CN105062536B - Direct-fired giving up moulds oil refining apparatus - Google Patents
Direct-fired giving up moulds oil refining apparatus Download PDFInfo
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- CN105062536B CN105062536B CN201510420243.5A CN201510420243A CN105062536B CN 105062536 B CN105062536 B CN 105062536B CN 201510420243 A CN201510420243 A CN 201510420243A CN 105062536 B CN105062536 B CN 105062536B
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- burner hearth
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- cage basket
- flue
- oil
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- 238000007670 refining Methods 0.000 title claims abstract description 17
- 239000007921 spray Substances 0.000 claims abstract description 94
- 239000004033 plastic Substances 0.000 claims abstract description 31
- 229920003023 plastic Polymers 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000002699 waste material Substances 0.000 claims abstract description 16
- 239000002912 waste gas Substances 0.000 claims abstract description 13
- 239000011521 glass Substances 0.000 claims abstract description 8
- 235000019198 oils Nutrition 0.000 claims description 51
- 241000883990 Flabellum Species 0.000 claims description 28
- 229910000831 Steel Inorganic materials 0.000 claims description 12
- 239000003245 coal Substances 0.000 claims description 12
- 238000005336 cracking Methods 0.000 claims description 12
- 239000010959 steel Substances 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 10
- 230000000694 effects Effects 0.000 claims description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- 238000010304 firing Methods 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 3
- 239000003830 anthracite Substances 0.000 claims description 3
- 238000005452 bending Methods 0.000 claims description 3
- 230000009286 beneficial effect Effects 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 239000011449 brick Substances 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 239000003638 chemical reducing agent Substances 0.000 claims description 3
- 239000010883 coal ash Substances 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 239000000446 fuel Substances 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 238000002844 melting Methods 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 235000019476 oil-water mixture Nutrition 0.000 claims description 3
- 230000001737 promoting effect Effects 0.000 claims description 3
- 238000005096 rolling process Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 238000010257 thawing Methods 0.000 claims description 3
- 238000004227 thermal cracking Methods 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 claims description 3
- 239000012535 impurity Substances 0.000 description 4
- 230000002159 abnormal effect Effects 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000003776 cleavage reaction Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 230000007017 scission Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
A kind of direct-fired giving up moulds oil refining apparatus, burner hearth, flue, induced duct, air-introduced machine, charging dustpan and spray column are connected to form；Being provided with rotatable flue in burner hearth, the cage basket of flue is in the anoxic zone of the surface of furnace flame；The ground of burner hearth dead ahead arranges charging dustpan；Waste plastics is enable to enter in flue；At the induced duct installed above of burner hearth, the other end of induced duct is connected with spray column；Installing air-introduced machine on induced duct, be configured with spray head in spray column, spray head is connected by pipeline, switch and high-pressure water；The bottom sidewall of spray column is provided with upper, middle and lower valve, is respectively used to discharge waste gas, You Heshui；Equipped with transparent glass bar on the tower body of spray column, observe oil, the level change situation of water in spray column with this.
Description
Technical field
A kind of direct-fired giving up moulds oil refining apparatus, belongs to white garbage processing equipment field.
Background technology
The equipment of small-sized useless oil of plasticating is existing a variety of, but these equipment are generally speaking, is all that the distillation technological design using heating indirectly is made；Its defect is that firing rate is slow, and production cost is high, and efficiency is low, and treating capacity does not reaches far away the target call eliminating white pollution.
Summary of the invention
The purpose of the application is to provide for a kind of direct-fired giving up and moulds oil refining apparatus, solves the problems referred to above with this, and this device is connected to form by burner hearth, flue, induced duct, air-introduced machine, charging dustpan and spray column；
Burner hearth use cuboid build burner hearth or iron box-type closed furnace by laying bricks or stones, the cross section of burner hearth is U-shaped in what Open Side Down；Burner hearth uses anthracite block coal to do fuel, reduces heating cost with this and reduces coal ash content in oil；The fire bars of burner hearth is distributed along the bottom of burner hearth, and the flame on fire bars can surround the flue of half；The firing rate of plastics is improved with this；
Being provided with flue in burner hearth, flue is arranged on the longitudinal axis at burner hearth center；Flue is a cage basket that can rotate；The fan being shaped like in the blower fan system of cabinet type air conditioner indoor set；The overall structure of flue is connected to form by support, reductor, motor, rotary shaft and cage basket (having the balek of cage feature, be called for short cage basket)；Cage basket is the open-top receptacle that a longitudinal section is C-shaped；The external diameter of cage basket is between 0.5 1.2 meters；The width of cage basket is between 0.5 1 meters；It is provided around flabellum at cage basket；Flabellum width is between 4 10 centimetres；Distance between flabellum 4 10 centimetres；The cross section of flabellum is with the radian of bending, and the angle of inclination of flabellum is between 30 60 degree；The two ends of flabellum and the sidewall of cage basket are vertically connected integral；Cage basket heat resisting steel is made；In cage basket, be placed with several solid steel balls (not drawing in figure), steel ball can in cage basket rotary rolling, whereby disturbance plastics and the inwall of friction cage basket, red-hot steel ball is the most beneficial to plastic melt and the carbon deposit removed on cage basket；
Install in place after, cage basket is in the anoxic zone of the surface of furnace flame；The flame of burner hearth can enter in cage basket by the slotted section of flabellum under the effect of air-introduced machine, and cage basket is used for holding, heating cracking waste plastics；From charging dustpan enter plastics rotate cage basket in by rapid omnibearing heating and melting, become oil vapour after cracking and enter in induced duct；Under the rotation of cage basket and the radian of flabellum act on jointly, the plastics of thawing can flow downward on flabellum but can not fall and together burn on lump coal；One end and the rotary shaft of cage basket are vertically connected integral at circle centre position；
Support is a trapezoidal general frame；On the basis of support is fixed on ground；Support is used for supporting flue；Being provided with reductor on support, reductor uses sole formula cycloidal planetary gear speed reducer, and the output speed of reductor is below 10 rpms；The output shaft of reductor and rotary shaft are fixedly linked integral；The other end at reductor installs motor, opens motor and cage basket can be driven to rotate in burner hearth；
The ground of burner hearth dead ahead arranges charging dustpan；Charging dustpan is made with one section of pipe, and below charging dustpan, connection has bracket, and what charging dustpan tilted is fixed on bracket；The framework that bracket angle bar or pipe are made, the lower end of charging dustpan can be entered into by the reserved opening of burner hearth in the cage basket of flue, so that waste plastics can be entered in flue by charging dustpan；
The hole of circle it is reserved with in the surface of burner hearth, connect at hole and have induced duct, induced duct is made as a segment pipe of L-type, and the broadening formation that Open Side Down is made in one end of induced duct, and the hole tangent line at the horn mouth of induced duct and the top of burner hearth seals and is connected as a body；
The other end of induced duct is deep in the top of spray column one section；The surrounding of induced duct is connected as a body with the top sealing of spray column；Installing air-introduced machine on induced duct in spray column, air-introduced machine is driven by motor, and motor uses totally enclosed damp-proof machine；Mounted air-introduced machine is suspended on induced duct；Open air-introduced machine and can make the burner hearth interior generation negative pressure of relative closure, thus accelerate oil vapour and leave the high-temperature region of burner hearth, shorten the oil vapour cracking in burner hearth high-temperature region and burning time, not only increase the oil yield of waste plastics, also reduce the content of oxide in oil product (colloidal impurity)；Meanwhile, the effect of negative pressure further improves the burning condition of the lump coal on fire bars, and the flame making lump coal is more vigorous, and the temperature to raising burner hearth is again a requisite promoting factor；
The cavity generally circular in shape of spray column closes container, and spray column is vertically located on the ground；Being configured with several spray heads not waited in spray column, spray head upwards sprays；Spray head is fixed on the sidewall of spray column after the sidewall of spray column by pipeline；Spray head after Gu Ding is unsettled in spray column；Spray head is connected by pipeline, switch and high-pressure water；Open the switch at water source, cold water in spray head, can be had to be sprayed onto in the cavity of spray column, so that be gathered in the bottom of spray column after oil vapour cooling liquefaction simultaneously with water；Being provided with three, the upper, middle and lower valve not waited on the bottom sidewall of spray column, upper valve is used for discharging waste gas, and waste gas carries out second-time burning in being incorporated into burner hearth by pipeline, removes the combustibles in waste gas with this；Middle valve is used for draining the oil, and lower valve is used for discharging water；Offering one section of groove on the tower body of spray column, cover transparent glass bar on groove, glass bar and groove seal and are connected as a body, and observe oil, the level change situation of water in spray column with this.
During oil refining, to burner hearth combustion preheater, after fire box temperature reaches 500 degrees Celsius, waste plastics is joined in flue by charging dustpan, opening flue rotation makes waste plastics by thermal cracking, open upper valve and the air-introduced machine of discharge waste gas simultaneously, lower the temperature in oil vapour after cracking is incorporated into spray column, the switch opening water source makes spray head upwards spray water, oil-water mixture in spray column is gathered in the bottom of tower, liquid level in spray column reaches during limit level (below air outlet valve), in opening respectively and adjusting, the flow of lower valve, the liquid level in spray column is made to be in metastable height；Fluid flows into oil storage tank through pipeline, and waste water enters sewer after processing.
What the application was useful has the technical effect that novel structure, without catalyst；Rate of cleavage is fast, and oil refining efficiency is high, can wash once to oil, greatly reduce the solid impurity in oil product and abnormal flavour in refining；It is the preferable oil refining apparatus of people.
Accompanying drawing explanation
In the accompanying drawings:
Fig. 1 is that direct-fired giving up moulds oil refining apparatus front view.
Description of reference numerals:
In figure, 1, burner hearth；2, flue；3, induced duct；4, air-introduced machine；5, charging dustpan；6, spray column；7, fire bars；8, support；9, reductor；10, motor；11, rotary shaft；12, cage basket；13, flabellum；14, bracket；15, spray head；16, pipeline；17, switch；18, water source；19, glass bar.
Detailed description of the invention
As shown in Fig. 1, a kind of direct-fired giving up moulds oil refining apparatus, and this device is connected to form by burner hearth 1, flue 2, induced duct 3, air-introduced machine 4, charging dustpan 5 and spray column 6；
What burner hearth 1 used cuboid builds burner hearth or iron box-type closed furnace by laying bricks or stones, and the cross section of burner hearth 1 is U-shaped in what Open Side Down；Burner hearth 1 uses anthracite block coal to do fuel, reduces heating cost with this and reduces coal ash content in oil；The fire bars 7 of burner hearth 1 is distributed along the bottom of burner hearth 1, and the flame on fire bars 1 can surround the flue 2 of half；The firing rate of plastics is improved with this；
Being provided with flue 2 in burner hearth 1, flue 2 is arranged on the longitudinal axis at burner hearth 1 center；Flue 2 is a cage basket that can rotate；The fan being shaped like in the blower fan system of cabinet type air conditioner indoor set；The overall structure of flue 2 is had the balek of cage feature by support 8, reductor 9, motor 10, rotary shaft 11 and cage basket 12(, is called for short cage basket) it is connected to form；Cage basket 12 is the open-top receptacle that a longitudinal section is C-shaped；The external diameter of cage basket 12 is between 0.5 1.2 meters；The width of cage basket 12 is between 0.5 1 meters；It is provided around flabellum 13 at cage basket 12；Flabellum 13 width is between 4 10 centimetres；Distance between flabellum 13 4 10 centimetres；The cross section band bending of flabellum 13 have radian, the angle of inclination of flabellum 13 is between 30 60 degree；The two ends of flabellum 13 and the sidewall of cage basket 12 are vertically connected integral；Cage basket 12 is made with heat resisting steel；In cage basket 12, be placed with several solid steel balls (not drawing in figure), steel ball can in cage basket 12 rotary rolling, whereby disturbance plastics and the inwall of friction cage basket 12, red-hot steel ball is the most beneficial to plastic melt and the carbon deposit removed on cage basket 12；
Install in place after, cage basket 12 is in the anoxic zone of the surface of the flame of burner hearth 1；The flame of burner hearth 1 can enter in cage basket 12 by the slotted section of flabellum 13 under the effect of air-introduced machine 4, and cage basket 12 is used for holding, heating cracking waste plastics；From charging dustpan 5 enter plastics rotate cage basket 12 in by rapid omnibearing heating and melting, become oil vapour after cracking and enter in induced duct 3；Under the rotation of cage basket 12 and the radian of flabellum 13 act on jointly, the plastics of thawing can flow downward on flabellum 13 but can not fall and together burn on lump coal；One end and the rotary shaft 11 of cage basket 12 are vertically connected integral at circle centre position；
Support 8 is a trapezoidal general frame；On the basis of support 8 is fixed on ground；Support 8 is used for supporting flue 2；Being provided with reductor 9 on support 8, reductor 9 uses sole formula cycloidal planetary gear speed reducer, and the output speed of reductor 9 is below 10 rpms；Output shaft and the rotary shaft 11 of reductor 9 are fixedly linked integral；The other end at reductor 9 installs motor 10, opens motor 10 and cage basket 12 can be driven to rotate in burner hearth 1；
The ground of the dead ahead of burner hearth 1 arranges charging dustpan 5；Charging dustpan 5 is made with one section of pipe, and below charging dustpan 5, connection has bracket 14, and what charging dustpan 5 tilted fixes on a pallet 14；The framework that bracket 14 is made with angle bar or pipe, the lower end of charging dustpan 5 can be entered into by the reserved opening of burner hearth 1 in the cage basket 12 of flue 2, so that waste plastics can be entered in flue 2 by charging dustpan 5；
The hole of circle it is reserved with in the surface of burner hearth 1, connect at hole and have induced duct 3, induced duct 3 is made as a segment pipe of L-type, and the broadening formation that Open Side Down is made in one end of induced duct 3, and the hole tangent line at the horn mouth of induced duct 3 and the top of burner hearth 1 seals and is connected as a body；
The other end of induced duct 3 is deep in the top of spray column 6 one section；The surrounding of induced duct 3 is connected as a body with the top sealing of spray column 6；Installing air-introduced machine 4 on induced duct 3 in spray column 6, air-introduced machine 4 is driven by motor, and motor uses totally enclosed damp-proof machine；Mounted air-introduced machine 4 is suspended on induced duct 3；Open air-introduced machine 4 and can make the burner hearth 1 interior generation negative pressure of relative closure, thus accelerate oil vapour and leave the high-temperature region of burner hearth 1, shorten the oil vapour cracking in the high-temperature region of burner hearth 1 and burning time, not only increase the oil yield of waste plastics, also reduce the content of oxide in oil product (colloidal impurity)；Meanwhile, the effect of negative pressure further improves the burning condition of the lump coal on fire bars 7, and the flame making lump coal is more vigorous, and the temperature to raising burner hearth 1 is again a requisite promoting factor；
The cavity generally circular in shape of spray column 6 closes container, and spray column 6 is vertically located on the ground；Being configured with several spray heads 15 not waited in spray column 6, spray head 15 upwards sprays；Spray head 15 is fixed on the sidewall of spray column 6 after the sidewall of spray column 6 by pipeline 16；Spray head 15 after Gu Ding is unsettled in spray column 6；Spray head 15 is connected by pipeline 16, switch 17 and high-pressure water 18；Open the switch 17 at water source 18, in spray head 15, cold water can be had to be sprayed onto in the cavity of spray column 6, so that be gathered in the bottom of spray column 6 after oil vapour cooling liquefaction simultaneously with water；Being provided with three, the upper, middle and lower valve not waited on the bottom sidewall of spray column 6, upper valve is used for discharging waste gas, and waste gas carries out second-time burning in being incorporated into burner hearth 1 by pipeline, removes the combustibles in waste gas with this；Middle valve is used for draining the oil, and lower valve is used for discharging water；Offering one section of groove on the tower body of spray column 6, cover transparent glass bar 19 on groove, glass bar 19 and groove seal and are connected as a body, and observe oil, the level change situation of water in spray column 6 with this.
During oil refining, to burner hearth 1 combustion preheater, after the temperature of burner hearth 1 reaches 500 degrees Celsius, waste plastics is joined in flue 2 by charging dustpan 5, opening flue 2 rotation makes waste plastics by thermal cracking, open upper valve and the air-introduced machine 4 of discharge waste gas simultaneously, oil vapour after cracking is incorporated into cooling in spray column 6, the switch opening water source 18 makes spray head 15 upwards spray water, oil-water mixture in spray column 6 is gathered in the bottom of tower, liquid level in spray column 6 reaches during limit level (below air outlet valve), in opening respectively and adjusting, the flow of lower valve, the liquid level in spray column 6 is made to be in metastable height；Fluid flows into oil storage tank through pipeline, and waste water enters sewer after processing.
What the application was useful has the technical effect that novel structure, without catalyst；Rate of cleavage is fast, and oil refining efficiency is high, can wash once to oil, greatly reduce the solid impurity in oil product and abnormal flavour in refining；It is the preferable oil refining apparatus of people.
Claims (1)
1. direct-fired giving up moulds oil refining apparatus, it is characterised in that: this device is connected to form by burner hearth (1), flue (2), induced duct (3), air-introduced machine (4), charging dustpan (5) and spray column (6)；
Burner hearth (1) use cuboid build burner hearth or iron box-type closed furnace by laying bricks or stones, the cross section of burner hearth (1) is U-shaped in what Open Side Down；Burner hearth (1) uses anthracite block coal to do fuel, reduces heating cost with this and reduces coal ash content in oil；The fire bars (7) of burner hearth (1) is distributed along the bottom of burner hearth (1), fire bars( 7 )On flame can surround the flue (2) of half；The firing rate of plastics is improved with this；
Being provided with flue (2) in burner hearth (1), flue (2) is arranged on the longitudinal axis at burner hearth (1) center；Flue (2) is a cage basket that can rotate；The fan being shaped like in the blower fan system of cabinet type air conditioner indoor set；The overall structure of flue (2) is connected to form by support (8), reductor (9), motor (10), rotary shaft (11) and cage basket (12)；Cage basket (12) is the open-top receptacle that a longitudinal section is C-shaped；The external diameter of cage basket (12) is between 0.5 1.2 meters；The width of cage basket (12) is between 0.5 1 meters；It is provided around flabellum (13) at cage basket (12)；The width of flabellum (13) is between 4 10 centimetres；Distance between flabellum (13) 4 10 centimetres；Transversal the wearing of flabellum (13)HaveThe radian of bending, the angle of inclination of flabellum (13) is between 30 60 degree；The two ends of flabellum (13) and the sidewall of cage basket (12) are vertically connected integral；Cage basket (12) is made with heat resisting steel；In cage basket (12), be placed with several solid steel balls, steel ball can in cage basket (12) rotary rolling, whereby disturbance plastics and the inwall of friction cage basket (12), red-hot steel ball is the most beneficial to plastic melt and the carbon deposit removed on cage basket (12)；
Install in place after, cage basket (12) is in the anoxic zone of the surface of the flame of burner hearth (1)；The flame of burner hearth (1) can enter in cage basket (12) by the slotted section of flabellum (13) under the effect of air-introduced machine (4), and cage basket (12) is used for holding, heating cracking waste plastics；From charging dustpan (5) plastics that enter in the cage basket (12) rotated by rapid omnibearing heating and melting, becoming oil vapour after cracking, to enter into induced duct (3) interior；Under the rotation of cage basket (12) and the radian of flabellum (13) act on jointly, the plastics of thawing can flow downward on flabellum (13) but can not fall and together burn on lump coal；One end and the rotary shaft (11) of cage basket (12) are vertically connected integral at circle centre position；
Support (8) is a trapezoidal general frame；On the basis of support (8) is fixed on ground；Support (8) is used for supporting flue (2)；Being provided with reductor (9) on support (8), reductor (9) uses sole formula cycloidal planetary gear speed reducer, and the output speed of reductor (9) is below 10 rpms；Output shaft and the rotary shaft (11) of reductor (9) are fixedly linked integral；The other end at reductor (9) installs motor (10), opens motor (10) and cage basket (12) can be driven to rotate in burner hearth (1)；
The ground of the dead ahead of burner hearth (1) arranges charging dustpan (5)；Charging dustpan (5) is made with one section of pipe, and below charging dustpan (5), connection has bracket (14), and what charging dustpan (5) tilted is fixed on bracket (14)；The framework that bracket (14) is made with angle bar or pipe, the lower end of charging dustpan (5) can be entered into by the reserved opening of burner hearth (1) in the cage basket (12) of flue (2), so that waste plastics can be entered in flue (2) by charging dustpan (5)；
The hole of circle it is reserved with in the surface of burner hearth (1), connect at hole and have induced duct (3), induced duct (3) is made as a segment pipe of L-type, the broadening formation that Open Side Down is made in one end of induced duct (3), and the hole tangent line at the horn mouth of induced duct (3) and the top of burner hearth (1) seals and is connected as a body；
The other end of induced duct (3) is deep in the top of spray column (6) one section；The surrounding of induced duct (3) is connected as a body with the top sealing of spray column (6)；Installing air-introduced machine (4) on induced duct (3) in spray column (6), air-introduced machine (4) is driven by motor, and motor uses totally enclosed damp-proof machine；Mounted air-introduced machine (4) is suspended on induced duct (3)；Open air-introduced machine (4) and burner hearth (1) the interior generation negative pressure of relative closure can be made, thus accelerate oil vapour and leave the high-temperature region of burner hearth (1), shorten the oil vapour cracking in the high-temperature region of burner hearth (1) and burning time, not only increase the oil yield of waste plastics, also reduce the content of oxide in oil product；Meanwhile, the effect of negative pressure further improves the burning condition of the lump coal on fire bars (7), and the flame making lump coal is more vigorous, and the temperature to raising burner hearth (1) is again a requisite promoting factor；
The cavity generally circular in shape of spray column (6) closes container, and spray column (6) is vertically located on the ground；Being configured with several spray heads (15) not waited in spray column (6), spray head (15) upwards sprays；Spray head (15) is fixed on the sidewall of spray column (6) after the sidewall of spray column (6) by pipeline (16)；Spray head (15) after Gu Ding is unsettled in spray column (6)；Spray head (15) is connected by pipeline (16), switch (17) and high-pressure water (18)；Open the switch (17) of water source (18), in spray head (15), cold water can be had to be sprayed onto in the cavity of spray column (6), so that be gathered in the bottom of spray column (6) after oil vapour cooling liquefaction simultaneously with water；Being provided with three, the upper, middle and lower valve not waited on the bottom sidewall of spray column (6), upper valve is used for discharging waste gas, and waste gas carries out second-time burning in being incorporated into burner hearth (1) by pipeline, removes the combustibles in waste gas with this；Middle valve is used for draining the oil, and lower valve is used for discharging water；Offering one section of groove on the tower body of spray column (6), cover transparent glass bar (19) on groove, glass bar (19) and groove seal and are connected as a body, and observe oil, the level change situation of water in spray column (6) with this；
During oil refining, to burner hearth (1) combustion preheater, after the temperature of burner hearth (1) reaches 500 degrees Celsius, waste plastics is joined in flue (2) by charging dustpan (5), opening flue (2) rotation makes waste plastics by thermal cracking, open upper valve and the air-introduced machine (4) of discharge waste gas simultaneously, oil vapour after cracking is incorporated into cooling in spray column (6), the switch opening water source (18) makes spray head (15) upwards spray water, oil-water mixture in spray column (6) is gathered in the bottom of tower, when liquid level in spray column (6) reaches limit level, in opening respectively and adjusting, the flow of lower valve, the liquid level in spray column (6) is made to be in metastable height；Fluid flows into oil storage tank through pipeline, and waste water enters sewer after processing.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201510420243.5A CN105062536B (en) | 2015-07-17 | 2015-07-17 | Direct-fired giving up moulds oil refining apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510420243.5A CN105062536B (en) | 2015-07-17 | 2015-07-17 | Direct-fired giving up moulds oil refining apparatus |
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| Publication Number | Publication Date |
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| CN105062536A CN105062536A (en) | 2015-11-18 |
| CN105062536B true CN105062536B (en) | 2016-09-28 |
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Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2615138Y (en) * | 2001-12-20 | 2004-05-12 | 史成科 | Horizontal converting waste plastics white pollution into fuel oil apparatus |
| CN1403537A (en) * | 2002-07-16 | 2003-03-19 | 上海绿人生态经济科技有限公司 | Comprehensive method and apparatus for hot cracked gas of waste tyre |
| CN101824332B (en) * | 2010-06-02 | 2013-10-09 | 华南再生资源（中山）有限公司 | Production equipment for comprehensively utilizing renewable energy resources of waste and old plastics, tires and waste engine oil |
| US8668810B1 (en) * | 2013-01-17 | 2014-03-11 | Amass Energy LLC | Device and methods for processing carbon based materials |
| CN104140827A (en) * | 2013-05-06 | 2014-11-12 | 周鼎力 | A rotary reactor for pyrolysis of coal or garbage organic waste |
| CN203621086U (en) * | 2013-12-19 | 2014-06-04 | 新冶高科技集团有限公司 | Equipment for treating waste tires by continuous environment-friendly fracture splitting processing |
| CN104479718A (en) * | 2014-11-14 | 2015-04-01 | 烟台荣盛压力容器制造有限公司 | Method for refining oil by adopting waste plastics |
| CN104560071B (en) * | 2014-12-26 | 2017-11-24 | 神雾科技集团股份有限公司 | Pyrolysis system and method for pyrolysis |
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2015
- 2015-07-17 CN CN201510420243.5A patent/CN105062536B/en active Active
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