CN212076977U - A clean production line for biomass pellets - Google Patents
A clean production line for biomass pellets Download PDFInfo
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- CN212076977U CN212076977U CN202020241723.1U CN202020241723U CN212076977U CN 212076977 U CN212076977 U CN 212076977U CN 202020241723 U CN202020241723 U CN 202020241723U CN 212076977 U CN212076977 U CN 212076977U
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 26
- 239000002028 Biomass Substances 0.000 title claims abstract description 25
- 239000008188 pellet Substances 0.000 title description 2
- 230000007246 mechanism Effects 0.000 claims abstract description 135
- 239000000428 dust Substances 0.000 claims abstract description 60
- 239000000463 material Substances 0.000 claims abstract description 35
- 239000002245 particle Substances 0.000 claims abstract description 24
- 238000000926 separation method Methods 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 16
- 239000007787 solid Substances 0.000 claims abstract description 16
- 238000004140 cleaning Methods 0.000 claims abstract description 15
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 6
- 238000005469 granulation Methods 0.000 claims description 21
- 230000003179 granulation Effects 0.000 claims description 21
- 238000003860 storage Methods 0.000 claims description 18
- 238000007885 magnetic separation Methods 0.000 claims description 13
- 238000004062 sedimentation Methods 0.000 claims description 9
- 238000012216 screening Methods 0.000 claims description 7
- 239000007790 solid phase Substances 0.000 claims description 7
- 239000002994 raw material Substances 0.000 claims description 4
- 238000002955 isolation Methods 0.000 claims description 3
- 238000005303 weighing Methods 0.000 claims description 3
- 239000007792 gaseous phase Substances 0.000 claims 2
- 239000008187 granular material Substances 0.000 claims 1
- 238000000605 extraction Methods 0.000 abstract description 16
- 238000012545 processing Methods 0.000 abstract description 7
- 239000000446 fuel Substances 0.000 abstract description 2
- 239000013067 intermediate product Substances 0.000 abstract 1
- 230000006872 improvement Effects 0.000 description 11
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 6
- 239000012071 phase Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000010881 fly ash Substances 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 206010008479 Chest Pain Diseases 0.000 description 1
- 206010008469 Chest discomfort Diseases 0.000 description 1
- 206010011224 Cough Diseases 0.000 description 1
- 206010013975 Dyspnoeas Diseases 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 206010036790 Productive cough Diseases 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011365 complex material Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000013024 troubleshooting Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Processing Of Solid Wastes (AREA)
Abstract
本实用新型公开了一种生物质颗粒清洁生产线,包括破碎机构、烘干机构和造粒机构,所述烘干机构设置于所述破碎机构的下游和所述造粒机构的上游,所述生物质清洁生产线还包括防尘机构,防尘机构包括负压集尘罩,所述负压集尘罩通过管道与抽气装置连接;本实用新型相比现有技术具有以下优点:在可能产生扬尘的位置设置负压集尘罩来有效隔绝灰尘并予以回收;采用合理的分离措施进行气固分离,加工处理能力高;使用加工中间产品作为燃料提供热能,集约化生产管理降低成本;整个生产线杜绝粉尘的泄漏的所有可能,实现了清洁化生产。
The utility model discloses a biomass particle cleaning production line, which comprises a crushing mechanism, a drying mechanism and a granulating mechanism. The drying mechanism is arranged downstream of the crushing mechanism and upstream of the granulating mechanism. The material cleaning production line also includes a dust-proof mechanism, and the dust-proof mechanism includes a negative-pressure dust-collecting hood, which is connected to the air extraction device through a pipeline; compared with the prior art, the utility model has the following advantages: when dust may be generated Set up a negative pressure dust hood at the location of the dust collector to effectively isolate and recycle dust; adopt reasonable separation measures for gas-solid separation, with high processing capacity; use processing intermediate products as fuel to provide heat energy, and intensify production management to reduce costs; the entire production line eliminates All possibilities of dust leakage realize cleaner production.
Description
技术领域technical field
本实用新型涉及生物质处置技术和清洁生产技术领域,尤其涉及的是一种生物质颗粒清洁生产线。The utility model relates to the field of biomass disposal technology and clean production technology, in particular to a clean production line of biomass particles.
背景技术Background technique
生物质的使用价值很高,作为一种可再生能源,相比其他可再生能源比如太阳能、氢能、风能等,具有储藏量大,投资利用风险低,可获得利润回报高并且不局限于气候地理温度等条件限制的优点,生物质加工厂可以用来直燃发电发热、制备纤维素乙醇、固化成型等,环保无污染并且可以降低燃煤使用率,节约经济成本,但是生物质成型颗粒在实际生产中产生的粉尘较多,粉尘浓度过高导致的粉尘爆炸,以及人体接触粉尘过久,会出现咳嗽、咳痰、胸闷、胸痛和呼吸困难等问题,更严重者会出现尘肺症状,秸秆生产过程中卸料过程以及各生产环节都会产生一定量的粉尘,所以粉尘处理问题是需要引起生产单位重视的,并且现有的秸秆成型颗粒生产需要人力操控,生产效率较低,无法做到无尘清洁化自动生产,造成秸秆成型颗粒产量受限,并且生产成本较高、对环境污染较为严重。The use value of biomass is very high. As a kind of renewable energy, compared with other renewable energy sources such as solar energy, hydrogen energy, wind energy, etc., it has large storage capacity, low investment and utilization risk, high profit return, and is not limited to climate. Due to the limitations of geographical temperature and other conditions, biomass processing plants can be used for direct combustion to generate heat, prepare cellulosic ethanol, solidify and form, etc., which are environmentally friendly and pollution-free, and can reduce the utilization rate of coal combustion and save economic costs. In actual production, there is a lot of dust, dust explosion caused by high dust concentration, and prolonged exposure of the human body to dust will cause problems such as coughing, expectoration, chest tightness, chest pain and difficulty breathing. In the production process, the unloading process and each production link will generate a certain amount of dust, so the problem of dust treatment needs to be paid attention to by the production unit, and the existing straw molding pellet production requires manual control, the production efficiency is low, and it is impossible to achieve no problem. The automatic production of dust cleaning results in limited output of straw shaped particles, high production cost and serious environmental pollution.
实用新型内容Utility model content
本实用新型的目的在于克服现有技术的不足,提供了一种生物质颗粒清洁生产线。The purpose of the utility model is to overcome the deficiencies of the prior art and provide a clean production line for biomass particles.
本实用新型是通过以下技术方案实现的:一种生物质颗粒清洁生产线,包括破碎机构、烘干机构和造粒机构,烘干机构设置于破碎机构的下游和造粒机构的上游,其特征在于:还包括防尘机构,防尘机构包括负压集尘罩,负压集尘罩通过管道与抽气装置连接。The utility model is realized by the following technical solutions: a biomass particle cleaning production line, comprising a crushing mechanism, a drying mechanism and a granulating mechanism, and the drying mechanism is arranged downstream of the crushing mechanism and upstream of the granulating mechanism, and is characterized in that : It also includes a dust-proof mechanism, and the dust-proof mechanism includes a negative-pressure dust-collecting cover, which is connected to the air extraction device through a pipeline.
作为对上述方案的进一步改进,抽气装置的入口处设置有气固分离装置,气固分离装置的固相出口与造粒机构的入口连接。As a further improvement to the above solution, a gas-solid separation device is provided at the inlet of the air extraction device, and the solid phase outlet of the gas-solid separation device is connected to the inlet of the granulation mechanism.
作为对上述方案的进一步改进,在负压集尘罩的周缘设置吊挂隔离帘。As a further improvement to the above solution, a hanging isolation curtain is arranged on the periphery of the negative pressure dust collecting hood.
作为对上述方案的进一步改进,破碎机构包括粗料破碎机构和粉碎机构,粗料破碎机构设置于粉碎机构的上游,负压集尘罩设置于粗料破碎机构的入口、粗料破碎机构的出口、粉碎机的入口和粉碎机构的出口中的一处或几处。As a further improvement to the above scheme, the crushing mechanism includes a coarse material crushing mechanism and a crushing mechanism, the coarse material crushing mechanism is arranged upstream of the crushing mechanism, and the negative pressure dust hood is arranged at the inlet of the coarse material crushing mechanism and the outlet of the coarse material crushing mechanism , one or more of the inlet of the pulverizer and the outlet of the pulverizing mechanism.
作为对上述方案的进一步改进,破碎机构包括还包括磁选机构,磁选机构设置于粗料破碎机构和粉碎机构之间,负压集尘罩还设置于磁选机构的入口和或磁选机构的出口处。As a further improvement to the above scheme, the crushing mechanism also includes a magnetic separation mechanism, the magnetic separation mechanism is arranged between the coarse material crushing mechanism and the crushing mechanism, and the negative pressure dust collecting hood is also arranged at the entrance of the magnetic separation mechanism and/or the magnetic separation mechanism. the exit.
作为对上述方案的进一步改进,造粒机构的物料出口上设置有负压筛料除尘机构,负压筛料除尘装置包括卸料滑道和设置于卸料滑道下方的负压仓,卸料滑道底板上设置有筛孔,筛孔直接与负压仓连通。As a further improvement to the above scheme, the material outlet of the granulation mechanism is provided with a negative pressure screening material dedusting mechanism, and the negative pressure screening material dedusting device includes a discharge slideway and a negative pressure bin arranged below the discharge slideway. Screen holes are arranged on the bottom plate of the slideway, and the screen holes are directly connected with the negative pressure bin.
作为对上述方案的进一步改进,造粒机构物料入口封闭设置,通过绞龙送料,造粒机构物料入口敞开设置,在其上方设置有负压集尘罩。As a further improvement to the above scheme, the material inlet of the granulation mechanism is closed and set, and the material is fed by the auger, and the material inlet of the granulation mechanism is set open, and a negative pressure dust collecting hood is set above it.
作为对上述方案的进一步改进,破碎机构与烘干机构之间还设置有沉降储料机构,沉降储料机构内腔与抽气装置连接。As a further improvement to the above solution, a sedimentation storage mechanism is also arranged between the crushing mechanism and the drying mechanism, and the inner cavity of the sedimentation storage mechanism is connected with the air extraction device.
作为对上述方案的进一步改进,烘干机构配置的热风炉是生物质热风炉,其原料来源于沉降储料机构或破碎机构。As a further improvement to the above scheme, the hot blast stove configured by the drying mechanism is a biomass hot blast stove, and its raw material comes from the sedimentation storage mechanism or the crushing mechanism.
作为对上述方案的进一步改进,烘干机构包括热风炉、滚筒烘干机和产品收集仓,滚筒烘干机的出口直接设置于产品收集仓内,产品收集仓顶部设置气相出口,产品收集仓底部设置固相出口与造粒机构连接,气相出口连接气固分离装置。As a further improvement to the above solution, the drying mechanism includes a hot blast stove, a tumble dryer and a product collection bin. The outlet of the tumble dryer is directly set in the product collection bin, the top of the product collection bin is provided with a gas phase outlet, and the bottom of the product collection bin is set up. The solid-phase outlet is set to be connected with the granulation mechanism, and the gas-phase outlet is connected to the gas-solid separation device.
作为对上述方案的进一步改进,在造粒机构的下游还设置有储仓,储仓的出口设置有称重装袋机构。As a further improvement to the above solution, a storage bin is also provided downstream of the granulation mechanism, and a weighing and bagging mechanism is provided at the outlet of the storage bin.
本实用新型相比现有技术具有以下优点:在可能产生扬尘的位置设置负压集尘罩来有效隔绝灰尘并予以回收;采用合理的分离措施进行气固分离,加工处理能力高;使用加工中间产品作为燃料提供热能,集约化生产管理降低成本;整个生产线杜绝粉尘的泄漏的所有可能,实现了清洁化生产。Compared with the prior art, the utility model has the following advantages: a negative pressure dust collecting hood is arranged at the position where dust may be generated to effectively isolate and recycle the dust; reasonable separation measures are adopted for gas-solid separation, and the processing capacity is high; the use of intermediate processing The product is used as fuel to provide heat energy, and intensive production management reduces costs; the entire production line eliminates all possibilities of dust leakage and realizes clean production.
附图说明Description of drawings
图1是本实用新型结构示意图。FIG. 1 is a schematic structural diagram of the present utility model.
图2是负压集尘罩结构示意图。Figure 2 is a schematic view of the structure of the negative pressure dust hood.
图3是负压筛料除尘机构结构示意图。Figure 3 is a schematic diagram of the structure of the negative pressure screening material dust removal mechanism.
具体实施方式Detailed ways
下面对本实用新型的实施例作详细说明,本实施例在以本实用新型技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本实用新型的保护范围不限于下述的实施例。The embodiments of the present utility model are described in detail below. The present embodiment is implemented on the premise of the technical solution of the present utility model, and provides detailed implementation methods and specific operation processes, but the protection scope of the present utility model is not limited to the following described embodiment.
一种生物质颗粒清洁生产线,包括破碎机构、烘干机构和造粒机构6,烘干机构设置于破碎机构的下游和造粒机构6的上游,还包括防尘机构,防尘机构包括负压集尘罩2,负压集尘罩2通过管道与抽气装置81连接;根据实际装置的布置,每个负压集尘罩2可以单独配置抽气装置81或与其他装置共用一套抽气装置81;如果几个负压集尘罩2布置在相邻或相近位置,在保证集尘抽气效果的前提下也可以使用一套抽气装置81为其提供负压。在附图中,我们在假设抽气装置81功率足够大的前提下,使用一套抽气装置81为所有的负压集尘罩2 提供负压;A biomass particle cleaning production line includes a crushing mechanism, a drying mechanism and a
抽气装置81的入口处设置有气固分离装置8,气固分离装置8的固相出口与造粒机构6的入口连接;扬尘或飞灰中的固相颗粒往往很小,容易随气流扬起,将其分离收集后直接送入造粒机构6,避免在其他加工操作中再次扬起,其量相对较少不会对造粒参数形成影响;气固分离装置8的数量根据实际需求和场地布置,可以一个负压集尘罩2单独配置或几个负压集尘罩2共用或负压集尘罩2与其他设备共用;A gas-solid separation device 8 is provided at the inlet of the air extraction device 81, and the solid-phase outlet of the gas-solid separation device 8 is connected to the inlet of the
在负压集尘罩2的周缘设置吊挂隔离帘21;吊挂隔离帘21通常由柔性材料制作便于安装,用于在负压集尘罩2下方隔离出一定的空间,限制扬尘的范围,从而增强负压集尘罩2的集尘效果;A hanging
破碎机构包括粗料破碎机构1和粉碎机构3,粗料破碎机构1设置于粉碎机构3的上游,负压集尘罩2可以设置于所有容易发生灰尘泄漏的场所,如粗料破碎机构1的入口、粗料破碎机构1的出口、粉碎机的入口和粉碎机构3的出口;生物质颗粒的整个加工过程中,破碎操作是产生扬尘的主要环节,而无论是粗料破碎机构1或粉碎机构3,其破碎腔室是封闭的结构,扬尘泄漏只可能发生在物料的进出口处;通过在破碎过程中会发生扬尘泄漏的位置布置负压集尘罩2,能够有效防止扬尘泄漏。The crushing mechanism includes a coarse material crushing mechanism 1 and a crushing mechanism 3. The coarse material crushing mechanism 1 is arranged upstream of the crushing mechanism 3, and the negative pressure
破碎机构包括还包括磁选机构11,磁选机构11设置于粗料破碎机构1和粉碎机构3之间;根据使用原料的差别,在使用建筑用废弃生物质原料(如费旧木材,竹材等)中含有部分铁钉等杂质,容易对粉碎机和造粒机造成损伤,因而设置磁选机构11来除去相应杂志,保证生产稳定进行。负压集尘罩2还可以设置于磁选机构11的入口和或磁选机构11的出口处。The crushing mechanism also includes a magnetic separation mechanism 11. The magnetic separation mechanism 11 is set between the coarse material crushing mechanism 1 and the crushing mechanism 3; ) contains some impurities such as iron nails, which are easy to cause damage to the pulverizer and granulator, so a magnetic separation mechanism 11 is set to remove the corresponding magazines to ensure stable production. The negative pressure
造粒机构6的物料出口上设置有负压筛料除尘机构,负压筛料除尘装置包括卸料滑道61和设置于卸料滑道61下方的负压仓63,卸料滑道61底板上设置有筛孔62,筛孔62直接与负压仓63连通。造粒过程中颗粒出口往往是正压状态,部分粉料没有挤压成型的,会随着颗粒一起排出,通过负压筛料除尘机构,一方面从颗粒中筛除粉料,同时设置于下方的负压仓63能够将颗粒出口喷出的扬尘悉数回收,在此过程中大量空气吹过颗粒表面,能够加快颗粒冷却,缩短包装前的冷却时间;负压仓63可以单独配置抽气装置81或者与负压集尘罩2 等其他设备共用抽气装置81(附图中采用了与负压集尘罩2共用抽气装置81的方案)。The material outlet of the
根据物料的差别,和造粒机构6的选型,造粒机构6物料入口可以选择封闭设置或敞开设置;入口封闭设置的可以通过绞龙送料,造粒机构6的入口封闭能够有效避免发生飞灰的情况,配合使用蛟龙喂料能够实现无尘化生产;入口敞开设置的在其上方设置有负压集尘罩2,对于物料成分复杂的原料,生产中常常会发生意外停机的情况,敞口的设计能够便于快速检修排除故障。According to the difference of materials and the selection of the
破碎机构与烘干机构之间还设置有沉降储料机构4,沉降储料机构4内腔与抽气装置81连接;破碎机构通常间歇式生产,为保证烘干机构和造粒机构6连续生产,我们设计沉降储料机构4来储存生物质粉末,且用抽气装置81将沉降储料机构4抽成负压,以避免灰尘泄漏。There is also a sedimentation storage mechanism 4 between the crushing mechanism and the drying mechanism, and the inner cavity of the sedimentation storage mechanism 4 is connected with the air extraction device 81; the crushing mechanism is usually produced intermittently, in order to ensure the continuous production of the drying mechanism and the
烘干机构配置的热风炉51是生物质热风炉51,其原料来源于沉降储料机构 4或破碎机构;The hot blast stove 51 configured by the drying mechanism is a biomass hot blast stove 51, and its raw material comes from the sedimentation storage mechanism 4 or the crushing mechanism;
烘干机构包括热风炉51、滚筒烘干机5和产品收集仓52,滚筒烘干机5的出口直接设置于产品收集仓52内,产品收集仓52顶部设置气相出口,产品收集仓52底部设置固相出口与造粒机构6连接,气相出口连接气固分离装置8;现有部分设备直接将滚筒烘干机5的出口连接到旋风除尘器上,由此造成旋风除尘器工作负荷大,严重限制了烘干产能;实际上烘干的粉状生物质,排出滚筒烘干机5后大部分能够直接沉降,本方案设计收集仓,热风和粉料进入收集仓后,风速降低直接将大部分粉料分离出来,少部分飞灰再随着热风进入除尘机分离(气固分离装置8在本案中并非指一个单独的设备,是泛指气固分离系统,可以由多台气固分离设备组成,共同承担各个单元操作的气固分离任务。) 在造粒机构6的下游还设置有储仓7,储仓7的出口设置有称重装袋机构71。The drying mechanism includes a hot blast stove 51, a
以上仅为本实用新型的较佳实施例而已,并不用以限制本实用新型,凡在本实用新型的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本实用新型的保护范围之内。The above are only preferred embodiments of the present utility model, and are not intended to limit the present utility model. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present utility model shall be included in the present utility model. within the scope of protection.
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