CN2352530Y - Equipment for continuously producing diesel and gasoline by using waste plastic as raw material - Google Patents
Equipment for continuously producing diesel and gasoline by using waste plastic as raw material Download PDFInfo
- Publication number
- CN2352530Y CN2352530Y CN 98204842 CN98204842U CN2352530Y CN 2352530 Y CN2352530 Y CN 2352530Y CN 98204842 CN98204842 CN 98204842 CN 98204842 U CN98204842 U CN 98204842U CN 2352530 Y CN2352530 Y CN 2352530Y
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- ash
- lime
- removing device
- gasoline
- waste plastic
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Abstract
The utility model relates to a device for continuously producing diesel oil and gasoline by using waste plastic as raw materials, which belongs to catalytic cracking devices. The utility model is mainly composed of a cracking kettle, a pre-heating device of cracking oil, a slag-removing device of ash slag, a drying device of ash slag, a distilling still, etc. The utility model is characterized in that the kettle bottom of the cracking kettle is provided with a belt type spiral slag-pushing device, a separating net and a mixing device. The tail end of the cracking kettle is connected with an outlet of ash slag, the slag-removing device of ash slag and the drying device of ash slag. The upper end is communicated with a waste plastic feeding machine. The utility model has the advantages of reasonable design, compact structure, simple and safe operation, non-pressure operation, continuous production, continuous slag removing and drying, high productive efficiency, good petroleum-product quality and low energy consumption.
Description
The utility model relates to a kind of device with waste plastic continuous production bavin gasoline, belongs to cat-cracker.
At present, the device that waste plastic is produced bavin gasoline of domestic use is all heavy, and the step mode of production of blowing out deslagging is all adopted in power consumption, numerous and diverse in whole process of production, produces with several cracking still exchanges, employing adds a furnace charge and refines a stove, the method of blowing out cooling deslagging, such mode of production benefit is obviously on the low side, and waste of fuel is very big, oil quality is poor, also makes production cost strengthen simultaneously; Though the equipment or the device of the production bavin gasoline that has have adopted catalytic principle in factory of oil refinery rectifying tower and the tracheae,, still exist the hydrofuge slag, decrease the high shortcoming of oily rate, to making the production quality be lower than GB owing to adopt gas mixture Catalysis Principles altogether.
The purpose of this utility model is to provide a kind of device with waste plastic continuous production bavin gasoline, to overcome the deficiency of the necessary blowing out deslagging batch production of existing apparatus.
The purpose of this utility model is to realize like this, it is mainly by cracking still (1), cracked oil preheater (2), ash cinder removing device (3), lime-ash baker (4), still kettle compositions such as (5), it is characterized in that combustion heating furnace (6) is provided with cracking still (1), be provided with belt spiral dregs removing device (7) at the bottom of the still of cracking still (1), belt spiral dregs removing device (7) is provided with filter (11), filter (11) is provided with agitator (12), the tail end of cracking still (1) is connected with lime-ash outlet (25), lime-ash outlet (25) is connected with grey cinder removing device (3), ash cinder removing device (3) is connected with lime-ash baker (4) by lime-ash import (26), the termination, top of cracking still (1) is communicated with plastic waste charging machine (13) by water jacket refrigerating unit (18), plastic waste charging machine (13) is provided with charging opening (17), another termination of the top of cracking still (1) is provided with floss hole (24), the top of cracking still (1) is provided with manhole (19) and oil gas vent (23), be connected with on the oil gas vent (23) and urge filter (21), urge filter (21) to be provided with catalyst chamber (22) and adsorber (20), urge the interior cracked oil condenser (31) of filter (21) and condensation water tank (30) to be connected, cracked oil condenser (31) is connected with cracked oil storage cylinder (34), cracked oil storage cylinder (34) is connected with cracked oil preheater (2), cracked oil preheater (2) is connected with still kettle (5) with toothed gear pump (48) by pre-hot gas bleed valve (37) respectively, still kettle (5) urges filter (38) and diesel oil to urge the interior gasoline condenser (32) of filter (39) and condensation water tank (30) to be connected with diesel oil condenser (33) by gasoline respectively, and gasoline condenser (32) is connected with bavin gasoline storage cylinder (36) respectively with diesel oil condenser (33).
Its feature is that also grey cinder removing device (3) is provided with lime-ash import (43), and export (25) by lime-ash import (43) and lime-ash and be connected, be provided with deslagging thruster (42) in the ash cinder removing device (3), motor (40) is connected with deslagging thruster (42) by step-down gear (41), ash cinder removing device (3) has lime-ash slag notch (46), be provided with lime-ash tightness system (45) in the other end of ash cinder removing device (3), another termination of grey cinder removing device (3) is provided with sealing regulator (44).
Its feature is that also motor (8) is connected with belt spiral dregs removing device (7) with quick-action wheel apparatus (10) by step-down gear (9).
Its feature is that also agitator (12) is provided with quick-action wheel apparatus (10) and is connected with quick-action wheel apparatus (10) on the belt spiral dregs removing device (7).
Its feature also is to be provided with in the condensation water tank (30) cracked oil condenser (31), gasoline condenser (32) and diesel oil condenser (33).
Its feature is that also lime-ash baker (4) is provided with pre-hot gas import (27), pre-hot gas outlet (28) and dried slag outlet (29).
Its feature is that also motor (14) is connected with stock pusher (16) by step-down gear (15), and stock pusher (16) is arranged in the plastic waste charging machine (13).
Its feature is that also cracked oil preheater (2) is provided with pre-hot gas import (35), and cracked oil preheater (2) has preheater flue outlet (47).
The utility model compared with prior art, it is reasonable in design, and is novel, compact construction, easy and simple to handle, safety can not have the operation of pressing, continuous production, continuous discharging slag and oven dry, the production efficiency height, oil quality is good, and cost is low, less investment is taken up an area of for a short time, power consumption less.
Below in conjunction with drawings and Examples the utility model is further specified:
Accompanying drawing 1 is the utility model overall appearance broken section structural representation.
Accompanying drawing 2 is the connection diagram of the utility model parts 3.
Among the figure: 1, cracking still, 2, the cracked oil preheater, 3, the ash cinder removing device, 4, the lime-ash baker, 5, still kettle, 6, combustion heating furnace, 7, belt spiral dregs removing device, 8, motor, 9, step-down gear, 10, the quick-action wheel apparatus, 11, filter, 12, strand is mixed device, 13, the plastic waste charging machine, 14, motor, 15, step-down gear, 16, stock pusher, 17, charging opening, 18, the water jacket refrigerating unit, 19, manhole, 20, adsorber, 21, urge filter, 22, catalyst chamber, 23, oil gas vent, 24, floss hole, 25, the lime-ash outlet, 26, the lime-ash import, 27, pre-hot gas import, 28, pre-hot gas outlet, 29, dried slag outlet, 30, condensation water tank, 31, the cracked oil condenser, 32, gasoline condenser, 33, the diesel oil condenser, 34, cracked oil storage cylinder, 35, pre-hot gas import, 36, bavin gas and oil storage cylinder, 37, pre-hot gas bleed valve, 38, gasoline is urged filter, and 39, diesel oil is urged filter, and 40, motor, 41, step-down gear, 42, the deslagging thruster, 43, the lime-ash import, 44, the sealing regulator, 45, the lime-ash tightness system, 46, the lime-ash slag notch, 47, the preheater flue outlet, 48, toothed gear pump.
Referring to accompanying drawing, the utility model designs according to national pressure container standard, material is selected through strict, whole cracking still (1) is to use 20# boiler plate weldering system, the kettle end face of cracking still (1) is fan-shaped length body structure for sleeping in, it at the bottom of the still of cracking still (1) the semicircle type structure of 30mm diameter, the semicircle center is provided with belt spiral dregs removing device (7), motor (8) is connected with belt spiral dregs removing device (7) with quick-action wheel apparatus (10) by step-down gear (9), belt spiral dregs removing device (7) is provided with filter (11), filter (11) is provided with agitator (12), belt spiral dregs removing device (7) all contacts with the bottom semicircular body of cracking still (1), the one, be beneficial to and push away slag, the 2nd, be beneficial to Stirring heat transfer, agitator (12) is provided with quick-action wheel apparatus (10) and is connected with quick-action wheel apparatus (10) on the belt spiral dregs removing device (7).
The tail end of cracking still (1) is provided with lime-ash outlet (25), lime-ash outlet (25) is connected with grey cinder removing device (3), then the wet slag of discharging is flowed to lime-ash baker (4) oven dry by lime-ash import (26), dried slag outlet (29) under the lime-ash baker (4) is discharged again, also is provided with pre-hot gas import (27) on the lime-ash baker (4) and pre-hot gas exports (28).
Ash cinder removing device (3) is provided with lime-ash import (43), and export (25) by lime-ash import (43) and lime-ash and be connected, be provided with deslagging thruster (42) in the ash cinder removing device (3), motor (40) is connected with deslagging thruster (42) by step-down gear (41), ash cinder removing device (3) has lime-ash slag notch (46), be provided with lime-ash tightness system (45) in the other end of ash cinder removing device (3), another termination of ash cinder removing device (3) is provided with sealing regulator (44), has just constituted to connect automatic incessantly grey cinder removing device
The termination, top of cracking still (1) is communicated with plastic waste charging machine (13) by water jacket refrigerating unit (18), plastic waste charging machine (13) is provided with charging opening (17), waste plastic joins in the plastic waste charging machine (13) by charging opening (17), motor (14), step-down gear (15) are socketed in the plastic waste charging machine (13) by stock pusher (16), stock pusher (16) is pushed the waste plastic in the plastic waste charging machine (13) in the cracking still (1) to, so plastic waste charging machine (13) is automatic pushing device.
Cracking still (1) has combustion heating furnace (6), another termination of cracking still (1) top is provided with floss hole (24), the top of cracking still (1) is provided with manhole (19) and oil gas vent (23), waste plastic in the cracking still (1) produces gas and enters into by the oil gas vent (23) above the cracking still (1) and urge in the filter (21) through adding thermally splitting, after reacting with catalyzer of urging the catalyst chamber (22) on the filter (21) and adsorber (20) again and adsorbing, enter cracked oil condenser (31) condensation, flow into cracked oil storage cylinder (34), carry out oily water separation, clean cracked oil after the separation flows into cracked oil preheater (2) preheating naturally, cracked oil preheater (2) is provided with pre-hot gas import (35), and cracked oil preheater (2) has preheater flue outlet (47).The thermal source of cracked oil preheater (2) is from combustion heating furnace (6), and the oil gas after the preheating enters still kettle (5) by pre-hot gas bleed valve (37) and toothed gear pump (48) respectively to be continued to heat, and carries out gas diesel oil by required separately temperature and decomposes.Gasoline finishes 180 ℃ and diesel oil each self-decomposition under 340 ℃ of temperature, can obtain GB 90# white gasoline and-the 35# solar oil.
Still kettle (5) urges filter (38) and diesel oil to urge the interior gasoline condenser (32) of filter (39) and condensation water tank (30) to be connected with diesel oil condenser (33) by gasoline respectively, and gasoline condenser (32) is connected with bavin gasoline storage cylinder (36) respectively with diesel oil condenser (33).
Urge filter (21), gasoline to urge filter (38) and diesel oil to urge the different catalyzer of packing in the filter (39), that is: plastic cracking catalyzer, gasoline catalyzing agent, diesel catalytic converter, reach after the catalysis condensation GB 90# white gasoline and-the 35# solar oil.
Claims (8)
1, a kind of device with waste plastic continuous production bavin gasoline it mainly by cracking still (1), cracked oil preheater (2), ash cinder removing device (3), lime-ash baker (4), still kettle compositions such as (5), it is characterized in that combustion heating furnace (6) is provided with cracking still (1), be provided with belt spiral dregs removing device (7) at the bottom of the still of cracking still (1), belt spiral dregs removing device (7) is provided with filter (11), filter (11) is provided with agitator (12), the tail end of cracking still (1) is connected with lime-ash outlet (25), lime-ash outlet (25) is connected with grey cinder removing device (3), ash cinder removing device (3) is connected with lime-ash baker (4) by lime-ash import (26), the termination, top of cracking still (1) is communicated with plastic waste charging machine (13) by water jacket refrigerating unit (18), plastic waste charging machine (13) is provided with charging opening (17), another termination of the top of cracking still (1) is provided with floss hole (24), the top of cracking still (1) is provided with manhole (19) and oil gas vent (23), be connected with on the oil gas vent (23) and urge filter (21), urge filter (21) to be provided with catalyst chamber (22) and adsorber (20), urge the interior cracked oil condenser (31) of filter (21) and condensation water tank (30) to be connected, cracked oil condenser (31) is connected with cracked oil storage cylinder (34), cracked oil storage cylinder (34) is connected with cracked oil preheater (2), cracked oil preheater (2) is connected with still kettle (5) with toothed gear pump (48) by pre-hot gas bleed valve (37) respectively, still kettle (5) urges filter (38) and diesel oil to urge the interior gasoline condenser (32) of filter (39) and condensation water tank (30) to be connected with diesel oil condenser (33) by gasoline respectively, and gasoline condenser (32) is connected with bavin gasoline storage cylinder (36) respectively with diesel oil condenser (33).
2, device with waste plastic continuous production bavin gasoline according to claim 1, its feature is that also grey cinder removing device (3) is provided with lime-ash import (43), and export (25) by lime-ash import (43) and lime-ash and be connected, be provided with deslagging thruster (42) in the ash cinder removing device (3), motor (40) is connected with deslagging thruster (42) by step-down gear (41), ash cinder removing device (3) has lime-ash slag notch (46), be provided with lime-ash tightness system (45) in the other end of ash cinder removing device (3), another termination of grey cinder removing device (3) is provided with sealing regulator (44).
3, the device with waste plastic continuous production bavin gasoline according to claim 1, its feature are that also motor (8) is connected with belt spiral dregs removing device (7) with quick-action wheel apparatus (10) by step-down gear (9).
4, the device with waste plastic continuous production bavin gasoline according to claim 1, its feature are that also agitator (12) is provided with quick-action wheel apparatus (10) and is connected with quick-action wheel apparatus (10) on the belt spiral dregs removing device (7).
5, the device with waste plastic continuous production bavin gasoline according to claim 1, its feature also are to be provided with in the condensation water tank (30) cracked oil condenser (31), gasoline condenser (32) and diesel oil condenser (33).
6, the device with waste plastic continuous production bavin gasoline according to claim 1, its feature are that also lime-ash baker (4) is provided with pre-hot gas import (27), pre-hot gas outlet (28) and dried slag outlet (29).
7, the device with waste plastic continuous production bavin gasoline according to claim 1, its feature are that also motor (14) is connected with stock pusher (16) by step-down gear (15), and stock pusher (16) is arranged in the plastic waste charging machine (13).
8, the device with waste plastic continuous production bavin gasoline according to claim 1, its feature are that also cracked oil preheater (2) is provided with pre-hot gas import (35), and cracked oil preheater (2) has preheater flue outlet (47).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98204842 CN2352530Y (en) | 1998-05-25 | 1998-05-25 | Equipment for continuously producing diesel and gasoline by using waste plastic as raw material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98204842 CN2352530Y (en) | 1998-05-25 | 1998-05-25 | Equipment for continuously producing diesel and gasoline by using waste plastic as raw material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2352530Y true CN2352530Y (en) | 1999-12-08 |
Family
ID=33961361
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 98204842 Expired - Fee Related CN2352530Y (en) | 1998-05-25 | 1998-05-25 | Equipment for continuously producing diesel and gasoline by using waste plastic as raw material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2352530Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007014489A1 (en) * | 2005-08-03 | 2007-02-08 | Weitian Zhang | A pyrolysis method for treating waste rubber and plastics and materials containing resins |
| CN101050137B (en) * | 2007-05-18 | 2010-12-22 | 中国林业科学研究院林业研究所 | Synthesizing method and equipment for fabricating light ground substance by using farming and forestry biomass |
| CN102161908A (en) * | 2011-03-24 | 2011-08-24 | 王团群 | Biomass energy cracking kettle and biomass energy cracking method |
| CN104438297A (en) * | 2014-12-10 | 2015-03-25 | 密西西比国际水务有限公司 | Method and device for treating organic refuse |
-
1998
- 1998-05-25 CN CN 98204842 patent/CN2352530Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007014489A1 (en) * | 2005-08-03 | 2007-02-08 | Weitian Zhang | A pyrolysis method for treating waste rubber and plastics and materials containing resins |
| CN101050137B (en) * | 2007-05-18 | 2010-12-22 | 中国林业科学研究院林业研究所 | Synthesizing method and equipment for fabricating light ground substance by using farming and forestry biomass |
| CN102161908A (en) * | 2011-03-24 | 2011-08-24 | 王团群 | Biomass energy cracking kettle and biomass energy cracking method |
| CN102161908B (en) * | 2011-03-24 | 2013-11-06 | 王团群 | Biomass energy cracking kettle and biomass energy cracking method |
| CN104438297A (en) * | 2014-12-10 | 2015-03-25 | 密西西比国际水务有限公司 | Method and device for treating organic refuse |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |