CN101240180A - Oil shale oil-refining, power generation and cement triple production integrated device - Google Patents
Oil shale oil-refining, power generation and cement triple production integrated device Download PDFInfo
- Publication number
- CN101240180A CN101240180A CNA2008100469964A CN200810046996A CN101240180A CN 101240180 A CN101240180 A CN 101240180A CN A2008100469964 A CNA2008100469964 A CN A2008100469964A CN 200810046996 A CN200810046996 A CN 200810046996A CN 101240180 A CN101240180 A CN 101240180A
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- oil shale
- cement
- fluid bed
- destructive distillation
- oil
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Abstract
An oil shale refining, power generating and cement tri-generating integrated device smashes the oil shale ore to 0 to 8mm and sends the oil shale ore to a carbonization device via a distributor to prepare the oil shale and fuel gas. The generated half coking castoff of oil shale with high temperature enters a circulating fluidized bed boiler via a conveyor to burn. The generated heat is converted to steam which can be applied to generating power, supplying heat and extracting high temperature soot at 550 degree C to 750 degree C from the circulating fluidized bed to enter the carbonization device as carbonization heat medium; slag discharged from the circulating fluidized bed boiler and part of discharged ash of the separator as well as precipitator dust directly enter a calciner for calcining, generating cement. The invention applies heat energy synthetically, which saves energy and protects environment.
Description
Technical field
The present invention relates to a kind of oil shale oil-refining, generating and cement triple production integrated device.
Background technology
The comprehensive utilization of oil refining, boiler combustion and the cement building material of resinous shale is at present finished in gas retort, circular fluid bed and cement building material factory respectively, be to finish by three covering devices independently, do not become one, so just have following problem: the oil refining gas retort of resinous shale can't directly be handled the 0-8mm oil shale particle; The semicoke that gas retort is discharged can't directly enter burning in circulating fluid bed boiler, needs intercooling with broken, the comprehensive utilization weak effect of resinous shale; The lime-ash of discharging from circulating fluidized bed can only making cement ginseng and material, can not directly produce cement of high index as cement clinker; Gas retort, circular fluid bed and cement kiln are relatively independent systems, do not realize coproduction, need intermediate transportation, so energy consumption is big, investment is big.
Summary of the invention
The purpose of this invention is to provide a kind of oil shale oil-refining, generating and cement triple production integrated device, it can get final product save energy with oil refining, the burning in circulating fluid bed boiler generating and cement triple production integrated finishing of resinous shale, reaches environment protecting again.
The present invention is achieved like this, it comprises shredding unit, destructive distillation device, condensing works, circular fluid bed, calcining furnace, variable valve, fly-ash separator, pulverizing mill, it is characterized in that shredding unit connects destructive distillation device, destructive distillation device connects shale oil condensing works and circular fluid bed, circular fluid bed connects fly-ash separator, destructive distillation device and calcining furnace, calcining furnace connects fly-ash separator and circular fluid bed, is connected with variable valve and separator at circular fluid bed and destructive distillation device and circular fluid bed and fly-ash separator.
Technique effect of the present invention is: the oil refining destructive distillation device can directly be handled 0-8mm oil page or leaf particle, produce shale oil and combustion gas, high temperature semicoke waste directly enters boiler combustion, the heat that produces is converted into steam and is used for generating electricity and heat supply, high-temperature flue gas enters destructive distillation device as the destructive distillation thermal medium, flue gas after the destructive distillation is back boiler again, and the high-temperature ash that boiler is discharged and the ash discharge of fly-ash separator directly enter calcining furnace and calcine production cement, promptly energy-conservation environmental protection again.
Description of drawings
Fig. 1 is a fundamental diagram of the present invention.
Embodiment
As shown in Figure 1, the present invention includes shredding unit 1, destructive distillation device 2, condensing works 3, circular fluid bed 4, calcining furnace 8, variable valve 5, fly-ash separator 7, pulverizing mill 9 features is that shredding unit 1 connects destructive distillation device 2, destructive distillation device 2 connects shale oil condensing works 3 and circular fluid bed 4, circular fluid bed 4 connects fly-ash separator 7, destructive distillation device 2 and calcining furnace 8, calcining furnace 8 connects fly-ash separators 7 and circular fluid beds 4, in being connected of circular fluid bed 4 and destructive distillation device 2 and circular fluid bed 4 and fly-ash separator 7 variable valve 5 is arranged.During use, resinous shale through shredding unit 1 broken be sized to 0 ~ 8mm after, send in preposition (or side) destructive distillation device 2 of circular fluid bed 4 and carry out destructive distillation, 450 ~ 600 ℃ of pyrolysis temperatures, the destructive distillation gas that destructive distillation produces enters condensing works 3, isolates shale oil and combustion gas; The high temperature that is produced in the oil shale distillation process (500 ~ 750 ℃) semicoke directly enters in the circular fluid bed 4 and so burns, and temperature of combustion is 750-950 ℃, and the heat of generation is converted into steam, can be used to generating and heat supply; 550 ~ 750 ℃ high temperature position is extracted flue gas out and is entered in the retort section of destructive distillation device 2 as the destructive distillation thermal medium from circular fluid bed 4, and 500 ~ 600 ℃ of flue gases after the destructive distillation return in the circular fluid bed 4 by flue.Boiler enters the preheating section that 150 ~ 250 ℃ partial fume before the fly-ash separator is introduced in the destructive distillation device 2 by variable valve 5, and resinous shale is carried out preheating; Last smoke evacuation enters fly-ash separator and enters chimney again after mixing; 700 ~ 850 ℃ of ash discharges of part of separator at the bottom of discharge from circular fluid bed 750 ~ 950 ℃ slag and the circular fluid bed and fly-ash separator ash discharge enter calcining furnace respectively and calcine, calcine required fuel and coagulate the combustible gas of discharging in the device 3,1100 ~ 1300 ℃ of calcining temperatures for destructive distillation air cooling.
Claims (1)
1, a kind of oil shale oil-refining, generating and cement triple production integrated device, it comprises shredding unit, destructive distillation device, condensing works, circular fluid bed, calcining furnace, variable valve, fly-ash separator, pulverizing mill, it is characterized in that shredding unit connects destructive distillation device, destructive distillation device connects shale oil condensing works and circular fluid bed, circular fluid bed connects fly-ash separator, destructive distillation device and calcining furnace, calcining furnace connects fly-ash separator and circular fluid bed, in being connected of circular fluid bed and destructive distillation device and circular fluid bed and fly-ash separator variable valve is arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100469964A CN101240180A (en) | 2008-03-03 | 2008-03-03 | Oil shale oil-refining, power generation and cement triple production integrated device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100469964A CN101240180A (en) | 2008-03-03 | 2008-03-03 | Oil shale oil-refining, power generation and cement triple production integrated device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101240180A true CN101240180A (en) | 2008-08-13 |
Family
ID=39932013
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2008100469964A Pending CN101240180A (en) | 2008-03-03 | 2008-03-03 | Oil shale oil-refining, power generation and cement triple production integrated device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101240180A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102585864A (en) * | 2012-03-20 | 2012-07-18 | 东北石油大学 | Oil shale surface retorting and power plant boiler and steam turbine exhaust comprehensive recycling process |
| CN103013546A (en) * | 2012-12-26 | 2013-04-03 | 江联重工股份有限公司 | Method for realizing oil shale refining and boiler combustion with steam cogeneration by integrating novel oil shale refining with differential fluidized bed combustion |
| CN106085489A (en) * | 2016-08-05 | 2016-11-09 | 南京绿帝环保能源科技有限公司 | Oil-sand cracking produces fuel oil and cement semi-finished product combined unit |
| CN107255287A (en) * | 2017-07-12 | 2017-10-17 | 重庆盎瑞悦科技有限公司 | A kind of high-efficiency comprehensive utilization method of high-moisture percentage oily sludge |
| CN108870381A (en) * | 2018-06-29 | 2018-11-23 | 西安西热锅炉环保工程有限公司 | A kind of biomass economy device and method based on coal-burning boiler high temperature flue gas |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1683472A (en) * | 2005-03-17 | 2005-10-19 | 上海交通大学 | Method for complex optimum using oil shale |
-
2008
- 2008-03-03 CN CNA2008100469964A patent/CN101240180A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1683472A (en) * | 2005-03-17 | 2005-10-19 | 上海交通大学 | Method for complex optimum using oil shale |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102585864A (en) * | 2012-03-20 | 2012-07-18 | 东北石油大学 | Oil shale surface retorting and power plant boiler and steam turbine exhaust comprehensive recycling process |
| CN103013546A (en) * | 2012-12-26 | 2013-04-03 | 江联重工股份有限公司 | Method for realizing oil shale refining and boiler combustion with steam cogeneration by integrating novel oil shale refining with differential fluidized bed combustion |
| CN106085489A (en) * | 2016-08-05 | 2016-11-09 | 南京绿帝环保能源科技有限公司 | Oil-sand cracking produces fuel oil and cement semi-finished product combined unit |
| CN106085489B (en) * | 2016-08-05 | 2018-06-26 | 南京绿帝环保能源科技有限公司 | A kind of combined unit of oil-sand cracking production fuel oil and cement semi-finished product |
| CN107255287A (en) * | 2017-07-12 | 2017-10-17 | 重庆盎瑞悦科技有限公司 | A kind of high-efficiency comprehensive utilization method of high-moisture percentage oily sludge |
| CN108870381A (en) * | 2018-06-29 | 2018-11-23 | 西安西热锅炉环保工程有限公司 | A kind of biomass economy device and method based on coal-burning boiler high temperature flue gas |
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Legal Events
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20080813 |