CN110117505A - It is a kind of using kitchen oil as industrial fuel of raw material and preparation method thereof - Google Patents
It is a kind of using kitchen oil as industrial fuel of raw material and preparation method thereof Download PDFInfo
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- CN110117505A CN110117505A CN201910413351.8A CN201910413351A CN110117505A CN 110117505 A CN110117505 A CN 110117505A CN 201910413351 A CN201910413351 A CN 201910413351A CN 110117505 A CN110117505 A CN 110117505A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
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Abstract
本发明公开了一种以餐厨油为原料的工业燃料,属于石油化工技术领域,原料按重量份由餐厨油70‑90份、丙酮8‑12份、辅助添加剂0.1‑0.3份、氧化钙4‑8份、松针5‑8份、烧碱3‑5份组成,其制备方法包括以下步骤:1、松针同烧碱混合置于过滤袋中备用;2、将1中过滤袋及其他原料放入燃料生产装置的离心搅拌机中;3、启动离心搅拌机对原料进行搅拌,停转后取出过滤袋;4、对离心搅拌机内的混合物进行过滤分离,并通过醋精调整滤液的PH值;5、静置滤液即可得到工业燃料;本发明相较于未经提取的低质量的生物燃料有良好的燃烧效果,而对比通过对生物体提炼制取高纯度燃料存在其成本则相对低廉,便于商业化生产。
The invention discloses an industrial fuel using cooking oil as a raw material, which belongs to the technical field of petrochemical industry. The raw materials are 70-90 parts of cooking oil, 8-12 parts of acetone, 0.1-0.3 parts of auxiliary additives, and calcium oxide in parts by weight. 4-8 parts, 5-8 parts of pine needles, 3-5 parts of caustic soda, its preparation method comprises the following steps: 1, pine needles are mixed with caustic soda and placed in a filter bag for standby; In the centrifugal mixer of the fuel production device; 3. Start the centrifugal mixer to stir the raw materials, and take out the filter bag after stopping; 4. Filter and separate the mixture in the centrifugal mixer, and adjust the pH value of the filtrate through vinegar essence; 5. Static The filtrate can be used to obtain industrial fuel; compared with unextracted low-quality biofuel, the present invention has a good combustion effect, and its cost is relatively low compared to the high-purity fuel produced by refining biomass, which is convenient for commercialization Production.
Description
技术领域technical field
本发明涉及石油化工技术领域,具体涉及一种以餐厨油为原料的工业燃料及其制备方法。The invention relates to the field of petrochemical technology, in particular to an industrial fuel using kitchen oil as a raw material and a preparation method thereof.
背景技术Background technique
常规能源除了不可以再生这一缺陷外,还存在着诸如燃煤、柴油、煤油等灯石油制品在燃烧时由于燃烧不完全而导致排出的废气中存在着以煤核、碳粒、油滴或积胶等形态的未燃烧燃料,而这些未燃烧的物质除了会造成燃料的浪费,同时还会污染大气,这也是开发新能源的原因之一。In addition to the defect that conventional energy cannot be regenerated, there are also coal nuclei, carbon particles, oil droplets or These unburned substances not only cause waste of fuel, but also pollute the atmosphere, which is one of the reasons for the development of new energy.
但常规能源,尤其是以石油加工制成的柴油、汽油等燃料仍然是目前主流的无法在短期内被新能源所替代的能源燃料,而目前可再生的燃料能源只有生物燃料,现在在工业生活中所接触到的生物燃料大多存在着燃烧生成杂质多,燃烧所提供的能源相对较低的问题,其问题出在对生物体直接作为燃料使用时其可燃成分较少,而如果对生物体进行提炼制取高纯度燃料又存在成本高昂,无法将其商业化使用的问题;另一方面,餐厨油作为通过动植物来提炼制得已经经过使用的油脂,也是一种生物提炼的物质,同时其具有良好的作为生物燃油的使用前景,但目前尚未有以餐厨油为原料制取燃料工业燃料的相关技术。However, conventional energy, especially diesel, gasoline and other fuels made from petroleum processing are still the mainstream energy fuels that cannot be replaced by new energy in the short term. Currently, the only renewable fuel energy is biofuel, which is now used in industrial life. Most of the biofuels that come into contact with in the field have the problems of high impurities generated by combustion and relatively low energy provided by combustion. Refining and producing high-purity fuels is costly and cannot be used commercially; on the other hand, cooking oil is a kind of bio-refined substance that has been extracted from animals and plants. It has good prospects for use as biofuel, but there is no relevant technology for producing industrial fuel from cooking oil as a raw material.
发明内容Contents of the invention
本发明所要解决的技术问题是:提供一种以餐厨油为原料的工业燃料及其制备方法,以解决当前使用生物燃料时存在低质量的生物燃料无法得到理想的燃烧效果,但直接通过对生物体提炼制取高纯度燃料存在成本高昂的问题。The technical problem to be solved by the present invention is: to provide an industrial fuel with kitchen oil as raw material and its preparation method, to solve the problem that low-quality biofuel cannot obtain ideal combustion effect when using biofuel, but directly through the There is a problem of high cost in the production of high-purity fuel from biomass extraction.
为解决上述问题,本发明提供了如下技术方案:In order to solve the above problems, the present invention provides the following technical solutions:
一种以餐厨油为原料的工业燃料;原料由经过处理后的餐厨油、丙酮、提高汽油辛烷值的辅助添加剂、氧化钙、松针和烧碱组成,按重量份为:餐厨油70-90份、丙酮8-12份、辅助添加剂0.1-0.3份、氧化钙4-8份、松针5-8份、烧碱3-5份。An industrial fuel using cooking oil as raw material; the raw material is composed of processed cooking oil, acetone, auxiliary additives for increasing the octane number of gasoline, calcium oxide, pine needles and caustic soda, in parts by weight: cooking oil 70 -90 parts, acetone 8-12 parts, auxiliary additives 0.1-0.3 parts, calcium oxide 4-8 parts, pine needles 5-8 parts, caustic soda 3-5 parts.
优选的,还包括如下重量分数的组分:无水硫酸钠6-8份。Preferably, the following components by weight fraction are also included: 6-8 parts of anhydrous sodium sulfate.
优选的,还包括如下重量分数的组分:三号喷气燃料6-8份。Preferably, the following components by weight fraction are also included: 6-8 parts of No. 3 jet fuel.
优选的,松针为新鲜松针,其含水量大于20%。Preferably, the pine needles are fresh pine needles with a water content greater than 20%.
优选的,辅助添加剂为燃料乙醇,丙酮为纯丙酮。Preferably, the auxiliary additive is fuel ethanol, and the acetone is pure acetone.
一种以餐厨油为原料的工业燃料的制备方法,包括以下步骤:A kind of preparation method of the industrial fuel that is raw material with cooking oil, comprises the following steps:
步骤一、将松针同烧碱混合置于过滤袋中备用;Step 1, the pine needles are mixed with caustic soda and placed in a filter bag for subsequent use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将其他原料放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2, install the filter bag with pine needles and caustic soda in step 1 on the rotating shaft of the centrifugal mixer in the fuel production device, put other raw materials into the centrifugal mixer, and make it contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持2500-3500r/min的转速40-60分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在45-150℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 2500-3500r/min for 40-60 minutes, and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 45-150°C. Take it out after it stops. filter bag on the shaft of the centrifugal mixer;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在15-35℃的环境温度下静置不低于24h,即可得到生物燃料。Step 5. Put the mixed liquid finally obtained in Step 4 at an ambient temperature of 15-35° C. for not less than 24 hours to obtain a biofuel.
优选的,所述燃料生产装置中的离心搅拌机包括开口朝上的搅拌桶以及伸入搅拌桶桶内的转轴;在转轴上沿其径向安装有一个以上搅拌叶片;在搅拌叶片的末端可拆卸地安装有过滤袋;转轴的一端通过传动装置与电机的输出端相连;在搅拌桶上沿其周向安装有环形的加热装置;在搅拌桶的顶部还安装有封口盖;在搅拌桶的底部还安装有带阀门的出料管。Preferably, the centrifugal mixer in the fuel production device includes a stirring barrel with an opening facing upwards and a rotating shaft extending into the stirring barrel; more than one stirring blade is installed on the rotating shaft along its radial direction; the end of the stirring blade is detachable A filter bag is installed on the ground; one end of the rotating shaft is connected to the output end of the motor through a transmission device; a ring-shaped heating device is installed on the mixing bucket along its circumference; a sealing cover is installed on the top of the mixing bucket; A discharge pipe with a valve is also installed.
进一步的,在搅拌叶片的末端设置可以开合的置物箱;过滤袋设置在置物箱内;且在置物箱上开有与其内部相通的滤孔;过滤袋为采用石棉布制成的套袋;且置物箱上的滤孔的孔径大小大于所述过滤袋上滤孔的大小;搅拌桶为一圆桶结构;转轴设置在搅拌桶的中部,搅拌叶片的长度不低于搅拌桶内径大小的三分之二;过滤袋中所装的物质为新鲜松针与烧碱的混合物。Further, a storage box that can be opened and closed is provided at the end of the stirring blade; the filter bag is arranged in the storage box; and a filter hole communicating with the inside is opened on the storage box; the filter bag is a bag made of asbestos cloth; And the size of the filter hole on the storage box is greater than the size of the filter hole on the filter bag; the mixing tank is a drum structure; the rotating shaft is arranged in the middle of the mixing tank, and the length of the mixing blade is not less than three times the inner diameter of the mixing tank. Two-thirds; the material contained in the filter bag is a mixture of fresh pine needles and caustic soda.
进一步的,传动装置为一个齿轮变速器;其控制端台设置在搅拌桶的侧端的底部位置;加热装置为一电控加热丝,且所述电控加热丝与传动装置共用一个控制端台。Further, the transmission device is a gear transmission; its control end platform is set at the bottom position of the side end of the mixing bucket; the heating device is an electric control heating wire, and the electric control heating wire and the transmission device share a control end platform.
进一步的,封口盖为台阶形结构,所述台阶形封口盖通过紧固螺钉固定在搅拌桶上;且在台阶形封口盖与搅拌桶相接处还设置有封油环;在出料管的侧端设置有观察窗;观察窗内安装有PH试笔,PH试笔的一端与搅拌桶的内部相连。Further, the sealing cover has a step-shaped structure, and the step-shaped sealing cover is fixed on the mixing barrel by fastening screws; and an oil sealing ring is also provided at the joint between the step-shaped sealing cover and the mixing barrel; An observation window is arranged at the side end; a pH test pen is installed in the observation window, and one end of the pH test pen is connected with the inside of the mixing tank.
本发明有益效果:Beneficial effects of the present invention:
本发明利用了餐厨油可以作为生物柴油进行燃烧的特性,并借助于添加的多种混合物质以辅助燃油彻底燃烧,当前使用生物燃料时存在低质量的生物燃料无法得到理想的燃烧效果,但直接通过对生物体提炼制取高纯度燃料存在成本高昂的问题;本发明的成品工业燃料具有良好的燃烧效果;同时还能够对餐厨油的回收利用提供了新的思路;在其主要成分中,餐厨油主要是作为燃料的主要成份,起到作为基质的效果。The present invention utilizes the characteristic that cooking oil can be used as biodiesel for combustion, and assists the complete combustion of fuel oil by means of various mixed substances added. Currently, when biofuels are used, low-quality biofuels cannot obtain ideal combustion effects, but There is a problem of high cost in directly producing high-purity fuel by refining organisms; the finished industrial fuel of the present invention has a good combustion effect; at the same time, it can also provide a new idea for the recovery and utilization of kitchen oil; among its main components , Kitchen oil is mainly used as the main component of fuel, and it acts as a matrix.
丙酮起到的效果在于作为溶剂以稀释调节餐厨油中的成团结构的脂类、盐、生物碱及酰胺类化合物等物质;The effect of acetone is to act as a solvent to dilute substances such as lipids, salts, alkaloids and amide compounds that adjust the agglomerated structure in kitchen oil;
加入辅助添加剂的目的是为了进一步提高燃料的燃烧效果,起到助燃的目的。The purpose of adding auxiliary additives is to further improve the combustion effect of the fuel and achieve the purpose of supporting combustion.
松针与氢氧化钠通过混合后得到的物质能够起到有效的抗凝作用,同时松针还能够对餐厨油中其他无法燃烧的杂质进行过滤吸附;松针与氢氧化钠的混合物放入过滤袋中,在离心机的搅拌过程中餐厨油中的杂质将会被吸附入过滤袋;从而实现过滤效果,同时松针还能够改善制得的燃料的气味。The substance obtained by mixing pine needles and sodium hydroxide can have an effective anticoagulant effect, and at the same time, pine needles can also filter and adsorb other incombustible impurities in cooking oil; the mixture of pine needles and sodium hydroxide is put into the filter bag , During the stirring process of the centrifuge, the impurities in the kitchen oil will be absorbed into the filter bag; thereby achieving the filtering effect, and at the same time, the pine needles can also improve the smell of the prepared fuel.
加入氧化钙的目的是为了吸收残留在餐厨油中未彻底处理的水分;通过反应生成的氢氧化钙还能够与氢氧化钠合同起到更好的抗凝效果。The purpose of adding calcium oxide is to absorb the water remaining in the kitchen oil that has not been completely treated; the calcium hydroxide generated through the reaction can also contract with sodium hydroxide to achieve a better anticoagulant effect.
附图说明Description of drawings
图1是本发明在实施例中的结构示意图;Fig. 1 is a structural representation of the present invention in an embodiment;
附图标记说明:1、搅拌桶,2、转轴,3、搅拌叶片,4、过滤袋,5、加热装置,6、封口盖,7、出料管,8、PH试笔,9、传动装置,31、置物箱,32、滤孔,33、观察窗,91、电机。Explanation of reference signs: 1. Stirring bucket, 2. Rotating shaft, 3. Stirring blade, 4. Filter bag, 5. Heating device, 6. Sealing cover, 7. Discharge pipe, 8. PH test pen, 9. Transmission device , 31, storage box, 32, filter hole, 33, observation window, 91, motor.
具体实施方式Detailed ways
下面结合具体的实施例对本发明进行进一步介绍:The present invention is further described below in conjunction with specific embodiment:
实施例1:本发明工业燃料的制备:Embodiment 1: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油70kg、纯丙酮8kg、燃料乙醇0.1kg、氧化钙4kg、含水量超过20%的新鲜松针5kg、烧碱3kg。Raw material ratio: 70kg of processed kitchen oil, 8kg of pure acetone, 0.1kg of fuel ethanol, 4kg of calcium oxide, 5kg of fresh pine needles with a water content exceeding 20%, and 3kg of caustic soda.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇和氧化钙放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2, install the filter bag with pine needles and caustic soda in step 1 on the rotating shaft of the centrifugal mixer in the fuel production device, put kitchen oil, acetone, fuel ethanol and calcium oxide in the centrifugal mixer, and make it in contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持2800r/min的转速40分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在60℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3: Start the centrifugal mixer in step 2, keep it at a speed of 2800r/min for 40 minutes, and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 60°C. After stopping, take out the filter on the shaft of the centrifugal mixer. bag;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置48h,即可得到工业燃料。Step 5. Put the mixed liquid finally obtained in Step 4 to stand for 48 hours at an ambient temperature of 27° C. to obtain an industrial fuel.
实施例2:本发明工业燃料的制备:Embodiment 2: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油90kg、纯丙酮12kg、燃料乙醇0.3kg、氧化钙8kg、含水量超过20%的新鲜松针8kg、烧碱5kg。Raw material ratio: 90kg of processed kitchen oil, 12kg of pure acetone, 0.3kg of fuel ethanol, 8kg of calcium oxide, 8kg of fresh pine needles with a water content exceeding 20%, and 5kg of caustic soda.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇和氧化钙放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2, install the filter bag with pine needles and caustic soda in step 1 on the rotating shaft of the centrifugal mixer in the fuel production device, put kitchen oil, acetone, fuel ethanol and calcium oxide in the centrifugal mixer, and make it in contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持3200r/min的转速60分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在120℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 3200r/min for 60 minutes and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 120°C. After stopping, take out the filter on the shaft of the centrifugal mixer. bag;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置48h,即可得到工业燃料。Step 5. Put the mixed liquid finally obtained in Step 4 to stand for 48 hours at an ambient temperature of 27° C. to obtain an industrial fuel.
实施例3:本发明工业燃料的制备:Embodiment 3: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油80kg、纯丙酮10kg、燃料乙醇0.2kg、氧化钙6kg、含水量超过20%的新鲜松针6.5kg、烧碱4kg。Raw material ratio: 80kg of processed kitchen oil, 10kg of pure acetone, 0.2kg of fuel ethanol, 6kg of calcium oxide, 6.5kg of fresh pine needles with water content exceeding 20%, 4kg of caustic soda.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇和氧化钙放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2, install the filter bag with pine needles and caustic soda in step 1 on the rotating shaft of the centrifugal mixer in the fuel production device, put kitchen oil, acetone, fuel ethanol and calcium oxide in the centrifugal mixer, and make it in contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持3000r/min的转速50分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在85℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 3000r/min for 50 minutes, and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 85°C. After stopping, take out the filter on the shaft of the centrifugal mixer. bag;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置48h,即可得到工业燃料。Step 5. Put the mixed liquid finally obtained in Step 4 to stand for 48 hours at an ambient temperature of 27° C. to obtain an industrial fuel.
实施例4:本发明工业燃料的制备:Embodiment 4: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油75kg、纯丙酮8.5kg、燃料乙醇0.18kg、氧化钙5kg、含水量超过20%的新鲜松针6kg、烧碱4.5kg、无水硫酸钠6.5kg。Raw material ratio: 75kg of processed kitchen oil, 8.5kg of pure acetone, 0.18kg of fuel ethanol, 5kg of calcium oxide, 6kg of fresh pine needles with water content exceeding 20%, 4.5kg of caustic soda, and 6.5kg of anhydrous sodium sulfate.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇、氧化钙和无水硫酸钠放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2, install the filter bag containing pine needles and caustic soda in step 1 on the shaft of the centrifugal mixer in the fuel production device, and put kitchen oil, acetone, fuel ethanol, calcium oxide and anhydrous sodium sulfate into the centrifugal mixer Inside, and make it contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持3000r/min的转速55分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在120℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 3000r/min for 55 minutes and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 120°C. After stopping, take out the filter on the shaft of the centrifugal mixer. bag;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置72h,即可得到工业燃料。Step 5. Put the mixed liquid finally obtained in Step 4 to stand for 72 hours at an ambient temperature of 27° C. to obtain an industrial fuel.
实施例5:本发明工业燃料的制备:Embodiment 5: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油85kg、纯丙酮11kg、燃料乙醇0.25kg、氧化钙6kg、含水量超过20%的新鲜松针7kg、烧碱4.8kg、无水硫酸钠7.5kg。Raw material ratio: 85kg of processed kitchen oil, 11kg of pure acetone, 0.25kg of fuel ethanol, 6kg of calcium oxide, 7kg of fresh pine needles with a water content exceeding 20%, 4.8kg of caustic soda, and 7.5kg of anhydrous sodium sulfate.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇、氧化钙和无水硫酸钠放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2, install the filter bag containing pine needles and caustic soda in step 1 on the shaft of the centrifugal mixer in the fuel production device, and put kitchen oil, acetone, fuel ethanol, calcium oxide and anhydrous sodium sulfate into the centrifugal mixer Inside, and make it contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持2700r/min的转速40分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在90℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 2700r/min for 40 minutes and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 90°C. After stopping, take out the filter on the shaft of the centrifugal mixer. bag;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置72h,即可得到工业燃料。Step 5. Put the mixed liquid finally obtained in Step 4 to stand for 72 hours at an ambient temperature of 27° C. to obtain an industrial fuel.
实施例6:本发明工业燃料的制备:Embodiment 6: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油80kg、纯丙酮10.5kg、燃料乙醇0.22kg、氧化钙5.8kg、含水量超过20%的新鲜松针6.4kg、烧碱4.2g、无水硫酸钠7.7kg。Raw material ratio: 80kg of processed kitchen oil, 10.5kg of pure acetone, 0.22kg of fuel ethanol, 5.8kg of calcium oxide, 6.4kg of fresh pine needles with a water content exceeding 20%, 4.2g of caustic soda, and 7.7kg of anhydrous sodium sulfate.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇、氧化钙和无水硫酸钠放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2, install the filter bag containing pine needles and caustic soda in step 1 on the shaft of the centrifugal mixer in the fuel production device, and put kitchen oil, acetone, fuel ethanol, calcium oxide and anhydrous sodium sulfate into the centrifugal mixer Inside, and make it contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持3100r/min的转速58分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在45-150℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 3100r/min for 58 minutes and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 45-150°C. After stopping, take out the centrifugal mixer on the shaft filter bags;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置72h,即可得到工业燃料。Step 5. Put the mixed liquid finally obtained in Step 4 to stand for 72 hours at an ambient temperature of 27° C. to obtain an industrial fuel.
实施例7:本发明工业燃料的制备:Embodiment 7: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油72kg、纯丙酮9kg、燃料乙醇0.1kg、氧化钙5kg、含水量超过20%的新鲜松针5.5kg、烧碱3.5kg、三号喷气燃料6.5kg。Raw material ratio: 72kg of processed kitchen oil, 9kg of pure acetone, 0.1kg of fuel ethanol, 5kg of calcium oxide, 5.5kg of fresh pine needles with water content exceeding 20%, 3.5kg of caustic soda, and 6.5kg of No. 3 jet fuel.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇、氧化钙和三号喷气燃料放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2. Install the filter bag containing pine needles and caustic soda in step 1 on the rotating shaft of the centrifugal mixer in the fuel production device, and put kitchen oil, acetone, fuel ethanol, calcium oxide and No. 3 jet fuel into the centrifugal mixer Inside, and make it contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持3400r/min的转速45分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在100℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 3400r/min for 45 minutes and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 100°C. After stopping, take out the filter on the shaft of the centrifugal mixer. bag;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置24h,即可得到工业燃料。Step 5. The final mixed liquid obtained in Step 4 is allowed to stand at an ambient temperature of 27° C. for 24 hours to obtain an industrial fuel.
实施例8:本发明工业燃料的制备:Embodiment 8: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油87kg、纯丙酮11kg、燃料乙醇0.3kg、氧化钙7kg、含水量超过20%的新鲜松针7.4kg、烧碱4.6kg、三号喷气燃料7.4kg。Raw material ratio: 87kg of processed kitchen oil, 11kg of pure acetone, 0.3kg of fuel ethanol, 7kg of calcium oxide, 7.4kg of fresh pine needles with a water content exceeding 20%, 4.6kg of caustic soda, and 7.4kg of No. 3 jet fuel.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇、氧化钙和三号喷气燃料放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2. Install the filter bag containing pine needles and caustic soda in step 1 on the rotating shaft of the centrifugal mixer in the fuel production device, and put kitchen oil, acetone, fuel ethanol, calcium oxide and No. 3 jet fuel into the centrifugal mixer Inside, and make it contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持2800r/min的转速60分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在130℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 2800r/min for 60 minutes and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 130°C. After stopping, take out the filter on the shaft of the centrifugal mixer. bag;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置24h,即可得到工业燃料。Step 5. The final mixed liquid obtained in Step 4 is allowed to stand at an ambient temperature of 27° C. for 24 hours to obtain an industrial fuel.
实施例9:本发明工业燃料的制备:Embodiment 9: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油80kg、纯丙酮10.5kg、燃料乙醇0.2kg、氧化钙6kg、含水量超过20%的新鲜松针5.8kg、烧碱4kg、三号喷气燃料7kg。Raw material ratio: 80kg of processed kitchen oil, 10.5kg of pure acetone, 0.2kg of fuel ethanol, 6kg of calcium oxide, 5.8kg of fresh pine needles with a water content exceeding 20%, 4kg of caustic soda, and 7kg of No. 3 jet fuel.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇、氧化钙和三号喷气燃料放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2. Install the filter bag containing pine needles and caustic soda in step 1 on the rotating shaft of the centrifugal mixer in the fuel production device, and put kitchen oil, acetone, fuel ethanol, calcium oxide and No. 3 jet fuel into the centrifugal mixer Inside, and make it contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持3400r/min的转速40-60分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在70℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2 and keep it at a speed of 3400r/min for 40-60 minutes, then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 70°C. After stopping, take it out and put it on the shaft of the centrifugal mixer. filter bags;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置24h,即可得到工业燃料。Step 5. The final mixed liquid obtained in Step 4 is allowed to stand at an ambient temperature of 27° C. for 24 hours to obtain an industrial fuel.
实施例10:本发明工业燃料的制备:Embodiment 10: the preparation of industrial fuel of the present invention:
原料配比:经过处理后的餐厨油80kg、纯丙酮10kg、燃料乙醇0.2kg、氧化钙6kg、含水量超过20%的新鲜松针6.5kg、烧碱4kg、三号喷气燃料7kg、无水硫酸钠7kg。Raw material ratio: 80kg of processed kitchen oil, 10kg of pure acetone, 0.2kg of fuel ethanol, 6kg of calcium oxide, 6.5kg of fresh pine needles with water content exceeding 20%, 4kg of caustic soda, 7kg of No. 3 jet fuel, anhydrous sodium sulfate 7kg.
制备方法:Preparation:
步骤一、将松针同烧碱混合置于过石棉套制成的滤袋中备用;Step 1, mix the pine needles with caustic soda and place them in a filter bag made of asbestos sleeves for later use;
步骤二、将步骤一中装有松针和烧碱的过滤袋安装到燃料生产装置中的离心搅拌机的转轴上,并将餐厨油、丙酮、燃料乙醇、氧化钙和三号喷气燃料放入离心搅拌机内,并使其与所述过滤袋相接触;Step 2. Install the filter bag containing pine needles and caustic soda in step 1 on the rotating shaft of the centrifugal mixer in the fuel production device, and put kitchen oil, acetone, fuel ethanol, calcium oxide and No. 3 jet fuel into the centrifugal mixer Inside, and make it contact with the filter bag;
步骤三、启动步骤二中的离心搅拌机,使其维持3000r/min的转速60分钟后关闭离心搅拌机,离心搅拌机机工作时其内部温度维持在120℃,待停转后取出离心搅拌机转轴上的过滤袋;Step 3. Start the centrifugal mixer in step 2, keep it at a speed of 3000r/min for 60 minutes, and then turn off the centrifugal mixer. When the centrifugal mixer is working, its internal temperature is maintained at 120°C. After stopping, take out the filter on the shaft of the centrifugal mixer. bag;
步骤四、将离心搅拌机内的混合物质通入过滤机中进行过滤,并将过滤所得的液体使用定性定量纸对其PH值进行分析检测;当PH值高于8时向混合液体中加醋精进行调节,直至PH在6-8之间,且在定性定量纸烘干之后其质量变化小于0.1%;Step 4. Pass the mixed substance in the centrifugal mixer into the filter for filtration, and use qualitative and quantitative paper to analyze and detect the pH value of the filtered liquid; when the pH value is higher than 8, add vinegar essence to the mixed liquid Adjust until the pH is between 6-8, and the mass change of the qualitative and quantitative paper is less than 0.1% after drying;
步骤五、将步骤四最后获得的混合液体在27℃的环境温度下静置48h,即可得到工业燃料。Step 5. Put the mixed liquid finally obtained in Step 4 to stand for 48 hours at an ambient temperature of 27° C. to obtain the industrial fuel.
参照图1,本实施例还提供一种用于以餐厨油为原料制备工业燃料的搅拌机,它包括开口朝上的搅拌桶1以及伸入搅拌桶1桶内的转轴2;在转轴2上沿其径向安装有一个以上搅拌叶片3;在搅拌叶片3的末端可拆卸地安装有过滤袋4;转轴2的一端通过传动装置9与电机5的输出端相连;在搅拌桶1上沿其周向安装有环形的加热装置5;在搅拌桶1的顶部还安装有封口盖6;在搅拌桶的底部还安装有带阀门的出料管。在本实施例中,搅拌桶的底部还设置有滚轮,可由拖车进行拖拽移动。With reference to Fig. 1, present embodiment also provides a kind of mixer that is used to prepare industrial fuel with kitchen oil as raw material, and it comprises the mixing tank 1 that opening is upwards and the rotating shaft 2 that stretches in mixing tank 1 bucket; On rotating shaft 2 More than one stirring blade 3 is installed along its radial direction; a filter bag 4 is detachably installed at the end of the stirring blade 3; one end of the rotating shaft 2 is connected with the output end of the motor 5 through a transmission device 9; An annular heating device 5 is installed in the circumferential direction; a sealing cover 6 is installed on the top of the mixing bucket 1; and a discharge pipe with a valve is installed on the bottom of the mixing bucket. In this embodiment, the bottom of the mixing bucket is also provided with rollers, which can be dragged and moved by a trailer.
在搅拌叶片3的末端设置可以开合的置物箱31;过滤袋4设置在置物箱31内;且在置物箱31上开有与其内部相通的滤孔32。过滤袋4为采用石棉布制成的套袋;且置物箱31上的滤孔32的孔径大小大于所述过滤袋4上滤孔的大小。使用置物箱31能够有效防止过滤袋4破裂时内部的过滤吸附物质漫溢到搅拌桶1内部,同时为了避免餐厨油中的待吸附物质无法通过置物箱31完成交互,对置物箱31上的滤孔32的大小进行了限制。A storage box 31 that can be opened and closed is arranged at the end of the stirring blade 3; the filter bag 4 is arranged in the storage box 31; The filter bag 4 is a bag made of asbestos cloth; The use of the storage box 31 can effectively prevent the filter adsorption substances inside from overflowing into the mixing tank 1 when the filter bag 4 is broken. The size of the hole 32 is limited.
搅拌桶1为一圆桶结构;转轴2设置在搅拌桶1的中部,搅拌叶片3的长度不低于搅拌桶1内径大小的三分之二。本实施例中搅拌桶1的开口朝上,转轴2沿搅拌桶1的轴线设置;故而在进行搅拌时在离心力的作用下混合液会贴着搅拌桶1的内壁活动,限制搅拌叶片3的长度能够有效提高过滤袋与混合液的有效接触面积,从而到达理想的过滤吸附作用。过滤袋4中所装的物质为新鲜松针与烧碱的混合物。The mixing bucket 1 is a drum structure; the rotating shaft 2 is arranged in the middle of the mixing bucket 1, and the length of the mixing blade 3 is not less than two-thirds of the inner diameter of the mixing bucket 1. In this embodiment, the opening of the mixing tank 1 faces upwards, and the rotating shaft 2 is arranged along the axis of the mixing tank 1; therefore, when stirring, the mixed liquid will move against the inner wall of the mixing tank 1 under the action of centrifugal force, limiting the length of the mixing blade 3 It can effectively increase the effective contact area between the filter bag and the mixed liquid, so as to achieve the ideal filtration and adsorption effect. The material contained in the filter bag 4 is a mixture of fresh pine needles and caustic soda.
传动装置9为一个齿轮变速器;其控制端台设置在搅拌桶1的侧端的底部位置。加热装置5为一电控加热丝,且所述电控加热丝与传动装置9共用一个控制端台。齿轮变速器调整转速简单,而沿桶壁设置的电控加热丝能够起到较好的加热效果,两者使用同一个控制端台也能够提高其集成控制效果。The transmission device 9 is a gear transmission; its control end platform is arranged at the bottom position of the side end of the mixing bucket 1 . The heating device 5 is an electric control heating wire, and the electric control heating wire and the transmission device 9 share a control end table. It is easy to adjust the speed of the gear transmission, and the electric control heating wire arranged along the wall of the barrel can achieve a better heating effect, and the use of the same control end table for both can also improve the integrated control effect.
封口盖6为台阶形结构,所述台阶形封口盖6通过紧固螺钉固定在搅拌桶1上;且在台阶形封口盖6与搅拌桶1相接处还设置有封油环。本实施例中,封油环未在图中进行示意。The sealing cover 6 is a step-shaped structure, and the step-shaped sealing cover 6 is fixed on the mixing bucket 1 by fastening screws; In this embodiment, the oil seal ring is not shown in the figure.
在出料管7的侧端设置有观察窗33;观察窗33内安装有PH试笔8,PH试笔8的一端与搅拌桶1的内部相连。通过设置观察窗33与PH试笔8能够对搅拌桶内混合搅拌液的PH进行实时观察。An observation window 33 is arranged at the side end of the discharge pipe 7; a pH test pen 8 is installed in the observation window 33, and one end of the pH test pen 8 is connected to the inside of the mixing tank 1. By arranging the observation window 33 and the pH test pen 8, the pH of the mixing liquid in the mixing tank can be observed in real time.
Claims (10)
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Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101163655A (en) * | 2005-04-22 | 2008-04-16 | 仲村训一 | Biofuel conversion process |
| CN101724475A (en) * | 2008-11-03 | 2010-06-09 | 秦才东 | Biomass base liquid fuel, utilizing method and engine structure |
| CN101831326A (en) * | 2010-05-18 | 2010-09-15 | 杭州绿洲能源科技有限公司 | Biomass fuel oil and preparation method thereof |
| CN102559392A (en) * | 2010-12-30 | 2012-07-11 | 通向成功私人有限公司 | Method for producing low-pour-point fatty acid methyl ester or ethyl ester by using any mixture of triacylglycerol and free fatty acid |
| CN103160336A (en) * | 2013-03-12 | 2013-06-19 | 海口腾旭中天科技有限公司 | Catering industry waste oil-based biological alcohol oil and preparation method thereof |
| CN104862018A (en) * | 2015-04-13 | 2015-08-26 | 内乡县龙翔生物科技有限公司 | Production process of antioxidant biodiesel |
| CN106544051A (en) * | 2016-11-25 | 2017-03-29 | 南宁市黑晶信息技术有限公司 | A kind of fuel oil and preparation method thereof |
| CN108559557A (en) * | 2018-05-16 | 2018-09-21 | 上海纽孚尔能源技术有限公司 | Microemulsified kitchen waste grease preparing bio-fuel |
| CN108865318A (en) * | 2018-07-02 | 2018-11-23 | 黄山市联兴生物质能源有限公司 | A kind of pecan biological particles and preparation method |
| CN208287869U (en) * | 2018-03-18 | 2018-12-28 | 南京联裕达化工新材料科技有限公司 | A kind of agitating device for Chemical Manufacture |
| CN208340541U (en) * | 2018-05-08 | 2019-01-08 | 汤丽红 | A kind of OIL IN LUBRICATING OIL PRODUCTION agitating device |
| CN109370697A (en) * | 2018-11-30 | 2019-02-22 | 彭翔 | A kind of biomass fuel preparation method for material |
-
2019
- 2019-05-17 CN CN201910413351.8A patent/CN110117505A/en active Pending
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101163655A (en) * | 2005-04-22 | 2008-04-16 | 仲村训一 | Biofuel conversion process |
| CN101724475A (en) * | 2008-11-03 | 2010-06-09 | 秦才东 | Biomass base liquid fuel, utilizing method and engine structure |
| CN101831326A (en) * | 2010-05-18 | 2010-09-15 | 杭州绿洲能源科技有限公司 | Biomass fuel oil and preparation method thereof |
| CN102559392A (en) * | 2010-12-30 | 2012-07-11 | 通向成功私人有限公司 | Method for producing low-pour-point fatty acid methyl ester or ethyl ester by using any mixture of triacylglycerol and free fatty acid |
| CN103160336A (en) * | 2013-03-12 | 2013-06-19 | 海口腾旭中天科技有限公司 | Catering industry waste oil-based biological alcohol oil and preparation method thereof |
| CN104862018A (en) * | 2015-04-13 | 2015-08-26 | 内乡县龙翔生物科技有限公司 | Production process of antioxidant biodiesel |
| CN106544051A (en) * | 2016-11-25 | 2017-03-29 | 南宁市黑晶信息技术有限公司 | A kind of fuel oil and preparation method thereof |
| CN208287869U (en) * | 2018-03-18 | 2018-12-28 | 南京联裕达化工新材料科技有限公司 | A kind of agitating device for Chemical Manufacture |
| CN208340541U (en) * | 2018-05-08 | 2019-01-08 | 汤丽红 | A kind of OIL IN LUBRICATING OIL PRODUCTION agitating device |
| CN108559557A (en) * | 2018-05-16 | 2018-09-21 | 上海纽孚尔能源技术有限公司 | Microemulsified kitchen waste grease preparing bio-fuel |
| CN108865318A (en) * | 2018-07-02 | 2018-11-23 | 黄山市联兴生物质能源有限公司 | A kind of pecan biological particles and preparation method |
| CN109370697A (en) * | 2018-11-30 | 2019-02-22 | 彭翔 | A kind of biomass fuel preparation method for material |
Non-Patent Citations (3)
| Title |
|---|
| 吕涯: "《石油产品添加剂》", 华东理工大学出版社, pages: 248 * |
| 宋应华: "《花生壳生物吸附剂的制备及其在含染料废水治理中的应用》", 31 March 2017, 重庆大学出版社, pages: 36 * |
| 沈本贤: "《化工类油气储运工程专业实验》", 31 July 2014, 华东理工大学出版社, pages: 248 * |
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