CN104927890B - Bitumen ball aoxidizes infusible scale manufacturing technique and its device - Google Patents
Bitumen ball aoxidizes infusible scale manufacturing technique and its device Download PDFInfo
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- CN104927890B CN104927890B CN201510311977.XA CN201510311977A CN104927890B CN 104927890 B CN104927890 B CN 104927890B CN 201510311977 A CN201510311977 A CN 201510311977A CN 104927890 B CN104927890 B CN 104927890B
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C3/00—Working-up pitch, asphalt, bitumen
- C10C3/02—Working-up pitch, asphalt, bitumen by chemical means reaction
- C10C3/04—Working-up pitch, asphalt, bitumen by chemical means reaction by blowing or oxidising, e.g. air, ozone
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Abstract
It is that bitumen ball is distributed in annular screen frame (1) that a kind of bitumen ball aoxidizes infusible scale manufacturing technique, dolly will be formed by rapid coupler (3) combination between screen frame combination box (4), rotated by scroll bar (8) and first dolly is entered the first storage trolley cabin from pending bit (22), turbine (7) drives annular screen frame (1) rotation by screen frame axle (2), air blast (P) extracts fresh air from inlet manifold (21), make air of each storage trolley space full of preheating, electric boiling plate component (11) is preheating to predetermined temperature, the oxidation of so bitumen ball is not melted and is started；Second pending bit dolly is pushed into the first storage trolley cabin, and first dolly recursion is in the second storage trolley cabin not after the thawing time by predetermined oxidation to be achieved, then is re-started the oxidation of bitumen ball and do not melted, by that analogy.The present invention have can large-scale production, the undamaged advantage of bitumen ball glossiness.
Description
Technical field
The invention belongs to a kind of bitumen ball aoxidizes infusible scale manufacturing technique and its device.
Background technology
Asphalt-base globular active carbon is regular spherical, high carbon left due to its outward appearance so which has higher pressure
Broken intensity and tear strength, are expected to obtain application in numerous areas.But the preparation of spheric active carbon be unable to do without the oxygen of bitumen ball
Changing and not melting, and bitumen ball is spoken of in many patents with regard to bitumen ball and aoxidizes that nonfused method is less, corresponding device is just
Less.
From the point of view of published patent at present, and in particular to the oxidation to bitumen ball is not melted the patent of technology and device and is
The patent of the CN201310227294.7 " bitumen ball aoxidizes non-fusible method " of the present inventor's invention.In that patent, have
It is as follows that method and apparatus is not melted in oxidation：Bitumen ball is put in revolving burner or fixed bed, air is passed through, then necessarily to heat up
Speed from room temperature to uniform temperature after stop a few hours；Afterwards the bitumen ball of the preliminary oxidation is proceeded to thermograde rising
Tunnel cave in aoxidized, obtain the non-fusible bitumen ball of oxidation.During although the patent successfully avoid bitumen blowing
Ignition issues, aoxidize the uniformity of the bitumen ball after not melting and production capacity has obtained a certain degree of improvement, but are limited to be carried
For method and apparatus, it is clear that uniformity and production capacity also have very big room for promotion.Further, since bitumen ball intensity itself is very
The glossiness for making bitumen ball is damaged using revolving burner and is even damaged by difference.
Content of the invention
It is an object of the invention to provide one kind can large-scale production, the undamaged bitumen ball of bitumen ball glossiness aoxidizes not
The scale manufacturing technique of fusing and its device.
The technique of the present invention is realized as follows：
(1), bitumen ball is distributed in bottom screen frame combination box annular screen frame and the screen frame combination box inner ring of belt wheel respectively
In shape screen frame, by between screen frame combination box, between the bottom screen frame combination box of screen frame combination box and belt wheel, pass through rapid coupler
Combination forms dolly；
(2), manual promotion trolley travelling opens push-and-pull separation door and deceleration electricity to the pending bit aoxidized before not thawing apparatus
Machine, and then the scroll bar connected by reducing motor is pushed into propulsion gear, so that claw is engaged each other with scroll bar, at scroll bar and turbine
In disengaged position, first dolly enters the first storage trolley cabin, cuts out push-and-pull separation door from pending bit, air blast is opened,
Electric boiling plate component, temperature indicate control and valve, scroll bar is pushed into rotation gear, engages each other scroll bar and turbine, claw
Disengaged position is in scroll bar, reducing motor M drives worm screw and turbine rotation, turbine drives annular screen frame rotation by screen frame axle
Turn, air blast extracts fresh air from inlet manifold, make air of each storage trolley space full of preheating, electric boiling plate component
Predetermined temperature is preheating to, the oxidation of such bitumen ball is not melted i.e. to start；
(3), predetermined oxidation to be achieved is closed electric rotating machine, opens all push-and-pull separation doors, afterwards not after the thawing time
Motor is pushed into propulsion and gear opens, and second pending bit dolly is pushed into the first storage trolley cabin, and first dolly recursion
To in the second storage trolley cabin, simultaneously close off all push-and-pull separation doors, switch motor is to rotating gear again, then reopen into
The valve that gas is in charge of, is passed through predetermined air capacity, carries out pitch in the first storage trolley cabin and the second storage trolley cabin respectively
The oxidation of ball is not melted；
(4), until dolly is released material by last storage trolley cabin and is and completes after oxidation do not melt
Bitumen ball product, after the dolly discharging that every time last storage trolley cabin is released, refills raw material and is pushed into pending bit by hand and enters the
One storage trolley cabin, so operates continuously and terminates to batches；
(5), shutdown phase is entered after the completion of batches input, dolly only export but no import, the stage start from first and deposit
Put little cabin and sky is walked, and end at last storage trolley cabin and sky is walked, close whole valves, reducing motor, air blast, electric boiling plate
Component and temperature indicate control.
The temperature in the first storage trolley cabin as above is 60-80 DEG C, and the temperature in last storage trolley cabin is 260-280
℃；Each cabin temperature between first storage trolley cabin and last storage trolley cabin is elevated successively, namely different little cabin set
Determine and run on different temperature.Adjacent several cabins can be identical or different temperature.
The time of staying in each storage trolley cabin is 0.5-2h as above；Dolly as above is through each storage cabin
The time required to the time of staying is homogeneous, and each cabin covered by dolly, summation is determined by process conditions.
The air capacity in each storage trolley cabin per kilogram bitumen ball 1.5-5.0m on an hourly basis as above3It is passed through, wherein
The hot-air come by previous stage heat chamber accounts for the 1/2-2/3 for being always passed through tolerance, and remainder fills into fresh air；
The sphere diameter of bitumen ball as above is between 0.1-1.2mm.
In order to the object of the invention is realized, a kind of non-fusible device of oxidation is devised, it includes dolly, dynamical system, body of heater,
Push-and-pull separation door, electric boiling plate, enter system of giving vent to anger, it is characterised in that dolly includes annular screen frame, screen frame axle, rapid coupler,
Screen frame combination box, the bottom screen frame combination box of belt wheel and turbine, screen frame combination box are no less than 2, have annular screen frame, ring in which
Shape screen frame is connected with the screen frame axle for being located at screen frame combination box center, and is rotated with screen frame axle together, the lower end of top screen frame axle
Hollow upper half a coupler is fixed with, the lower half a coupler with post core is connected to the upper end of lower floor's screen frame axle, the like, it is located at
There is card one end that there is turbine, the bottom screen frame combination box bottom of belt wheel the lower end of the screen frame axle of the bottom screen frame combination box of belt wheel
Pawl, by the flexible connection of screen frame combination box circumferential side frame, the bottom screen frame combination box of belt wheel and upper strata screen frame between screen frame combination box
It is flexibly connected by circumferential side frame between combination box, body of heater has push-and-pull separation door in front and back, in front and back structure between body of heater and push-and-pull separation door
Become storage trolley cabin, the storage trolley cabin has no less than 10, is connected to electric boiling plate, Qian Houlu in front and back on furnace body outer wall
Internal wall has cloth wind chamber respectively；Dynamical system includes bearing block assembly, turbine, worm screw, claw, the fortune of reducing motor M and belt wheel
Moving platform, bearing block assembly support worm screw two ends, and bearing block assembly is located on the motion platform of belt wheel, the motion platform of belt wheel
It is located on basis, turbine is connected by rotating gear with worm screw, claw is connected by advancing gear with worm screw；Enter system of giving vent to anger
It is in charge of including giving vent to anger, air inlet is in charge of, valve, blowdown pipe, engine manifold, inlet manifold, cloth wind chamber, temperature indicates control and air blast
Machine, has air inlet to be in charge of connection air blast and valve on the rear furnace body in last storage trolley cabin, and blower inlet is total with air inlet
Pipe connects, and blower outlet is communicated with cloth wind chamber through valve, gives vent to anger and be in charge of on the front furnace body in last storage trolley cabin
Connection air blast and valve, blower inlet are connected with two valves respectively, and a valve is connected with the cloth wind chamber of front furnace body,
Another valve blowdown pipe by being connected with inlet manifold, blower outlet respectively with engine manifold and above storage trolley cabin
Front furnace body cloth wind chamber connection, positioned above storage trolley space rear furnace body side fan inlet respectively pass through valve
Men Yubu wind chamber and blowdown pipe connection, blowdown pipe is connected with inlet manifold, positioned at the rear furnace body side in above storage trolley cabin
Air blast gas outlet is connected with engine manifold and above the cloth wind chamber of the rear furnace body in storage trolley cabin respectively, the like, it is located at
The air blast gas outlet in the first storage trolley cabin is only connected with engine manifold, and temperature indicates that control is indicated and controls storage trolley empty
Between temperature.
Screen frame combination box as above is 2-20.
Storage trolley cabin as above is 10-15.
Rapid coupler as above is made up of hollow upper half a coupler and the lower half a coupler with post core, works as screen frame
When piling up, the post core of the lower half a coupler with post core play the guiding role, and causes concentric and firm with each axle in dolly.
It can be electric synchronous that push-and-pull separation door as above is opened, Pneumatic synchronous, or many operators
Member Each performs its own functions and almost synchronization push-and-pull.The same plate of push-and-pull separation door, a pair of push-and-pull separation door just stop per lobe
Half range passage, two lobes just align closed channel.
Advantages of the present invention：
1 this patent is due to employing the rotation of material so that the volume of equipment can be amplified according to capacity requirements, then plus
On can also substep continuous feed, therefore its production capacity is remarkably enhanced so that preparation is not melted in the scale oxidation of bitumen ball
Become a reality；
2 due to employing the method that screen frame holds bitumen ball so that bitumen ball itself does not occur any motion, so no longer
Stand collision between bitumen ball each other, abrasion so that the surface gloss of bitumen ball after oxidation is not melted is maintained original
The gloss of material, it is ensured which is attractive in appearance beautiful；
3, due to the circular screen frame of employing, filling finite thickness of such bitumen ball in every layer of screen frame, can so prevent pitch
Ball is in oxidation not catching fire in melting process, while also being fully contacted beneficial to air and bitumen ball, makes bitumen ball realization more equal
Even oxidation is not melted；
The method that 4 this patents enter next stage low temperature chamber using the part hot-air of upper level heat chamber, can be greatly reduced
Heating energy consumption and air consumption；
5 can be by technique initialization due to the temperature in adjacent each cabin, and such bitumen ball is in the stop of a certain temperature range
Between can extend, bitumen ball can be met and aoxidize nonfused requirement, improve its nonfused uniformity of oxidation.
Description of the drawings
Fig. 1 is the positive structure schematic of apparatus of the present invention.
Fig. 2 is the overlooking the structure diagram of apparatus of the present invention.
Fig. 3 is I-I partial structural diagram of the present invention.
Fig. 4 is П-П partial structural diagram of the present invention.
As illustrated, 1 be annular screen frame 2 be screen frame axle 3 be rapid coupler 4 be screen frame combination box 5 be push-and-pull separation door 6
It is the bottom screen frame combination box of belt wheel, 7 is turbine, 8 is worm screw, 9 is to give vent to anger to be in charge of, 10 is that air inlet is in charge of, and 11 is electric boiling plate
Component, 12 is valve, and 13 is blowdown pipe, and 14 is cloth wind chamber, and 15 is bearing block assembly, and 16 is the motion platform of belt wheel, and 17 is base
Plinth, 18 is claw, and 19 is body of heater, and 20 is engine manifold, and 21 is inlet manifold, and 22 is pending bit, and M is reducing motor, and TIC is temperature
Degree indicates control, and P is air blast, and III is rotation gear, and IV is propulsion gear.
Specific embodiment
In embodiment, bitumen ball aoxidizes non-fusible degree and can calculate by bonding rate：Non-fusible bitumen ball will be aoxidized in N2Atmosphere
In be warmed up to 800 DEG C after stop 1h, obtain charing bitumen ball；The bitumen ball after 30-50 charing is randomly selected, is adhered to each other
Total number of particles account for total particle number percentage be bonding rate.
Embodiment 1
A kind of non-fusible device of oxidation, it includes dolly, dynamical system, body of heater 19, push-and-pull separation door 5, electric boiling plate 11,
Enter system of giving vent to anger, it is characterised in that dolly includes annular screen frame 1, screen frame axle 2, rapid coupler 3, screen frame combination box 4, belt wheel
Bottom screen frame combination box 6 and turbine 7, screen frame combination box 4 are 4, have annular screen frame 1 which in, annular screen frame 1 with positioned at screen frame group
The screen frame axle 2 at 4 center of mould assembling connects, and is rotated with screen frame axle 2 together, and the lower end of top screen frame axle 2 is fixed with hollow upper
Half a coupler 3b, the lower half a coupler 3a with post core are connected to the upper end of lower floor screen frame axle 2, the like, positioned at the bottom of belt wheel
There is claw 18 one end that there is turbine 7,6 bottom of bottom screen frame combination box of belt wheel the lower end of the screen frame axle 2 of layer screen frame combination box 6,
It is flexibly connected by 4 circumferential side frame of screen frame combination box between screen frame combination box 4, bottom screen frame combination box 6 and the upper strata screen frame of belt wheel
It is flexibly connected by circumferential side frame between combination box 4, body of heater 19 has push-and-pull separation door 5 in front and back, in front and back body of heater 19 and push-and-pull separation door 5
Between constitute storage trolley cabin, the storage trolley cabin has 10, is connected to electric boiling plate 11 in front and back on 19 outer wall of body of heater, front
19 inwall of rear furnace body has cloth wind chamber 14 respectively；Dynamical system includes bearing block assembly 15, turbine 7, worm screw 8, claw 18, deceleration electricity
The motion platform 16 of machine M and belt wheel, bearing block assembly 15 support 8 two ends of worm screw, and bearing block assembly 15 is located at the motion of belt wheel and puts down
On platform 16, the motion platform 16 of belt wheel is located on basis 17, and turbine 7 is connected by rotating gear III with worm screw 8, claw
18 are connected by advancing gear IV with worm screw 8；Enter the system of giving vent to anger and include to give vent to anger to be in charge of 9, air inlet is in charge of 10, valve 12, blowdown pipe
13, engine manifold 20, inlet manifold 21, cloth wind chamber 14, and temperature indicates control TIC and air blast P, in last storage trolley cabin
Air inlet is had to be in charge of 10 connection air blast P and valve 12 on rear furnace body 19, air blast P air inlet is connected with inlet manifold 21, air blast
Machine P air outlet is communicated with cloth wind chamber 14 through valve 12, gives vent to anger and be in charge of 10 companies on the front furnace body 19 in last storage trolley cabin
Air blast P and valve 12 is connect, air blast P air inlet is connected with two valves 12 respectively, the cloth of a valve 12 and front furnace body 19
Wind chamber 14 connects, and, by being connected with inlet manifold 21, air blast P air outlet is total with tail gas respectively for another 12 blowdown pipe 13 of valve
The cloth wind chamber 14 of the front furnace body 19 in pipe 20 and above storage trolley cabin connects, positioned at the rear furnace body 19 1 in above storage trolley space
The air blast P air inlet of side is connected with cloth wind chamber 14 and blowdown pipe 13 by valve 12 respectively, blowdown pipe 13 and inlet manifold 21,
Be located at the air blast P gas outlet of above 19 side of rear furnace body in storage trolley cabin respectively with engine manifold 20 and above storage trolley
The cloth wind chamber 14 of the rear furnace body 19 in cabin connects, the like, positioned at air blast P gas outlet and the tail gas in the first storage trolley cabin
House steward 20 connects, and temperature indicates that control TIC indicates and control the temperature in storage trolley space.
(1), bitumen ball is distributed in respectively in the 6 annular screen frame 1 of bottom screen frame combination box and screen frame combination box 4 of belt wheel
In annular screen frame 1, by between screen frame combination box 4, pass through between the bottom screen frame combination box 6 of screen frame combination box 4 and belt wheel quick
The combination of shaft coupling 3 forms dolly；
(2), manual promotion trolley travelling is opened push-and-pull separation door 5 and is subtracted to the pending bit 22 aoxidized before not thawing apparatus
Speed motor M, and then the scroll bar 8 connected by reducing motor M is pushed into propulsion gear IV, so that claw 18 is engaged each other with scroll bar 8,
Scroll bar 8 and turbine 7 are in disengaged position, and first dolly enters the first storage trolley cabin, cuts out push-and-pull separation from pending bit
Door 5, opens air blast P, and electric boiling plate component 11, temperature indicate control TIC and valve 12, scroll bar 8 is pushed into rotation gear
III, engages each other scroll bar 8 and turbine 7, and claw 18 is in disengaged position with scroll bar 8, and reducing motor M drives worm screw 8 and turbine
7 rotations, turbine 7 drive annular screen frame 1 to rotate by screen frame axle, and air blast P extracts fresh air from inlet manifold 21, makes each
Air of the storage trolley space full of preheating, electric boiling plate component 11 are preheating to predetermined temperature, and the oxidation of such bitumen ball is not melted
Change i.e. to start；
(3), predetermined oxidation to be achieved is closed electric rotating machine M, opens all push-and-pull separation doors 5 not after the thawing time, it
Rear motor M is pushed into propulsion and gear IV opens, and second pending bit dolly is pushed into the first storage trolley cabin, and first dolly
Recursion simultaneously closes off all push-and-pull separation doors 5 in the second storage trolley cabin, and switch motor M extremely rotates gear III again, then
The valve 12 that air inlet is in charge of on 10 is reopened, predetermined air capacity is passed through, carry out the first storage trolley cabin and second respectively and deposit
The oxidation for putting bitumen ball in little cabin is not melted；
(4), until dolly is released material by last storage trolley cabin and is and completes after oxidation do not melt
Bitumen ball product, after the dolly discharging that last storage trolley cabin is released every time, refills raw material and is pushed into pending bit 22 by hand and enters
First storage trolley cabin, so operates continuously and terminates to batches；
(5), shutdown phase is entered after the completion of batches input, dolly only export but no import, the stage start from first and deposit
Put little cabin and sky is walked, and end at last storage trolley cabin and sky is walked, whole valves 12 are closed, reducing motor M, air blast P, electricity add
Hot plate component 11 and temperature indicate control TIC.
The temperature in described storage trolley cabin is 60 DEG C, and the temperature in last storage trolley cabin is 280 DEG C, and remaining respectively deposits little
The temperature of cabin is shown in Table 1.The time of staying of the dolly through each storage cabin is shown in Table 1
The air capacity in described each storage trolley cabin is passed through by table 1, and the hot-air come wherein by previous stage heat chamber is accounted for
Always it is passed through tolerance and 1 is shown in Table, remainder fills into fresh air；
The sphere diameter of described bitumen ball does not melt in the oxidation of 0.1mm, 10kg bitumen ball, and each cabin time of staying is 0.5h,
The each cabin technological parameter of table 1：
The bonding rate for aoxidizing products obtained therefrom after not melting is 0.8%.
Embodiment 2
Storage trolley cabin has 13, and screen frame combination box 4 is 10, and remaining is with embodiment 1.
Method according to embodiment carries out the oxidation of the 50kg bitumen ball of 0.5mm and does not melt, and each cabin time of staying is 0.5h,
Each cabin technological parameter such as table 2：
The bonding rate for aoxidizing products obtained therefrom after not melting is 0.6%.
Embodiment 3
Storage trolley cabin has 15, and screen frame combination box 4 is 15, and remaining is with embodiment 1.
Method according to embodiment carries out the oxidation of the 20kg bitumen ball of 1mm and does not melt, and each cabin time of staying is 1h, each cabin
Technological parameter such as table 3：
The bonding rate for aoxidizing products obtained therefrom after not melting is 0.5%.
Embodiment 4
Storage trolley cabin has 15, and screen frame combination box 4 is 20, and remaining is with embodiment 1.
Method according to embodiment carries out the oxidation of the 30kg bitumen ball of 1.2mm and does not melt, and each cabin time of staying is 1.5h,
Each cabin technological parameter such as table 4：
The bonding rate for aoxidizing products obtained therefrom after not melting is 0.7%.
Embodiment 5
Storage trolley cabin has 11, and screen frame combination box 4 is 10, and remaining is with embodiment 1.
Method according to embodiment carries out the oxidation of the 100kg bitumen ball of 0.8mm and does not melt, and each cabin time of staying is 2h,
Each cabin technological parameter such as table 5：
The bonding rate for aoxidizing products obtained therefrom after not melting is 0.4%.
Claims (12)
1. a kind of bitumen ball aoxidizes infusible scale manufacturing technique, it is characterised in that comprise the steps of：
(1), bitumen ball is distributed in bottom screen frame combination box (6) annular screen frame (1) and the screen frame combination box (4) of belt wheel respectively
In annular screen frame (1), by between screen frame combination box (4), bottom screen frame combination box (6) of screen frame combination box (4) and belt wheel it
Between by rapid coupler (3) combination form dolly；
(2), manual promotion trolley travelling is opened push-and-pull separation door (5) and is subtracted to the pending bit (22) aoxidized before not thawing apparatus
Speed motor (M), and then the scroll bar (8) connected by reducing motor (M) is pushed into propulsion gear (IV), makes claw (18) and scroll bar
(8) engage each other, scroll bar (8) and turbine (7) are in disengaged position, first dolly is entered first from pending bit (22) and is deposited
Little cabin, close push-and-pull separation door (5), open air blast ((P)), electric boiling plate component (11), temperature indicate control (TIC) and
Valve (12), scroll bar (8) is pushed into rotation gear (III), engages each other scroll bar (8) and turbine (7), claw (18) and scroll bar
(8) disengaged position is in, reducing motor (M) drives worm screw (8) and turbine (7) rotation, turbine (7) is driven by screen frame axle (2)
Annular screen frame (1) rotates, and air blast (P) extracts fresh air from inlet manifold (21), makes each storage trolley space full of pre-
The air of heat, electric boiling plate component (11) are preheating to predetermined temperature, and the oxidation of such bitumen ball is not melted i.e. to start；
(3), predetermined oxidation to be achieved is closed electric rotating machine (M), opens all push-and-pull separation door (5) not after the thawing time, it
Rear motor (M) is pushed into propulsion gear and (IV) opens, and second pending bit dolly is pushed into the first storage trolley cabin, and first
Dolly recursion simultaneously closes off all push-and-pull separation door (5) in the second storage trolley cabin, and switch motor (M) is to rotation shelves again
Position (III), then the valve (12) that air inlet is in charge of on (10) is reopened, predetermined air capacity is passed through, carries out the first storage respectively
In little cabin and the second storage trolley cabin, the oxidation of bitumen ball is not melted；
(4), the like, until dolly releases material by last storage trolley cabin as completes the pitch after oxidation is not melted
Ball product, after the dolly discharging that every time last storage trolley cabin is released, refills raw material and is pushed into pending bit by hand and enters first and deposit
Little cabin is put, is so operated continuously and terminates to batches；
(5), when batches input after the completion of enter shutdown phase, dolly only export but no import, it is little that the stage starts from the first storage
Cabin walks sky, and ends at last storage trolley cabin and walk sky, closes whole valve (12), reducing motor (M), air blast (P), electricity
Heating board assembly (11) and temperature indicate control (TIC).
2. a kind of bitumen ball aoxidizes infusible scale manufacturing technique as claimed in claim 1, it is characterised in that described
It is identical or different temperature that each cabin temperature between first storage trolley cabin and last storage trolley cabin is adjacent cabin.
3. a kind of bitumen ball aoxidizes infusible scale manufacturing technique as claimed in claim 2, it is characterised in that described
The temperature in the first storage trolley cabin is 60-80 DEG C, and the temperature in last storage trolley cabin is 260-280 DEG C；First storage trolley cabin
Each cabin temperature between last storage trolley cabin is elevated successively.
4. a kind of bitumen ball aoxidizes infusible scale manufacturing technique as claimed in claim 1, it is characterised in that described
The time of staying in each storage trolley cabin is 0.5-2h.
5. a kind of bitumen ball aoxidizes infusible scale manufacturing technique as claimed in claim 1, it is characterised in that described
The air capacity in each storage trolley cabin per kilogram bitumen ball 1.5-5.0m on an hourly basis3It is passed through.
6. a kind of bitumen ball aoxidizes infusible scale manufacturing technique as claimed in claim 5, it is characterised in that air capacity
Be by previous stage heat chamber and come hot-air account for the 1/2-2/3 for being always passed through tolerance, remainder fills into fresh air.
7. a kind of bitumen ball aoxidizes infusible scale manufacturing technique as claimed in claim 1, it is characterised in that described
The sphere diameter of bitumen ball is between 0.1-1.2mm.
8. one kind aoxidizes non-fusible device, and it includes dolly, dynamical system, body of heater (19), push-and-pull separation door (5), electric boiling plate
(11), enter system of giving vent to anger, it is characterised in that dolly includes annular screen frame (1), screen frame axle (2), rapid coupler (3), screen frame group
Mould assembling (4), bottom screen frame combination box (6) of belt wheel and turbine (7), screen frame combination box (4) is no less than 2, has annular in which
Screen frame (1), annular screen frame (1) are connected with the screen frame axle (2) for being located at screen frame combination box (4) center, and are turned with screen frame axle (2) together
Dynamic, the lower end of top screen frame axle (2) is fixed with hollow upper half a coupler (3b), the connection of the lower half a coupler (3a) with post core
In the upper end of lower floor's screen frame axle (2), the like, the lower end positioned at the screen frame axle (2) of bottom screen frame combination box (6) of belt wheel has
Turbine (7), one end of bottom screen frame combination box (6) bottom of belt wheel have claw (18), by screen frame group between screen frame combination box (4)
Mould assembling (4) circumferential side frame is flexibly connected, by surrounding between bottom screen frame combination box (6) of belt wheel and upper strata screen frame combination box (4)
Frame is flexibly connected, and body of heater (19) has push-and-pull separation door (5) in front and back, is constituted in front and back between body of heater (19) and push-and-pull separation door (5)
Storage trolley cabin, the storage trolley cabin have no less than 10, are connected to electric boiling plate (11) in front and back on body of heater (19) outer wall,
Body of heater (19) inwall has cloth wind chamber (14) respectively in front and back；Dynamical system includes bearing block assembly (15), turbine (7), worm screw (8),
Claw (18), the motion platform (16) of reducing motor M and belt wheel, bearing block assembly (15) support worm screw (8) two ends, bearing block group
Part (15) is located on the motion platform (16) of belt wheel, and the motion platform (16) of belt wheel is located on basic (17), turbine (7) with
Worm screw (8) is connected by advancing gear (IV) with worm screw (8) by rotating gear (III) connection, claw (18)；Enter to give vent to anger and be
System includes to give vent to anger to be in charge of (9), and air inlet is in charge of (10), valve (12), blowdown pipe (13), engine manifold (20), inlet manifold (21),
Cloth wind chamber (14), temperature indicate control (TIC) and air blast (P), have air inlet on the rear furnace body (19) in last storage trolley cabin
It is in charge of (10) connection air blast (P) and valve (12), air blast (P) air inlet is connected with inlet manifold (21), and air blast (P) goes out
Air port is communicated with cloth wind chamber (14) through valve (12), gives vent to anger and be in charge of (10) on the front furnace body (19) in last storage trolley cabin
Connection air blast (P) and valve (12), air blast (P) air inlet are connected with two valves (12) respectively, a valve (12) and
Cloth wind chamber (14) connection of front furnace body (19), another valve (12) blowdown pipe (13) are roused by being connected with inlet manifold (21)
Blower fan (P) air outlet is connected with engine manifold (20) and above the cloth wind chamber (14) of the front furnace body (19) in storage trolley cabin respectively,
Air blast (P) air inlet of above rear furnace body (19) side in storage trolley space is located at respectively by valve (12) and cloth wind chamber
(14) connect with blowdown pipe (13), blowdown pipe 13 is connected with inlet manifold (21), positioned at the rear furnace body in above storage trolley cabin
(19) air blast (P) gas outlet of side respectively with engine manifold (20) and the above cloth wind of the rear furnace body (19) in storage trolley cabin
Chamber (14) connects, the like, air blast (P) gas outlet positioned at the first storage trolley cabin is only connected with engine manifold (20),
Temperature indicates that control (TIC) indicates and control the temperature in storage trolley space.
9. one kind as claimed in claim 8 aoxidizes non-fusible device, it is characterised in that described screen frame combination box (4) is 2-20
Individual.
10. one kind as claimed in claim 8 aoxidizes non-fusible device, it is characterised in that described storage trolley cabin is 10-15
Individual.
11. one kind as claimed in claim 8 aoxidize non-fusible device, it is characterised in that described rapid coupler (3) is by sky
The upper half a coupler (3b) of the heart and the composition of the lower half a coupler (3a) with post core.
12. one kind as claimed in claim 8 aoxidize non-fusible device, it is characterised in that described push-and-pull separation door (5) is opened
It is electric synchronous, Pneumatic synchronous, or operating personnel's synchronization push-and-pull.
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1186043A (en) * | 1996-12-24 | 1998-07-01 | 中国科学院山西煤炭化学研究所 | Method for producing activated carbon with high specific surface area from asphalt |
| CN103272533A (en) * | 2013-06-08 | 2013-09-04 | 中国科学院山西煤炭化学研究所 | Pitch sphere oxidative stabilization method |
| CN103663410A (en) * | 2013-11-25 | 2014-03-26 | 陕西煤业化工技术研究院有限责任公司 | Ultrasonic atomization method and device for preparing mesocarbon microbeads |
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| US7998376B2 (en) * | 2008-02-06 | 2011-08-16 | Honeywell International Inc. | Method for reducing variability in friction performance |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1186043A (en) * | 1996-12-24 | 1998-07-01 | 中国科学院山西煤炭化学研究所 | Method for producing activated carbon with high specific surface area from asphalt |
| CN103272533A (en) * | 2013-06-08 | 2013-09-04 | 中国科学院山西煤炭化学研究所 | Pitch sphere oxidative stabilization method |
| CN103663410A (en) * | 2013-11-25 | 2014-03-26 | 陕西煤业化工技术研究院有限责任公司 | Ultrasonic atomization method and device for preparing mesocarbon microbeads |
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