CN105316023A - Oil sand cracking device - Google Patents

Oil sand cracking device Download PDF

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Publication number
CN105316023A
CN105316023A CN201510876568.4A CN201510876568A CN105316023A CN 105316023 A CN105316023 A CN 105316023A CN 201510876568 A CN201510876568 A CN 201510876568A CN 105316023 A CN105316023 A CN 105316023A
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CN
China
Prior art keywords
cyclonic separator
oil
heating chamber
outlet
combustion chamber
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Pending
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CN201510876568.4A
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Chinese (zh)
Inventor
韩玉龙
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Nanjing Ld Environment Protection Energy Technology Co Ltd
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Nanjing Ld Environment Protection Energy Technology Co Ltd
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Application filed by Nanjing Ld Environment Protection Energy Technology Co Ltd filed Critical Nanjing Ld Environment Protection Energy Technology Co Ltd
Priority to CN201510876568.4A priority Critical patent/CN105316023A/en
Publication of CN105316023A publication Critical patent/CN105316023A/en
Pending legal-status Critical Current

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Abstract

The invention discloses an oil sand cracking device. The oil sand cracking device structurally comprises a first cyclone separator, a second cyclone separator, a third cyclone separator, a fourth cyclone separator, a discharging device, a spiral propeller, a first heating chamber, a second heating chamber, a first combustion chamber, a second combustion chamber, a transition cabin, a heat exchanger and a fractionating tower. The oil sand cracking device can be used for continuously and efficiently cracking oil sand, and byproducts produced at a high temperature state can be directly used for producing semi-finished product auxiliary materials of cement.

Description

A kind of oil-sand cracker
Technical field
The present invention relates to environmental protection sciemtifec and technical sphere, particularly relate to a kind of oil-sand cracker.
Background technology
Traditional oil-sand process has following several mode: 1. adopt tensio-active agent to heat washing, this mode wastes a large amount of water resourcess, and heat energy consumption is large.2. adopt rotary kiln Pintsch process, the oil-sand treatment capacity of this mode process is little, oil yield is low, and heat energy can not reclaim.3. adopt the mode of floating bed high-temperature gasification, the high but wayward risk of this mode factor of created gase, the rate of recovery is low.The by-product that this several device cracking oil-sand above-mentioned produces all is not suitable for manufacture calcium carbonate, calcium oxide, cement semi-finished product auxiliary material.
Summary of the invention
In order to solve the problems of the prior art, the invention provides a kind of oil-sand cracker, this device can by oil-sand cracking, and the by-product of generation is directly used in production cement semi-finished product.
The present invention is achieved through the following technical solutions: a kind of oil-sand cracker, comprise the first cyclonic separator, second cyclonic separator, 3rd cyclonic separator, 4th cyclonic separator, blanking device, spiral propeller, first heating chamber, second heating chamber, first combustion chamber, second combustion chamber, entry locker, interchanger, separation column, the first described cyclonic separator lower end is connected with spiral propeller 6 entrance through blanking device, spiral propeller outlet is successively through the second cyclonic separator, 3rd cyclonic separator is connected with separation column, bottom the second described cyclonic separator, an outlet is connected with the first heating chamber, another outlet is connected with entry locker entrance, the 3rd described cyclonic separator is all connected with entry locker entrance by pipeline with the lower end outlet of the 4th cyclonic separator, described entry locker outlet successively with the second heating chamber, second combustion chamber, interchanger is connected.
The first described heating chamber upper end is connected with the first combustion chamber by riser tube, and an outlet of the first combustion chamber is connected with spiral propeller entrance, and another outlet is connected with the entrance of the 4th cyclonic separator.
The exit of described entry locker is provided with blower fan.
Described interchanger is also connected with generator, for thermal power generation.
Described separation column also arranges oil-gas separator and vacuum pump, and heavy constituent is connected with the second heating chamber through heavy oil tank, for providing fuel; Light constituent is connected with the first heating chamber and the second heating chamber after oil-gas separator, vacuum pump, gas-holder.
The pneumatic outlet of the first described cyclonic separator is connected with chimney through flue gas processing device.
The material inlet of the first described cyclonic separator also can connect dryer and pulverizer.
In the first described heating chamber and the second heating chamber, all burner is set.
The present invention compared to existing technology, has following beneficial effect: the present invention can continuous high-efficient carry out oil-sand cracking, turnout is large, and the by-product produced under the condition of high temperature is directly used in produces cement semi-finished product auxiliary material.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Wherein: 1-first cyclonic separator, 2-second cyclonic separator, 3-the 3rd cyclonic separator, 4-the 4th cyclonic separator, 5-blanking device, 6-spiral propeller, 7-first heating chamber, 8-second heating chamber, 9-first combustion chamber, 10-second combustion chamber, 11-entry locker, 12-interchanger, 13-separation column, 14-generator, 15-oil-gas separator, 16-vacuum pump, 17-heavy oil tank, 18-gas-holder, 19-flue gas processing device, 20-chimney, 21-dryer, 22-pulverizer, 23-burner, 24-blower fan.
Embodiment
Below in conjunction with drawings and Examples, the present invention is further illustrated.
As shown in the figure.A kind of oil-sand cracker, comprise the first cyclonic separator 1, second cyclonic separator 2, 3rd cyclonic separator 3, 4th cyclonic separator 4, blanking device 5, spiral propeller 6, first heating chamber 7, second heating chamber 8, first combustion chamber 9, second combustion chamber 10, entry locker 11, interchanger 12, separation column 13, the first described cyclonic separator 1 lower end is connected with spiral propeller 6 entrance through blanking device 5, spiral propeller 6 exports successively through the second cyclonic separator 2, 3rd cyclonic separator 3 is connected with separation column 13, bottom the second described cyclonic separator 2, an outlet is connected with the first heating chamber 7, another outlet is connected with entry locker 11 entrance, the 3rd described cyclonic separator 3 is all connected with entry locker 11 entrance by pipeline with the lower end outlet of the 4th cyclonic separator 4, described entry locker outlet 11 successively with the second heating chamber 8, second combustion chamber 10, interchanger 12 is connected.
The first described heating chamber 7 upper end is connected with the first combustion chamber 9 by riser tube, and an outlet of the first combustion chamber 9 is connected with spiral propeller 6 entrance, and another outlet is connected with the entrance of the 4th cyclonic separator 4.
The exit of described entry locker 11 is provided with blower fan 24.
Described interchanger 12 is also connected with generator 14, for thermal power generation.
Described separation column 13 is also arranged oil-gas separator 15 and vacuum pump 16, heavy constituent is connected with the second heating chamber 8, for providing fuel through heavy oil tank 17; Light constituent is connected with the first heating chamber 7 and the second heating chamber 8 after oil-gas separator 15, vacuum pump 16, gas-holder 18.
The pneumatic outlet of the first described cyclonic separator 1 is connected with chimney 20 through flue gas processing device 19.
The material inlet of the first described cyclonic separator 1 also can connect dryer 21 and pulverizer 22.
In the first described heating chamber 7 and the second heating chamber 8, burner 23 is all set.
Principle of work of the present invention is as follows:
Material after drying, pulverizing enters the first cyclonic separator 1, through first time solid and gas separation, solid after separation is after the transmission of blanking device 5 and spiral propeller 6, successively through the second cyclonic separator 2, the 3rd cyclonic separator 3, finally enter separation column 13, gas is discharged by chimney 20 after flue gas processing device 19 processes; The first combustion chamber 9 is arrived after a solid part for the second cyclonic separator 2 separation enters the first heating chamber 7, the outlet of the first combustion chamber 9 is connected with the opening for feed of the 4th cyclonic separator 4, carry out the 4th solid and gas to be separated, the solids exit mouth of the second cyclonic separator 2, the 3rd cyclonic separator 3, the 4th cyclonic separator 4 is also connected with entry locker 11, the material that entry locker is 11 li enters through blower fan 24 effect heat energy that the second heating chamber 8 and the second combustion chamber 10, combustion chamber 10, second produce and enters generator 14 through interchanger 12 and generate electricity;
Separation column 13 is also arranged oil-gas separator 15 and vacuum pump 16, heavy constituent is connected with the second heating chamber 8, for providing fuel through heavy oil tank 17; Light constituent is connected with the first heating chamber 7 and the second heating chamber 8 after oil-gas separator 15, vacuum pump 16, gas-holder 18.

Claims (8)

1. an oil-sand cracker, is characterized in that: comprise the first cyclonic separator (1), second cyclonic separator (2), 3rd cyclonic separator (3), 4th cyclonic separator (4), blanking device (5), spiral propeller (6), first heating chamber (7), second heating chamber (8), first combustion chamber (9), second combustion chamber (10), entry locker (11), interchanger (12), separation column (13), described the first cyclonic separator (1) lower end is connected with spiral propeller (6) entrance through blanking device (5), and spiral propeller (6) outlet is successively through the second cyclonic separator (2), 3rd cyclonic separator (3) is connected with separation column (13), described the second cyclonic separator (2) bottom one outlet is connected with the first heating chamber (7), another outlet is connected with entry locker (11) entrance, the lower end outlet of the 3rd described cyclonic separator (3) and the 4th cyclonic separator (4) is all connected with entry locker (11) entrance by pipeline, described entry locker export (11) successively with the second heating chamber (8), second combustion chamber (10), interchanger (12) is connected.
2. oil-sand cracker according to claim 1, it is characterized in that: described the first heating chamber (7) upper end is connected with the first combustion chamber (9) by riser tube, one outlet of the first combustion chamber (9) is connected with spiral propeller (6) entrance, and another outlet is connected with the entrance of the 4th cyclonic separator (4).
3. oil-sand cracker according to claim 1, is characterized in that: the exit of described entry locker (11) is provided with blower fan (24).
4. oil-sand cracker according to claim 1, is characterized in that: described interchanger (12) is also connected, for thermal power generation with generator (14).
5. oil-sand cracker according to claim 1, is characterized in that: described separation column (13) is also arranged oil-gas separator (15) and vacuum pump (16), heavy constituent is connected with the second heating chamber (8), for providing fuel through heavy oil tank (17); Light constituent is connected with the first heating chamber (7) and the second heating chamber (8) after oil-gas separator (15), vacuum pump (16), gas-holder (18).
6. oil-sand cracker according to claim 1, is characterized in that: the pneumatic outlet of described the first cyclonic separator (1) is connected with chimney (20) through flue gas processing device (19).
7. oil-sand cracker according to claim 1, is characterized in that: the material inlet of described the first cyclonic separator (1) also can connect dryer (21) and pulverizer (22).
8. oil-sand cracker according to claim 1, is characterized in that: all arrange burner (23) in described the first heating chamber (7) and the second heating chamber (8).
CN201510876568.4A 2015-12-03 2015-12-03 Oil sand cracking device Pending CN105316023A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510876568.4A CN105316023A (en) 2015-12-03 2015-12-03 Oil sand cracking device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510876568.4A CN105316023A (en) 2015-12-03 2015-12-03 Oil sand cracking device

Publications (1)

Publication Number Publication Date
CN105316023A true CN105316023A (en) 2016-02-10

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CN201510876568.4A Pending CN105316023A (en) 2015-12-03 2015-12-03 Oil sand cracking device

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108277034A (en) * 2018-01-23 2018-07-13 浙江华耘环保科技有限公司 A kind of oil-sand cracker

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1962818A (en) * 2005-11-08 2007-05-16 李效时 Process for preparing bio-oil by using rapid thermal cleavage technology
CN101691495A (en) * 2009-10-28 2010-04-07 中国科学院广州能源研究所 Method and device for preparing bio-oil and chemicals by pyrolyzing biomass in steps
CN102031131A (en) * 2010-12-20 2011-04-27 河南中埠新能源有限公司 Pyrolytic process and device capable of directly transforming straws into petrol and diesel
WO2012172527A2 (en) * 2011-06-17 2012-12-20 Amit Tandon Method and apparatus for continuous recycling of waste plastic into liquid fuels
CN103031139A (en) * 2012-10-22 2013-04-10 华北电力大学 Device and method for preparing bio-oil through rapid biomass pyrolysis
CN103289714A (en) * 2013-06-28 2013-09-11 庆华集团新疆和丰能源化工有限公司 Dry distiller and oil sand pyrolysis-dry distillation system
CN103497776A (en) * 2013-09-09 2014-01-08 山东理工大学 Heat-carrier self-loop heating type agricultural waste cracking liquefying system
CN205241603U (en) * 2015-12-03 2016-05-18 南京绿帝环保能源科技有限公司 Oil sand cracker

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1962818A (en) * 2005-11-08 2007-05-16 李效时 Process for preparing bio-oil by using rapid thermal cleavage technology
CN101691495A (en) * 2009-10-28 2010-04-07 中国科学院广州能源研究所 Method and device for preparing bio-oil and chemicals by pyrolyzing biomass in steps
CN102031131A (en) * 2010-12-20 2011-04-27 河南中埠新能源有限公司 Pyrolytic process and device capable of directly transforming straws into petrol and diesel
WO2012172527A2 (en) * 2011-06-17 2012-12-20 Amit Tandon Method and apparatus for continuous recycling of waste plastic into liquid fuels
CN103031139A (en) * 2012-10-22 2013-04-10 华北电力大学 Device and method for preparing bio-oil through rapid biomass pyrolysis
CN103289714A (en) * 2013-06-28 2013-09-11 庆华集团新疆和丰能源化工有限公司 Dry distiller and oil sand pyrolysis-dry distillation system
CN103497776A (en) * 2013-09-09 2014-01-08 山东理工大学 Heat-carrier self-loop heating type agricultural waste cracking liquefying system
CN205241603U (en) * 2015-12-03 2016-05-18 南京绿帝环保能源科技有限公司 Oil sand cracker

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108277034A (en) * 2018-01-23 2018-07-13 浙江华耘环保科技有限公司 A kind of oil-sand cracker

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