CN105295982A - Oil shale and biomass poly-generation comprehensive utilization system and process thereof - Google Patents
Oil shale and biomass poly-generation comprehensive utilization system and process thereof Download PDFInfo
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- CN105295982A CN105295982A CN201510794082.6A CN201510794082A CN105295982A CN 105295982 A CN105295982 A CN 105295982A CN 201510794082 A CN201510794082 A CN 201510794082A CN 105295982 A CN105295982 A CN 105295982A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Abstract
The present invention discloses an oil shale and biomass poly-generation comprehensive utilization system, which comprises a material bin, a dry distillation furnace, an oil tank, an oil-gas separation device, a gas purification device, a high-temperature gas heating furnace, a gas storage tank, a gas burner, a low-temperature gas heating furnace, a gas turbine, a heat exchanger, a fuel cylinder, a steam turbine, a circulating fluidized bed boiler and a material feeder, wherein an oil shale and biomass mixture is used to be subjected to dry distillation. The present invention further discloses a process, wherein combustible gas is divided into three parts through the gas storage tank, the first part is adopted as the gas heat carrier of the dry distillation furnace, the second part is adopted as the fuel so as to be burned in the gas burner and the generated high-temperature flue gas is used for heating the gas heat carrier in the high-temperature gas heating furnace, and the third part is conveyed into the gas turbine so as to be burned and the generated high-temperature flue gas enters the low-temperature gas heating furnace after the work so as to heat the gas heat carrier. According to the present invention, the oil shale and the biomass are subjected to mixed dry distillation, such that the yield of the combustible gas is improved, and the purposes of heat supply, mass transfer and the heat carrying of the combustible gas burning are achieved.
Description
Technical field
The invention belongs to oil shale resources and utilize technical field, particularly relate to a kind of Poly-generation utilization system and technique thereof of resinous shale attendants.
Background technology
Resinous shale is a kind of important unconventional petroleum resources, reserves are huge, in the destructive distillation device of 400 ~ 600 DEG C, after pyrolysis, just availability matter is similar to the shale oil of natural oil, in the age of world's oil supply anxiety, supplements the energy as very important oil always.At present, explored shale oil reserves hundred million tons (by oil shale in-situ calculation of reserves) more than 4000, verify workable reserve higher than world's crude oil far away in the world.China is oil shale resources reserves big countries, has verified oil shale resources reserves 7199.37 hundred million tons, and the reserves being converted to shale oil are 476.44 hundred million tons.
For alleviating the nervous situation of world today's oil supply, resinous shale is subject to the favor of more and more national.Many countries and scientific research institution are on the basis of long period of development work, develop multiple distillation process, representative at present have Australian ATP retorting technique, Brazilian Petrosix retorting technique, Estonia Galoter and Kiviter retorting technique and China's fushun retort oven retorting technique etc. for industrial retorting technique.Although through years development, these technology are gradually improved, but still there are some difficult problems in actual motion, cannot be solved.Such as ATP retorting technique thermosteresis is comparatively large, and Galoter technical process is complicated, and the oil shale powder scrap that fushun retort oven retorting technique produces and oil shale semi-coke are not effectively recycled, and meanwhile, water resources is also wasted seriously.In view of these problems, the resinous shale workers of the country such as China, the U.S., Estonia advise more and more oil shale industry preferably walk the Comprehensive of " liquefaction-generating-chemical industry and building materials " utilize technological line, thus realize oil shale resources efficiently and clean utilization.
Patent of invention CN200810013088.5 discloses gas full-circulation oil-shale grading dry distillation technique and device, semicoke mixing gas combustion is adopted to provide heat for carbonization furnace, but the semicoke in this technique needs first through water-cooled before combustion, thus cause water resource pollution and the waste of semicoke sensible heat, meanwhile, semicoke calorific value through water logging is relatively low, and ratio of combustion is more difficult.Publication CN201210189395.5 and patent of invention CN201110443734.3 proposes gas-solid built-up type heat-carrying oil shale fluidized bed dry distillation system and Oil shale rotary kiln destructive distillation and circulating fluidized bed combustion technique respectively, adopt the shale ashes of oil shale combustion generation as oil shale distillation solid thermal carriers, but the transmission relative difficulty of high temperature shale ashes, too much shale ashes can cause very strong adsorption to oil shale retort product simultaneously, thus yield of the product is reduced.
Summary of the invention
In order to improve the output of inflammable gas in oil shale distillation process, and solving the material transferring problem of solid thermal carriers, the object of this invention is to provide a kind of Poly-generation utilization system and technique thereof.The Poly-generation utilization system of a kind of resinous shale attendants provided by the invention, comprise feed bin, gas retort, gas and oil separating plant, oil tank, also comprise high temperature gas heating furnace, mash gas purification apparatus, gas storage tank, nondestructive inspection gas burner, internal combustion turbine, chimney, low temperature gas heating furnace, steam turbine, interchanger, circular fluid bed and feeding machine; Wherein,
Feed bin is connected with gas retort, for sample introduction; The top of gas retort is connected with gas and oil separating plant; Gas and oil separating plant is connected with oil tank and mash gas purification apparatus; Mash gas purification apparatus is connected with gas storage tank; Gas storage tank is connected with nondestructive inspection gas burner, internal combustion turbine and low temperature gas heating furnace respectively; Nondestructive inspection gas burner is all connected with high temperature gas heating furnace with low temperature gas heating furnace; Internal combustion turbine is connected with low temperature gas heating furnace; High temperature gas heating furnace is connected with gas retort;
The bottom of gas retort is connected with feeding machine; Feeding machine is connected with circular fluid bed; Circular fluid bed is connected with steam turbine through interchanger;
Low temperature gas heating furnace, high temperature gas heating furnace are all connected with chimney with interchanger;
Poly-generation utilization system uses the mixture of resinous shale and biomass to carry out destructive distillation.
Further, low temperature gas heating furnace, high temperature gas heating furnace are all connected with chimney with interchanger, be connected with the second Y-pipe with high temperature gas heating furnace, interchanger respectively particular by the first Y-pipe, the second Y-pipe connects low temperature gas heating furnace and chimney again respectively.
Further, internal combustion turbine and steam turbine are connected power generation assembly or heating plant respectively.
Further, the top of gas retort is connected with feed bin.
Further, the top of gas retort is connected with gas and oil separating plant; The bottom of gas retort is connected with feeding machine.
The present invention also provides a kind of technique using the Poly-generation utilization system of above-described resinous shale attendants, comprises the following steps:
Step one, the resinous shale after dry, fragmentation is mixed with biomass after send into feed bin;
Step 2, the mixture of the resinous shale in feed bin and biomass is sent into gas retort, carry out low-temperature pyrolysis and produce inflammable gas, oil vapour and solid waste semicoke;
Inflammable gas in step 3, step 2 and oil vapour leave from gas retort top, are separated into inflammable gas and oil through gas and oil separating plant, and inflammable gas is stored in gas storage tank after mash gas purification apparatus purification, and oil is stored in oil tank;
The inflammable gas that step 3 produces is divided into three parts by step 4, gas storage tank: first part, as gaseous heat-carrier, sends into gas retort after low temperature gas heating furnace and the heating of high temperature gas heating furnace; Second section burns at nondestructive inspection gas burner as fuel, and the high-temperature flue gas of generation is for heating the gaseous heat-carrier in high temperature gas heating furnace; Part III sends into gas turbine combustion, leaves internal combustion turbine, enter low temperature gas heating furnace heated air thermal barrier after the high-temperature flue gas acting of generation.
Further, also comprise:
The solid waste semicoke that step 5, step 2 produce enters burning in circulating fluid bed boiler through feeding machine.
Further, also comprise:
Working-medium water in the high-temperature flue gas heating heat exchanger that in step 6, step 5, burning in circulating fluid bed boiler produces, produces high-temperature steam and enters steam turbine, for supplying heat and generating power.
Further, also comprise:
Flue gas flow equalizing in flue gas in step 7, step 6 in interchanger, step 4 in low temperature gas heating furnace and high temperature gas heating furnace enters chimney and is discharged.
Further, also comprise:
Step 8, the shale lime-ash produced in circular fluid bed in step 5 to be used as building materials and industrial chemicals.
Wherein, there is not sequencing in step 3 and step 5 and step 6; There is not sequencing in step 5 and step 3 and step 4; There is not sequencing in step 8 and step 3, step 4, step 6, step 7.
Its technique effect comprises:
1) using resinous shale attendants as propellant combination, make up the many characteristics of the few oil of oil shale gas less with biogas heavy wool, produce and sufficient not only can be used as thermal barrier, but also can be used as the inflammable gas of fuel.
2) adopt the biomass energy as a supplement, mixing oil shale retorting produces more inflammable gas, and the inflammable gas liberated heat overcoming the independent destructive distillation generation of resinous shale is not enough to maintain the heat needed for itself destructive distillation.
3) thermal barrier that gas retort is used is the inflammable gas through two-step heating, thus overcomes the difficulty of solid thermal carriers transmission.
4) take two-step heating stove to provide heat for thermal barrier, successfully also effectively utilize the calorific value in destructive distillation discharge inflammable gas, realize the recycle of energy.
5) circular fluid bed operating temperature is 850 ~ 900 DEG C, belongs to low-temperature burning, effectively controls generation and the discharge of NOx, and semicoke fixed carbon can be fully used, and in shale ashes, carbon content is few, can directly as building materials and industrial chemicals.
6) present invention achieves the comprehensive optimal control of resinous shale, decrease power loss dramatically, and achieve product diversification, produce shale oil, gas, electricity etc. simultaneously.
7) using the high-temp solid waste of gas retort generation as circulating fluidized bed boiler fuel, the high-temperature flue gas gasifying boiler feedwater produced, the steam produced is used for heat supply and acting, generating, achieve the recycling of solid waste semicoke, add the added benefit that oil shale distillation utilizes, improve energy utilization rate simultaneously, decrease chemical pollution and the thermal pollution of oil shale residues.
8) thermal barrier of institute's heat requirement using inflammable gas as oil shale distillation, thus overcome the difficulty of solid thermal carriers transmission.
9) whole system oil shale distillation oil yield rate is higher, avoids the problem of environmental pollution of solid waste semicoke, thus achieves cleaning, the efficiency utilization of oil shale resources.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the Poly-generation utilization system of a kind of resinous shale attendants of the present invention.
Wherein, 1-feed bin, 2-gas retort, 3-gas and oil separating plant, 4-oil tank, 5-high temperature gas heating furnace, 6-mash gas purification apparatus, 7-gas storage tank, 8-nondestructive inspection gas burner, 9-internal combustion turbine, 10-chimney, 11-low temperature gas heating furnace, 12-steam turbine, 13-interchanger, 14-circular fluid bed and 15-feeding machine.
Embodiment
Be described further below with reference to the technique effect of accompanying drawing to design of the present invention, concrete structure and generation, to understand object of the present invention, characteristic sum effect fully.
As shown in Figure 1, the resinous shale after dry, fragmentation mixes rear feeding feed bin 1 by a certain percentage with biomass, under be advanced into gas retort 2, low-temperature pyrolysis generation inflammable gas, oil vapour and solid waste semicoke.Inflammable gas and oil vapour leave from gas retort 2 top, are separated into inflammable gas and oil through gas and oil separating plant 3, and inflammable gas is stored in gas storage tank 7 after mash gas purification apparatus 6 purifies, and oil is stored in oil tank 4; Semicoke enters circular fluid bed 14 through feeding machine 15 and burns; Inflammable gas is divided into three parts by gas storage tank 7: first part, as gaseous heat-carrier, sends into gas retort 2 after low temperature gas heating furnace 11 and high temperature gas heating furnace 5 heat; Second section burns at nondestructive inspection gas burner 8 as fuel, and the high-temperature flue gas of generation is for heating gaseous heat-carrier in high temperature gas heating furnace 5; Part III is sent into internal combustion turbine 9 and is burnt, and leaves internal combustion turbine 9, enter low temperature gas heating furnace 11 heated air thermal barrier after the acting of the high-temperature flue gas of generation, generating; Working-medium water in the high-temperature flue gas heating heat exchanger 13 that circular fluid bed 14 produces, produces high-temperature steam and enters steam turbine 12, for supplying heat and generating power; Chimney 10 is flowed in the lump after gathering from the flue gas of interchanger 13, low temperature gas heating furnace 11 and high temperature gas heating furnace 5; The shale lime-ash that circular fluid bed 14 produces can be used as building materials and industrial chemicals.
More than describe preferred embodiment of the present invention in detail.Should be appreciated that those of ordinary skill in the art just design according to the present invention can make many modifications and variations without the need to creative work.Therefore, all technician in the art, all should by the determined protection domain of claims under this invention's idea on the basis of existing technology by the available technical scheme of logical analysis, reasoning, or a limited experiment.
Claims (10)
1. the Poly-generation utilization system of a resinous shale attendants, comprise feed bin, gas retort, gas and oil separating plant, oil tank, it is characterized in that, also comprise high temperature gas heating furnace, mash gas purification apparatus, gas storage tank, nondestructive inspection gas burner, internal combustion turbine, chimney, low temperature gas heating furnace, steam turbine, interchanger, circular fluid bed and feeding machine; Wherein,
Described feed bin is connected with described gas retort, for sample introduction; The top of described gas retort is connected with described gas and oil separating plant; Described gas and oil separating plant is connected with described oil tank and described mash gas purification apparatus; Described mash gas purification apparatus is connected with described gas storage tank; Described gas storage tank is connected with described nondestructive inspection gas burner, described internal combustion turbine and described low temperature gas heating furnace respectively; Described nondestructive inspection gas burner is all connected with described high temperature gas heating furnace with described low temperature gas heating furnace; Described internal combustion turbine is connected with described low temperature gas heating furnace; Described high temperature gas heating furnace is connected with described gas retort;
The bottom of described gas retort is connected with described feeding machine; Described feeding machine is connected with described circular fluid bed; Described circular fluid bed is connected with described steam turbine through described interchanger;
Described low temperature gas heating furnace, described high temperature gas heating furnace are all connected with described chimney with described interchanger;
Described Poly-generation utilization system uses the mixture of resinous shale and biomass to carry out destructive distillation.
2. the Poly-generation utilization system of resinous shale attendants as claimed in claim 1, it is characterized in that, described low temperature gas heating furnace, described high temperature gas heating furnace are all connected with described chimney with described interchanger, be connected with the second Y-pipe with described high temperature gas heating furnace, described interchanger respectively particular by the first Y-pipe, described second Y-pipe connects again described low temperature gas heating furnace and described chimney respectively.
3. the Poly-generation utilization system of resinous shale attendants as claimed in claim 1, it is characterized in that, described internal combustion turbine is connected power generation assembly or heating plant respectively with described steam turbine.
4. the Poly-generation utilization system of resinous shale attendants as claimed in claim 1, it is characterized in that, the top of described gas retort is connected with described feed bin.
5. the Poly-generation utilization system of resinous shale attendants as claimed in claim 1, it is characterized in that, the top of described gas retort is connected with described gas and oil separating plant; The bottom of described gas retort is connected with described feeding machine.
6. use a technique for the Poly-generation utilization system of resinous shale attendants as claimed in claim 1, it is characterized in that, comprise the following steps:
Step one, the resinous shale after dry, fragmentation mixed with biomass and sends into described feed bin afterwards;
Step 2, the mixture of the resinous shale in described feed bin and biomass is sent into described gas retort, carry out low-temperature pyrolysis and produce inflammable gas, oil vapour and solid waste semicoke;
Described inflammable gas in step 3, described step 2 and described oil vapour leave from described gas retort top, inflammable gas and oil is separated into through described gas and oil separating plant, described inflammable gas is stored in described gas storage tank after described mash gas purification apparatus purification, and described oil is stored in described oil tank;
The described inflammable gas that described step 3 produces by step 4, described gas storage tank is divided into three parts: first part, as gaseous heat-carrier, sends into described gas retort after described low temperature gas heating furnace and the heating of described high temperature gas heating furnace; Second section burns at described nondestructive inspection gas burner as fuel, and the high-temperature flue gas of generation is for heating the described gaseous heat-carrier in described high temperature gas heating furnace; Part III sends into described gas turbine combustion, leaves described internal combustion turbine, enter described low temperature gas heating furnace and heat described gaseous heat-carrier after the high-temperature flue gas acting of generation.
7. the technique of the Poly-generation utilization system of resinous shale attendants as claimed in claim 6, is characterized in that, further comprising the steps of:
The described solid waste semicoke that step 5, described step 2 produce enters described burning in circulating fluid bed boiler through described feeding machine.
8. the technique of the Poly-generation utilization system of resinous shale attendants as claimed in claim 7, is characterized in that, further comprising the steps of:
The high-temperature flue gas that burning in circulating fluid bed boiler described in step 6, described step 5 produces heats the working-medium water in described interchanger, produces high-temperature steam and enters described steam turbine, for supplying heat and generating power.
9. the technique of the Poly-generation utilization system of resinous shale attendants as claimed in claim 8, is characterized in that, further comprising the steps of:
Flue gas flow equalizing in low temperature gas heating furnace described in flue gas in interchanger described in step 7, described step 6, described step 4 and described high temperature gas heating furnace enters described chimney and is discharged.
10. the technique of the Poly-generation utilization system of resinous shale attendants as claimed in claim 9, is characterized in that, further comprising the steps of:
Step 8, the shale lime-ash produced in circular fluid bed in described step 5 to be used as building materials and industrial chemicals.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105255508A (en) * | 2015-11-18 | 2016-01-20 | 上海交通大学 | Poly-generation utilization system of oil shale with highly-volatile coal and process of system |
| CN105295983A (en) * | 2015-11-18 | 2016-02-03 | 上海交通大学 | Oil shale and organic solid waste poly-generation utilization system and process thereof |
| CN111978972A (en) * | 2020-08-05 | 2020-11-24 | 上海工程技术大学 | Straw waste coupling oil shale comprehensive utilization system and process |
| CN111996020A (en) * | 2020-08-06 | 2020-11-27 | 上海工程技术大学 | Biomass waste coupling wet garbage multi-state co-production comprehensive utilization system and process |
| CN112195034A (en) * | 2020-09-15 | 2021-01-08 | 上海工程技术大学 | Biomass waste volatile component catalytic oil shale dry distillation coupling system and method |
| CN112899000A (en) * | 2019-11-19 | 2021-06-04 | 上海工程技术大学 | Biomass waste volatile component catalytic oil shale dry distillation coupling system and method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102942943A (en) * | 2012-11-16 | 2013-02-27 | 东北电力大学 | Oil shale gas-solid heat carrier dry distillation and semicoke combustion electricity generation integral process |
| CN102977904A (en) * | 2012-11-16 | 2013-03-20 | 东北电力大学 | Oil shale synthesized utilization method |
| CN103038317A (en) * | 2010-04-13 | 2013-04-10 | 耐克斯奥尔股份公司 | Method for thermally cleaving organic waste having high molecular weight |
| CN105295983A (en) * | 2015-11-18 | 2016-02-03 | 上海交通大学 | Oil shale and organic solid waste poly-generation utilization system and process thereof |
-
2015
- 2015-11-18 CN CN201510794082.6A patent/CN105295982B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103038317A (en) * | 2010-04-13 | 2013-04-10 | 耐克斯奥尔股份公司 | Method for thermally cleaving organic waste having high molecular weight |
| CN102942943A (en) * | 2012-11-16 | 2013-02-27 | 东北电力大学 | Oil shale gas-solid heat carrier dry distillation and semicoke combustion electricity generation integral process |
| CN102977904A (en) * | 2012-11-16 | 2013-03-20 | 东北电力大学 | Oil shale synthesized utilization method |
| CN105295983A (en) * | 2015-11-18 | 2016-02-03 | 上海交通大学 | Oil shale and organic solid waste poly-generation utilization system and process thereof |
Non-Patent Citations (2)
| Title |
|---|
| 生物质与油页岩混合热解特性研究;田红，廖正祝;《洁净煤技术》;20150531;第21卷(第3期);第94页引言部分 * |
| 田红，廖正祝: "生物质与油页岩混合热解特性研究", 《洁净煤技术》 * |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105255508A (en) * | 2015-11-18 | 2016-01-20 | 上海交通大学 | Poly-generation utilization system of oil shale with highly-volatile coal and process of system |
| CN105295983A (en) * | 2015-11-18 | 2016-02-03 | 上海交通大学 | Oil shale and organic solid waste poly-generation utilization system and process thereof |
| CN112899000A (en) * | 2019-11-19 | 2021-06-04 | 上海工程技术大学 | Biomass waste volatile component catalytic oil shale dry distillation coupling system and method |
| CN111978972A (en) * | 2020-08-05 | 2020-11-24 | 上海工程技术大学 | Straw waste coupling oil shale comprehensive utilization system and process |
| CN111996020A (en) * | 2020-08-06 | 2020-11-27 | 上海工程技术大学 | Biomass waste coupling wet garbage multi-state co-production comprehensive utilization system and process |
| CN112195034A (en) * | 2020-09-15 | 2021-01-08 | 上海工程技术大学 | Biomass waste volatile component catalytic oil shale dry distillation coupling system and method |
| CN112195034B (en) * | 2020-09-15 | 2021-10-08 | 上海工程技术大学 | Biomass waste volatile component catalytic oil shale dry distillation coupling system and method |
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