CN111520712A - Ultrasonic atomization combustion system and method suitable for pyrolysis oil - Google Patents
Ultrasonic atomization combustion system and method suitable for pyrolysis oil Download PDFInfo
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 69
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 54
- 238000000889 atomisation Methods 0.000 title claims abstract description 50
- 238000000034 method Methods 0.000 title claims abstract description 14
- 238000004945 emulsification Methods 0.000 claims abstract description 31
- 239000002028 Biomass Substances 0.000 claims abstract description 16
- 238000002156 mixing Methods 0.000 claims abstract description 15
- 230000010355 oscillation Effects 0.000 claims abstract description 12
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 18
- 239000007789 gas Substances 0.000 claims description 13
- 239000003546 flue gas Substances 0.000 claims description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 10
- 239000000839 emulsion Substances 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 7
- 239000002283 diesel fuel Substances 0.000 claims description 6
- 239000003595 mist Substances 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 238000009413 insulation Methods 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims 1
- 239000000779 smoke Substances 0.000 abstract description 3
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- 239000003995 emulsifying agent Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D11/00—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
- F23D11/10—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour
- F23D11/12—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour characterised by the shape or arrangement of the outlets from the nozzle
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
- B01F31/80—Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D11/00—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
- F23D11/36—Details, e.g. burner cooling means, noise reduction means
- F23D11/38—Nozzles; Cleaning devices therefor
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- Chemical Kinetics & Catalysis (AREA)
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- Pressure-Spray And Ultrasonic-Wave- Spray Burners (AREA)
Abstract
本发明公开了一种适用于热解油的超声波雾化燃烧系统及方法,属于涉及生物质热解油领域,以解决目前热解油燃烧系统在运行中容易出现的燃烧不完全而冒黑烟、污染物排放量高等问题。该系统包括超声波乳化罐、伴热油路、燃烧室、超声波发生器、超声波雾化喷嘴,所述超声波乳化罐一侧为进油口,另一侧接有伴热油路,超声波乳化罐的下方设有加热器;所述超声波雾化喷嘴包括雾化空气外腔、油腔、雾化空气内腔、超声波油气混合振荡腔。本发明利用超声波乳化罐在热解油雾化之前对热解油进行超声波乳化处理,改善了热解油的性质,降低热解油粘度。同时,伴热油路和特殊的雾化喷嘴结构都适用于粘稠的热解油。
The invention discloses an ultrasonic atomization combustion system and method suitable for pyrolysis oil, which belongs to the field related to biomass pyrolysis oil, so as to solve the problem that the combustion of the current pyrolysis oil combustion system is easy to occur due to incomplete combustion and black smoke. , high pollutant emissions. The system includes an ultrasonic emulsification tank, a heat tracing oil circuit, a combustion chamber, an ultrasonic generator, and an ultrasonic atomization nozzle. One side of the ultrasonic emulsification tank is an oil inlet, and the other side is connected with a heat tracing oil circuit. A heater is arranged below; the ultrasonic atomizing nozzle includes an atomizing air outer cavity, an oil cavity, an atomizing air inner cavity, and an ultrasonic oil-gas mixing oscillation cavity. The invention utilizes an ultrasonic emulsification tank to perform ultrasonic emulsification treatment on the pyrolysis oil before the pyrolysis oil is atomized, thereby improving the properties of the pyrolysis oil and reducing the viscosity of the pyrolysis oil. At the same time, the heat tracing oil circuit and the special atomizing nozzle structure are suitable for viscous pyrolysis oil.
Description
技术领域technical field
本发明属于涉及生物质热解油领域,具体涉及一种适用于热解油的超声波雾化燃烧系统及方法。The invention belongs to the field of biomass pyrolysis oil, and in particular relates to an ultrasonic atomization combustion system and method suitable for pyrolysis oil.
背景技术Background technique
生物质热解油具有较高的热值和含氧量,是可再生能源技术研究的重要对象之一。然而生物质热解油存在粘度较高,杂质较多等问题,阻碍了其资源化利用。目前,生物质焦油的提质改性处理方法主要有乳化法和化学法等,其中化学法存在工艺复杂、改性成本高等问题。Biomass pyrolysis oil has high calorific value and oxygen content, and is one of the important objects of renewable energy technology research. However, biomass pyrolysis oil has problems such as high viscosity and many impurities, which hinder its resource utilization. At present, the methods for upgrading and modifying biomass tar mainly include emulsification method and chemical method, among which the chemical method has the problems of complicated process and high modification cost.
超声乳化法是一种工艺简单、成本低的油品改性方法。在超声波作用下,两种不相溶液体和表面活性剂因超声空化效应,破坏了溶液原有分子间的表面张力,促使两种液体相互溶解,形成稳定的乳化液,能够降低热解油粘度,提高生物焦油的燃烧性能和能源品位。Ultrasonic emulsification is a simple and low-cost oil modification method. Under the action of ultrasonic waves, the two immiscible liquids and the surfactant destroy the original intermolecular surface tension of the solution due to the ultrasonic cavitation effect, and promote the mutual dissolution of the two liquids to form a stable emulsion, which can reduce the amount of pyrolysis oil. Viscosity, improve the combustion performance and energy grade of bio-tar.
对于生物质热解油等高粘度液体燃料而言,喷嘴技术是雾化燃烧技术的核心,喷嘴性能好坏直接影响雾化效果及喷嘴自身的使用寿命,关系到燃烧过程能否正常稳定运行。由于生物质热解油黏度大、密度大、表面张力大、雾化困难等特点,目前能够应用于生物质热解油的喷嘴较少。For high-viscosity liquid fuels such as biomass pyrolysis oil, nozzle technology is the core of atomization combustion technology. The performance of the nozzle directly affects the atomization effect and the service life of the nozzle itself, which is related to the normal and stable operation of the combustion process. Due to the characteristics of high viscosity, high density, high surface tension and difficult atomization of biomass pyrolysis oil, there are few nozzles that can be applied to biomass pyrolysis oil at present.
发明内容SUMMARY OF THE INVENTION
本发明的目的是提供一种适用于热解油的超声波雾化燃烧系统,以解决目前热解油燃烧系统在运行中容易出现的燃烧不完全而冒黑烟、污染物排放量高等问题。The purpose of the present invention is to provide an ultrasonic atomization combustion system suitable for pyrolysis oil, so as to solve the problems of incomplete combustion, black smoke and high pollutant discharge that are easy to occur in the current pyrolysis oil combustion system during operation.
本发明技术方案如下:一种适用于热解油的超声波雾化燃烧系统,包括超声波乳化罐、伴热油路、燃烧室、超声波发生器、超声波雾化喷嘴,伴热油路末端连接超声波雾化喷嘴,超声波雾化喷嘴出口端插入燃烧室中,超声波雾化喷嘴还连接超声波发生器;所述超声波乳化罐一侧为进油口,另一侧接有伴热油路,超声波乳化罐的下方设有加热器;所述超声波雾化喷嘴包括雾化空气外腔、油腔、雾化空气内腔、超声波油气混合振荡腔,最外层为雾化空气外腔,中间层为油腔,最内层为雾化空气内腔,雾化空气外腔的前端设有雾化空气通孔,油腔的缩口端斜面四周均匀布置旋流喷头,超声波油气混合振荡腔的外壁设有超声波振荡器。The technical scheme of the present invention is as follows: an ultrasonic atomization combustion system suitable for pyrolysis oil, comprising an ultrasonic emulsification tank, a heat tracing oil circuit, a combustion chamber, an ultrasonic generator, and an ultrasonic atomizing nozzle, and the end of the heat tracing oil circuit is connected with ultrasonic mist The outlet end of the ultrasonic atomizing nozzle is inserted into the combustion chamber, and the ultrasonic atomizing nozzle is also connected to an ultrasonic generator; one side of the ultrasonic emulsification tank is an oil inlet, and the other side is connected with a heat tracing oil circuit. A heater is provided below; the ultrasonic atomizing nozzle includes an atomizing air outer cavity, an oil cavity, an atomizing air inner cavity, and an ultrasonic oil-gas mixing oscillation cavity. The outermost layer is the atomizing air outer cavity, and the middle layer is the oil cavity. The innermost layer is the atomizing air inner cavity, the front end of the outer atomizing air cavity is provided with an atomizing air through hole, the swirl nozzles are evenly arranged around the inclined surface of the constricted end of the oil cavity, and the outer wall of the ultrasonic oil-gas mixing oscillation cavity is provided with ultrasonic oscillation. device.
进一步的,所述旋流喷头为8-12个,每个喷头两侧设置旋流槽。Further, there are 8-12 swirl nozzles, and swirl grooves are arranged on both sides of each nozzle.
进一步的,所述伴热油路为两条,其上均设有篮式过滤器,伴热油路上还设有油压泵。Further, there are two heat tracing oil circuits, both of which are provided with basket filters, and an oil pressure pump is also provided on the heat tracing oil circuits.
进一步的,所述伴热油路内部为管道,外部设有加热保温层。Further, the inside of the heat tracing oil circuit is a pipeline, and the outside is provided with a heating insulation layer.
用上述的一种适用于热解油的超声波雾化燃烧系统进行雾化燃烧的方法,其特征在于包括如下步骤:Carry out the method for atomization combustion with the above-mentioned ultrasonic atomization combustion system applicable to pyrolysis oil, it is characterized in that comprising the following steps:
A、选取体积含量为45-55%的生物质热解油,体积含量为10-20%助乳剂甲醇,体积含量为35-45%的柴油均匀混合加入超声波乳化罐,并设定加热器加热温度为80-100℃,连接油路; 打开超声波发生器的电源,设定超声功率密度为0.9-0.95W/mL,超声作用时间为17-23min;利用超声乳化将混合液乳化为热解油-柴油乳化液;A. Select biomass pyrolysis oil with a volume content of 45-55%, methanol with a volume content of 10-20%, and diesel oil with a volume content of 35-45%, evenly mix them into the ultrasonic emulsification tank, and set the heater to heat The temperature is 80-100°C, connect the oil circuit; turn on the power of the ultrasonic generator, set the ultrasonic power density to 0.9-0.95W/mL, and the ultrasonic action time to 17-23min; use ultrasonic emulsification to emulsify the mixture into pyrolysis oil - diesel emulsion;
B、打开空压机和储气罐,将空气作为雾化剂通过伴热气路充入超声波雾化喷嘴;打开油路及油压泵,调节生物质热解油雾化压力;打开超声波发生器连接于喷嘴内超声波振荡器的开关,热解油进入三级超声波雾化喷嘴后被打碎成小于10um的液滴颗粒;B. Open the air compressor and air storage tank, and fill the air as atomizing agent into the ultrasonic atomizing nozzle through the heat tracing air circuit; open the oil circuit and oil pressure pump to adjust the atomization pressure of biomass pyrolysis oil; open the ultrasonic generator Connected to the switch of the ultrasonic oscillator in the nozzle, the pyrolysis oil is broken into droplets smaller than 10um after entering the three-stage ultrasonic atomizing nozzle;
第一次雾化发生在雾化空气外腔与油腔之间,热解焦油经过油腔后由环形布置的旋流喷头喷出,The first atomization occurs between the outer cavity of the atomizing air and the oil cavity. After the pyrolysis tar passes through the oil cavity, it is ejected by the annularly arranged swirl nozzle.
第二次雾化发生在雾化空气内腔与喷嘴外壳之间,高压空气经过雾化空气内腔后与一次雾化的液滴相混合,对液滴进行二次雾化,二次雾化后油雾进入超声波油气混合振荡腔,The second atomization occurs between the inner cavity of the atomizing air and the nozzle shell. After passing through the inner cavity of the atomizing air, the high-pressure air is mixed with the first atomized droplets, and the droplets are atomized for the second time. After the oil mist enters the ultrasonic oil-gas mixing oscillation cavity,
在超声波振荡器的作用下,受超声波油气混合振荡腔和超声波振荡器的挤压和导向,进行第三次雾化,再经总喷头喷出;Under the action of the ultrasonic oscillator, it is squeezed and guided by the ultrasonic oil-gas mixing oscillating cavity and the ultrasonic oscillator for the third atomization, and then sprayed out through the main nozzle;
C、液滴颗粒喷入燃烧器的燃烧室,打开点火器进行点火燃烧;开启高压风机和列管换热器,对燃烧器和烟气换热,高压风机与温度信号采用闭环控制原理,保证烟气出口温度在200℃以下。C. The droplet particles are sprayed into the combustion chamber of the burner, and the igniter is turned on for ignition and combustion; the high-pressure fan and the tube heat exchanger are turned on to exchange heat between the burner and the flue gas. The high-pressure fan and the temperature signal adopt the closed-loop control principle to ensure The flue gas outlet temperature is below 200°C.
进一步的,加入超声波乳化罐的混合油的组成为体积含量为55%的生物质热解油,体积含量为10%助乳剂甲醇,体积含量为35%的柴油。Further, the composition of the mixed oil added to the ultrasonic emulsification tank is biomass pyrolysis oil with a volume content of 55%, a volume content of 10% co-emulsion methanol, and a volume content of diesel oil with a volume content of 35%.
本发明机理如下:热解油超声波雾化燃烧系统将热解油通过超声乳化降低热解油的粘度,提高热解油的雾化性质,利用超声波式三级雾化大大提高热解油乳化剂的雾化效果,将热解油乳化剂雾化为微小的液滴颗粒,在燃烧室内充分燃烧和烟气换热,能够有效实现高效燃烧、低污染排放。The mechanism of the invention is as follows: the pyrolysis oil ultrasonic atomization combustion system reduces the viscosity of the pyrolysis oil through ultrasonic emulsification, improves the atomization properties of the pyrolysis oil, and uses the ultrasonic three-stage atomization to greatly improve the pyrolysis oil emulsifier. The atomization effect of the pyrolysis oil emulsifier is atomized into tiny droplet particles, which are fully burned in the combustion chamber and the flue gas heat exchange, which can effectively achieve high-efficiency combustion and low pollution emissions.
本发明特点如下:The characteristics of the present invention are as follows:
(1)利用超声波乳化罐在热解油雾化之前对热解油进行超声波乳化处理,改善了热解油的性质,降低热解油粘度。同时,伴热油路和特殊的雾化喷嘴结构都适用于粘稠的热解油。(1) The pyrolysis oil is ultrasonically emulsified before the pyrolysis oil is atomized by the ultrasonic emulsification tank, which improves the properties of the pyrolysis oil and reduces the viscosity of the pyrolysis oil. At the same time, the heat tracing oil circuit and the special atomizing nozzle structure are suitable for viscous pyrolysis oil.
(2)超声波雾化喷嘴具有特殊的三级雾化结构,内混式空气雾化和超声波雾化相结合的雾化方式,使热解油雾化完全、雾化颗粒小,雾化均匀。采用超声波雾化喷嘴的热解油燃烧器,点火容易,出火均匀,燃烧完全,黑烟少。(2) The ultrasonic atomizing nozzle has a special three-stage atomization structure, and the atomization method combining internal mixing air atomization and ultrasonic atomization makes the pyrolysis oil fully atomized, the atomized particles are small, and the atomization is uniform. The pyrolysis oil burner with ultrasonic atomizing nozzle is easy to ignite, the fire is even, the combustion is complete, and the black smoke is less.
(3)超声波超声波雾化燃烧系统可连续进行热解油的超声乳化、雾化及燃烧三道工序,实现了热解油的改质燃烧过程的连续化和一体化,减少了热解油处理和运输过程中造成的污染。(3) The ultrasonic ultrasonic atomization combustion system can continuously carry out the three processes of ultrasonic emulsification, atomization and combustion of pyrolysis oil, realizing the continuity and integration of the reforming and combustion process of pyrolysis oil, and reducing the treatment of pyrolysis oil. and pollution during transportation.
附图说明Description of drawings
图1是一种适用于热解油的超声波雾化燃烧系统的结构示意图;1 is a schematic structural diagram of an ultrasonic atomization combustion system suitable for pyrolysis oil;
图2一种适用于热解油的超声波雾化燃烧系统中超声波雾化喷嘴的结构示意图;2 is a schematic structural diagram of an ultrasonic atomizing nozzle in an ultrasonic atomizing combustion system suitable for pyrolysis oil;
图3是图2的侧视图。FIG. 3 is a side view of FIG. 2 .
附图标记含义如下:1-超声波乳化罐;2-伴热油路;3-篮式过滤器;4-油压泵;5-超声波雾化喷嘴;6-燃烧室;7-超声波发生器;8-伴热气路;9-储气罐;10-空压机;11-加热器;12-超声波换能器;21-加热保温层;50-旋流槽;51-旋流喷头;52-雾化空气外腔;53-油腔;54-喷嘴外壳;55-雾化空气内腔;56-雾化空气通孔;57-超声波振荡器;58-超声波油气混合振荡腔;59-总喷头;61-燃烧腔;62-换热空气出口器;63-列管换热器;64-烟气出口;65-火焰观察孔;66-高压风机;67-鼓风机。The meanings of the reference numerals are as follows: 1-ultrasonic emulsification tank; 2-heat tracing oil circuit; 3-basket filter; 4-hydraulic pump; 5-ultrasonic atomizing nozzle; 6-combustion chamber; 7-ultrasonic generator; 8-Tracking gas path; 9-Air storage tank; 10-Air compressor; 11-Heater; 12-Ultrasonic transducer; 21-Heating insulation layer; 50-Swirl tank; 51-Swirl nozzle; 52- Atomizing air outer cavity; 53-Oil cavity; 54-Nozzle shell; 55-Atomizing air inner cavity; 56-Atomizing air through hole; 57-Ultrasonic oscillator; 58-Ultrasonic oil-gas mixing cavity; 59-Total nozzle ; 61 - combustion chamber; 62 - heat exchange air outlet; 63 - tube heat exchanger; 64 - flue gas outlet; 65 - flame observation hole; 66 - high pressure fan; 67 - blower.
具体实施方式Detailed ways
下面结合附图对本发明做进一步详细的说明。The present invention will be described in further detail below with reference to the accompanying drawings.
如图1所示,一种适用于热解油的超声波雾化燃烧系统,包括超声波乳化罐1、伴热油路2、燃烧室6、超声波发生器7、超声波雾化喷嘴5,伴热油路2末端连接超声波雾化喷嘴5,超声波雾化喷嘴5出口端插入燃烧室6中,超声波雾化喷嘴5还连接超声波发生器7。超声波乳化罐1左侧为进油口,右侧接有伴热油路2,加热器11安装于超声波乳化罐1的下方,为乳化罐内的乳化剂提供较高的温度环境。超声波发生器7通过超声波换能器12与超声波乳化罐1相连。伴热油路内部为管道,外部附有加热保温层21,可保持乳化剂的较高温度,提高乳化剂流动性,放止冷凝堵塞。伴热油路的两条分路上设有篮式过滤器3,对乳化剂的杂质进行过滤,防止喷嘴堵塞。伴热油路上还安装有油压泵4,控制乳化剂雾化压力。伴热油路2的末端连接有超声波雾化喷嘴5。As shown in Figure 1, an ultrasonic atomization combustion system suitable for pyrolysis oil includes ultrasonic emulsification tank 1, heat tracing oil circuit 2, combustion chamber 6, ultrasonic generator 7, ultrasonic atomizing nozzle 5, heat tracing oil The end of the road 2 is connected to the ultrasonic atomizing nozzle 5 , the outlet end of the ultrasonic atomizing nozzle 5 is inserted into the combustion chamber 6 , and the ultrasonic atomizing nozzle 5 is also connected to the ultrasonic generator 7 . The left side of the ultrasonic emulsification tank 1 is the oil inlet, and the right side is connected with the heat tracing oil circuit 2. The heater 11 is installed under the ultrasonic emulsification tank 1 to provide a higher temperature environment for the emulsifier in the emulsification tank. The ultrasonic generator 7 is connected to the ultrasonic emulsification tank 1 through the ultrasonic transducer 12 . The inside of the heat tracing oil circuit is a pipeline, and the outside is attached with a heating insulation layer 21, which can maintain a higher temperature of the emulsifier, improve the fluidity of the emulsifier, and prevent condensation and blockage. Basket filters 3 are arranged on the two branches of the heat tracing oil circuit to filter the impurities of the emulsifier and prevent the nozzle from being blocked. A hydraulic pump 4 is also installed on the heat tracing oil circuit to control the atomization pressure of the emulsifier. An ultrasonic atomizing nozzle 5 is connected to the end of the heat tracing oil circuit 2 .
超声波雾化喷嘴5包括雾化空气外腔52、油腔53和雾化空气内腔55、超声波油气混合振荡腔58,最外层为雾化空气外腔52,中间层为油腔53,最内层为雾化空气内腔55,雾化空气外腔52的前端设有雾化空气通孔56,油腔53的缩口端斜面四周均匀布置旋流喷头51,超声波油气混合振荡腔58的外壁设有超声波振荡器57。The ultrasonic atomizing nozzle 5 includes an atomizing air
超声波雾化喷嘴5出口处插入燃烧室6中。超声波雾化喷嘴5的下方设置有点火器,点燃油雾,使油雾在燃烧室年内的燃烧腔61中充分燃烧。燃烧室6顶部装有换热空气出口器62,内部装有列管换热器63,燃烧室6的侧端设有烟气出64,热烟气流经列管换热器63的内侧,冷空气流经列管换热器63的外侧,实现烟气的高效换热。燃烧室还设有火焰观察孔65,用于观测火焰长度和查看燃烧状态; 燃烧室下方设有高压风机66和鼓风机67,既可增加氧气与雾化液滴的接触量,使之更充分燃烧,又可加速烟气换热。The outlet of the ultrasonic atomizing nozzle 5 is inserted into the combustion chamber 6 . An igniter is arranged below the ultrasonic atomizing nozzle 5 to ignite the oil mist, so that the oil mist is fully burned in the
超声波雾化喷嘴原理:采用内混式空气雾化和超声波振荡雾化相结合的方式,整体结构分为雾化空气外腔52、油腔53和雾化空气内腔55、超声波油气混合振荡腔58,径向来看,最外层为雾化空气外腔52,中间层为油腔53,最内层为雾化空气内腔55,其中油腔53的缩口端斜面四周均匀布置 8-12 个旋流喷头51。第一次雾化发生在雾化空气外腔52与油腔53之间,热解焦油经过油腔53后由环形布置的旋流喷头51喷出,每个喷头两侧设置旋流槽50,雾化空气外腔的高压空气经过旋流槽50与旋流喷头51喷出的热解焦油液滴相撞击,形成一次雾化; 第二次雾化发生在雾化空气内腔55与喷嘴外壳54之间,高压空气经过雾化空气内腔55后与一次雾化的液滴相混合,对液滴进行二次雾化,二次雾化后油雾进入超声波油气混合振荡腔58,在超声波振荡器57的作用下,受混合腔58和超声波振荡器57的挤压和导向,进行第三次雾化,进一步雾化为更小的颗粒,再经总喷头59喷出,该结构设计迫使热解焦油滴经历三次雾化过程,达到较好的雾化效果。Principle of ultrasonic atomizing nozzle: It adopts the combination of internal mixing air atomization and ultrasonic oscillation atomization. 58. From the radial point of view, the outermost layer is the atomizing air
实施例1Example 1
设备工作时,选取体积含量为 55%的生物质热解油,体积含量为 10%助乳剂甲醇,体积含量为35%的柴油均匀混合加入超声波乳化罐,并设定加热器加热温度为 80℃,连接油路;打开超声波发生器7电源,设定超声功率密度为 0.9W/mL,超声作用时间为17min。利用超声乳化将混合液乳化为热解油-柴油乳化液。打开空压机10和储气罐将9空气作为雾化剂通过伴热气路8充入超声波雾化喷嘴5。打开油路及油压泵,调节生物质热解油雾化压力。打开超声波发生器连接于喷嘴内超声波振荡器57的开关,热解油进入三级超声波雾化喷嘴后被打碎成小于10um的液滴颗粒。之后喷入燃烧器的燃烧室,打开点火器进行点火燃烧;开启高压风机66和列管换热器63,对燃烧器和烟气换热,高压风机与温度信号采用闭环控制原理,保证烟气出口温度在 200℃以下。布置12 个旋流喷头When the equipment is working, select biomass pyrolysis oil with a volume content of 55%, methanol with a volume content of 10%, and diesel oil with a volume content of 35%, evenly mix them into the ultrasonic emulsification tank, and set the heating temperature of the heater to 80 °C. , connect the oil circuit; turn on the power of the ultrasonic generator 7, set the ultrasonic power density to 0.9W/mL, and the ultrasonic action time to 17min. The mixed solution was emulsified into a pyrolysis oil-diesel emulsion by ultrasonic emulsification. Turn on the
实施例2-超声波乳化罐内的超声乳化处理:Ultrasonic emulsification treatment in embodiment 2-ultrasonic emulsification tank:
布置 8个旋流喷头;选取生物质热解油体积含量为45%, 助乳剂甲醇体积含量为10%,柴油体积含量为45%。将混合液注入超声波乳化罐1内。超声波发生器设定超声功率密度为0.95W/mL, 超声作用时间为23min,加热器温度设定为100℃,当高强度超声波作用于热解油时,由于热解油内具有一定切应力。在剪切应力作用下,热解油、助乳剂与柴油充分混合,使热解油乳化,并在相浓度达到一定值时,改变热解油的乳状液类型,使其粘度降低。Eight swirl nozzles were arranged; the volume content of biomass pyrolysis oil was 45%, the volume content of methanol as co-emulsion agent was 10%, and the volume content of diesel oil was 45%. The mixed solution was injected into the ultrasonic emulsification tank 1 . The ultrasonic generator sets the ultrasonic power density to 0.95W/mL, the ultrasonic action time to 23min, and the heater temperature to 100°C. When high-intensity ultrasonic waves act on the pyrolysis oil, there is a certain shear stress in the pyrolysis oil. Under the action of shear stress, the pyrolysis oil, co-emulsion agent and diesel oil are fully mixed to emulsify the pyrolysis oil, and when the phase concentration reaches a certain value, the emulsion type of the pyrolysis oil is changed to reduce its viscosity.
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