CN102561140B - Method for making molding powder and gravel road, and appliance therefor - Google Patents
Method for making molding powder and gravel road, and appliance therefor Download PDFInfo
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- CN102561140B CN102561140B CN201110372386.5A CN201110372386A CN102561140B CN 102561140 B CN102561140 B CN 102561140B CN 201110372386 A CN201110372386 A CN 201110372386A CN 102561140 B CN102561140 B CN 102561140B
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Abstract
The invention discloses a method for making a molding powder and gravel road. The method comprises the following steps of: crushing white waste materials and chemical fibers which are sorted from urban garbage waste materials into fragments, of which the diameters are 3 to 5 centimeters; grinding the fragments into molding powder and chemical fiber powder of 40 to 60 meshes; mixing the ground molding powder and chemical fiber powder, wherein the mixture of the molding powder and the chemical fiber powder comprises 60 to 70 weight percent of molding powder, 25 to 30 weight percent of chemical fiber powder and 5 to 10 weight percent of impurities; sorting and crushing urban building garbage, industrial waste slag, stone blocks and ceramic into gravels, of which the diameters is 0.5 to 1.5 centimeters; controlling the weight ratio (kilogram) of the mixture of the molding powder to the chemical fiber powder to the gravels to be 1:(9-1.5):8.5; mixing the molding powder, the chemical fiber powder and the gravels by a molding powder, chemical fiber powder and gravel synthesizer module; conveying the mixed molding powder, chemical fiber powder and gravel to the construction site through a special heat preservation truck; and paving the molding powder and gravel road by the mixed molding powder, chemical fiber powder and gravel at the temperature of between 150 and 180 DEG C.
Description
Technical field the present invention relates to and a kind ofly utilizes waste plastics, useless chemical fibre material, give up in paper mill the garbage waste abrasive dust moulding the cities such as woollen mixes the method for laying highway with stone.
The process of background technology municipal refuse waste material is the difficult problem in urban development process always, and the way of common disposal of refuse is sent to dumping area after collecting, or incinerate with incinerator.But both all can the problem of manufacturing environment protection, the garbage disposal in dumping area is improper can polluted underground water and stinking, and a lot of city can be fewer and feweri for the area of landfill.Incinerate and then inevitably produce toxic gas, harm organism.Municipal refuse waste material can be allowed to turn waste into wealth, and benign cycle utilizes, and is the development trend in municipal refuse waste treatment process.
Summary of the invention is in order to overcome shortcomings and deficiencies of the prior art part, the invention provides the method for production of a kind of molding powder, stone highway, the molding powder be laid to, stone highway are compared with bituminous highway, and equipment investment is little, technique is simple, good waterproof performance, lays the material source of highway in city mineral products waste material, building waste etc., energy-conserving and environment-protective, recycled by processing waste material, turn waste into wealth, solve a difficult problem for waste disposal in municipal refuse.
The present invention for the technical scheme realizing goal of the invention and provide is:
The method for production of a kind of molding powder, stone highway: 1, by broken to the white waste material, the chemical fibre that sub-elect in municipal refuse waste material, be broken into the particle of 3-5CM, then particle worn into 40-60 object molding powder, chemical fibre powder, by the molding powder after abrasive dust, the mixing of chemical fibre powder, molding powder 60%-70% by weight percentage in mixed molding powder, chemical fibre powder, chemical fibre powder 25%-30%, impurity 5%-10%, the building waste in city, industrial residue, stone, ceramic sorting are broken into the stone particle of 0.5cm, 0.5cm-1.5cm, 1.5cm-3cm, by electronic scale and flow measuring unit, the molding powder of mixing, chemical fibre powder are controlled at 1:9 to 1.5:8.5 with the weight of stone by a kilogram ratio, 2, by mixed molding powder, chemical fibre powder is transported to molding powder, the mixed loader of chemical fibre powder height, molding powder, chemical fibre powder is through hopper, discharging opening is transported to by loader, entering high mixing through discharging opening stirs in glassware, the high mixed oil inlet pipe stirring glassware warp and be connected with high temperature oil oven, oil return pipe is heated, controlling electronic valve by sensor makes temperature control at 90 DEG C-110 DEG C, high mixed stir glassware and be provided with exhaust opening, high mixed stir glassware be uniformly mixed after molding powder, molding powder in the process of chemical fibre powder, moisture in chemical fibre powder is discharged by exhaust opening, molding powder after humidity discharging, chemical fibre powder enters heated type loader by pneumatic type discharging opening, the oil inlet pipe of heated type loader through being connected with high temperature oil oven, oil return pipe is heated, controlling electronic valve by sensor makes temperature control at 90 DEG C-110 DEG C, double-axle stirrer is being transported to through heated type loader, the outlet of heated type loader is provided with vibrosieve, double-axle stirrer outside connects the oil inlet pipe be connected with high temperature oil oven, oil return pipe, and heat-preservation guard shield, double-axle stirrer makes temperature control at 180 DEG C-220 DEG C by sensor Controlling solenoid valve, at molding powder, while the mixed loader of chemical fibre powder height runs, stone particle through first step processing is sent in stone High Temperature Rotating kiln, stone is heated to 220 DEG C-240 DEG C by stone High Temperature Rotating kiln, stone after heating sends into heated type loader by self-emptying mouth, temperature in heated type loader remains on 220 DEG C-240 DEG C, stone is transported to double-axle stirrer through heated type loader, 3, mixed molding powder, chemical fibre powder are through vibrosieve and stone Homogeneous phase mixing, and need not any additive in mixed process, after the mixing of molding powder, chemical fibre powder, stone, the high temperature of stone makes molding powder, chemical fibre powder dissolves, molding powder, chemical fibre powder and stone are integrated, the below of double-axle stirrer is provided with storage bin, is provided with pressure and temp control valve below storage bin, 4, after storage bin is filled with, after mixing, molding powder, chemical fibre powder, stone are controlled by pressure and temp control valve, special-purpose thermal insulation car is entered through self-emptying mouth, mixed molding powder, chemical fibre powder, stone are transported to job site through special-purpose thermal insulation car, ensure that mixed molding powder, chemical fibre powder, stone temperature lay molding powder, stone highway at 150 DEG C-180 DEG C.
A kind of molding powder, stone synthesizer unit, comprise molding powder, the mixed loader of chemical fibre powder height, stone High Temperature Rotating kiln, double-axle stirrer, molding powder, the mixed loader of chemical fibre powder height is provided with hopper, hopper connects loader, be provided with high mixing below pneumatic type discharging opening and stir glassware, high mixed stir glassware and be provided with exhaust opening, outside is provided with oil-feed, return line, sensor, oil-feed, return line is connected with high temperature oil oven, high mixed stirring below glassware discharging opening has heated type loader, be provided with outside heated type loader and be connected oil-feed with high temperature oil oven, return line, the outlet of heated type loader is provided with vibrosieve, double-axle stirrer is provided with below heated type loader discharging opening, stone High Temperature Rotating kiln is provided with charging aperture, sensor, self-emptying mouth, heated type loader is provided with below self-emptying mouth, double-axle stirrer is provided with below heated type loader discharging opening, there is the oil inlet pipe connecting high temperature oil oven double-axle stirrer outside, oil return pipe, and heat-preservation guard shield, the below of double-axle stirrer is provided with storage bin, pressure and temp control valve is provided with below storage bin.
The invention has the advantages that: lay molding powder, chemical fibre powder, stone highway, the material source such as molding powder, chemical fibre powder, stone used is in municipal refuse waste material, and need not any additive in molding powder, chemical fibre powder and stone mixed process, without glue, formaldehydeless, compared with equal bituminous highway, cost of production is low, asphalt price: 2300 yuan-5000 yuan/ton, and the waste plastics that refuse classification goes out, useless chemical fibre material, paper mill is useless moulds woollen and reclaims direct abrasive dust about 1000-1800 yuan/ton; Bituminous highway, stone require purity high, Su Shi highway, stone is less demanding, in building waste, brick, watt, the above particle of stone 0.5cm; Pitch in process of production, must make pitch flow by high temperature, and with high-temperature high pressure pump pitch ejection and stone mix lubricant one, asphalt high-temperature produces gas has harm to human body.Molding powder, chemical fibre powder just mix with stone after mixing humidity discharging, utilize that the high temperature of stone makes molding powder, chemical fibre powder dissolves, with stone be integrated molding powder, chemical fibre powder fusion temperature only have about 200 DEG C, without excitatory smell, can shut down at any time, need not clear up.
Description of drawings 1 is molding powder, stone synthesizer set structure schematic diagram;
Fig. 2 is the structural representation of high temperature oil oven of the present utility model.
In figure 1, hopper; 2, loader; 3, discharging opening; 4, high mixed agitator; 5, high temperature oil oven; 6, oil inlet pipe; 7, oil return pipe; 8, sensor; 9, exhaust opening; 10, special-purpose thermal insulation car; 11, pneumatic type discharging opening; 12, heated type loader; 13, stone High Temperature Rotating kiln; 14, self-emptying mouth; 15, storage bin.
Detailed description of the invention 1, the white waste material by sub-electing in municipal refuse waste material, chemical fibre fragmentation, be broken into the particle of 3-5CM, then particle worn into 40-60 object molding powder, chemical fibre powder, by the molding powder after abrasive dust, the mixing of chemical fibre powder, molding powder 60%-70% by weight percentage in mixed molding powder, chemical fibre powder, chemical fibre powder 25%-30%, impurity 5%-10%, the building waste in city, industrial residue, stone, ceramic sorting are broken into the stone particle of 0.5cm, 0.5cm-1.5cm, 1.5cm-3cm, by electronic scale and flow measuring unit, the molding powder of mixing, chemical fibre powder are controlled at 1:9 to 1.5:8.5 with the weight of stone by a kilogram ratio, 2, by mixed molding powder, chemical fibre powder is transported to molding powder, the mixed loader of chemical fibre powder height, molding powder, chemical fibre powder is through hopper 1, discharging opening 3 is transported to by loader 2, entering high mixing through discharging opening 3 stirs in glassware 4, the high mixed oil inlet pipe 6 stirring glassware 4 and connect through high temperature oil oven 5, oil return pipe 7 is heated, controlling electronic valve by sensor 8 makes temperature control at 110 DEG C, high mixed stir glassware 4 and be provided with gas port 9, the high mixed molding powder stirring glassware 4 and be uniformly mixed, molding powder in the process of chemical fibre powder, moisture in chemical fibre powder is discharged by gas port 9, molding powder after humidity discharging, chemical fibre powder enters heated type loader 12 by pneumatic type discharging opening 11, the oil inlet pipe 6 that heated type loader 12 connects through high temperature oil oven 5, oil return pipe 7 is heated, controlling electronic valve by sensor 8 makes temperature control at 110 DEG C, double-axle stirrer is being transported to through heated type loader 12, heated type loader 12 outlet is provided with vibrosieve, there is the oil inlet pipe 6 connecting high temperature oil oven 5 double-axle stirrer outside, oil return pipe 7, double-axle stirrer makes temperature control at 220 DEG C by sensor 8 Controlling solenoid valve, at molding powder, while the mixed loader of chemical fibre powder height runs, stone particle through first step processing is sent in stone High Temperature Rotating kiln, stone is heated to 300 DEG C by stone High Temperature Rotating kiln, stone after heating sends into heated type loader 12 by self-emptying mouth, temperature in heated type loader 12 remains on 300 DEG C, stone is transported to double-axle stirrer through heated type loader 12, 3, need not any additive in molding powder, chemical fibre powder and stone mixed process, after the mixing of molding powder, chemical fibre powder, stone, the high temperature of stone makes molding powder, chemical fibre powder dissolves, molding powder, chemical fibre powder and stone are integrated, the below of double-axle stirrer is provided with storage bin, is provided with pressure and temp control valve below storage bin, 4, after storage bin is filled with, after mixing, molding powder, chemical fibre powder, stone are controlled by pressure and temp control valve, special-purpose thermal insulation car 10 is entered through self-emptying mouth, mixed molding powder, chemical fibre powder, stone are transported to job site through special-purpose thermal insulation car 10, ensure that mixed molding powder, chemical fibre powder, stone temperature lay molding powder, stone highway at 150 DEG C-180 DEG C.
Molding powder, the price comparison of stone highway and bituminous highway: asphalt price: 2300 yuan-5000 yuan/ton, the waste plastics that refuse classification goes out, useless chemical fibre material, paper mill is useless moulds woollen and reclaims direct abrasive dust about 1000-1800 yuan/ton, stone price: bituminous highway, stone requires that purity is high, price is relatively high, Su Shi highway, stone is less demanding, in building waste, brick, watt, the above particle of stone 0.5cm, molding powder, stone highway and bituminous highway process ration: bituminous highway: stone is sent into mixing and blending machine with feeder, stone is heated to 200 DEG C-300 DEG C, filling pitch heats 200 DEG C-300 DEG C, with high-temperature high pressure pump, pitch ejection and stone mix lubricant one.Molding powder, stone highway production technology: stone heats 200 DEG C-300 DEG C, molding powder, chemical fibre powder, mixing humidity discharging 90 DEG C-110 DEG C, molding powder, chemical fibre powder be after just mixing humidity discharging mixes with stone, utilizes that the high temperature of stone makes molding powder, chemical fibre powder dissolves, and is integrated with stone.Asphalt high-temperature produces gas has harm to human body, and molding powder, chemical fibre powder just mix humidity discharging, and after mixing with stone, the fusion temperature of molding powder, chemical fibre powder only has about 200 DEG C, without excitatory smell, can shut down at any time, need not clear up.
The raw material manufacture craft of molding powder, stone highway is simple, and the cost of material is low, and by the garbage waste in city, sorting is processed, and recycling, energy-conserving and environment-protective, is the new direction of future city garbage disposal.
Claims (2)
1. a method for production for molding powder, stone highway, comprises the following steps:
(1) the white waste material, by sub-electing in municipal refuse waste material, chemical fibre fragmentation, be broken into the particle of 3-5CM, then particle worn into 40-60 object molding powder, chemical fibre powder; By the plastics after abrasive dust, the mixing of chemical fibre powder, mixed molding powder, chemical fibre powder molding powder 60%-70% by weight percentage, chemical fibre powder 25%-30%, impurity 5%-10%; The building waste in city, industrial residue, stone, ceramic sorting are broken into the stone particle of 0.5cm-1.5cm; By electronic scale and flow measuring unit, the molding powder of mixing, chemical fibre powder are controlled at 1:9 to 1.5:8.5 with the weight of stone by a kilogram ratio as a whole;
(2), by mixed molding powder, chemical fibre powder is transported to molding powder, the mixed loader of chemical fibre powder height, molding powder, chemical fibre powder is through hopper (1), discharging opening (3) is transported to by loader (2), entering high mixing through discharging opening stirs in glassware (4), the high mixed oil inlet pipe (6) stirring glassware and connect through high temperature oil oven (5), oil return pipe (7) is heated, controlling electronic valve by sensor (8) makes temperature control at 90 DEG C-110 DEG C, high mixed stir glassware and be provided with exhaust opening (9), high mixed stir glassware be uniformly mixed after molding powder, molding powder in the process of chemical fibre powder, moisture in chemical fibre powder is discharged by exhaust opening, molding powder after humidity discharging, chemical fibre powder enters heated type loader (12) by pneumatic type discharging opening (11), the oil inlet pipe of heated type loader through being connected with high temperature oil oven, oil return pipe is heated, controlling electronic valve by sensor (8) makes temperature control at 90 DEG C-110 DEG C, double-axle stirrer is being transported to through heated type loader, the outlet of heated type loader is provided with vibrosieve, there is the oil inlet pipe connecting high temperature oil oven double-axle stirrer outside, oil return pipe, and heat-preservation guard shield, double-axle stirrer makes temperature control at 180 DEG C-220 DEG C by sensor Controlling solenoid valve, at molding powder, while the mixed loader of chemical fibre powder height runs, stone particle through first step processing is sent in stone High Temperature Rotating kiln (13), stone is heated to 220 DEG C-240 DEG C by stone High Temperature Rotating kiln, stone after heating sends into heated type loader by self-emptying mouth (14), temperature in heated type loader remains on 220 DEG C-240 DEG C, stone is transported to double-axle stirrer through heated type loader,
(3), mixed molding powder, chemical fibre powder are through vibrosieve and stone Homogeneous phase mixing, and need not any additive in mixed process, after the mixing of molding powder, chemical fibre powder, stone, the high temperature of stone makes molding powder, chemical fibre powder dissolves, molding powder, chemical fibre powder and stone are integrated, the below of double-axle stirrer is provided with storage bin (15), is provided with pressure and temp control valve below storage bin; (4) after, storage bin is filled with, after mixing, molding powder, chemical fibre powder, stone are controlled by pressure and temp control valve, special-purpose thermal insulation car (10) is entered through self-emptying mouth, mixed molding powder, chemical fibre powder, stone are transported to job site through special-purpose thermal insulation car, ensure that mixed molding powder, chemical fibre powder, stone temperature lay molding powder, stone highway at 150 DEG C-180 DEG C.
2. a molding powder, stone synthesizer unit, is characterized in that: comprise molding powder, the mixed loader of chemical fibre powder height, stone High Temperature Rotating kiln, double-axle stirrer, molding powder, the mixed loader of chemical fibre powder height is provided with hopper, and hopper connects loader, is provided with highly mixedly to stir glassware below discharging opening, highly mixedly stirs glassware and is provided with exhaust opening, and outside is provided with oil-feed, oil return pipe, sensor, oil-feed, oil return pipe is connected with high temperature oil oven, has heated type loader below pneumatic type discharging opening, is provided with the oil-feed be connected with high temperature oil oven outside heated type loader, oil return pipe, the outlet of heated type loader is provided with vibrosieve, and be provided with double-axle stirrer below heated type loader discharging opening, stone High Temperature Rotating kiln is provided with charging aperture, sensor, self-emptying mouth, is provided with heated type loader below self-emptying mouth, be provided with double-axle stirrer below heated type loader discharging opening, and there is the oil inlet pipe connecting high temperature oil oven double-axle stirrer outside, oil return pipe, and heat-preservation guard shield, the below of double-axle stirrer is provided with storage bin, is provided with pressure and temp control valve below storage bin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110372386.5A CN102561140B (en) | 2011-11-22 | 2011-11-22 | Method for making molding powder and gravel road, and appliance therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110372386.5A CN102561140B (en) | 2011-11-22 | 2011-11-22 | Method for making molding powder and gravel road, and appliance therefor |
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| Publication Number | Publication Date |
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| CN102561140A CN102561140A (en) | 2012-07-11 |
| CN102561140B true CN102561140B (en) | 2015-05-13 |
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| CN201110372386.5A Expired - Fee Related CN102561140B (en) | 2011-11-22 | 2011-11-22 | Method for making molding powder and gravel road, and appliance therefor |
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| CN109958027A (en) * | 2017-12-23 | 2019-07-02 | 侯林杰 | A kind of crushing gravel asphalt mixing unit |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0116816A1 (en) * | 1983-01-20 | 1984-08-29 | Ab Skanska Cementgjuteriet | Method of re-using asphalt covering and asphalt covering mass produced according to the method |
| US6000877A (en) * | 1995-11-09 | 1999-12-14 | Plasphalt Project Ltd. Co. | Plastic asphalt paving material and method of making same |
| JP2004091535A (en) * | 2002-08-29 | 2004-03-25 | Sumitomo Osaka Cement Co Ltd | Grout for frozen ground, its preparation and grouting method |
| CN101701446A (en) * | 2009-10-15 | 2010-05-05 | 冯海赓 | Equipment for reclaiming old bituminous concrete |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202323628U (en) * | 2011-11-22 | 2012-07-11 | 韩进军 | Molding powder and pebble synthesizer unit |
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- 2011-11-22 CN CN201110372386.5A patent/CN102561140B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0116816A1 (en) * | 1983-01-20 | 1984-08-29 | Ab Skanska Cementgjuteriet | Method of re-using asphalt covering and asphalt covering mass produced according to the method |
| US6000877A (en) * | 1995-11-09 | 1999-12-14 | Plasphalt Project Ltd. Co. | Plastic asphalt paving material and method of making same |
| JP2004091535A (en) * | 2002-08-29 | 2004-03-25 | Sumitomo Osaka Cement Co Ltd | Grout for frozen ground, its preparation and grouting method |
| CN101701446A (en) * | 2009-10-15 | 2010-05-05 | 冯海赓 | Equipment for reclaiming old bituminous concrete |
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| CN102561140A (en) | 2012-07-11 |
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