the dimethyl ethyl) -4-HBAs -2,4- of 3,5- that concentration is 54ppm~76ppm
Propyl) 76~152 parts of phenyl ester, double 113~230 parts of (1,1- the dimethyl ethyl) -4- hydroxy benzoic propionates of octadecyl -3,5-,
152~196 parts of 2 hydroxybenzoic acid -4- (1,1- dimethyl ethyl) phenylester, 63~152 parts of crosslinking agent, adipic acid and 2- second
Base -2- (methylol) -53~125 parts of 1,3-PD, 1,1- 60~150 parts of cyclopropyl diethyl dicarboxylate, 1,3- different benzo
18~68 parts of furasndione, 2- ethyls -2- methylols -67~123 parts of 1,3-PD；
The crosslinking agent is 2,2- dihydroxymethyl -1,3- propylene glycol, 2- ethyl -2- methylol -1,3- propylene glycol, 1,3- bis-
Any one in isocyanatomethylbenzene；
2nd, the manufacturing process of filler 3-1-6-2, comprises the steps of：
1st step：Ultra-pure water 1300~2200 part of the electrical conductivity for the μ S/cm of 4.25 μ S/cm~6.45 is added in a kettle,
Start reaction kettle in blender, rotating speed be 65rpm~130rpm, start heat pump, make reactor temperature rise to 82 DEG C~
110℃；Sequentially add methene cyclopropane -2,2- diethyl dicarboxylates, 1- cyano cyclopropane -1- carboxylic acid, ethyl esters, trans- 4- third
Base-cyclohexane-carboxylic acid -4- ethyoxyl phenyl esters, to being completely dissolved, it is 3.8~7.5 to adjust pH value, and agitator speed is adjusted to for stirring
85rpm~158rpm, temperature is 120 DEG C~150 DEG C, when esterification 15~30 is small；
2nd step：Take 4- cyclopropyl (hydroxyl) methylene -3,5- diketone cyclohexanecarboxylate, 3- methyl -3- [4- (2- first
Base propyl) phenyl] oxirane carboxylic acid ethyl ester crushes, and powder diameter is 600~1000 mesh；Add in trans -4- ethyls ring
Hexane formic acid 4- [2- (trans -4- propylcyclohexyls) ethyl] phenylester is uniformly mixed, is laid in pallet, and tiling thickness is
12mm~24mm uses the alpha ray irradiation 150~280 that dosage is 7.0MeV~12.0MeV for 6.8kGy~9.2kGy, energy
Minute and the same dose of β x ray irradiation xs 150~280 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in double (1,1- dimethyl ethyls) -4-HBA -2 of 3,5-,
In double (1, the 1- dimethyl propyl) phenyl esters of 4-, add in reaction kettle, agitator speed is 90rpm~190rpm, temperature for 65 DEG C~
125 DEG C, starting vacuum pump makes the vacuum degree of reaction kettle reach -0.15MPa~1.25MPa, keeps this state response 25~40 small
When；Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure for 0.55MPa~0.75MPa, when heat preservation standing 15~30 is small；Blender
Rotating speed is promoted to 130rpm~240rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add the double (1,1- bis- of octadecyl -3,5-
Methylethyl) after -4- hydroxy benzoic propionates, 2 hydroxybenzoic acid -4- (1,1- dimethyl ethyl) phenylester be completely dissolved, add in
Crosslinking agent is stirred so that the hydrophilic lipophilic balance of reaction kettle solution is 5.7~9.5, when heat preservation standing 15~35 is small；
4th step：When agitator speed is 212rpm~275rpm, adipic acid and 2- ethyls -2- (hydroxyl first are sequentially added
Base) -1,3- propylene glycol, 1,1- cyclopropyl diethyl dicarboxylate, 1,3- isobenzofurandiones and 2- ethyl -2- methylol -1,
3-propanediol promotes reactor pressure, reaches 0.65MPa~1.55MPa, and temperature is 145 DEG C~220 DEG C, polymerisation
20~35 it is small when；Reacting kettle inner pressure is down to 0MPa after the completion of reaction, is cooled to 25 DEG C~40 DEG C, discharging enters molding press i.e.
Filler 3-1-6-2 can be made.
Further, the invention also discloses the method for work that a kind of biomass straw crushes briquetting all-in-one machine, this method
Including following steps：
1st step：Power on, electric control box 8 exports signal, and control crushes motor 2 and opens, and operator is by sending at this time
Material mouth 1 conveys stalk, and at the same time 3 interior humidity sensor 3-3 of pulverizing chamber starts to work, and generates electric signal and is sent to electric-controlled
Case 8 processed, electric control box 8 control the stream of 4 internal mix liquid of mixed liquor conveyance conduit according to humidity sensor 3-3 feedacks
Amount；When 3 internal relative humidity of pulverizing chamber is less than 80%, electric control box 8 controls water pump to increase inside mixed liquor conveyance conduit 4
The flow of mixed liquor；When 3 internal relative humidity of pulverizing chamber is higher than 80%, it is defeated that electric control box 8 controls water pump to reduce mixed liquor
Send the flow of 4 internal mix liquid of pipeline；
2nd step：During stalk crushing, 3 inner primary crushing knife 3-1-3 and level-one sieve 3-5 are to stalk for pulverizing chamber
Carry out preliminary crushing screening；Enter two level crushing knife 3-1-4 and three-level crushing knife 3-1-5 again by the stalk of level-one sieve 3-5
Secondary crushing, then stalk after crushing are swept the pushing of swing arm 3-1-6 by pushing away and are entered by two level sieve 3-4 in surge chamber 5-1
Portion；
3rd step：Stalk inside surge chamber 5-1 is entered in compression push plate 5-2 and compression baffle 5-3 and is compressed, and is pressed
Stalk after contracting is rolled out automatically by the inclined plate 5-4 that discharges via discharge port 7, while the most of mixed liquor contained in stalk is squeezed
Go out, the mixed liquor of extrusion flow to 5 bottom of discharge chambe by compressing the through hole on baffle 5-3 and discharging inclined plate 5-4, when discharge chambe 5
When bottoms level reaches liquid level sensor 5-6 setting values, liquid level sensor 5-6 generates electric signal and sends electric control box 8 to, electricity
Gas control cabinet 8 controls water pump that mixed liquor is made to be flowed out by waste solution channel 6.
A kind of biomass straw disclosed by the invention crushes briquetting all-in-one machine, the advantage is that：
(1) device is controlled using PLC, and high degree of automation is easy to operate, and work efficiency is high；
(2) apparatus structure is compact, convenient for installation and maintenance, and floor space is small；
(3) the device integrated treatment multiclass stalk, it is vdiverse in function；
(4) device can effectively prevent stalk from crushing the dust pollution generated during stalk is handled.
A kind of biomass straw of the present invention crushes briquetting all-in-one machine, and the apparatus structure is compact, floor space is small, certainly
Dynamicization degree is high, vdiverse in function, adapts to the work that the crushing of comprehensive multiple types stalk and the compression of stalk are packaged, and is stalk
It is convenient that subsequent processing, transport and use provide, and effectively raises the utilization rate of agricultural crop straw.
Description of the drawings
Fig. 1 is that a kind of heretofore described biomass straw crushes briquetting all-in-one machine structure schematic diagram.
Fig. 2 is heretofore described pulverizing chamber structure diagram.
Fig. 3 is heretofore described reducing mechanism structure diagram.
Fig. 4 is that swing arm structure diagram is swept in heretofore described pushing away.
Fig. 5 is heretofore described discharge chambe structure diagram.
Fig. 6 is that heretofore described filler fatigue strength changes over time figure.
In figure 1 above~Fig. 5, feeding port 1 crushes motor 2, pulverizing chamber 3, reducing mechanism 3-1, central shaft 3-1-1, auxiliary
Swing arm 3-1-2, level-one crushing knife 3-1-3, two level crushing knife 3-1-4, three-level crushing knife 3-1-5 are pushed away and are swept swing arm 3-1-6, filling
Groove 3-1-6-1, filler 3-1-6-2, mixed liquor nozzle 3-2, humidity sensor 3-3, two level sieve 3-4, level-one sieve 3-
5, mixed liquor conveyance conduit 4, discharge chambe 5, surge chamber 5-1, compression push plate 5-2 compress baffle 5-3, discharging inclined plate 5-4, waste liquid
Export 5-5, liquid level sensor 5-6, waste solution channel 6, discharge port 7, electric control box 8.
Specific embodiment
Briquetting all-in-one machine is crushed into traveling to a kind of biomass straw provided by the invention with reference to the accompanying drawings and examples
One step explanation.
As shown in Figure 1, it is that a kind of heretofore described biomass straw crushes briquetting all-in-one machine structure schematic diagram.From figure
Find out in 1, including：Feeding port 1 crushes motor 2, pulverizing chamber 3, mixed liquor conveyance conduit 4, discharge chambe 5, waste solution channel 6, discharging
Mouth 7, electric control box 8；Wherein described discharge chambe 5 is in rectangular parallelepiped structure, and 5 upper face of discharge chambe is disposed with pulverizing chamber 3, wherein
3 top half structure of pulverizing chamber is wedge shaped, and the latter half structure is cylinder, and pulverizing chamber 3 is penetrated through with discharge chambe 5；The crushing
3 top of room, which is equipped with, crushes motor 2, and 3 one side of pulverizing chamber is equipped with feeding port 1, and 3 opposite side of pulverizing chamber is equipped with mixed liquor conveyance conduit 4,
Wherein feeding port 1 and mixed liquor conveyance conduit 4 is penetrated through with pulverizing chamber 3；The waste solution channel 6 is located at 5 one side bottom of discharge chambe,
Discharge port 7 is located at 5 another side bottom of discharge chambe, wherein discharge port 7 and 5 hinge connection of discharge chambe；The electric control box 8 is placed in
5 front surface one side of discharge chambe, electric control box 8 are fixed with discharge chambe 5 and welded；The crushing motor 2 passes through conducting wire and electric-controlled
The control of case 8 processed is connected.
As shown in Fig. 2, it is heretofore described pulverizing chamber structure diagram.Find out from Fig. 2 or Fig. 1, pulverizing chamber 3 is wrapped
It includes：Reducing mechanism 3-1, mixed liquor nozzle 3-2, humidity sensor 3-3, two level sieve 3-4, level-one sieve 3-5；Wherein described powder
Broken 3 inside center of room is equipped with reducing mechanism 3-1, and wherein reducing mechanism 3-1 is with crushing 2 output shaft coaxial rotating of motor；Described one
Grade sieve 3-5 and the equal levels of two level sieve 3-4 are fixed on 3 the latter half cylindrical inner surface of pulverizing chamber, and are filled through crushing
Put 3-1；The mixed liquor nozzle 3-2 is located at 3 top half inclined-plane inner wall of pulverizing chamber, and mixed liquor nozzle 3-2 is conveyed with mixed liquor
4 seamless welding of pipeline；The 3 lower half cylindrical inner surface side wall of pulverizing chamber is disposed with humidity sensor 3-3, humidity sensor
3-3 is connected by conducting wire with the control of electric control box 8.
As shown in figure 3, it is heretofore described reducing mechanism structure diagram.Find out from Fig. 3 or Fig. 2, crush dress
Putting 3-1 includes：Central shaft 3-1-1, aids in swing arm 3-1-2, level-one crushing knife 3-1-3, two level crushing knife 3-1-4, and three-level crushes
Knife 3-1-5 is pushed away and is swept swing arm 3-1-6；The central shaft 3-1-1 has been sequentially arranged auxiliary swing arm 3-1-2 from top to bottom, level-one crushes
It knife 3-1-3, two level crushing knife 3-1-4, three-level crushing knife 3-1-5 and pushes away and sweeps swing arm 3-1-6, wherein auxiliary swing arm 3-1-2 is with sending
In the same horizontal line, level-one crushing knife 3-1-3 is located at level-one sieve 3-5 tops at material mouth 1 center, level-one crushing knife 3-1-3 with
Level-one sieve 3-5 spacing is 50mm~100mm, and two level crushing knife 3-1-4, three-level crushing knife 3-1-5 sweep swing arm 3-1-6 with pushing away
It between level-one sieve 3-5 and two level sieve 3-4 and is equally spaced, spacing is 40mm~70mm.
As shown in figure 4, it is that swing arm structure diagram is swept in heretofore described pushing away.Find out from Fig. 4 or Fig. 3, push away and sweep rotation
Bar 3-1-6 includes：Fill groove 3-1-6-1, filler 3-1-6-2；Wherein described push away sweeps swing arm 3-1-6 structures as triangular prism,
Push away sweep swing arm 3-1-6 two sides be arranged with filling groove 3-1-6-1, filling groove 3-1-6-1 be internally provided with filler 3-1-
6-2, wherein filler 3-1-6-2 are high molecular material.
As shown in figure 5, it is heretofore described discharge chambe structure diagram.Find out from Fig. 5 or Fig. 1, discharge chambe 5 wraps
It includes：Surge chamber 5-1, compression push plate 5-2 compress baffle 5-3, and discharge inclined plate 5-4, waste liquid outlet 5-5 liquid level sensors 5-6；Its
Described in 5 inner tip of discharge chambe be equipped with surge chamber 5-1, surge chamber 5-1 is identical with 5 structure of discharge chambe and upper bottom surface size one
Sample, surge chamber 5-1 thickness are 80cm~100cm；The surge chamber 5-1 lower parts are equipped with compression push plate 5-2 and compression baffle 5-3,
Wherein compression push plate 5-2 and compression baffle 5-3 compresses baffle 5-3 tables by the Driven by Hydraulic Cylinder being fixed on 5 inner wall of discharge chambe
Face is uniformly distributed through hole, and through-hole diameter is between 5mm~8mm；The discharging inclined plate 5-4 is located at 5 inner bottom of discharge chambe, discharging
Inclined plate 5-4 surfaces are uniformly distributed through hole, and between 5mm~8mm, discharging inclined plate 5-4 shows through-hole diameter with 5 bottom surface angle of discharge chambe
For α, α codomains are 45 °~60 °；The 5 bottom side wall of discharge chambe is equipped with waste liquid outlet 5-5,5 lower front wall of discharge chambe
Liquid level sensor 5-6 is equipped with, wherein liquid level sensor 5-6 is connected by conducting wire with the control of electric control box 8.
The course of work that a kind of biomass straw of the present invention crushes briquetting all-in-one machine is：
1st step：Power on, electric control box 8 exports signal, and control crushes motor 2 and opens, and operator is by sending at this time
Material mouth 1 conveys stalk, and at the same time 3 interior humidity sensor 3-3 of pulverizing chamber starts to work, and generates electric signal and is sent to electric-controlled
Case 8 processed, electric control box 8 control the stream of 4 internal mix liquid of mixed liquor conveyance conduit according to humidity sensor 3-3 feedacks
Amount；When 3 internal relative humidity of pulverizing chamber is less than 80%, electric control box 8 controls water pump to increase inside mixed liquor conveyance conduit 4
The flow of mixed liquor；When 3 internal relative humidity of pulverizing chamber is higher than 80%, it is defeated that electric control box 8 controls water pump to reduce mixed liquor
Send the flow of 4 internal mix liquid of pipeline；
2nd step：During stalk crushing, 3 inner primary crushing knife 3-1-3 and level-one sieve 3-5 are to stalk for pulverizing chamber
Carry out preliminary crushing screening；Enter two level crushing knife 3-1-4 and three-level crushing knife 3-1-5 again by the stalk of level-one sieve 3-5
Secondary crushing, then stalk after crushing are swept the pushing of swing arm 3-1-6 by pushing away and are entered by two level sieve 3-4 in surge chamber 5-1
Portion；
3rd step：Stalk inside surge chamber 5-1 is entered in compression push plate 5-2 and compression baffle 5-3 and is compressed, and is pressed
Stalk after contracting is rolled out automatically by the inclined plate 5-4 that discharges via discharge port 7, while the most of mixed liquor contained in stalk is squeezed
Go out, the mixed liquor of extrusion flow to 5 bottom of discharge chambe by compressing the through hole on baffle 5-3 and discharging inclined plate 5-4, when discharge chambe 5
When bottoms level reaches liquid level sensor 5-6 setting values, liquid level sensor 5-6 generates electric signal and sends electric control box 8 to, electricity
Gas control cabinet 8 controls water pump that mixed liquor is made to be flowed out by waste solution channel 6.
A kind of biomass straw of the present invention crushes briquetting all-in-one machine, and the apparatus structure is compact, floor space is small, certainly
Dynamicization degree is high, vdiverse in function, adapts to the work that the crushing of comprehensive multiple types stalk and the compression of stalk are packaged, and is stalk
It is convenient that subsequent processing, transport and use provide, and effectively raises the utilization rate of agricultural crop straw.
It is the embodiment of the manufacturing process of filler 3-1-6-2 of the present invention below, embodiment is in order to furtherly
Bright present disclosure, but should not be construed as limiting the invention.Without departing from the spirit and substance of the case in the present invention, it is right
The modification and replacement that the method for the present invention, step or condition are made, all belong to the scope of the present invention.
Unless otherwise specified, the conventional means that technological means used in embodiment is well known to those skilled in the art.
Embodiment 1
Filler 3-1-6-2 of the present invention is manufactured according to following steps, and is counted in parts by weight：
1st step：1300 parts of the ultra-pure water that electrical conductivity is 4.25 μ S/cm is added in a kettle, starts stirring in reaction kettle
Device, rotating speed 65rpm start heat pump, reactor temperature are made to rise to 82 DEG C；Sequentially add methene cyclopropane -2,2-
30 parts of diethyl dicarboxylate, 12 parts of 1- cyano cyclopropane -1- carboxylic acid, ethyl esters, trans- 4- propyl-cyclohexyls alkane carboxylic acid -4- ethoxybenzenes
41 parts of ester, to being completely dissolved, it is 3.8 to adjust pH value for stirring, agitator speed is adjusted to 85rpm, temperature is 120 DEG C, and esterification is anti-
Answer 15 it is small when；
2nd step：Take 52 parts of 4- cyclopropyl (hydroxyl) methylene -3,5- diketone cyclohexanecarboxylate, 3- methyl -3- [4-
(2- methyl-propyls) phenyl] 85 parts of oxirane carboxylic acid ethyl ester crushes, and powder diameter is 600 mesh；Add in trans -4- ethyls
43 parts of naphthenic acid 4- [2- (trans -4- propylcyclohexyls) ethyl] phenylester is uniformly mixed, and is laid in pallet, and tiling is thick
It spends for 12mm, the alpha ray that dosage is used to be 7.0MeV for 6.8kGy, energy irradiates 150 minutes and the same dose of β rays
Irradiation 150 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in double (1,1- dimethyl ethyls) -4- of 3,5- that concentration is 54ppm
In double 76 parts of (1, the 1- dimethyl propyl) phenyl esters of hydroxybenzoic acid -2,4-, reaction kettle, agitator speed 90rpm, temperature are added in
For 65 DEG C, starting vacuum pump makes the vacuum degree of reaction kettle reach -0.15MPa, when keeping this state response 25 small；Pressure release is simultaneously passed through
Radon gas makes reacting kettle inner pressure for 0.55MPa, when heat preservation standing 15 is small；Agitator speed is promoted to 130rpm, simultaneous reactions kettle
Pressure release is to 0MPa；Sequentially add octadecyl -3,5- double 113 parts of (1,1- dimethyl ethyls) -4- hydroxy benzoic propionates, 2- hydroxyls
After 152 parts of benzoic acid -4- (1,1- dimethyl ethyl) phenylester is completely dissolved, adds in 63 parts of crosslinking agent and be stirred so that is anti-
The hydrophilic lipophilic balance for answering kettle solution is 5.7, when heat preservation standing 15 is small；
4th step：When agitator speed is 212rpm, adipic acid and 2- ethyls -2- (methylol) -1,3- third are sequentially added
53 parts of glycol, 60 parts of 1,1- cyclopropyl diethyl dicarboxylate, 18 parts of 1,3- isobenzofurandiones and 2- ethyl -2- methylols -
67 parts of 1,3-PD promotes reactor pressure, reaches 0.65MPa, temperature is 145 DEG C, when polymerisation 20 is small；Reaction
Reacting kettle inner pressure is down to 0MPa after finishing, is cooled to 25 DEG C, discharging enters molding press and can be prepared by filler 3-1-6-2.
The crosslinking agent is 2,2- dihydroxymethyl -1,3- propylene glycol.
Embodiment 2
Filler 3-1-6-2 of the present invention is manufactured according to following steps, and is counted in parts by weight：
1st step：2200 parts of the ultra-pure water that electrical conductivity is 6.45 μ S/cm is added in a kettle, starts stirring in reaction kettle
Device, rotating speed 130rpm start heat pump, reactor temperature are made to rise to 110 DEG C；Methene cyclopropane -2 are sequentially added,
65 parts of 2- diethyl dicarboxylates, 45 parts of 1- cyano cyclopropane -1- carboxylic acid, ethyl esters, trans- 4- propyl-cyclohexyls alkane carboxylic acid -4- ethyoxyls
89 parts of phenyl ester, to being completely dissolved, it is 7.5 to adjust pH value for stirring, agitator speed is adjusted to 158rpm, temperature is 150 DEG C, esterification
React 30 it is small when；
2nd step：Take 130 parts of 4- cyclopropyl (hydroxyl) methylene -3,5- diketone cyclohexanecarboxylate, 3- methyl -3- [4-
(2- methyl-propyls) phenyl] 212 parts of oxirane carboxylic acid ethyl ester crushes, and powder diameter is 1000 mesh；Add in trans -4- second
98 parts of Butylcyclohexanecarboxylic acid 4- [2- (trans -4- propylcyclohexyls) ethyl] phenylester is uniformly mixed, and is laid in pallet, is tiled
Thickness is 24mm, and the alpha ray that dosage is used to be 12.0MeV for 9.2kGy, energy, which irradiates 280 minutes and the same dose of β, to be penetrated
Line irradiates 280 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in double (1,1- dimethyl ethyls) -4- of 3,5- that concentration is 76ppm
In double 152 parts of (1, the 1- dimethyl propyl) phenyl esters of hydroxybenzoic acid -2,4-, reaction kettle, agitator speed 190rpm, temperature are added in
It spends for 125 DEG C, starting vacuum pump makes the vacuum degree of reaction kettle reach 1.25MPa, when keeping this state response 40 small；Pressure release is simultaneously led to
Enter radon gas, make reacting kettle inner pressure for 0.75MPa, when heat preservation standing 30 is small；Agitator speed is promoted to 240rpm, simultaneous reactions
Kettle pressure release is to 0MPa；Sequentially add octadecyl -3,5- double 230 parts of (1,1- dimethyl ethyls) -4- hydroxy benzoic propionates, 2- hydroxyls
After 196 parts of yl benzoic acid -4- (1,1- dimethyl ethyl) phenylester is completely dissolved, adds in 152 parts of crosslinking agent and be stirred so that
The hydrophilic lipophilic balance of reaction kettle solution is 9.5, when heat preservation standing 35 is small；
4th step：When agitator speed is 275rpm, adipic acid and 2- ethyls -2- (methylol) -1,3- third are sequentially added
125 parts of glycol, 150 parts of 1,1- cyclopropyl diethyl dicarboxylate, 68 parts of 1,3- isobenzofurandiones and 2- ethyl -2- hydroxyl first
123 parts of base -1,3-PD promotes reactor pressure, reaches 1.55MPa, temperature is 220 DEG C, when polymerisation 35 is small；
Reacting kettle inner pressure is down to 0MPa after the completion of reaction, is cooled to 40 DEG C, discharging enters molding press and can be prepared by filler 3-1-6-
2。
The crosslinking agent closes methylbenzene for 1,3- diisocyanates root.
Embodiment 3
Filler 3-1-6-2 of the present invention is manufactured according to following steps, and is counted in parts by weight：
1st step：1750 parts of the ultra-pure water that electrical conductivity is 5.35 μ S/cm is added in a kettle, starts stirring in reaction kettle
Device, rotating speed 95rpm start heat pump, reactor temperature are made to rise to 96 DEG C；Sequentially add methene cyclopropane -2,2-
52 parts of diethyl dicarboxylate, 28 parts of 1- cyano cyclopropane -1- carboxylic acid, ethyl esters, trans- 4- propyl-cyclohexyls alkane carboxylic acid -4- ethoxybenzenes
65 parts of ester, to being completely dissolved, it is 5.8 to adjust pH value for stirring, agitator speed is adjusted to 120rpm, temperature is 135 DEG C, and esterification is anti-
Answer 22 it is small when；
2nd step：Take 90 parts of 4- cyclopropyl (hydroxyl) methylene -3,5- diketone cyclohexanecarboxylate, 3- methyl -3- [4-
(2- methyl-propyls) phenyl] 97 parts of oxirane carboxylic acid ethyl ester crushes, and powder diameter is 800 mesh；Add in trans -4- ethyls
72 parts of naphthenic acid 4- [2- (trans -4- propylcyclohexyls) ethyl] phenylester is uniformly mixed, and is laid in pallet, and tiling is thick
It spends for 18mm, the alpha ray that dosage is used to be 9.5MeV for 7.2kGy, energy irradiates 215 minutes and the same dose of β rays
Irradiation 215 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in double (1,1- dimethyl ethyls) -4- of 3,5- that concentration is 65ppm
In double 116 parts of (1, the 1- dimethyl propyl) phenyl esters of hydroxybenzoic acid -2,4-, reaction kettle, agitator speed 140rpm, temperature are added in
It spends for 95 DEG C, starting vacuum pump makes the vacuum degree of reaction kettle reach 0.55MPa, when keeping this state response 32 small；Pressure release is simultaneously led to
Enter radon gas, make reacting kettle inner pressure for 0.65MPa, when heat preservation standing 22 is small；Agitator speed is promoted to 195rpm, simultaneous reactions
Kettle pressure release is to 0MPa；Sequentially add octadecyl -3,5- double 172 parts of (1,1- dimethyl ethyls) -4- hydroxy benzoic propionates, 2- hydroxyls
After 174 parts of yl benzoic acid -4- (1,1- dimethyl ethyl) phenylester is completely dissolved, adds in 110 parts of crosslinking agent and be stirred so that
The hydrophilic lipophilic balance of reaction kettle solution is 7.5, when heat preservation standing 25 is small；
4th step：When agitator speed is 243rpm, adipic acid and 2- ethyls -2- (methylol) -1,3- third are sequentially added
89 parts of glycol, 105 parts of 1,1- cyclopropyl diethyl dicarboxylate, 43 parts of 1,3- isobenzofurandiones and 2- ethyl -2- methylols -
96 parts of 1,3-PD promotes reactor pressure, reaches 1.05MPa, temperature is 176 DEG C, when polymerisation 27 is small；Reaction
Reacting kettle inner pressure is down to 0MPa after finishing, is cooled to 35 DEG C, discharging enters molding press and can be prepared by filler 3-1-6-2.
The crosslinking agent is 2- ethyl -2- methylol -1,3- propylene glycol.
Reference examples
Reference examples are the filler of certain commercially available brand.
Embodiment 4
Filler described in the filler 3-1-6-2 and reference examples that Examples 1 to 3 is prepared carries out using effect pair
Than.The two hardness, corrosion rate, tensile strength, maximum operation (service) temperature are counted, the results are shown in Table 1.
As seen from Table 1, filler 3-1-6-2 of the present invention, hardness, corrosion rate, tensile strength, highest use
The indexs such as temperature are superior to the product of prior art production.
In addition, as shown in fig. 6, it is that heretofore described filler fatigue strength changes over time figure.Find out in figure, it is real
Filler 3-1-6-2 used in example 1~3 is applied, fatigue of materials intensity is significantly better than existing product with usage time variation degree.
Claims (5)
1. a kind of biomass straw crushes briquetting all-in-one machine, including：Feeding port（1）, crush motor（2）, pulverizing chamber（3）, mixing
Liquid conveyance conduit（4）, discharge chambe（5）, waste solution channel（6）, discharge port（7）, electric control box（8）；It is characterized in that, the pressure
Contracting room（5）In rectangular parallelepiped structure, discharge chambe（5）Upper face is disposed with pulverizing chamber（3）, wherein pulverizing chamber（3）Top half knot
Structure is wedge shaped, and the latter half structure is cylinder, pulverizing chamber（3）With discharge chambe（5）Perforation；The pulverizing chamber（3）Top is equipped with
Crush motor（2）, pulverizing chamber（3）One side is equipped with feeding port（1）, pulverizing chamber（3）Opposite side is equipped with mixed liquor conveyance conduit（4）,
Wherein feeding port（1）With mixed liquor conveyance conduit（4）And pulverizing chamber（3）Perforation；The waste solution channel（6）Positioned at discharge chambe
（5）One side bottom, discharge port（7）Positioned at discharge chambe（5）Another side bottom, wherein discharge port（7）With discharge chambe（5）Hinge connects
It connects；The electric control box（8）It is placed in discharge chambe（5）Front surface one side, electric control box（8）With discharge chambe（5）Fixed welding；
The crushing motor（2）Pass through conducting wire and electric control box（8）Control is connected；
The pulverizing chamber（3）Including：Reducing mechanism（3-1）, mixed liquor nozzle（3-2）, humidity sensor（3-3）, two level sieve
（3-4）, level-one sieve（3-5）；Wherein described pulverizing chamber（3）Inside center is equipped with reducing mechanism（3-1）, wherein reducing mechanism
（3-1）With crushing motor（2）Output shaft coaxial rotating；The level-one sieve（3-5）With two level sieve（3-4）Equal level is fixed on
Pulverizing chamber（3）The latter half cylindrical inner surface, and through reducing mechanism（3-1）；The mixed liquor nozzle（3-2）Positioned at powder
Broken room（3）Top half inclined-plane inner wall, mixed liquor nozzle（3-2）With mixed liquor conveyance conduit（4）Seamless welding；The pulverizing chamber
（3）Lower half cylindrical inner surface side wall is disposed with humidity sensor（3-3）, humidity sensor（3-3）By conducting wire and electrically
Control cabinet（8）Control is connected；
The reducing mechanism（3-1）Including：Central shaft（3-1-1）, aid in swing arm（3-1-2）, level-one crushing knife（3-1-3）, two
Grade crushing knife（3-1-4）, three-level crushing knife（3-1-5）, push away and sweep swing arm（3-1-6）；The central shaft（3-1-1）From top to bottom according to
It is secondary to be disposed with auxiliary swing arm（3-1-2）, level-one crushing knife（3-1-3）, two level crushing knife（3-1-4）, three-level crushing knife（3-1-5）
Swing arm is swept with pushing away（3-1-6）, wherein aiding in swing arm（3-1-2）With feeding port（1）Center in the same horizontal line, level-one crushing knife
（3-1-3）Positioned at level-one sieve（3-5）Top, level-one crushing knife（3-1-3）With level-one sieve（3-5）Spacing for 50mm~
100mm, two level crushing knife（3-1-4）, three-level crushing knife（3-1-5）Swing arm is swept with pushing away（3-1-6）Positioned at level-one sieve（3-5）With
Two level sieve（3-4）Between and be equally spaced, spacing be 40mm~70mm.
2. a kind of biomass straw according to claim 1 crushes briquetting all-in-one machine, which is characterized in that described push away sweeps swing arm
（3-1-6）Including：Fill groove（3-1-6-1）, filler（3-1-6-2）；Wherein described push away sweeps swing arm（3-1-6）Structure is three
Prism pushes away and sweeps swing arm（3-1-6）Two sides are arranged with filling groove（3-1-6-1）, fill groove（3-1-6-1）It is internally provided with
Filler（3-1-6-2）, wherein filler（3-1-6-2）For high molecular material.
3. a kind of biomass straw according to claim 2 crushes briquetting all-in-one machine, which is characterized in that the discharge chambe
（5）Including：Surge chamber（5-1）, compression push plate（5-2）, compress baffle（5-3）, discharge inclined plate（5-4）, waste liquid outlet（5-5）Liquid
Level sensor（5-6）；Wherein described discharge chambe（5）Inner tip is equipped with surge chamber（5-1）, surge chamber（5-1）With discharge chambe（5）
Structure is identical and upper bottom surface size is the same, surge chamber（5-1）Thickness is 80cm~100cm；The surge chamber（5-1）Lower part is set
There is compression push plate（5-2）With compression baffle（5-3）, wherein compression push plate（5-2）With compression baffle（5-3）It is compressed by being fixed on
Room（5）Driven by Hydraulic Cylinder on inner wall compresses baffle（5-3）Surface is uniformly distributed through hole, and through-hole diameter is between 5mm~8mm；
The discharging inclined plate（5-4）Positioned at discharge chambe（5）Inner bottom, discharge inclined plate（5-4）Surface is uniformly distributed through hole, through-hole diameter
Between 5mm~8mm, discharge inclined plate（5-4）With discharge chambe（5）Bottom surface angle is shown as α, and α codomains are 45 °~60 °；The compression
Room（5）Bottom side wall is equipped with waste liquid outlet（5-5）, discharge chambe（5）Lower front wall is equipped with liquid level sensor（5-6）,
Wherein liquid level sensor（5-6）Pass through conducting wire and electric control box（8）Control is connected.
4. a kind of biomass straw according to claim 3 crushes briquetting all-in-one machine, which is characterized in that the filler
（3-1-6-2）It is molded by high molecular material pressing mold, filler（3-1-6-2）Constituent and manufacturing process it is as follows：
First, filler（3-1-6-2）Constituent：
It counts in parts by weight, 30~65 parts of methene cyclopropane -2,2- diethyl dicarboxylate, 1- cyano cyclopropane -1- carboxylic acid second
12~45 parts of ester, trans- 41~89 parts of 4- propyl-cyclohexyls alkane carboxylic acid -4- ethyoxyls phenyl ester, 4- cyclopropyl (hydroxyl) methylene -3,
52~130 parts of 5- diketone cyclohexanecarboxylate, 3- methyl -3- [4- (2- methyl-propyls) phenyl] oxirane carboxylic acid ethyl ester 85
~212 parts, trans 43~98 parts of phenylester of -4- ethyl cyclohexanes formic acid 4- [2- (trans -4- propylcyclohexyls) ethyl], concentration
It is double (1,1- dimethyl propyls) for double (the 1,1- dimethyl ethyls) -4-HBAs -2,4- of 3,5- of the ppm of 54 ppm~76
76~152 parts of phenyl ester, double 113~230 parts of (1,1- the dimethyl ethyl) -4- hydroxy benzoic propionates of octadecyl -3,5-, 2- hydroxyls
152~196 parts of benzoic acid -4- (1,1- dimethyl ethyl) phenylester, 63~152 parts of crosslinking agent, 2- ethyls -2- (methylol) -
53~125 parts of 1,3-PD, 1,1- 60~150 parts of cyclopropyl diethyl dicarboxylate, 1,3- isobenzofurandione 18~68
Part, 2- ethyls -2- methylols -67~123 parts of 1,3-PD；
The crosslinking agent is 2,2- dihydroxymethyl -1,3- propylene glycol, 2- ethyl -2- methylol -1,3- propylene glycol, bis- isocyanides of 1,3-
Acid group closes any one in methylbenzene；
2nd, filler（3-1-6-2）Manufacturing process, comprise the steps of：
1st step：Ultra-pure water 1300~2200 part of the electrical conductivity for the μ S/cm of 4.25 μ S/cm~6.45 is added in a kettle, is opened
Blender in dynamic reaction kettle, rotating speed are the rpm of 65 rpm~130, start heat pump, make reactor temperature rise to 82 DEG C~
110 ℃；Sequentially add methene cyclopropane -2,2- diethyl dicarboxylates, 1- cyano cyclopropane -1- carboxylic acid, ethyl esters, trans- 4- third
Base-cyclohexane-carboxylic acid -4- ethyoxyl phenyl esters, to being completely dissolved, it is 3.8~7.5 to adjust pH value, and agitator speed is adjusted to for stirring
The rpm of 85 rpm~158, temperature is 120 DEG C~150 DEG C, when esterification 15~30 is small；
2nd step：Take 4- cyclopropyl (hydroxyl) methylene -3,5- diketone cyclohexanecarboxylate, 3- methyl -3- [4- (2- methyl-props
Base) phenyl] oxirane carboxylic acid ethyl ester crushes, and powder diameter is 600~1000 mesh；Add in trans -4- ethyl cyclohexanes
Formic acid 4- [2- (trans -4- propylcyclohexyls) ethyl] phenylester is uniformly mixed, is laid in pallet, and tiling thickness is 12 mm
~24 mm use dosage as alpha ray irradiation 150~280 that the kGy of 6.8 kGy~9.2, energy are the MeV of 7.0 MeV~12.0
Minute and the same dose of β x ray irradiation xs 150~280 minutes；
3rd step：It is double that the mixed-powder handled through the 2nd step is dissolved in double (the 1,1- dimethyl ethyls) -4-HBA -2,4- of 3,5-
In (1,1- dimethyl propyl) phenyl ester, reaction kettle is added in, agitator speed is the rpm of 90 rpm~190, and temperature is 65 DEG C~125
DEG C, starting vacuum pump makes the vacuum degree of reaction kettle reach the MPa of -0.15 MPa~1.25, keeps this state response 25~40 small
When；Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure for the MPa of 0.55 MPa~0.75, heat preservation stand 15~30 it is small when；Stirring
Device rotating speed is promoted to the rpm of 130 rpm~240, simultaneous reactions kettle pressure release to 0 MPa；Sequentially add octadecyl -3,5- it is double (1,
1- dimethyl ethyls) after -4- hydroxy benzoic propionates, 2 hydroxybenzoic acid -4- (1,1- dimethyl ethyl) phenylester be completely dissolved,
It adds in crosslinking agent to be stirred so that the hydrophilic lipophilic balance of reaction kettle solution is 5.7~9.5, and it is small that heat preservation stands 15~35
When；
4th step：When agitator speed is 212 rpm~275 rpm, sequentially add adipic acid and 2- ethyls -2- (methylol) -
1,3- propylene glycol, 1,1- cyclopropyl diethyl dicarboxylate, 1,3- isobenzofurandiones and 2- ethyl -2- methylols -1,3- third
Glycol promotes reactor pressure, reaches the MPa of 0.65 MPa~1.55, and temperature is 145 DEG C~220 DEG C, polymerisation 20
~35 it is small when；Reacting kettle inner pressure is down to 0 MPa after the completion of reaction, is cooled to 25 DEG C~40 DEG C, discharging enters molding press i.e.
Filler can be made（3-1-6-2）.
5. a kind of biomass straw crushes the method for work of briquetting all-in-one machine, which is characterized in that this method includes following step
Suddenly：
1st step：Power on, electric control box（8）Signal is exported, control crushes motor（2）It opens, operator is by sending at this time
Material mouth（1）Stalk is conveyed, at the same time pulverizing chamber（3）Interior humidity sensor（3-3）It starts to work, generates electric signal and be sent to
Electric control box（8）, electric control box（8）According to humidity sensor（3-3）Feedack controls mixed liquor conveyance conduit（4）
The flow of internal mix liquid；Work as pulverizing chamber（3）When internal relative humidity is less than 80%, electric control box（8）Water pump is controlled to increase mixed
Close liquid conveyance conduit（4）The flow of internal mix liquid；Work as pulverizing chamber（3）When internal relative humidity is higher than 80%, electric control box
（8）Water pump is controlled to reduce mixed liquor conveyance conduit（4）The flow of internal mix liquid；
2nd step：During stalk crushing, pulverizing chamber（3）Inner primary crushing knife（3-1-3）With level-one sieve（3-5）To straw
Stalk carries out preliminary crushing screening；By level-one sieve（3-5）Stalk enter two level crushing knife（3-1-4）With three-level crushing knife
（3-1-5）It crushes again, then the stalk after crushing sweeps swing arm by pushing away（3-1-6）Pushing and pass through two level sieve（3-4）Into
Enter surge chamber（5-1）It is internal；
3rd step：Surge chamber（5-1）Internal stalk enters compression push plate（5-2）With compression baffle（5-3）In be compressed,
Compressed stalk passes through the inclined plate that discharges（5-4）Via discharge port（7）Automatically roll out, while the most of mixing contained in stalk
Liquid is extruded, and the mixed liquor of extrusion is by compressing baffle（5-3）With discharging inclined plate（5-4）On through hole flow to discharge chambe（5）Bottom
Portion works as discharge chambe（5）Bottoms level reaches liquid level sensor（5-6）During setting value, liquid level sensor（5-6）Electric signal is generated to pass
Give electric control box（8）, electric control box（8）Control water pump makes mixed liquor pass through waste solution channel（6）Outflow.
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| CN106902937A (en) * | 2017-03-03 | 2017-06-30 | 安徽安丰堂动物药业有限公司 | A kind of intelligent veterinary drug powder patent medicine system |
| CN109611822A (en) * | 2017-10-04 | 2019-04-12 | 镇江润德节能科技有限公司 | A kind of biomass combustion machine |
| CN107820871A (en) * | 2017-10-24 | 2018-03-23 | 蚌埠市徐善种植农民专业合作社 | A kind of stalk crasher |
| CN107931082B (en) * | 2017-12-26 | 2024-03-26 | 安徽鼎梁生物能源科技开发有限公司 | Straw powder cutting machine result partial shipment mechanism |
| CN109556934B (en) * | 2018-12-18 | 2019-10-08 | 无锡市第二人民医院 | It is crushed containing genetic substance and extracts all-in-one machine working method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101736850A (en) * | 2009-12-22 | 2010-06-16 | 山东农业大学 | Wheat straw compression molding block |
| US8753410B2 (en) * | 2009-02-17 | 2014-06-17 | University Of Kentucky Research Foundation | Method for producing fuel briquettes from high moisture fine coal or blends of high moisture fine coal and biomass |
| CN103935065A (en) * | 2014-03-21 | 2014-07-23 | 北京林业大学 | Plunger type biomass forming machine |
| CN203888247U (en) * | 2014-03-10 | 2014-10-22 | 江西理工大学 | Energy-saving straw compression solidification forming processing device |
| CN205238629U (en) * | 2015-12-23 | 2016-05-18 | 芜湖禾沐农业科技有限公司 | Wheat straw compression molding machine |
| CN205408692U (en) * | 2016-03-14 | 2016-08-03 | 郑州大学 | Compression blocking machine is smashed to straw |
-
2016
- 2016-08-15 CN CN201610666704.1A patent/CN106258252B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8753410B2 (en) * | 2009-02-17 | 2014-06-17 | University Of Kentucky Research Foundation | Method for producing fuel briquettes from high moisture fine coal or blends of high moisture fine coal and biomass |
| CN101736850A (en) * | 2009-12-22 | 2010-06-16 | 山东农业大学 | Wheat straw compression molding block |
| CN203888247U (en) * | 2014-03-10 | 2014-10-22 | 江西理工大学 | Energy-saving straw compression solidification forming processing device |
| CN103935065A (en) * | 2014-03-21 | 2014-07-23 | 北京林业大学 | Plunger type biomass forming machine |
| CN205238629U (en) * | 2015-12-23 | 2016-05-18 | 芜湖禾沐农业科技有限公司 | Wheat straw compression molding machine |
| CN205408692U (en) * | 2016-03-14 | 2016-08-03 | 郑州大学 | Compression blocking machine is smashed to straw |
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