WO2023060946A1 - System and method for incinerating oil sludge by using power station pulverized coal boiler - Google Patents
System and method for incinerating oil sludge by using power station pulverized coal boiler Download PDFInfo
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- WO2023060946A1 WO2023060946A1 PCT/CN2022/102023 CN2022102023W WO2023060946A1 WO 2023060946 A1 WO2023060946 A1 WO 2023060946A1 CN 2022102023 W CN2022102023 W CN 2022102023W WO 2023060946 A1 WO2023060946 A1 WO 2023060946A1
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- coal
- oil sludge
- boiler
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- combustion
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- 239000010802 sludge Substances 0.000 title claims abstract description 142
- 239000003245 coal Substances 0.000 title claims abstract description 135
- 238000000034 method Methods 0.000 title claims abstract description 28
- 238000002485 combustion reaction Methods 0.000 claims abstract description 57
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000003546 flue gas Substances 0.000 claims abstract description 25
- 239000000203 mixture Substances 0.000 claims abstract description 22
- 238000000746 purification Methods 0.000 claims abstract description 20
- 239000003795 chemical substances by application Substances 0.000 claims description 20
- 230000003750 conditioning effect Effects 0.000 claims description 20
- 239000000428 dust Substances 0.000 claims description 14
- 239000000843 powder Substances 0.000 claims description 13
- 238000010298 pulverizing process Methods 0.000 claims description 13
- 239000000126 substance Substances 0.000 claims description 12
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 10
- 230000008569 process Effects 0.000 claims description 9
- 230000008520 organization Effects 0.000 claims description 8
- 239000003344 environmental pollutant Substances 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- 231100000719 pollutant Toxicity 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 239000000446 fuel Substances 0.000 claims description 6
- 239000005995 Aluminium silicate Substances 0.000 claims description 5
- 239000000809 air pollutant Substances 0.000 claims description 5
- 231100001243 air pollutant Toxicity 0.000 claims description 5
- 235000012211 aluminium silicate Nutrition 0.000 claims description 5
- 239000000292 calcium oxide Substances 0.000 claims description 5
- 235000012255 calcium oxide Nutrition 0.000 claims description 5
- 238000006477 desulfuration reaction Methods 0.000 claims description 5
- 230000023556 desulfurization Effects 0.000 claims description 5
- 239000010881 fly ash Substances 0.000 claims description 5
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 5
- 230000004048 modification Effects 0.000 claims description 5
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- 239000002245 particle Substances 0.000 claims description 4
- 238000004458 analytical method Methods 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 230000002349 favourable effect Effects 0.000 claims description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 3
- 239000011707 mineral Substances 0.000 claims description 3
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- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 230000000704 physical effect Effects 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 239000013589 supplement Substances 0.000 claims description 3
- 238000002411 thermogravimetry Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 238000005457 optimization Methods 0.000 claims description 2
- 238000010791 quenching Methods 0.000 claims description 2
- 230000000171 quenching effect Effects 0.000 claims description 2
- 238000003860 storage Methods 0.000 claims description 2
- 238000005496 tempering Methods 0.000 claims description 2
- 238000012360 testing method Methods 0.000 claims description 2
- 238000000227 grinding Methods 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 description 10
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- 230000008901 benefit Effects 0.000 description 6
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- 238000010586 diagram Methods 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 3
- 150000002013 dioxins Chemical class 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 230000032258 transport Effects 0.000 description 3
- 239000002956 ash Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000003129 oil well Substances 0.000 description 2
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- 230000002195 synergetic effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/50—Control or safety arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K1/00—Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L9/00—Passages or apertures for delivering secondary air for completing combustion of fuel
-
- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Definitions
- the application belongs to the technical field of coal-fired boilers, and in particular relates to a system and method for incinerating oil sludge using a pulverized coal boiler of a power station.
- Oil sludge is one of the main solid wastes generated during the exploitation, transportation and utilization of petroleum and biomass oil. Since oil sludge is a hazardous waste with stable structure and difficult to handle, it cannot be disposed of by simple landfill method like traditional waste.
- Existing oil sludge treatment technologies mainly include: incineration, centrifugal separation, solvent extraction, and biological methods, among which incineration is the lowest cost and most widely used method.
- the traditional oil sludge incineration treatment is mainly carried out by establishing a dedicated incinerator separately.
- the difficulty of incinerator construction approval is increasing, and the construction cost is increasing day by day.
- the temperature of the incineration process is relatively low, and there may be organic pollutants such as dioxins in the flue gas generated at the furnace outlet, and the dioxins in the exhausted flue gas
- organic pollutants such as dioxins in the flue gas generated at the furnace outlet
- the dioxins in the exhausted flue gas The content of dust, NOx and SOx is generally much higher than the ultra-low emission standard required by the current environmental protection, which will cause great pollution to the surrounding environment.
- oil sludge has physical and chemical properties that are very different from raw coal. How to embed the transportation and combustion control of oil sludge in the existing pulverized coal power plant boiler system to form a system and method that can solve the problem of burning oil sludge in power plant pulverized coal boilers, especially Whether or not the existing boiler system can meet the incineration needs of oil sludge is also an important subject that needs to be studied urgently.
- the purpose of this application is to provide a system and method for incinerating oil sludge using a pulverized coal boiler in a power station.
- the oil sludge can be directly mixed with raw coal after a certain pretreatment, and passed through the boiler
- the existing pulverizing system is crushed and transported into the furnace of the boiler for incineration, and then purified by the existing flue gas purification device of the boiler to realize the utilization and harmless treatment of oil sludge.
- a method for burning oil sludge using a pulverized coal boiler of a power station comprising the steps of:
- Step 1 according to the analysis of the characteristics of the sludge, configure the sludge conditioner, and use the configured conditioner to modify the sludge with strong volatility and high water content;
- Step 2 feed the oil sludge and the prepared conditioning agent into the mixer respectively, fully stir them evenly in the mixer, use the conditioning agent to modify the oil sludge, reduce the physical properties and volatility of the liquid flow of the oil sludge, and make it Similar solid properties to raw coal;
- Step 3 Send the oil sludge after conditioning to the raw coal conveyor belt, and blend it with the raw coal on the coal conveyor belt according to the set ratio.
- the mass ratio of the blend is determined by the best ratio obtained from the blending test. ;
- Step 4 The mixed oil sludge and raw coal are sent to the existing pulverization system for pulverization, and then sent to the furnace of the pulverized coal power plant boiler through the powder feeding system for high-temperature incineration.
- the incineration process is a mixed combustion process of coal powder and oil sludge powder The temperature is controlled in the range of 1300-1600 °C to ensure the harmless treatment of harmful substances in the oil sludge, and the control of the mixed combustion process is adjusted in conjunction with the optimization control of the entire boiler combustion;
- Step 5 the dust, NOx and SOx pollutants produced by the combustion of raw coal and oil sludge in the boiler are purified through the denitrification, dust removal and desulfurization devices arranged in the flue at the tail of the boiler.
- step 1 the formulation of the conditioner is based on the specific indicators of the moisture and volatile content of the oil sludge, and the quicklime, fly ash and kaolin are used to configure according to the mass percentage, and the proportion of the configuration is mainly quicklime, accounting for 50-60%, fly ash accounts for 20-40%, and other minerals such as kaolin account for 10-20%.
- the final proportion of each component is determined by the composition characteristics of the oil sludge. The thermal gravimetric analysis experiment effect of oil sludge modification is confirmed by comparison.
- step 2 the oil sludge is modified with a conditioning agent, and a custom-made modulator is added based on favorable physical and chemical characteristics indicators to improve the fluidity and volatile characteristics of the oil sludge, specifically including
- the preparation agent After adding the preparation agent, the mud state with a high water content that is not suitable for storage is transformed into a solid state similar to coal with a water content below 20%, which is easy to store and transport.
- those volatile and flammable components are also contained in the preparation agent. Adsorbed by the porous modulator, the volatile performance is greatly reduced, and the mass ratio of the modulator is 20-30%.
- step 3 the tempered oil sludge and raw coal are blended on the coal conveyor belt according to the set ratio, and the mass ratio of the oil sludge that can be blended on the coal conveyor belt does not exceed 20%.
- a system for incinerating oil sludge using a pulverized coal boiler in a power station including a boiler, an air preheater, a blower, a primary fan, a flue gas purification device, a coal mill, a separator, a combustion system, a coal bunker, a coal conveyor belt, and a spiral agitator Device and mixer inlet;
- the heat generated by the combustion of fuel in the boiler passes through the heat exchange surface, and the secondary air and primary air sent by the blower and the primary fan are heated by the air preheater, and the heated secondary air passes through the organization of the boiler combustion system.
- the high-pressure head hot primary air sent by the primary fan is sent to the coal mill through the pipeline, and the raw coal and oil sludge mixture in the coal mill are dried and transported;
- Sludge and conditioning agent are respectively added to the feed inlet of the mixer at the entrance of the spiral agitator, and then the sludge and conditioning agent are stirred in the spiral agitator and mixed evenly and tempered, and the conditioned sludge is transported to Blending is carried out on the coal conveyor belt; the mixture of coal and oil sludge is sent to the coal bunker through the coal conveyor belt, and the mixture of raw coal and coal slime in the coal bunker is sent to the coal mill through the coal drop pipe, and after grinding and drying, Carried by the primary air, it enters the pulverized coal separator, and the pulverized coal separator transports the pulverized coal and oil sludge powder with qualified particle size to the combustion system through the powder delivery pipeline, and sends them into the boiler for combustion under the organization of the combustion system; the combustion produces
- the dust, NOx and SOx pollutants are purified by the dust removal, denitrification and desulfurization devices included in the flue gas purification device arranged on the tail flue.
- a further improvement of the present application is that the flue gas purified from air pollutants is discharged through the chimney.
- a further improvement of the present application is that the primary air volume is adjusted through the primary air adjustment door according to the actual needs of the pulverizing system.
- a further improvement of the present application is that the secondary air volume is adjusted through the secondary air adjustment door according to the actual needs of boiler combustion.
- This application provides a system and method for direct combustion of oil sludge based on pulverized coal power plant boilers. Based on the existing pulverizing system, combustion system and environmental protection equipment for flue gas purification of pulverized coal power plant boilers widely distributed in China, the After the oil sludge is modified by the conditioning agent, the oil sludge is mixed with the raw coal on the coal conveyor belt, then sent to the coal bunker, and then pulverized by the coal mill and sent to the boiler furnace for combustion.
- the system is simple, the construction cost is low, and there is no need to build a dedicated sludge incinerator and corresponding flue gas environmental protection equipment, saving a lot of infrastructure equipment and operation and maintenance costs;
- the thermal efficiency of oil sludge utilization is high, the temperature in the boiler is high, the combustion organization is advanced, the combustion efficiency can reach more than 98%, and cogeneration of heat and power can also be used.
- the thermal efficiency of the system is much higher than that of special oil sludge incinerators;
- the boiler incineration temperature is high, the temperature inside the boiler can usually be as high as 1600°C, and the toxic and harmful substances in the sludge can be completely harmless treated;
- the flue gas emission control has high environmental protection standards.
- the flue gas purification equipment of the power plant is advanced. Pollutants such as NOx, dust and SOx produced by sludge incineration can be treated by the existing environmental protection equipment of the power plant to meet the ultra-low emission standard and meet the Relevant requirements of environmental regulations.
- Fig. 1 is a flow chart of a method for incinerating oil sludge using a pulverized coal power plant boiler.
- Figure 2 is a structural block diagram of a system for incinerating oil sludge using a pulverized coal power plant boiler.
- Figure 3 is a schematic diagram of by-products of an oil well.
- Figure 4 is a schematic diagram of the appearance of a by-product of an oil well after quenching and tempering.
- this application makes full use of the system and equipment characteristics of the current coal-based power plant pulverized coal boiler, and modifies the sludge by adding a conditioner to the sludge to reduce the fluidity and volatility of the sludge.
- the modification process mainly It is carried out in a spiral agitator, and the oil sludge that has been tempered and modified is sent to the raw coal conveyor belt, sent to the coal bunker, and then pulverized and ground, and then burned in the furnace through the organization of the combustion system, and the flue gas passes through the environmental protection of the boiler system
- the device is purified to meet the emission standard of ultra-low emission.
- the application has a simple system structure and does not need to build a new oil sludge incinerator, oil sludge pre-treatment equipment and flue gas purification equipment, saving a lot of construction costs and equipment operation and maintenance costs.
- the pulverized coal power plant boiler has the advantages of large capacity, high combustion temperature, high boiler combustion and thermal efficiency, and good flue gas purification performance of the boiler flue gas purification equipment, the oil sludge can be treated more thoroughly and harmlessly, and can be fully Utilize the thermal resources of oil sludge, and give full play to the comprehensive effect of harmless disposal of oil sludge and synergistic power generation in the process of co-combustion of oil sludge and coal.
- the application can reduce the cost of oil sludge incineration and disposal, on the other hand, it can also realize the improvement of comprehensive benefits of pulverized coal power plant boiler oil sludge incineration and collaborative power generation, and enhance the comprehensive competitiveness of power generation enterprises.
- the by-product sludge of an oil production well is composed of 60% oil, 8% water, 7% solid combustibles, and about 25% of other non-combustible substances such as ash, and the calorific value is as high as 33MJ/ kg. Due to the high oil content of this sludge, it has the characteristics of high calorific value. However, due to its large molecular weight of oil, the viscosity of the oil on the whole is high, and transportation is difficult and poses a greater safety risk. On the other hand, moisture and non-combustible substances also contain certain toxic and harmful substances, which need to be harmlessly treated at high temperatures. Using the method of the present application, the following steps can be adopted to carry out incineration, so as to realize the comprehensive utilization of the calorific value of the oil sludge and the harmless treatment of harmful substances.
- the main physical and chemical indicators of the oil sludge are analyzed, and it is determined that the oil sludge can be sent to the high-temperature combustion pulverized coal boiler of the power plant for comprehensive utilization and harmless treatment through the method of this aspect;
- the temperature determined by the thermogravimetric analysis experiment compared with a large amount of volatilization analysis is controlled at about 300 ° C, and the composition of the preparation agent is determined to be about quicklime 45%, fly ash is 40%, kaolin is 15%, and the mass ratio of conditioning agent and oil sludge is 1:2.
- the water content of the oil sludge after conditioning is about 3%, that in the sludge is about 35%, the mass proportion of non-combustible minerals such as ash is increased to 47%, and the calorific value is about 20MJ/kg.
- the appearance diagram of the oil sludge after conditioning is as follows As shown in Figure 4, it shows that the physical properties and calorific value of the modified oil sludge are also close to those of ordinary raw coal, which is suitable for transportation and combustion in the coal transportation system of power plants.
- the sludge is transported to the feed port of the mixer of the sludge and coal in a power plant through a special tank truck, etc., and Control the oil sludge and conditioning agent to be fed at a ratio of 2:1, and then the mixture of oil sludge and conditioning agent is further mixed and transported in the spiral agitator to realize the conditioning process of oil sludge.
- the rotation speed of the spiral agitator can be controlled, and the quality of the tempered oil sludge transported to the coal conveying belt through the spiral agitator can be controlled within about 1:9 of the mass ratio of the oil sludge and the coal conveyed on the coal conveying substitute.
- the raw coal and modified oil sludge are sent to the raw coal bunker through the coal conveyor belt for mixing, and then the raw coal is mixed with modified oil sludge in the pulverization process of the coal mill to achieve secondary mixing.
- the mixture of oil sludge and coal is sent into the boiler for combustion through the original powder conveying and combustion system of the boiler.
- the temperature in the pulverized coal boiler of the power station is usually as high as 1300-1600 °C, and the high-temperature incineration time of oil sludge and other particles in the furnace is about 2 -3 seconds, organic pollutants such as dioxins and heavy metals that are easily produced during the sludge combustion process will generate dust and flue gas after being incinerated under long-term high-temperature conditions in the boiler. Purification treatment is carried out, and the emission reaches the ultra-low emission standard of current thermal power plants.
- the feeding system of the oil sludge and the preparation agent can use mature products such as conventional grab machines and elevators, and add related equipment such as mixers and spiral agitators of this application.
- the modified tempered oil sludge can be mixed with raw coal, and the comprehensive utilization of heat and ultra-low emission of pollutants can be realized through the existing pulverization, combustion and exhaust gas purification devices of the boiler.
- the system is simple, the construction cost is low, and it also has the advantages of The advantages of high efficiency and low pollution.
- a system for incinerating oil sludge using a pulverized coal boiler in a power station includes: a boiler 1, an air preheater 2, a blower 3, a primary fan 4, a flue gas purification device 5, a chimney 6, two Secondary air adjustment door 7, primary air adjustment door 8, coal mill 9, separator 10, combustion system 11, coal bunker 12, coal conveyor belt 13, spiral agitator 14 and mixer feed port 15.
- the heat generated by the combustion of fuel in the boiler 1 passes through the heat exchange surface, and the secondary air and the primary air sent by the blower 3 and the primary fan 4 are heated by the air preheater 2, and the heated secondary air passes through the boiler.
- the organization of the combustion system 11 supplements the amount of oxygen for the combustion of the fuel in the furnace, and the size of the secondary air volume can be adjusted through 7 according to the actual needs of the boiler combustion; the high-pressure head hot primary air sent by the primary fan 4 is sent through the pipeline
- the coal mill 9 is used to dry and convey the mixture of raw coal and oil sludge in the coal mill, and its primary air volume can be adjusted through the primary air adjustment door 8 according to the actual needs of the pulverizing system.
- Sludge and conditioning agent are respectively added to the feed port 15 of the mixer at the entrance of the spiral agitator 14, and then the sludge and conditioning agent are stirred in the spiral agitator 14 and mixed evenly and tempered well.
- the oil sludge is transported to the coal conveyor belt 13 for blending; the mixture of coal and sludge is sent to the coal bunker 12 through the coal conveyor belt 13, and the mixture of raw coal and coal slime in the coal bunker 12 is transported to the coal mill 9 through the coal drop pipe
- the pulverized coal separator 10 carried by the primary air, and the pulverized coal separator 10 transports the pulverized coal and oil sludge powder with a particle size qualified to the combustion system 11 through the pulverized feeding pipeline.
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Abstract
A system and a method for incinerating oil sludge by using a power station pulverized coal boiler. The system comprises a boiler (1), an air preheater (2), an air feeder (3), a primary fan (4), a flue gas purification device (5), a coal mill (9), a separator (10), a combustion system (11), a coal bin (12), a coal conveying belt (13), a spiral stirrer (14) and a mixer feeding port (15). By means of the method, without providing any intermediate oil sludge incineration device, oil sludge can be directly mixed with raw coal after a certain pretreatment is carried out on the oil sludge; a mixture is crushed by means of an existing powdering system of the boiler (1) and conveyed into a hearth of the boiler (1) for incineration; and then purification is carried out by means of an existing flue gas purification device of the boiler (1), thereby utilizing the oil sludge and realizing treatment on the oil sludge to make same harmless.
Description
相关申请的交叉引用Cross References to Related Applications
本申请要求在2021年10月15日提交中国专利局、申请号为202111205644.0、发明名称为“一种利用电站煤粉锅炉焚烧油泥的系统和方法”的中国专利申请的优先权,其全部内容通过引用的方式并入本文中。This application claims the priority of the Chinese patent application submitted to the China Patent Office on October 15, 2021, with the application number 202111205644.0, and the title of the invention is "A System and Method for Burning Oil Sludge Using Power Plant Pulverized Coal Boiler", the entire content of which is passed Incorporated herein by reference.
本申请属于燃煤锅炉技术领域,具体涉及一种利用电站煤粉锅炉焚烧油泥的系统和方法。The application belongs to the technical field of coal-fired boilers, and in particular relates to a system and method for incinerating oil sludge using a pulverized coal boiler of a power station.
油泥是石油和生物质油等在开采、运输和利用过程中,产生的主要固体废弃物之一。由于油污泥是一种结构稳定、难以处理的危险废弃物,因此无法与传统垃圾一样使用简单的填埋法进行处理。现有的油污泥处理技术主要包括:焚烧法、离心分离法、溶剂萃取和生物法等,其中焚烧法是处理成本最低,应用最广的一种方式。传统的油污泥焚烧处理,主要是通过单独建立专用的焚烧炉来进行焚烧,一方面存在随着环保法规的日益严格,焚烧炉建设审批难度日益增大、建设成本与日俱增,且油污泥燃烧后的热量回收效率低、运行成本高等问题,另一方面焚烧过程温度相对较低,炉膛出口烟气中后产生的烟气中可能存在二噁英等有机污染物,且排放烟气中存在的灰尘、NOx与SOx含量一般都远高于当前环保要求的超低排放标准,会对周边环境造成较大污染。Oil sludge is one of the main solid wastes generated during the exploitation, transportation and utilization of petroleum and biomass oil. Since oil sludge is a hazardous waste with stable structure and difficult to handle, it cannot be disposed of by simple landfill method like traditional waste. Existing oil sludge treatment technologies mainly include: incineration, centrifugal separation, solvent extraction, and biological methods, among which incineration is the lowest cost and most widely used method. The traditional oil sludge incineration treatment is mainly carried out by establishing a dedicated incinerator separately. On the one hand, with the increasingly stringent environmental protection regulations, the difficulty of incinerator construction approval is increasing, and the construction cost is increasing day by day. On the other hand, the temperature of the incineration process is relatively low, and there may be organic pollutants such as dioxins in the flue gas generated at the furnace outlet, and the dioxins in the exhausted flue gas The content of dust, NOx and SOx is generally much higher than the ultra-low emission standard required by the current environmental protection, which will cause great pollution to the surrounding environment.
全国不同区域都分布有数量巨大的煤粉电站锅炉,采用煤粉电站锅炉处理油泥是一种处理成本低、综合效益高的方案。采用这种方案处理油泥,一方面可以省去焚烧炉建设成本高的问题,另一方面煤粉电站锅炉具有燃烧温度高、燃烧效率和热效率高的特点,可以大幅提高油泥的热利用效率,且电站锅炉都已经有建成的烟气超低排放环保设施,可以实现排放烟气中的灰尘、 NOx与SOx超低排放的问题。但油泥具有和原煤差异极大的理化性质,油泥的输运和燃烧的控制在现有煤粉电站锅炉系统里如何嵌入,形成一套能够解决在电站煤粉锅炉焚烧油泥的系统和方法,特别是不设让现有锅炉系统能够满足油泥的焚烧需要也是亟需研究的一个重要课题。There are a huge number of pulverized coal power plant boilers distributed in different regions of the country. Using pulverized coal power plant boilers to treat oil sludge is a solution with low processing cost and high comprehensive benefits. Using this solution to deal with oil sludge, on the one hand, can save the problem of high construction cost of incinerators; on the other hand, pulverized coal power plant boilers have the characteristics of high combustion temperature, high combustion efficiency and high thermal efficiency, which can greatly improve the heat utilization efficiency of oil sludge, and Power plant boilers have already built ultra-low emission environmental protection facilities for flue gas, which can achieve ultra-low emission of dust, NOx and SOx in the flue gas. However, oil sludge has physical and chemical properties that are very different from raw coal. How to embed the transportation and combustion control of oil sludge in the existing pulverized coal power plant boiler system to form a system and method that can solve the problem of burning oil sludge in power plant pulverized coal boilers, especially Whether or not the existing boiler system can meet the incineration needs of oil sludge is also an important subject that needs to be studied urgently.
发明内容Contents of the invention
本申请的目的在于提供一种利用电站煤粉锅炉焚烧油泥的系统和方法,能够在不设置中间油泥焚烧装置的条件下,通过对油泥进行一定的预处理后,直接与原煤进行混合,通过锅炉已有的制粉系统进行粉碎和输运进入锅炉的炉膛进行焚烧,然后通过锅炉已有的烟气净化装置进行净化,实现油泥的利用和无害化处理。The purpose of this application is to provide a system and method for incinerating oil sludge using a pulverized coal boiler in a power station. Under the condition of not installing an intermediate oil sludge incineration device, the oil sludge can be directly mixed with raw coal after a certain pretreatment, and passed through the boiler The existing pulverizing system is crushed and transported into the furnace of the boiler for incineration, and then purified by the existing flue gas purification device of the boiler to realize the utilization and harmless treatment of oil sludge.
本申请是通过以下技术方案来实现:The application is realized through the following technical solutions:
一种利用电站煤粉锅炉焚烧油泥的方法,包括如下步骤:A method for burning oil sludge using a pulverized coal boiler of a power station, comprising the steps of:
步骤1,根据油泥特性分析,配置油泥调质剂,利用配置的调质剂对挥发性强且含水量较高的有油泥进行改性;Step 1, according to the analysis of the characteristics of the sludge, configure the sludge conditioner, and use the configured conditioner to modify the sludge with strong volatility and high water content;
步骤2,将油泥和配置好的调质剂分别送入搅拌器,在搅拌器内充分搅拌均匀,利用调质剂对油泥进行改性,降低油泥的液态流动的物理性能和挥发性,使其与原煤具有类似的固体属性;Step 2, feed the oil sludge and the prepared conditioning agent into the mixer respectively, fully stir them evenly in the mixer, use the conditioning agent to modify the oil sludge, reduce the physical properties and volatility of the liquid flow of the oil sludge, and make it Similar solid properties to raw coal;
步骤3,将调质后的油泥送入原煤输送皮带,按设定的比例与原煤在输煤皮带上进行掺混,掺混的质量占比通过掺配适烧试验得到的最佳配比决定;Step 3. Send the oil sludge after conditioning to the raw coal conveyor belt, and blend it with the raw coal on the coal conveyor belt according to the set ratio. The mass ratio of the blend is determined by the best ratio obtained from the blending test. ;
步骤4,掺混好的油泥和原煤送入现有制粉系统进行粉末化,然后通过送粉系统送入煤粉电站锅炉炉膛进行高温焚烧,焚烧过程是煤粉和油泥粉末的混合掺烧过程温度控制在1300-1600℃范围,以保证对油泥内的有害物质进行无害化处理,对混合掺烧过程的控制结合整个锅炉燃烧优化控制进行调节;Step 4. The mixed oil sludge and raw coal are sent to the existing pulverization system for pulverization, and then sent to the furnace of the pulverized coal power plant boiler through the powder feeding system for high-temperature incineration. The incineration process is a mixed combustion process of coal powder and oil sludge powder The temperature is controlled in the range of 1300-1600 ℃ to ensure the harmless treatment of harmful substances in the oil sludge, and the control of the mixed combustion process is adjusted in conjunction with the optimization control of the entire boiler combustion;
步骤5,原煤和油泥在在锅炉内燃烧产生的粉尘、NOx和SOx污染物,通过锅炉尾部烟道布置的脱硝、除尘和脱硫装置进行净化。 Step 5, the dust, NOx and SOx pollutants produced by the combustion of raw coal and oil sludge in the boiler are purified through the denitrification, dust removal and desulfurization devices arranged in the flue at the tail of the boiler.
本申请进一步的改进在于,步骤1中,调质剂的配方是根据油泥的水分、挥发分具体指标,采用生石灰、粉煤灰和高岭土按质量百分数进行配置,配置的比例以生石灰为主,占50-60%,粉煤灰占20-40%,高岭土等其他矿物 占比10-20%,各组分的最终占比由油泥的组分特点决定,通过前期不同组分占比的配方对油泥改性作用的热重分析实验效果对比确定。The further improvement of the present application is that in step 1, the formulation of the conditioner is based on the specific indicators of the moisture and volatile content of the oil sludge, and the quicklime, fly ash and kaolin are used to configure according to the mass percentage, and the proportion of the configuration is mainly quicklime, accounting for 50-60%, fly ash accounts for 20-40%, and other minerals such as kaolin account for 10-20%. The final proportion of each component is determined by the composition characteristics of the oil sludge. The thermal gravimetric analysis experiment effect of oil sludge modification is confirmed by comparison.
本申请进一步的改进在于,步骤2中,利用调质剂对油泥进行改性,加入根据有利的物理化学特性指标,定制的调制剂,对油泥流动性特性和易挥发的特性进行改良,具体包括加入调制剂后,由含水率较高不宜存储的泥浆状态转为含水率20%以下的类似煤炭的固态,从而易于存储和运输,另一方面那些易挥发的易燃组分也被调制剂中多孔的调制剂所吸附,挥发性能大为降低,调制剂的质量占比为20-30%。The further improvement of the present application lies in that in step 2, the oil sludge is modified with a conditioning agent, and a custom-made modulator is added based on favorable physical and chemical characteristics indicators to improve the fluidity and volatile characteristics of the oil sludge, specifically including After adding the preparation agent, the mud state with a high water content that is not suitable for storage is transformed into a solid state similar to coal with a water content below 20%, which is easy to store and transport. On the other hand, those volatile and flammable components are also contained in the preparation agent. Adsorbed by the porous modulator, the volatile performance is greatly reduced, and the mass ratio of the modulator is 20-30%.
本申请进一步的改进在于,步骤3中,按设定的比例将调质后的油泥与原煤在输煤皮带上进行掺混,且输煤皮带上可掺混的油泥质量占比不超过20%。The further improvement of the present application is that in step 3, the tempered oil sludge and raw coal are blended on the coal conveyor belt according to the set ratio, and the mass ratio of the oil sludge that can be blended on the coal conveyor belt does not exceed 20%. .
一种利用电站煤粉锅炉焚烧油泥的系统,包括锅炉、空气预热器、送风机、一次风机、烟气净化装置、磨煤机、分离器、燃烧系统、煤仓、输煤皮带、螺旋式搅拌器以及混合器进料口;A system for incinerating oil sludge using a pulverized coal boiler in a power station, including a boiler, an air preheater, a blower, a primary fan, a flue gas purification device, a coal mill, a separator, a combustion system, a coal bunker, a coal conveyor belt, and a spiral agitator Device and mixer inlet;
其中,锅炉内燃料燃烧产生的热量经过换热面换热后,通过空预器对送风机和一次风机送来的二次风和一次风进行加热,经过加热的二次风通过锅炉燃烧系统的组织,为炉内燃料的燃烧补充氧量;一次风机送来的高压头热一次风通过管路送入磨煤机,对磨煤机中的原煤和油泥混合物进行干燥和输送;Among them, the heat generated by the combustion of fuel in the boiler passes through the heat exchange surface, and the secondary air and primary air sent by the blower and the primary fan are heated by the air preheater, and the heated secondary air passes through the organization of the boiler combustion system. , to supplement oxygen for the combustion of fuel in the furnace; the high-pressure head hot primary air sent by the primary fan is sent to the coal mill through the pipeline, and the raw coal and oil sludge mixture in the coal mill are dried and transported;
油泥和调质剂,分别加入螺旋式搅拌器入口的混合器进料口中,然后油泥和调质剂在螺旋式搅拌器中进行搅拌并混合均匀并调质好后,调质好的油泥输送到输煤皮带上进行掺混;煤和油泥的混合物通过输煤皮带送入煤仓,煤仓中的原煤和煤泥的混合物通过落煤管输送到磨煤机中,经过碾磨和干燥后,在一次风的携带下进入煤粉分离器,煤粉分离器将粒径合格煤粉和油泥粉末,通过送粉管道输送到燃烧系统,在燃烧系统的组织下送入锅炉内进行燃烧;燃烧产生的粉尘、NOx和SOx污染物,通过布置在尾部烟道上的烟气净化装置中包含的除尘、脱硝和脱硫装置进行空气污染物的净化。Sludge and conditioning agent are respectively added to the feed inlet of the mixer at the entrance of the spiral agitator, and then the sludge and conditioning agent are stirred in the spiral agitator and mixed evenly and tempered, and the conditioned sludge is transported to Blending is carried out on the coal conveyor belt; the mixture of coal and oil sludge is sent to the coal bunker through the coal conveyor belt, and the mixture of raw coal and coal slime in the coal bunker is sent to the coal mill through the coal drop pipe, and after grinding and drying, Carried by the primary air, it enters the pulverized coal separator, and the pulverized coal separator transports the pulverized coal and oil sludge powder with qualified particle size to the combustion system through the powder delivery pipeline, and sends them into the boiler for combustion under the organization of the combustion system; the combustion produces The dust, NOx and SOx pollutants are purified by the dust removal, denitrification and desulfurization devices included in the flue gas purification device arranged on the tail flue.
本申请进一步的改进在于,空气污染物净化后的烟气通过烟囱排出。A further improvement of the present application is that the flue gas purified from air pollutants is discharged through the chimney.
本申请进一步的改进在于,一次风量的大小根据制粉系统的实际需要通过一次风调整门进行调节。A further improvement of the present application is that the primary air volume is adjusted through the primary air adjustment door according to the actual needs of the pulverizing system.
本申请进一步的改进在于,二次风量的大小根据锅炉燃烧的实际需要通过二次风调整门口进行调节。A further improvement of the present application is that the secondary air volume is adjusted through the secondary air adjustment door according to the actual needs of boiler combustion.
本申请至少具有如下有益的技术效果:The application has at least the following beneficial technical effects:
本申请提供一种基于煤粉电站锅炉的直接燃烧油泥的系统和方法,基于当前国内分布广泛的煤粉电站锅炉已有的制粉系统、燃烧系统和尾部烟道烟气净化的环保设备,将油泥通过调质剂改性后,在输煤皮带上将油泥与原煤进行混合,然后送入煤仓,再通过磨煤机磨制成粉后送入锅炉炉膛进行燃烧。炉膛内油泥和煤粉的燃烧过程中,同步完成油泥热量的利用和对有害物质的高温无害化处理,并将燃烧产生的大气污染物利用尾部烟道的烟气净化装置进行净化处理,达到超低排放的环保标准。其具有如下优点,This application provides a system and method for direct combustion of oil sludge based on pulverized coal power plant boilers. Based on the existing pulverizing system, combustion system and environmental protection equipment for flue gas purification of pulverized coal power plant boilers widely distributed in China, the After the oil sludge is modified by the conditioning agent, the oil sludge is mixed with the raw coal on the coal conveyor belt, then sent to the coal bunker, and then pulverized by the coal mill and sent to the boiler furnace for combustion. During the combustion process of sludge and coal powder in the furnace, the heat utilization of sludge and the high-temperature harmless treatment of harmful substances are simultaneously completed, and the air pollutants produced by combustion are purified by the flue gas purification device at the tail flue to achieve Environmental standards for ultra-low emissions. It has the following advantages,
第一:系统简单,建设成本低,不需要新建油泥专用的焚烧炉和对应的烟气环保设备,节省大量的基建设备和运维费用;First: the system is simple, the construction cost is low, and there is no need to build a dedicated sludge incinerator and corresponding flue gas environmental protection equipment, saving a lot of infrastructure equipment and operation and maintenance costs;
第二:油泥的预处理过程简单,只需要加入针对有利特性设计好的调质剂,在搅拌器中搅拌混合完成预处理即可;Second: The pretreatment process of oil sludge is simple, only need to add a conditioner designed for favorable characteristics, and stir and mix in the mixer to complete the pretreatment;
第三:油泥的粉碎、输送和燃烧,都可以利用现有制粉系统完成,系统新增设备少;Third: The pulverization, transportation and combustion of oil sludge can all be completed by using the existing pulverizing system, and there are few new equipment added to the system;
第四:油泥利用热效率高,锅炉内的温度高,燃烧组织先进,燃烧效率可以达到98%以上,还可以用热电联产,系统热效率比专用的油泥焚烧炉高出许多;Fourth: The thermal efficiency of oil sludge utilization is high, the temperature in the boiler is high, the combustion organization is advanced, the combustion efficiency can reach more than 98%, and cogeneration of heat and power can also be used. The thermal efficiency of the system is much higher than that of special oil sludge incinerators;
第五:锅炉焚烧温度高,锅炉内的温度通常可以高达1600℃,油泥内的有毒有害物质可以彻底无害化处理;Fifth: The boiler incineration temperature is high, the temperature inside the boiler can usually be as high as 1600°C, and the toxic and harmful substances in the sludge can be completely harmless treated;
第六:烟气排放控制环保标准高,电厂的烟气净化设备先进,油泥焚烧产生的NOx、粉尘和SOx等污染物可以通过电厂已有的环保设备进行处理,达到超低排放的标准,满足环保法规的相关要求。Sixth: The flue gas emission control has high environmental protection standards. The flue gas purification equipment of the power plant is advanced. Pollutants such as NOx, dust and SOx produced by sludge incineration can be treated by the existing environmental protection equipment of the power plant to meet the ultra-low emission standard and meet the Relevant requirements of environmental regulations.
图1为一种利用煤粉电站锅炉焚烧油泥的方法流程图。Fig. 1 is a flow chart of a method for incinerating oil sludge using a pulverized coal power plant boiler.
图2为一种利用煤粉电站锅炉焚烧油泥的系统结构框图。Figure 2 is a structural block diagram of a system for incinerating oil sludge using a pulverized coal power plant boiler.
图3为某油井副产品示意图。Figure 3 is a schematic diagram of by-products of an oil well.
图4为某油井副产品调质后外形示意图。Figure 4 is a schematic diagram of the appearance of a by-product of an oil well after quenching and tempering.
下面将参照附图更详细地描述本公开的示例性实施例。虽然附图中显示了本公开的示例性实施例,然而应当理解,可以以各种形式实现本公开而不应被这里阐述的实施例所限制。相反,提供这些实施例是为了能够更透彻地理解本公开,并且能够将本公开的范围完整的传达给本领域的技术人员。需要说明的是,在不冲突的情况下,本申请中的实施例及实施例中的特征可以相互组合。下面将参考附图并结合实施例来详细说明本申请。Exemplary embodiments of the present disclosure will be described in more detail below with reference to the accompanying drawings. Although exemplary embodiments of the present disclosure are shown in the drawings, it should be understood that the present disclosure may be embodied in various forms and should not be limited by the embodiments set forth herein. Rather, these embodiments are provided for more thorough understanding of the present disclosure and to fully convey the scope of the present disclosure to those skilled in the art. It should be noted that, in the case of no conflict, the embodiments in the present application and the features in the embodiments can be combined with each other. The present application will be described in detail below with reference to the accompanying drawings and embodiments.
如图1所示,本申请充分利用当前煤基电站煤粉锅炉的系统和设备特点,通过将调质剂加入油泥,对油泥进行改性,降低油泥流动性和易挥发性能,改性过程主要在螺旋搅拌器中进行,调质改性好的油泥送上原煤输送皮带,送入煤仓,再经过制粉磨制,然后通过燃烧系统的组织在炉膛内燃烧,烟气通过锅炉系统的环保装置进行净化,达到超低排放的排放标准。本申请在系统构成简单,不需要新建油泥焚烧炉及油泥前处理设备和烟气净化设备,节省了大量的建设费用和设备运行维护费用。同时,由于煤粉电站锅炉具有容量大、燃烧温度高、锅炉燃烧和热效率高、锅炉烟气净化设备对烟气净化性能好等优点,可以将油泥进行较为彻底的无害化处理,且可以充分利用油泥的热资源,充分发挥油泥和燃煤混烧过程中对油泥的无害化处置和协同发电的综合效应。本申请一方面可以降低油泥焚烧处置的成本,另一方面也可以实现提升煤粉电站锅炉油泥焚烧和协同发电综合效益,增强发电企业的综合竞争力。As shown in Figure 1, this application makes full use of the system and equipment characteristics of the current coal-based power plant pulverized coal boiler, and modifies the sludge by adding a conditioner to the sludge to reduce the fluidity and volatility of the sludge. The modification process mainly It is carried out in a spiral agitator, and the oil sludge that has been tempered and modified is sent to the raw coal conveyor belt, sent to the coal bunker, and then pulverized and ground, and then burned in the furnace through the organization of the combustion system, and the flue gas passes through the environmental protection of the boiler system The device is purified to meet the emission standard of ultra-low emission. The application has a simple system structure and does not need to build a new oil sludge incinerator, oil sludge pre-treatment equipment and flue gas purification equipment, saving a lot of construction costs and equipment operation and maintenance costs. At the same time, because the pulverized coal power plant boiler has the advantages of large capacity, high combustion temperature, high boiler combustion and thermal efficiency, and good flue gas purification performance of the boiler flue gas purification equipment, the oil sludge can be treated more thoroughly and harmlessly, and can be fully Utilize the thermal resources of oil sludge, and give full play to the comprehensive effect of harmless disposal of oil sludge and synergistic power generation in the process of co-combustion of oil sludge and coal. On the one hand, the application can reduce the cost of oil sludge incineration and disposal, on the other hand, it can also realize the improvement of comprehensive benefits of pulverized coal power plant boiler oil sludge incineration and collaborative power generation, and enhance the comprehensive competitiveness of power generation enterprises.
实例:Example:
如图3所示的某采油井副产品油泥,其组成为油分60%,水分为8%,固体可燃物为7%,其他灰分等不可燃物质的占比约为25%,热值高达33MJ/kg。由于该油泥含油量高,具有热值较高的特点,但由于其含油分子量大,整体上油的黏度大,输运较为困难且有较大安全风险。另一方面水分和不可燃物质中还含有一定的有毒有害物质,需要经过高温进行无害化处理。采用本申请的方法可以采用下述步骤进焚烧,实现油泥热值的综合利用和对有害物质的无害化处理。As shown in Figure 3, the by-product sludge of an oil production well is composed of 60% oil, 8% water, 7% solid combustibles, and about 25% of other non-combustible substances such as ash, and the calorific value is as high as 33MJ/ kg. Due to the high oil content of this sludge, it has the characteristics of high calorific value. However, due to its large molecular weight of oil, the viscosity of the oil on the whole is high, and transportation is difficult and poses a greater safety risk. On the other hand, moisture and non-combustible substances also contain certain toxic and harmful substances, which need to be harmlessly treated at high temperatures. Using the method of the present application, the following steps can be adopted to carry out incineration, so as to realize the comprehensive utilization of the calorific value of the oil sludge and the harmless treatment of harmful substances.
首先,如上文所述,对油泥的主要理化指标进行分析,确定可以通过该 油泥可以本方面的方法,送入电厂的高温燃烧的煤粉锅炉进行综合利用和无害化处理;First, as mentioned above, the main physical and chemical indicators of the oil sludge are analyzed, and it is determined that the oil sludge can be sent to the high-temperature combustion pulverized coal boiler of the power plant for comprehensive utilization and harmless treatment through the method of this aspect;
接下来,根据该油泥其组成为油分60%,水分为8%的特点等主要指标,通过热重分析实验对比大量挥发分析出的温度控制在300℃左右,确定调制剂的组分约为生石灰45%,粉煤灰为40%,高岭土为15%,调制剂与油泥质量占比为1:2。调质后的油泥的水分约为3%,油泥中的约为35%,灰分等不可燃矿物的质量占比提升至47%,热值为约20MJ/kg,调质后的油泥外形示意图如图4所示,显示改性后的油泥外观的物理属性、热值也与一般原煤接近,适合电厂输煤系统进行输运和燃用。Next, according to the main indicators such as the composition of the oil sludge with 60% oil and 8% water, the temperature determined by the thermogravimetric analysis experiment compared with a large amount of volatilization analysis is controlled at about 300 ° C, and the composition of the preparation agent is determined to be about quicklime 45%, fly ash is 40%, kaolin is 15%, and the mass ratio of conditioning agent and oil sludge is 1:2. The water content of the oil sludge after conditioning is about 3%, that in the sludge is about 35%, the mass proportion of non-combustible minerals such as ash is increased to 47%, and the calorific value is about 20MJ/kg. The appearance diagram of the oil sludge after conditioning is as follows As shown in Figure 4, it shows that the physical properties and calorific value of the modified oil sludge are also close to those of ordinary raw coal, which is suitable for transportation and combustion in the coal transportation system of power plants.
进一步的,在实验室研究工作确定调制剂的配方和调制剂和油泥质量配比的基础上,通过专用的槽罐车等,将油泥运输至某电厂的油泥和煤的混合器进料口,并控制油泥和调制剂按2:1送入,然后油泥和调制剂的混合物在螺旋式搅拌器内进一步混合和输送,实现油泥的调质过程。Further, on the basis of laboratory research to determine the formula of the preparation and the mass ratio of the preparation and the sludge, the sludge is transported to the feed port of the mixer of the sludge and coal in a power plant through a special tank truck, etc., and Control the oil sludge and conditioning agent to be fed at a ratio of 2:1, and then the mixture of oil sludge and conditioning agent is further mixed and transported in the spiral agitator to realize the conditioning process of oil sludge.
进一步的,通过螺旋搅拌器的转动速度可以控制,通过螺旋搅拌器输送至输煤皮带上的调质油泥的质量,控制油泥与输煤替代上的输煤的质量比约为1:9之内,通过输煤皮带将原煤和调质改性的油泥送入原煤仓实现混合,再通过在磨煤机的制粉过程中将原煤有改性油泥实现二次混合。Further, the rotation speed of the spiral agitator can be controlled, and the quality of the tempered oil sludge transported to the coal conveying belt through the spiral agitator can be controlled within about 1:9 of the mass ratio of the oil sludge and the coal conveyed on the coal conveying substitute. , the raw coal and modified oil sludge are sent to the raw coal bunker through the coal conveyor belt for mixing, and then the raw coal is mixed with modified oil sludge in the pulverization process of the coal mill to achieve secondary mixing.
进一步的,通过锅炉原有输粉和燃烧系统将油泥和煤的混合物送入锅炉进行燃烧,电站煤粉锅炉炉内温度通常高达1300-1600℃,油泥等颗粒物在炉内高温焚烧时间约为2-3秒,油泥燃烧过程中容易产生的二噁英等有机污染物和重金属在锅炉的长时间高温条件下焚烧后产生粉尘和烟气,烟气可以通过锅炉尾部的环保岛脱硝、除尘和脱硫进行净化处理,排放达到当前火力发电厂超低排放的标准。Furthermore, the mixture of oil sludge and coal is sent into the boiler for combustion through the original powder conveying and combustion system of the boiler. The temperature in the pulverized coal boiler of the power station is usually as high as 1300-1600 °C, and the high-temperature incineration time of oil sludge and other particles in the furnace is about 2 -3 seconds, organic pollutants such as dioxins and heavy metals that are easily produced during the sludge combustion process will generate dust and flue gas after being incinerated under long-term high-temperature conditions in the boiler. Purification treatment is carried out, and the emission reaches the ultra-low emission standard of current thermal power plants.
整个油泥在电厂锅炉燃烧的过程中,使用的油泥和调制剂的上料系统,可以使用常规的抓斗机和提升机等成熟产品,新增本申请混合器、螺旋搅拌器等相关设备,就可以将改性后的调质油泥与原煤进行掺混,通过锅炉现有制粉、燃烧和尾气净化装置实现热量的综合利用的和污染物的超低排放,系统简单、建设成本低,还具有高效低污染的优点。During the combustion process of the whole oil sludge in the boiler of the power plant, the feeding system of the oil sludge and the preparation agent can use mature products such as conventional grab machines and elevators, and add related equipment such as mixers and spiral agitators of this application. The modified tempered oil sludge can be mixed with raw coal, and the comprehensive utilization of heat and ultra-low emission of pollutants can be realized through the existing pulverization, combustion and exhaust gas purification devices of the boiler. The system is simple, the construction cost is low, and it also has the advantages of The advantages of high efficiency and low pollution.
如图2所示,本申请提供的一种利用电站煤粉锅炉焚烧油泥的系统,包括:锅炉1、空气预热器2、送风机3、一次风机4、烟气净化装置5、烟囱 6、二次风调整门口7、一次风调整门8、磨煤机9、分离器10、燃烧系统11、煤仓12、输煤皮带13、螺旋式搅拌器14以及混合器进料口15。其中,锅炉1内燃料燃烧产生的热量经过换热面换热后,通过空预器2对送风机3和一次风机4送来的二次风和一次风进行加热,经过加热的二次风通过锅炉燃烧系统11的组织,为炉内燃料的燃烧补充氧量,其二次风量的大小可以根据锅炉燃烧的实际需要通过7进行调节;一次风机4送来的高压头热一次风通过管路送入磨煤机9,对磨煤机中的原煤和油泥混合物进行干燥和输送,其一次风量的大小可以根据制粉系统的实际需要通过一次风调整门8进行调节。As shown in Figure 2, a system for incinerating oil sludge using a pulverized coal boiler in a power station provided by the present application includes: a boiler 1, an air preheater 2, a blower 3, a primary fan 4, a flue gas purification device 5, a chimney 6, two Secondary air adjustment door 7, primary air adjustment door 8, coal mill 9, separator 10, combustion system 11, coal bunker 12, coal conveyor belt 13, spiral agitator 14 and mixer feed port 15. Among them, the heat generated by the combustion of fuel in the boiler 1 passes through the heat exchange surface, and the secondary air and the primary air sent by the blower 3 and the primary fan 4 are heated by the air preheater 2, and the heated secondary air passes through the boiler. The organization of the combustion system 11 supplements the amount of oxygen for the combustion of the fuel in the furnace, and the size of the secondary air volume can be adjusted through 7 according to the actual needs of the boiler combustion; the high-pressure head hot primary air sent by the primary fan 4 is sent through the pipeline The coal mill 9 is used to dry and convey the mixture of raw coal and oil sludge in the coal mill, and its primary air volume can be adjusted through the primary air adjustment door 8 according to the actual needs of the pulverizing system.
油泥和调质剂,分别加入螺旋式搅拌器14入口的混合器进料口15中,然后油泥和调质剂在螺旋式搅拌器14中进行搅拌并混合均匀并调质好后,调质好的油泥输送到输煤皮带13上进行掺混;煤和油泥的混合物通过输煤皮带13送入煤仓12,煤仓12中的原煤和煤泥的混合物通过落煤管输送到磨煤机9中,经过碾磨和干燥后,在一次风的携带下进入煤粉分离器10,煤粉分离器10将粒径合格煤粉和油泥粉末,通过送粉管道输送到燃烧系统11中,在燃烧系统11的组织下送入锅炉1内进行燃烧;燃烧产生的粉尘、NOx和SOx等污染物,通过布置在尾部烟道上的烟气净化装置5中包含的除尘、脱硝和脱硫装置进行空气污染物的净化。Sludge and conditioning agent are respectively added to the feed port 15 of the mixer at the entrance of the spiral agitator 14, and then the sludge and conditioning agent are stirred in the spiral agitator 14 and mixed evenly and tempered well. The oil sludge is transported to the coal conveyor belt 13 for blending; the mixture of coal and sludge is sent to the coal bunker 12 through the coal conveyor belt 13, and the mixture of raw coal and coal slime in the coal bunker 12 is transported to the coal mill 9 through the coal drop pipe In the process, after being milled and dried, it enters the pulverized coal separator 10 carried by the primary air, and the pulverized coal separator 10 transports the pulverized coal and oil sludge powder with a particle size qualified to the combustion system 11 through the pulverized feeding pipeline. Under the organization of the system 11, it is fed into the boiler 1 for combustion; the dust, NOx and SOx and other pollutants produced by the combustion are removed from the air pollutants by the dust removal, denitrification and desulfurization devices included in the flue gas purification device 5 arranged on the tail flue. purification.
虽然,上文中已经用一般性说明及具体实施方案对本申请作了详尽的描述,但在本申请基础上,可以对之作一些修改或改进,这对本领域技术人员而言是显而易见的。因此,在不偏离本申请精神的基础上所做的这些修改或改进,均属于本申请要求保护的范围。Although the present application has been described in detail with general descriptions and specific implementations above, it is obvious to those skilled in the art that some modifications or improvements can be made on the basis of the present application. Therefore, the modifications or improvements made on the basis of not departing from the spirit of the present application all belong to the protection scope of the present application.
Claims (8)
- 利用电站煤粉锅炉焚烧油泥的方法,其特征在于,包括如下步骤:Utilize the method for incinerating oil sludge in power plant pulverized coal boiler, it is characterized in that, comprises the following steps:步骤1,根据油泥特性分析,配置油泥调质剂,利用配置的调质剂对挥发性强且含水量较高的有油泥进行改性;Step 1, according to the analysis of the characteristics of the sludge, configure the sludge conditioner, and use the configured conditioner to modify the sludge with strong volatility and high water content;步骤2,将油泥和配置好的调质剂分别送入搅拌器,在搅拌器内充分搅拌均匀,利用调质剂对油泥进行改性,降低油泥的液态流动的物理性能和挥发性,使其与原煤具有类似的固体属性;Step 2, feed the oil sludge and the prepared conditioning agent into the mixer respectively, fully stir them evenly in the mixer, use the conditioning agent to modify the oil sludge, reduce the physical properties and volatility of the liquid flow of the oil sludge, and make it Similar solid properties to raw coal;步骤3,将调质后的油泥送入原煤输送皮带,按设定的比例与原煤在输煤皮带上进行掺混,掺混的质量占比通过掺配适烧试验得到的最佳配比决定;Step 3. Send the oil sludge after conditioning to the raw coal conveyor belt, and blend it with the raw coal on the coal conveyor belt according to the set ratio. The mass ratio of the blend is determined by the best ratio obtained from the blending test. ;步骤4,掺混好的油泥和原煤送入现有制粉系统进行粉末化,然后通过送粉系统送入煤粉电站锅炉炉膛进行高温焚烧,焚烧过程是煤粉和油泥粉末的混合掺烧过程温度控制在1300-1600℃范围,以保证对油泥内的有害物质进行无害化处理,对混合掺烧过程的控制结合整个锅炉燃烧优化控制进行调节;Step 4. The mixed oil sludge and raw coal are sent to the existing pulverization system for pulverization, and then sent to the furnace of the pulverized coal power plant boiler through the powder feeding system for high-temperature incineration. The incineration process is a mixed combustion process of coal powder and oil sludge powder The temperature is controlled in the range of 1300-1600 ℃ to ensure the harmless treatment of harmful substances in the oil sludge, and the control of the mixed combustion process is adjusted in conjunction with the optimization control of the entire boiler combustion;步骤5,原煤和油泥在在锅炉内燃烧产生的粉尘、NOx和SOx污染物,通过锅炉尾部烟道布置的脱硝、除尘和脱硫装置进行净化。Step 5, the dust, NOx and SOx pollutants produced by the combustion of raw coal and oil sludge in the boiler are purified through the denitrification, dust removal and desulfurization devices arranged in the flue at the tail of the boiler.
- 根据权利要求1所述的利用电站煤粉锅炉焚烧油泥的方法,其特征在于,步骤1中,调质剂的配方是根据油泥的水分、挥发分具体指标,采用生石灰、粉煤灰和高岭土按质量百分数进行配置,配置的比例以生石灰为主,占50-60%,粉煤灰占20-40%,高岭土等其他矿物占比10-20%,各组分的最终占比由油泥的组分特点决定,通过前期不同组分占比的配方对油泥改性作用的热重分析实验效果对比确定。The method for incinerating oil sludge using a pulverized coal boiler in a power station according to claim 1, wherein in step 1, the formula of the conditioner is based on the moisture and volatile content of the oil sludge, using quicklime, fly ash and kaolin according to The proportion of the configuration is mainly quicklime, accounting for 50-60%, fly ash accounting for 20-40%, kaolin and other minerals accounting for 10-20%, the final proportion of each component is determined by the composition of oil sludge It is determined by the characteristics, and determined by comparing the experimental effects of thermogravimetric analysis on the modification of oil sludge by formulas with different proportions of components in the early stage.
- 根据权利要求1所述的利用电站煤粉锅炉焚烧油泥的方法,其特征在于,步骤2中,利用调质剂对油泥进行改性,加入根据有利的物理化学特性指标,定制的调制剂,对油泥流动性特性和易挥发的特性进行改良,具体包括加入调制剂后,由含水率较高不宜存储的泥浆状态转为含水率20%以下的类似煤炭的固态,从而易于存储和运输,另一方面那些易挥发的易燃组分 也被调制剂中多孔的调制剂所吸附,挥发性能大为降低,调制剂的质量占比为20-30%。According to claim 1, the method for incinerating oil sludge using a pulverized coal boiler in a power station is characterized in that, in step 2, the oil sludge is modified by using a conditioner, and a custom-made modulating agent is added according to favorable physical and chemical characteristic indicators. The fluidity and volatile characteristics of the oil sludge are improved, specifically including that after adding the conditioner, the mud state with a high moisture content that is not suitable for storage is transformed into a solid state similar to coal with a moisture content of less than 20%, so that it is easy to store and transport. Another On the other hand, those volatile and flammable components are also adsorbed by the porous modulator in the modulator, and the volatile performance is greatly reduced, and the mass ratio of the modulator is 20-30%.
- 根据权利要求1所述的利用电站煤粉锅炉焚烧油泥的方法,其特征在于,步骤3中,按设定的比例将调质后的油泥与原煤在输煤皮带上进行掺混,且输煤皮带上可掺混的油泥质量占比不超过20%。According to claim 1, the method for incinerating oil sludge using a pulverized coal boiler in a power station is characterized in that in step 3, the oil sludge after quenching and tempering is mixed with raw coal on the coal conveyor belt according to the set ratio, and the coal is transported The proportion of oil sludge that can be blended on the belt does not exceed 20%.
- 利用电站煤粉锅炉焚烧油泥的系统,其特征在于,包括锅炉(1)、空气预热器(2)、送风机(3)、一次风机(4)、烟气净化装置(5)、磨煤机(9)、分离器(10)、燃烧系统(11)、煤仓(12)、输煤皮带(13)、螺旋式搅拌器(14)以及混合器进料口(15);A system for incinerating oil sludge using a pulverized coal boiler in a power station is characterized in that it includes a boiler (1), an air preheater (2), a blower (3), a primary fan (4), a flue gas purification device (5), and a coal pulverizer (9), separator (10), combustion system (11), coal bunker (12), coal conveyor belt (13), spiral agitator (14) and mixer inlet (15);其中,锅炉(1)内燃料燃烧产生的热量经过换热面换热后,通过空预器(2)对送风机(3)和一次风机(4)送来的二次风和一次风进行加热,经过加热的二次风通过锅炉燃烧系统(11)的组织,为炉内燃料的燃烧补充氧量;一次风机(4)送来的高压头热一次风通过管路送入磨煤机(9),对磨煤机(9)中的原煤和油泥混合物进行干燥和输送;Among them, the heat generated by the combustion of fuel in the boiler (1) is heated by the air preheater (2) to the secondary air and primary air sent by the blower (3) and the primary blower (4) after heat exchange on the heat exchange surface. The heated secondary air passes through the organization of the boiler combustion system (11) to supplement the amount of oxygen for the combustion of fuel in the furnace; the high-pressure hot primary air sent by the primary fan (4) is sent to the coal mill (9) through the pipeline , drying and transporting the raw coal and oil sludge mixture in the coal mill (9);油泥和调质剂,分别加入螺旋式搅拌器(14)入口的混合器进料口(15)中,然后油泥和调质剂在螺旋式搅拌器(14)中进行搅拌并混合均匀并调质好后,调质好的油泥输送到输煤皮带(13)上进行掺混;煤和油泥的混合物通过输煤皮带(13)送入煤仓(12),煤仓(12)中的原煤和煤泥的混合物通过落煤管输送到磨煤机(9)中,经过碾磨和干燥后,在一次风的携带下进入煤粉分离器(10),煤粉分离器(10)将粒径合格煤粉和油泥粉末,通过送粉管道输送到燃烧系统(11)中,在燃烧系统(11)的组织下送入锅炉(1)内进行燃烧;燃烧产生的粉尘、NOx和SOx污染物,通过布置在尾部烟道上的烟气净化装置(5)中包含的除尘、脱硝和脱硫装置进行空气污染物的净化。Sludge and conditioning agent are respectively added to the feed inlet (15) of the mixer at the inlet of the spiral agitator (14), and then the sludge and conditioning agent are stirred in the spiral agitator (14) and mixed evenly and tempered After that, the oil sludge that has been tempered is transported to the coal conveyor belt (13) for blending; the mixture of coal and oil sludge is sent into the coal bunker (12) by the coal conveyor belt (13), and the raw coal and the The mixture of coal slime is transported to the coal mill (9) through the coal falling pipe, and after being ground and dried, it enters the pulverized coal separator (10) under the carrying of the primary air, and the pulverized coal separator (10) separates the particle size Qualified pulverized coal and oil sludge powder are delivered to the combustion system (11) through the powder delivery pipeline, and are sent into the boiler (1) for combustion under the organization of the combustion system (11); the dust, NOx and SOx pollutants produced by combustion, Air pollutants are purified through the dust removal, denitrification and desulfurization devices included in the flue gas purification device (5) arranged on the tail flue.
- 根据权利要求5所述的利用电站煤粉锅炉焚烧油泥的系统,其特征在于,空气污染物净化后的烟气通过烟囱(6)排出。According to claim 5, the system for incinerating oil sludge by using pulverized coal boiler of power station is characterized in that the flue gas after the purification of air pollutants is discharged through the chimney (6).
- 根据权利要求5所述的利用电站煤粉锅炉焚烧油泥的系统,其特征 在于,一次风量的大小根据制粉系统的实际需要通过一次风调整门(8)进行调节。According to claim 5, the system for incinerating oil sludge by using the pulverized coal boiler of the power station is characterized in that the primary air volume is adjusted through the primary air adjustment door (8) according to the actual needs of the pulverizing system.
- 根据权利要求5所述的利用电站煤粉锅炉焚烧油泥的系统,其特征在于,二次风量的大小根据锅炉燃烧的实际需要通过二次风调整门口(7)进行调节。According to claim 5, the system for incinerating sludge by using pulverized coal boiler of power station is characterized in that the size of the secondary air volume is adjusted through the secondary air adjustment door (7) according to the actual needs of boiler combustion.
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