CN106914170A - A kind of biomass type coal adhesive preparation facilities and preparation method - Google Patents
A kind of biomass type coal adhesive preparation facilities and preparation method Download PDFInfo
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- CN106914170A CN106914170A CN201710219780.2A CN201710219780A CN106914170A CN 106914170 A CN106914170 A CN 106914170A CN 201710219780 A CN201710219780 A CN 201710219780A CN 106914170 A CN106914170 A CN 106914170A
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- inner cylinder
- biomass
- outer barrel
- electric
- water
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- 239000002028 Biomass Substances 0.000 title claims abstract description 55
- 238000002360 preparation method Methods 0.000 title claims abstract description 39
- 239000003245 coal Substances 0.000 title claims abstract description 33
- 239000000853 adhesive Substances 0.000 title claims abstract description 21
- 230000001070 adhesive effect Effects 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 239000007788 liquid Substances 0.000 claims abstract description 25
- 239000011230 binding agent Substances 0.000 claims abstract description 21
- 239000000706 filtrate Substances 0.000 claims abstract description 21
- 238000003756 stirring Methods 0.000 claims abstract description 20
- 239000007921 spray Substances 0.000 claims abstract description 12
- 239000003814 drug Substances 0.000 claims abstract description 11
- 238000005406 washing Methods 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims abstract description 6
- 238000004140 cleaning Methods 0.000 claims abstract description 6
- 238000011049 filling Methods 0.000 claims description 38
- 239000007787 solid Substances 0.000 claims description 19
- 239000011259 mixed solution Substances 0.000 claims description 14
- 238000010438 heat treatment Methods 0.000 claims description 13
- 239000003795 chemical substances by application Substances 0.000 claims description 9
- 238000002347 injection Methods 0.000 claims description 9
- 239000007924 injection Substances 0.000 claims description 9
- 230000004048 modification Effects 0.000 claims description 9
- 238000012986 modification Methods 0.000 claims description 9
- 239000000243 solution Substances 0.000 claims description 9
- 238000002156 mixing Methods 0.000 claims description 8
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 6
- 230000000694 effects Effects 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 238000005507 spraying Methods 0.000 claims description 4
- 230000009471 action Effects 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 238000005485 electric heating Methods 0.000 claims description 3
- 238000005259 measurement Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims 1
- 238000007599 discharging Methods 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000004484 Briquette Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000010902 straw Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 230000003321 amplification Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 235000009973 maize Nutrition 0.000 description 2
- 238000003199 nucleic acid amplification method Methods 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229910052681 coesite Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 235000019795 sodium metasilicate Nutrition 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/51—Methods thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/53—Mixing liquids with solids using driven stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/10—Maintenance of mixers
- B01F35/145—Washing or cleaning mixers not provided for in other groups in this subclass; Inhibiting build-up of material on machine parts using other means
- B01F35/1452—Washing or cleaning mixers not provided for in other groups in this subclass; Inhibiting build-up of material on machine parts using other means using fluids
- B01F35/1453—Washing or cleaning mixers not provided for in other groups in this subclass; Inhibiting build-up of material on machine parts using other means using fluids by means of jets of fluid, e.g. air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/181—Preventing generation of dust or dirt; Sieves; Filters
- B01F35/188—Preventing generation of dust or dirt; Sieves; Filters using sieves in mixers for purposes other than mixing, e.g. eliminating dust during venting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F35/92—Heating or cooling systems for heating the outside of the receptacle, e.g. heated jackets or burners
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F2035/99—Heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/36—Mixing of ingredients for adhesives or glues; Mixing adhesives and gas
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
A kind of biomass type coal adhesive preparation facilities and preparation method, it includes outer barrel, inner cylinder, electric control box, electric mixer, electric up-down sieve plate, electrothermal tube, water inlet pipe, discharging tube and part etc. liquid level peephole.To being added water in inner cylinder, inner cylinder is heated using outer barrel reclaimed water, it is stirred after medicament is put into inner cylinder, biomass after proportioning are put into inner cylinder, are proceeded stirring and is realized modified-reaction, it is to be mixed fully after separated sticky mass and filtrate using electric up-down sieve plate, to inner cylinder spray washing, cleaning solution discharges inner cylinder with filtrate, and outer barrel draining, operation terminates.Its simple structure, preparation process automation, easy to operate, based on the good development prospect of biomass binding agent, dissemination is great.
Description
Technical field
The present invention is applied to a kind of adhesive preparation facilities and preparation method, is particularly suited for biomass modified preparation and is combined
The production of type biomass binding agent prepares the biomass type coal adhesive preparation facilities and preparation method for using.
Background technology
Biomass are regenerative resources, and wide material sources, cheap, them can be processed through microbial project or straight
Connect utilization.They do not only have preferable caloric value, while not increasing the ash of moulded coal also, have after chemically treated preferable
Caking property, the moulded coal burning-point of production is low, not slagging scorification of burning, therefore biomass make binding agent
Recently gradually it is subject to attention both domestic and external.With biomass straw binding agent, in the bar without any other additive
The moulded coal mechanical strength produced under part is improved with the increase of consumption of binder, and with preferable water resistance, can be met
Long-distance transport, the requirement of outdoor storage；And the moulded coal volatile matter of production is far above raw coal, sulfur content is far below raw coal, and this is not
Only be conducive to improved-type coal ignitability energy, and environmental pollution can be reduced, reach the requirement of Combustion of Mould Coal.As biomass are bonded
The embodiment of agent important function, with continuous popularization and the development of national clean moulded coal, the good biomass of low cost, environmental protection characteristic are glued
Knot agent is prepared on a large scale turns into inevitable, supporting preparation facilities be particularly important.
The content of the invention
In place of in view of the shortcomings of the prior art, there is provided a kind of high degree of automation, simple to operate, energy industrialization prepare biological
The biomass type coal adhesive preparation facilities and preparation method of matter binding agent.
To realize above-mentioned technical purpose, biomass type coal adhesive preparation facilities of the invention, including device cylinder and electricity
Gas control cabinet, device cylinder top is provided with device top cover, and wherein device cylinder includes outer barrel, is provided with inner cylinder in outer barrel, outer barrel with
Space tank is provided between inner cylinder, heater is provided with the tank of space, device top cover is provided with water filling port, agitator speed control
Button processed, digital display screen and agitator time switch；Device top cover is provided with flexible agitator to extension in inner cylinder, is set in inner cylinder
There is electric up-down sieve plate, modified filtrate space is provided between electric up-down sieve plate and inner cylinder bottom, modified filtrate space is provided with to be stretched
The modified filtrate space discharge pipe gone out to outside outer barrel, outer barrel side-lower is provided with what the space tank between outer barrel and inner cylinder was connected
Outer barrel drainpipe, the electric control box is connected with heater and temperature sensor, and temperature sensor is used to gather outer barrel
(1) the interstitial water trough inner water temperature and inner cylinder between, and temperature signal is converted into resistance value, by the amplification of integrated amplifier, ratio
After relatively, output control signal efficiently controls the average heating power of electric heating tube, the water in the tank of space is kept constant temperature,
Electric control box has been provided with temperature setting display screen and power switch button.
The heater is the heating tube for being arranged on space bottom of gullet between outer barrel and inner cylinder.The outer barrel is provided with
Liquid level peephole, inner cylinder is transparent, high temperature resistant, resistant material, and scale measurement is just provided with to the inner cylinder at liquid level peephole
Volume.The blade of described flexible agitator is scalable with bar, by the different adjustment leaf blade size of inner cylinder modification liquid concentration, it is necessary to
Bar is stretched during stirring, it is not necessary to shrink bar when stirring.The electric up-down sieve plate can be different according to modified biomass granularity
And the different sieve plates for changing different pore size of modification degree, biomass binding agent can be by lifting sieve plate to modified after the completion of preparing
The viscous solid for being filtered out by sieve plate afterwards is filtered and separated.Water filling port can realize the effect of water filling and spray, inside and outside
Using heavy caliber water filling when cylinder discharges water, solid portion is entered using high-pressure spraying mode after removing to inner cylinder after the completion of binding agent preparation
Row washing, with double action.
A kind of biomass put coal briquette bond preparation method, and its step is as follows：
A. the electric up-down sieve plate in control inner cylinder drops to inner cylinder bottommost, by water filling port to water filling in inner cylinder, profit
The water injection rate in inner cylinder is controlled with liquid level peephole, by the space between outer barrel and inner cylinder after water injection rate reaches preset requirement
Water filling in tank, water filling is stopped after water injection rate reaches requirement；
B. heating is carried out to the water in outer barrel so as to be heated to inner cylinder using electric control box control heater, and
Will be in the deployed medicament input inner cylinder than you, the flexible agitator of control stretches out and medicament and water is stirred, make medicament with
Water stops stirring after being thoroughly mixed to form mixed solution；
C. after the mixed solution temperature in inner cylinder reaches preset value, open top cover and add according to biomass caking agent formula
Plus the biomass after drying and crushing, close top cover and start flexible agitator, and control as needed flexible agitator rotating speed and
Mixing time is so that mixed solution and biomass are modified reaction；
D. after flexible agitator is stirred to be stopped, shrinking flexible agitator, start electric up-down sieve plate from inner cylinder bottom to
It is raised, as the thick solid that the rising of electric up-down sieve plate will be left in being filtered on electric up-down sieve plate takes out and loads
Container, is not stayed in inner cylinder by the filtrate that electric up-down sieve plate is filtered out；
E. spray washing liquid is carried out to inner cylinder using water filling port, afterwards cleaning solution with do not filtered out by electric up-down sieve plate
Filtrate is common to be discharged through filtered fluid discharge pipe and uses container collection；
F. end is prepared, outer barrel is discharged with the water conservancy at the tank of inner cylinder space with outer barrel drainpipe.
The vapor evaporated during mixed solution and biomass heating stirring in the inner cylinder liquefies after top cover condensation
Again inner cylinder is dripped back into, realizes that condensation keeps water loss excessive.
Beneficial effect：
(1) can realize prepared by the large-scale production of biomass modified binding agent；
(2) device top cover equipment electric mixing device, agitator is scalable, and stirring is evenly；
(3) mixing time and stir speed (S.S.) can be set, is regularly stirred, it is biomass modified more abundant；
(4) inner cylinder bottom has can according to the actual requirements change varigrained sieve plate with the sieve plate of automatic lifting, while
Separation of solid and liquid can be carried out after the completion of preparation, thick solid part rises immigration special container by sieve plate, and liquid component leads to
Filtered fluid discharge pipe is collected to special container, gives over to proportioning；
(5) water inlet of device top cover can realize the effect of water filling and spray, be noted using heavy caliber when inner/outer tube discharges water
Water, solid portion is washed using spray mode after removing to inner cylinder after the completion of binding agent preparation, effective protection equipment.
(6) plant automation degree is high, simple to operate, as biomass binding agent advantage constantly attracts attention, dress
Put and have a good application prospect；
Brief description of the drawings
Fig. 1 is the primary structure schematic diagram of biomass type coal adhesive preparation facilities of the present invention；
Fig. 2 is the top cover composition structural representation of biomass type coal adhesive preparation facilities of the present invention；
Fig. 3 is the sieve plate lifting track schematic diagram of the inner cylinder side wall of biomass type coal adhesive preparation facilities of the present invention；
Fig. 4 is the outer barrel liquid level peephole schematic diagram of biomass type coal adhesive preparation facilities of the present invention.
In figure：Equipment outer cylinder bodies of the 1- with liquid level peephole, 2- is used to prepare the inner cylinder of biomass binding agent, 3- equipment
Top cover, 4- electric control boxes, 5- stretches agitator, 6- electric up-down sieve plates, the modified filtrate discharge pipes of 7-, 8- electrothermal tubes, outside 9-
Cylinder drainpipe, 10- water filling ports, 11- agitator speed control buttons, 12- digital display screens, 13- agitator time switches, 14-
Temperature sets display screen, 15- power switch buttons, 16- sieve plates lifting track, 17- liquid level peepholes.
Specific embodiment
Embodiments of the invention are described further below in conjunction with the accompanying drawings：
As depicted in figs. 1 and 2, biomass type coal adhesive preparation facilities of the invention, including device cylinder and electric-controlled
Case processed 4, device cylinder top is provided with device top cover 3, and wherein device cylinder includes being provided with inner cylinder 2 in outer barrel 1, outer barrel 1, described outer
Cylinder 1 is provided with liquid level peephole 17, and inner cylinder 2 is transparent, high temperature resistant, resistant material, just to the inner cylinder 2 at liquid level peephole 17
Scale measurement volume is provided with, space tank is provided between outer barrel 1 and inner cylinder 2, heater and temperature are provided with the tank of space
Sensor, the heater is the heating tube 8 for being arranged on space bottom of gullet between outer barrel 1 and inner cylinder 2, on device top cover 3
It is provided with water filling port 10, agitator speed control button 11, digital display screen 12 and agitator time switch 13；Water filling port 10 can be with
The effect of water filling and spray is realized, solid portion is removed after the completion of using heavy caliber water filling, binding agent to prepare when inner/outer tube discharges water
Inner cylinder is washed using high-pressure spraying mode afterwards, with double action, device top cover 3 is provided with flexible to extension in inner cylinder 2
Agitator 5, the blade of described flexible agitator 5 is scalable with bar, big by the different adjustment blades of the modification liquid concentration of inner cylinder 2
It is small, it is necessary to bar is stretched when stirring, it is not necessary to bar is shunk when stirring, is provided with electric up-down sieve plate 6 in inner cylinder 2, it is described electronic
Lifting sieve plate 6 can glue according to modified biomass granularity difference and the different sieve plates for changing different pore size of modification degree, biomass
Knot agent can be filtered and separated by lifting sieve plate after the completion of preparing to the modified viscous solid filtered out by sieve plate, electricity
Modified filtrate space is provided between dynamic lifting sieve plate 6 and the bottom of inner cylinder 2, modified filtrate space is provided with and reaches changing outside outer barrel 1
Property filtrate space discharge pipe 7, the side-lower of outer barrel 1 is provided with the outer barrel drainpipe that space tank is connected between outer barrel 1 and inner cylinder 2
9, the electric control box 4 is provided with temperature setting display screen 14 and power switch button 15, electric control box 4 and heater
It is connected with temperature sensor, temperature sensor is used to gather interstitial water trough inner water temperature between outer barrel 1 and inner cylinder 2, and by temperature
Signal is converted to resistance value, amplification by integrated amplifier, compare after, output control signal efficiently controls electric heating tube
Average heating power, make water in the tank of space keep constant temperature, electric control box 4 to be provided with the temperature setting He of display screen 14
Power switch button 15.
As shown in Figure 3：Inner cylinder side wall is provided with after the completion of prepared by sieve plate lifting track 16 binding agent by electric up-down sieve plate 6
Solid sticky part is separated with filtrate.
As shown in Figure 4：The liquid level peephole 17 that outer tube wall side is provided with, liquid level peephole 17 is used to observe inner cylinder 2
The liquid level of reclaimed water, it is ensured that the accuracy of proportioning.
Only it is the preferred embodiment of the present invention described in upper, it should be pointed out that：For the person of ordinary skill of the art,
Under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications should also be as being considered as
Protection scope of the present invention.
A kind of biomass coal adhesive preparation method, its step is as follows：
A. the electric up-down sieve plate 6 in control inner cylinder 2 drops to the bottommost of inner cylinder 2, is noted in inner cylinder 2 by water filling port 10
Water, using the water injection rate in the control inner cylinder 2 of liquid level peephole 17, will be to outer barrel 1 and inner cylinder 2 after water injection rate reaches preset requirement
Between space tank in water filling, stop water filling after water injection rate reaches requirement；
B. heating is carried out to the water in outer barrel 1 so as to be added to inner cylinder 2 using the control heater of electric control box 4
Heat, and by the deployed medicament input inner cylinder 2 than you, the flexible agitator 5 of control stretches out and medicament and water is stirred, and makes
Medicament and water stop stirring after being thoroughly mixed to form mixed solution, in inner cylinder 2 during mixed solution and biomass heating stirring
The vapor of evaporation liquefies after the condensation of top cover 3 and drips back into inner cylinder again, realizes that condensation keeps water loss excessive；
C. after the mixed solution temperature in inner cylinder 2 reaches preset value, top cover 3 is opened according to biomass caking agent formula
Biomass after addition drying and crushing, close top cover 3 and start flexible agitator 5, and control turning for flexible agitator 5 as needed
Speed and mixing time are so that mixed solution and biomass are modified reaction；
D. after flexible agitator 5 is stirred to be stopped, flexible agitator 5 is shunk, starts electric up-down sieve plate 6 by the bottom of inner cylinder 2
Portion is raised above, as electric up-down sieve plate 6 rises the thick solid taking-up that will be left in being filtered on electric up-down sieve plate 6
And load container, do not stayed in inner cylinder 2 by the filtrate that electric up-down sieve plate 6 is filtered out；
E. spray washing liquid is carried out to inner cylinder 2 using water filling port 10, afterwards cleaning solution with do not filtered by electric up-down sieve plate 6
The filtrate fallen is discharged through filtered fluid discharge pipe 7 and uses container collection jointly.
F. end is prepared, outer barrel 1 is discharged with the water conservancy outer barrel drainpipe 9 at the space tank of inner cylinder 2.
As shown in Figure 2：Biomass binding agent preparation facilities of the invention includes device top cover, it is characterised in that：It is right to realize
Effective control of inner/outer tube water filling and flexible agitator.10 is water filling port, it is possible to achieve water filling is put with the effect for spraying, inner/outer tube
Solid portion is washed using spray mode after removing to inner cylinder after the completion of using heavy caliber water filling, binding agent to prepare during water,
Effective protection equipment.11 is agitator speed control button, can set stir speed (S.S.), and 13 is agitator time switch, can be with
Stirring is timed by setting, timing agitation can ensure binder modification more in biomass modified preparation adhesive process
Fully, the parameter of setting is shown on digital display screen.
Example 1：Turn on the power, set heating-up temperature as 80 DEG C are heated, the medicaments such as NaOH, curing agent are thrown by proportioning
After entering inner cylinder 2, start flexible agitator 5 and be stirred, be well mixed solution.1 after the solution temperature of inner cylinder 2 reaches 80 DEG C:
30 solid water is crushed to 2mm and dried maize straw than addition, then covers equipment top cover 3, sets mixing time and is
1.2h, stir speed (S.S.) is 60r/min, and modified-reaction opens equipment top cover 3, shrinks agitator 5 after carrying out 2h, presses power switch
Button 15 closes power supply, starts electric up-down sieve plate 6 and thick solid is moved into special container as sieve plate rises, and then turns on
Water filling port 10 carries out spray washing to inner cylinder 2, and cleaning solution is collected through filtered fluid discharge pipe discharge with special container jointly with filtrate.
According to the biomass modified setting for preparing coal briquette bond technical scheme, liquid is 3 with solid in mass ratio:7 ratio mixing
Prepare specific coal briquette bond.After preparation terminates, the water in outer barrel 1 is discharged through outer barrel drainpipe 9.
Example 2：Water filling port 10 is opened, water filling is carried out to outer barrel 1, turn on the power 15, set heating-up temperature as 80 DEG C are carried out
Heating, is 1% preparation NaOH solution according to concentration, is opened including water filling port, and 2 water filling 90L press flexible agitator 5 and stirred
Mix, be well mixed solution.1 after the solution temperature of inner cylinder 2 reaches 80 DEG C:After 10 solid water is crushed to 2mm and dries than addition
Maize straw 9Kg, then cover equipment top cover 3, setting mixing time is 1.2h, and stir speed (S.S.) is 60r/min, modified-reaction
Equipment top cover 3 is opened after carrying out 2h, magnesia, magnesium chloride, each 9g of sodium metasilicate is added as curing agent, by solution gross mass 1-
3% adds the sulphur-fixing agent compounded by materials such as Ca (OH) 2, CaCO3, Fe2O3, SiO2, Al2O3, opens agitator 5 and stirs
15min, startup power supply shift knob 15 closes power supply, starts electric up-down sieve plate 6 and moves thick solid as sieve plate rises
Enter special container, then turning on 10 mouthfuls of water filling carries out spray washing to inner cylinder, and cleaning solution is common with filtrate through filtered fluid discharge pipe
After discharge is collected with special container, the coal for being crushed to 2mm with 90-180g puts into agitator jointly carries out one kind has energy-saving and emission-reduction
The environment-friendly coal of benefit.Binding agent is prepared after terminating, and the water in outer barrel 1 is discharged through outer barrel drainpipe 9.
Claims (8)
1. a kind of biomass type coal adhesive preparation facilities, it is characterised in that：It includes device cylinder and electric control box (4),
Device cylinder top is provided with device top cover (3), and wherein device cylinder includes being provided with inner cylinder (2), outer barrel in outer barrel (1), outer barrel (1)
(1) space tank is provided with and inner cylinder (2) between, heater and temperature sensor is provided with the tank of space, on device top cover (3)
It is provided with water filling port (10), agitator speed control button (11), digital display screen (12) and agitator time switch (13)；Device
Top cover (3) is provided with flexible agitator (5), inner cylinder (2) to extension in inner cylinder (2) and is provided with electric up-down sieve plate (6), electric up-down
It is provided with modified filtrate space between sieve plate (6) and inner cylinder (2) bottom, modified filtrate space is provided with and reaches outer barrel (1) changing outward
Property filtrate space discharge pipe (7), it is outer that outer barrel (1) side-lower is provided with that the space tank between outer barrel (1) and inner cylinder (2) is connected
Cylinder drainpipe (9), the electric control box (4) is connected with heater and temperature sensor, and temperature sensor is used to gather
Interstitial water trough inner water temperature between outer barrel (1) and inner cylinder (2), and temperature signal is converted into resistance value, by integrated amplifier
After amplifying, comparing, output control signal efficiently controls the average heating power of electric heating tube, protects the water in the tank of space
Constant temperature is held, electric control box (4) has been provided with temperature and has set display screen (14) and power switch button (15).
2. biomass type coal adhesive preparation facilities according to claim 1, it is characterised in that：The heater is to set
Put the heating tube (8) of the space bottom of gullet between outer barrel (1) and inner cylinder (2).
3. biomass type coal adhesive preparation facilities according to claim 1, it is characterised in that：Set on the outer barrel (1)
There is liquid level peephole (17), inner cylinder (2) is transparent, high temperature resistant, resistant material, just to the inner cylinder at liquid level peephole (17) place
(2) it is provided with scale measurement volume.
4. biomass type coal adhesive preparation facilities according to claim 1, it is characterised in that：Described flexible agitator
(5) blade is scalable with bar, by the different adjustment leaf blade sizes of inner cylinder (2) modification liquid concentration, it is necessary to stretch bar when stirring,
Bar is shunk when need not stir.
5. biomass type coal adhesive preparation facilities according to claim 1, it is characterised in that：The electric up-down sieve plate
(6) can be according to modified biomass granularity difference and the different sieve plates for changing different pore size of modification degree, biomass binding agent system
The modified viscous solid filtered out by sieve plate can be filtered and separated by lifting sieve plate after the completion of standby.
6. biomass type coal adhesive preparation facilities according to claim 1, it is characterised in that：Water filling port (10) can be real
Existing water filling and the effect of spray, use heavy caliber water filling, after solid portion is removed after the completion of binding agent preparation when inner/outer tube discharges water
Inner cylinder is washed using high-pressure spraying mode, with double action.
7. a kind of usage right requires the biomass coal adhesive preparation method of 1 described device, it is characterised in that step is as follows：
A. the electric up-down sieve plate (6) in control inner cylinder (2) drops to inner cylinder (2) bottommost, by water filling port (10) to inner cylinder
(2) water filling in, the water injection rate in inner cylinder (2) is controlled using liquid level peephole (17), will be to after water injection rate reaches preset requirement
Water filling in space tank between outer barrel (1) and inner cylinder (2), water filling is stopped after water injection rate reaches requirement；
B. heating is carried out to the water in outer barrel (1) so as to be added to inner cylinder (2) using electric control box (4) control heater
Heat, and by deployed medicament input inner cylinder (2) than you, the flexible agitator (5) of control stretches out and medicament and water is stirred
Mix, medicament is stopped stirring after being thoroughly mixed to form mixed solution with water；
C. after the mixed solution temperature in inner cylinder (2) reaches preset value, top cover (3) is opened according to biomass caking agent formula
Biomass after addition drying and crushing, close top cover (3) and start flexible agitator (5), and control flexible agitator as needed
(5) rotating speed and mixing time is so that mixed solution and biomass are modified reaction；
D. after flexible agitator (5) is stirred to stop, flexible agitator (5) is shunk, starts electric up-down sieve plate (6) by inner cylinder
(2) bottom up rises, as electric up-down sieve plate (6) rises will be left in being filtered on electric up-down sieve plate (6) sticky
Shape solid takes out and loads container, is not stayed in inner cylinder (2) by the filtrate that electric up-down sieve plate (6) is filtered out；
E. spray washing liquid is carried out to inner cylinder (2) using water filling port (10), afterwards cleaning solution with not by electric up-down sieve plate (6) mistake
The filtrate for filtering is discharged through filtered fluid discharge pipe (7) and uses container collection jointly.
F. end is prepared, outer barrel (1) is discharged with the water conservancy at the tank of inner cylinder (2) space with outer barrel drainpipe (9).
8. biomass binding agent preparation method according to claim 7, it is characterised in that：Inner cylinder (2) interior mixed solution and
The vapor evaporated during biomass heating stirring liquefies after top cover (3) condensation and drips back into inner cylinder again, realizes that condensation is protected
Hold water loss excessive.
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| CN111871246A (en) * | 2017-08-04 | 2020-11-03 | 夏尔人类遗传性治疗公司 | Antibody-resin coupling apparatus and method |
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| CN114602353A (en) * | 2022-04-13 | 2022-06-10 | 铜陵瑞莱科技有限公司 | Washing device for obtaining low-viscosity iron oxide yellow |
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