CN105018171B - Compound modified biomass solid molding fuel preparation facilities - Google Patents
Compound modified biomass solid molding fuel preparation facilities Download PDFInfo
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- CN105018171B CN105018171B CN201510422563.4A CN201510422563A CN105018171B CN 105018171 B CN105018171 B CN 105018171B CN 201510422563 A CN201510422563 A CN 201510422563A CN 105018171 B CN105018171 B CN 105018171B
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- 238000002156 mixing Methods 0.000 claims abstract description 147
- 239000002994 raw material Substances 0.000 claims abstract description 87
- 239000000843 powder Substances 0.000 claims abstract description 59
- 238000000465 moulding Methods 0.000 claims abstract description 57
- 239000002028 Biomass Substances 0.000 claims abstract description 49
- 239000007788 liquid Substances 0.000 claims abstract description 37
- 239000000446 fuel Substances 0.000 claims abstract description 31
- 239000007787 solid Substances 0.000 claims abstract description 27
- 238000002360 preparation method Methods 0.000 claims abstract description 21
- 150000001875 compounds Chemical class 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 3
- 238000007493 shaping process Methods 0.000 claims 4
- 238000007599 discharging Methods 0.000 claims 3
- 239000004744 fabric Substances 0.000 claims 1
- 239000002131 composite material Substances 0.000 abstract description 10
- 238000007792 addition Methods 0.000 description 22
- 230000005540 biological transmission Effects 0.000 description 13
- 239000004484 Briquette Substances 0.000 description 10
- 229920002472 Starch Polymers 0.000 description 9
- 239000008107 starch Substances 0.000 description 9
- 235000019698 starch Nutrition 0.000 description 9
- 230000009467 reduction Effects 0.000 description 8
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 7
- 238000001125 extrusion Methods 0.000 description 7
- 239000010902 straw Substances 0.000 description 7
- 241000209094 Oryza Species 0.000 description 6
- 235000007164 Oryza sativa Nutrition 0.000 description 6
- 235000009566 rice Nutrition 0.000 description 6
- 239000000654 additive Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000032258 transport Effects 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000012467 final product Substances 0.000 description 3
- 235000011187 glycerol Nutrition 0.000 description 3
- 239000010705 motor oil Substances 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 2
- 238000000280 densification Methods 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000004449 solid propellant Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 238000010335 hydrothermal treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B11/00—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
- B30B11/20—Roller-and-ring machines, i.e. with roller disposed within a ring and co-operating with the inner surface of the ring
- B30B11/201—Roller-and-ring machines, i.e. with roller disposed within a ring and co-operating with the inner surface of the ring for extruding material
- B30B11/207—Feed means
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明公开了一种复合改性生物质固体成型燃料制备装置,包括原料供应仓、粉料添加仓、液体原料添加仓、混合单元和致密成型单元;原料供应仓和粉料添加仓的出料口位于混合单元入料口侧,并通过混合单元入料口与混合单元的混合腔连通,液体原料添加仓出料口与混合单元混合腔连通,致密成型单元位于混合单元出料口端,混合单元出料口与致密成型单元进料口相连;本发明能够将改性液体原料和粉体原料自动按需添加,并实现与生物质原料的均匀混合,可高效率的制备出生物质固体成型燃料。
The invention discloses a composite modified biomass solid molding fuel preparation device, which comprises a raw material supply bin, a powder addition bin, a liquid raw material addition bin, a mixing unit and a compact molding unit; the raw material supply bin and the powder addition bin are discharged The inlet is located on the side of the mixing unit inlet, and communicates with the mixing chamber of the mixing unit through the inlet of the mixing unit. The outlet of the liquid raw material addition chamber is connected with the mixing chamber of the mixing unit. The compact molding unit is located at the outlet of the mixing unit. The unit discharge port is connected to the compact molding unit feed port; the invention can automatically add modified liquid raw materials and powder raw materials as needed, and realize uniform mixing with biomass raw materials, and can efficiently prepare biomass solid molding fuels .
Description
技术领域technical field
本发明属于生物质能源化利用以及固体废弃物处理技术领域,特别是一种种复合改性生物质固体成型燃料制备装置。The invention belongs to the technical field of biomass energy utilization and solid waste treatment, in particular to a compound modified biomass solid briquette fuel preparation device.
背景技术Background technique
目前,全世界正面临着能源与环境的双重压力。一方面,社会经济的发展需要能源作为动力,由于化石能源储量有限,按目前消费量推算,世界石油资源在将今后50年到80年间消耗殆尽;另一方面,过度消费化石燃料,打破了自然界的能量和碳平衡,带来了臭氧层破坏、全球气候变暖、酸雨等日益严重的环境问题。因此具有环保、清洁和可持续利用特点的生物质能的开发利用受到许多国家的高度重视。At present, the whole world is facing the dual pressure of energy and environment. On the one hand, social and economic development requires energy as a driving force. Due to the limited reserves of fossil energy, the world’s oil resources will be exhausted in the next 50 to 80 years based on current consumption estimates; on the other hand, excessive consumption of fossil fuels has broken the The energy and carbon balance in nature has brought about increasingly serious environmental problems such as ozone layer depletion, global warming, and acid rain. Therefore, the development and utilization of biomass energy with the characteristics of environmental protection, cleanliness and sustainable utilization has been highly valued by many countries.
我国是一个农业大国,具有大量的生物质资源,仅农作物秸秆就有20多种,每年可生产7亿多吨,是世界上生物质资源最为丰富的国家之一,但每年被废弃或焚烧的农业生物质能占到总量的40%以上,随意焚烧不仅会带来严重的环境污染,也是对资源的巨大浪费。鉴于以上情况,对我国储量庞大的农林生物质资源进行能源化利用以缓解当前的能源环境问题已成为非常迫切的任务。my country is a large agricultural country with a large amount of biomass resources. There are more than 20 kinds of crop straws alone, which can produce more than 700 million tons per year. It is one of the countries with the most abundant biomass resources in the world. Agricultural biomass can account for more than 40% of the total, and random incineration will not only cause serious environmental pollution, but also a huge waste of resources. In view of the above situation, it has become a very urgent task to use the huge reserves of agricultural and forestry biomass resources in my country to alleviate the current energy and environmental problems.
生物质能源化利用的各种途径中,挤压致密成型具有工艺简单、生产率高等优势,且生物质成型燃料(Biomass Densification Briquetting Fuel,BDBF)的密度和强度较高,便于运输和燃烧,已经逐渐成为欧美等发达国家的主流技术。Among the various ways of biomass energy utilization, extrusion compaction has the advantages of simple process and high productivity, and the density and strength of biomass briquette fuel (Biomass Densification Briquetting Fuel, BDBF) are high, easy to transport and burn, and have gradually It has become the mainstream technology in developed countries such as Europe and the United States.
由于生物质具有原料特性(原料成分、粒径和水分等)不易控制的特殊性,且各类原料特性差异较大,国内对该项技术的研究起步较晚,基础理论尚不完善。生物质致密成型设备在实际应用中存在三个比较突出的问题:成型设备能耗高、模具磨损快和所生产的成型燃料热值低。Because biomass has the particularity that the raw material characteristics (raw material composition, particle size and moisture, etc.) are not easy to control, and the characteristics of various raw materials are quite different, domestic research on this technology started relatively late, and the basic theory is not yet perfect. There are three prominent problems in the practical application of biomass densification molding equipment: high energy consumption of molding equipment, fast mold wear and low calorific value of the molding fuel produced.
而通过复合改性技术可以有效改善原料特性,降低成型能耗、延长模具寿命,并且可提升燃料热值。但是由于复合改性生物质燃料成型工艺相对传统致密成型工艺复杂,对成型设备的要求也更高,当前传统的生物质致密成型装置尚不能满足使用需求。The composite modification technology can effectively improve the characteristics of raw materials, reduce the energy consumption of molding, prolong the life of the mold, and increase the calorific value of fuel. However, because the composite modified biomass fuel molding process is more complicated than the traditional compact molding process, the requirements for molding equipment are also higher, and the current traditional biomass compact molding equipment cannot meet the needs of use.
查阅国内外文献,专利CN 102862312 A公布了一种生物质挤压成型联合机组,通过将动力、操作控制、剪切、轧碾、挤压成型、成品挤光断开、称重包装机构装置组成并安装在同一机架上,利用该生物质挤压成型联合机组可实现对生物质连续挤压成型,但机组不具备改性原料的添加和混合功能。专利CN 201479886 U公布了一种卧式饲料混合制粒机组,该机组由粉碎风吸进料口、辅料提升机、混合搅拌仓和制粒室组合而成,可实现混合和制粒一次完成,但无法添加液体改性原料,并且无法实现原料添加比例的自动控制。Consulting domestic and foreign literature, the patent CN 102862312 A discloses a biomass extrusion molding unit, which is composed of power, operation control, shearing, rolling, extrusion molding, finished product extrusion and disconnection, and weighing and packaging mechanisms. And installed on the same frame, the biomass extrusion combined unit can realize the continuous extrusion of biomass, but the unit does not have the function of adding and mixing modified raw materials. Patent CN 201479886 U discloses a horizontal feed mixing and granulating unit, which is composed of a crushing air suction inlet, an auxiliary material elevator, a mixing chamber and a granulating chamber, which can realize mixing and granulating at one time. However, it is impossible to add liquid modified raw materials, and it is impossible to realize the automatic control of raw material addition ratio.
发明内容Contents of the invention
本发明的目的在于提供一种能够将改性液体原料和粉体原料自动按需添加,并实现与生物质原料的均匀混合,可高效率的制备出生物质固体成型燃料的复合改性生物质固体成型燃料制备装置。The purpose of the present invention is to provide a compound modified biomass solid that can automatically add modified liquid raw materials and powder raw materials on demand, and realize uniform mixing with biomass raw materials, and can efficiently prepare biomass solid molding fuels Shaped fuel preparation device.
实现本发明目的的技术解决方案为:The technical solution that realizes the object of the present invention is:
一种复合改性生物质固体成型燃料制备装置,包括原料供应仓、粉料添加仓、液体原料添加仓、混合单元和致密成型单元;A composite modified biomass solid briquette fuel preparation device, comprising a raw material supply bin, a powder material addition bin, a liquid raw material addition bin, a mixing unit and a compact molding unit;
原料供应仓和粉料添加仓的出料口位于混合单元入料口侧,并通过混合单元入料口与混合单元的混合腔连通,The outlets of the raw material supply bin and the powder addition bin are located on the side of the inlet of the mixing unit, and communicate with the mixing chamber of the mixing unit through the inlet of the mixing unit.
液体原料添加仓出料口与混合单元混合腔连通,The outlet of the liquid raw material adding bin is connected with the mixing chamber of the mixing unit,
致密成型单元位于混合单元出料口端,混合单元出料口与致密成型单元进料口相连;The compact forming unit is located at the discharge port of the mixing unit, and the discharge port of the mixing unit is connected to the feed port of the compact forming unit;
其中,原料仓送料螺旋均布于原料仓螺旋轴上,粉料添加仓螺旋均布于粉料添加仓螺旋轴上,混合螺旋均布于位于混合单元出料口一端的混合螺旋轴上,原料仓螺旋轴、粉料添加仓螺旋轴与混合螺旋轴分别位于原料仓体、粉料添加仓体和混合单元混合腔的底部;加料驱动电机通过原料仓传动链条和粉料添加仓传动链条分别同时驱动原料仓螺旋轴和粉料添加仓螺旋轴转动;混合桨叶均布于混合轴上,混合轴位于混合螺旋轴正上方,混合驱动电机通过混合轴驱动链条和混合螺旋轴驱动链条分别同时驱动混合轴和混合螺旋轴转动。Among them, the feeding screw of the raw material bin is evenly distributed on the screw shaft of the raw material bin, the screw of the powder adding bin is evenly distributed on the screw shaft of the powder adding bin, and the mixing screw is evenly distributed on the mixing screw shaft at the end of the outlet of the mixing unit. The screw shaft of the bin, the screw shaft of the powder adding bin and the mixing screw shaft are located at the bottom of the raw material bin, the powder adding bin and the mixing chamber of the mixing unit respectively; Drive the screw shaft of the raw material bin and the screw shaft of the powder adding bin to rotate; the mixing paddles are evenly distributed on the mixing shaft, the mixing shaft is located directly above the mixing screw shaft, and the mixing drive motor is driven simultaneously by the mixing shaft driving chain and the mixing screw shaft driving chain The mixing shaft and mixing screw shaft rotate.
本发明与现有技术相比,其显著优点:Compared with the prior art, the present invention has significant advantages:
(1)本发明所提出的复合改性固体成型燃料制备装置,能够同时实现降低成型能耗、提升制品品质和延长模具寿命的目的,可解决制约生物质固体成型燃料广泛应用的瓶颈问题,促进生物质固体成型燃料技术的推广。(1) The compound modified solid briquette fuel preparation device proposed by the present invention can simultaneously achieve the purpose of reducing molding energy consumption, improving product quality and prolonging mold life, and can solve the bottleneck problem that restricts the wide application of biomass solid briquette fuel, and promote Promotion of biomass solid briquette fuel technology.
(2)本发明可实现液体改性原料和粉体改性原料的同时添加、混合,并且可自动控制原料的添加比例。(2) The present invention can realize simultaneous addition and mixing of liquid modified raw materials and powder modified raw materials, and can automatically control the ratio of raw materials added.
(3)本发明能适应各类预处理后的生物质原料,可极大的促进生物质资源的高效利用。(3) The present invention can adapt to various pretreated biomass raw materials, and can greatly promote the efficient utilization of biomass resources.
(4)本发明可同时实现原料的添加、混合和挤压成型,能有效提升生物质致密成型燃料的生产效率。(4) The present invention can realize the addition, mixing and extrusion molding of raw materials at the same time, and can effectively improve the production efficiency of biomass dense molding fuel.
下面结合附图对本发明作进一步详细描述。The present invention will be described in further detail below in conjunction with the accompanying drawings.
附图说明Description of drawings
图1是本发明复合改性生物质固体成型燃料制备装置的结构示意图。Fig. 1 is a schematic structural diagram of a device for preparing composite modified biomass solid briquettes according to the present invention.
图2是本发明复合改性生物质固体成型燃料制备装置的俯视图。Fig. 2 is a top view of the device for preparing composite modified biomass solid briquettes of the present invention.
图3是本发明复合改性生物质固体成型燃料制备装置的左视图。Fig. 3 is a left view of the compound modified biomass solid briquette fuel preparation device of the present invention.
图4是本发明复合改性生物质固体成型燃料制备装置混合轴及桨叶的结构示意图。Fig. 4 is a structural schematic diagram of a mixing shaft and blades of a composite modified biomass solid briquette fuel preparation device of the present invention.
图5是本发明复合改性生物质固体成型燃料制备装置环模致密成型示意图。Fig. 5 is a schematic diagram of the dense molding of the ring die of the composite modified biomass solid briquette fuel preparation device of the present invention.
图6是本发明复合改性生物质固体成型燃料制备装置中环模成型装置采用立式放置方式的结构示意图。Fig. 6 is a schematic structural view of the vertical placement of the ring die molding device in the composite modified biomass solid molding fuel preparation device of the present invention.
具体实施方式Detailed ways
结合图1:Combined with Figure 1:
本发明一种复合改性生物质固体成型燃料制备装置,包括原料供应仓、粉料添加仓、液体原料添加仓、混合单元和致密成型单元;A compound modified biomass solid molding fuel preparation device of the present invention includes a raw material supply bin, a powder adding bin, a liquid raw material adding bin, a mixing unit and a dense molding unit;
原料供应仓和粉料添加仓的出料口位于混合单元入料口侧,并通过混合单元入料口与混合单元的混合腔连通,The outlets of the raw material supply bin and the powder addition bin are located on the side of the inlet of the mixing unit, and communicate with the mixing chamber of the mixing unit through the inlet of the mixing unit.
液体原料添加仓出料口与混合单元混合腔连通,The outlet of the liquid raw material adding bin is connected with the mixing chamber of the mixing unit,
致密成型单元位于混合单元出料口端,混合单元出料口与致密成型单元进料口相连;The compact forming unit is located at the discharge port of the mixing unit, and the discharge port of the mixing unit is connected to the feed port of the compact forming unit;
其中,原料仓送料螺旋1均布于原料仓螺旋轴2上,粉料添加仓螺旋3均布于粉料添加仓螺旋轴4上,混合螺旋5均布于位于混合单元出料口一端的混合螺旋轴6上,原料仓螺旋轴2、粉料添加仓螺旋轴4与混合螺旋轴6分别位于原料仓体7、粉料添加仓体8和混合单元混合腔的底部;加料驱动电机9通过原料仓传动链条10和粉料添加仓传动链条11分别同时驱动原料仓螺旋轴2和粉料添加仓螺旋轴4转动;混合桨叶均布于混合轴12上,混合轴12位于混合螺旋轴6正上方,混合驱动电机13通过混合轴驱动链条14和混合螺旋轴驱动链条15分别同时驱动混合轴12和混合螺旋轴6转动。Among them, the feeding screw 1 of the raw material bin is evenly distributed on the screw shaft 2 of the raw material bin, the screw 3 of the powder adding bin is evenly distributed on the screw shaft 4 of the powder adding bin, and the mixing screw 5 is evenly distributed on the mixing unit located at one end of the outlet of the mixing unit. On the screw shaft 6, the screw shaft 2 of the raw material bin, the screw shaft 4 of the powder adding bin and the mixing screw shaft 6 are respectively located at the bottom of the raw material bin body 7, the powder adding bin body 8 and the mixing chamber of the mixing unit; the feeding drive motor 9 passes through the raw material The bin transmission chain 10 and the powder addition bin transmission chain 11 simultaneously drive the raw material bin screw shaft 2 and the powder addition bin screw shaft 4 to rotate respectively; Above, the mixing drive motor 13 drives the mixing shaft 12 and the mixing screw shaft 6 to rotate simultaneously through the mixing shaft driving chain 14 and the mixing screw shaft driving chain 15 respectively.
混合桨叶包括混合大桨叶16和混合小桨叶17,混合大桨叶16和混合小桨叶17间隔均布在混合轴12上。The mixing paddles include large mixing paddles 16 and small mixing paddles 17 , and the large mixing paddles 16 and small mixing paddles 17 are uniformly distributed on the mixing shaft 12 at intervals.
混合大桨叶16的叶片与混合轴12的中心线呈70°~80°夹角。The blades of the large mixing paddles 16 form an included angle of 70° to 80° with the center line of the mixing shaft 12 .
加料驱动电机9上的加料驱动链轮18和粉料添加仓螺旋轴4上的粉料添加仓链轮19的组合减速比的范围为5~10。The combined reduction ratio of the feeding drive sprocket 18 on the feeding drive motor 9 and the powder adding bin sprocket 19 on the powder adding bin screw shaft 4 ranges from 5 to 10.
液体原料添加仓的液体添加仓仓体20通过输送管21与混合单元混合腔靠近混合单元入料口的一端连通,且输送管21上设置有阀门22和液体泵23。The liquid addition chamber body 20 of the liquid raw material addition chamber communicates with the end of the mixing chamber of the mixing unit close to the feed inlet of the mixing unit through the delivery pipe 21 , and the delivery pipe 21 is provided with a valve 22 and a liquid pump 23 .
致密成型单元中包括环模成型装置24、变速器25,成型驱动电机26和底座27,其中,环模成型装置24、变速器25、成型驱动电机26位于底座27上,环模成型装置24通过变速器25与成型驱动电机26的输出轴连接。The compact molding unit includes a ring molding device 24, a transmission 25, a forming drive motor 26 and a base 27, wherein the ring molding device 24, a transmission 25, and the forming drive motor 26 are located on the base 27, and the ring molding device 24 passes through the transmission 25 It is connected with the output shaft of the forming drive motor 26.
结合图1~图3:Combined with Figure 1 ~ Figure 3:
本发明的原料供应仓包括原料仓体7、原料仓螺旋轴2、原料仓送料螺旋1、加料驱动电机9和原料仓传动链条10,粉料添加仓包括粉料仓体8、粉料添加仓螺旋轴4、粉料添加仓螺旋3、粉料添加仓驱动链条11和粉料添加仓链轮19,混合单元包括混合大桨叶16、混合小桨叶17、混合轴12、混合螺旋轴6、混合螺旋5、混合驱动电机13、混合轴驱动链条14和混合螺旋轴驱动链条15,液体原料添加仓包括液体添加仓仓体20、液体泵23、阀门22和输送管21,致密成型单元包括环模成型装置24、变速器25、成型驱动电机26和底座27。The raw material supply bin of the present invention includes a raw material bin body 7, a raw material bin screw shaft 2, a raw material bin feeding screw 1, a feeding drive motor 9 and a raw material bin transmission chain 10, and the powder adding bin includes a powder feeding bin body 8, a powder adding bin Screw shaft 4, powder adding bin screw 3, powder adding bin drive chain 11 and powder adding bin sprocket 19, mixing unit includes mixing large paddle 16, mixing small paddle 17, mixing shaft 12, mixing screw shaft 6 , mixing screw 5, mixing drive motor 13, mixing shaft driving chain 14 and mixing screw shaft driving chain 15, the liquid raw material adding bin includes a liquid adding bin body 20, a liquid pump 23, a valve 22 and a delivery pipe 21, and the dense molding unit includes Ring molding device 24 , transmission 25 , molding drive motor 26 and base 27 .
具体实施过程为:将加料驱动链轮18和粉料添加仓链轮19调节至合适的减速比,通过加料驱动电机9带动原料仓螺旋轴2和粉料添加仓螺旋轴4转动,使生物质原料和添加粉料传输至混合单元内,然后与液体原料添加仓输送的添加原料在混合单元内均匀混合,再通过混合螺旋5输出至成型单元内成型为固体燃料。The specific implementation process is: adjust the feeding drive sprocket 18 and the powder adding bin sprocket 19 to a suitable reduction ratio, drive the raw material bin screw shaft 2 and the powder adding bin screw shaft 4 to rotate through the feeding driving motor 9, and make the biomass The raw material and the added powder are transferred to the mixing unit, and then uniformly mixed with the added raw material delivered by the liquid raw material adding chamber in the mixing unit, and then output to the molding unit through the mixing screw 5 to be formed into solid fuel.
图4为本发明复合改性生物质固体成型燃料制备装置混合大桨叶16结构及布置示意图。混合大桨叶16和混合小桨叶17均布于混合轴12上,混合大桨叶16的叶片与混合轴12的中心线呈70°~80°夹角,利用该角度可实现原料在混合单元内的混合和以一定的速度向出料口推送。Fig. 4 is a schematic diagram of the structure and layout of the large mixing paddle 16 of the composite modified biomass solid briquette fuel preparation device of the present invention. The large mixing paddles 16 and small mixing paddles 17 are evenly distributed on the mixing shaft 12. The blades of the large mixing paddles 16 form an included angle of 70°-80° with the center line of the mixing shaft 12. Using this angle, the raw materials can be mixed Mixing in the unit and pushing to the outlet at a certain speed.
图5为本发明复合改性生物质固体成型燃料制备装置成型示意图,成型原料送入成型单元后,填充与压辊轮与环模构成的成型腔内,随着压辊和环模的旋转,从模孔挤出特定成型密度的生物质固体燃料。Fig. 5 is a schematic diagram of the molding of the compound modified biomass solid molding fuel preparation device of the present invention. After the molding raw material is sent into the molding unit, it is filled in the molding cavity formed by the pressure roller and the ring mold. With the rotation of the pressure roller and the ring mold, Extrude biomass solid fuel with a specific molding density from the die hole.
实施例1Example 1
结合图1~图5:Combined with Figure 1 to Figure 5:
在该实施例中,以稻秸为原料,破碎至5mm以下,水热处理后烘干至含水率10%左右,输送至原料供应仓内;以淀粉为添加粉料,输送至粉料添加仓;以粗甘油为液体添加料,输送至液体原料添加仓。加料驱动链轮18和粉料添加仓链轮19组合减速比为9。驱动电机9通过原料仓传动链条10和粉料添加仓传动链条11带动原料仓螺旋轴2和粉料添加仓螺旋轴4转动,稻秸原料以一定速度送入混合单元,同时利用已设置的减速比实现淀粉添加料自动按比例添加。打开阀门22,同时液体泵23开始工作,通过输送管21将粗甘油以一定的速率添加至混合单元内。混合大桨叶16的叶片与混合轴12的中心线夹角为75°,混合驱动电机13开始工作,通过混合驱动链条14和混合螺旋轴驱动链条15带动混合轴12和混合螺旋轴6转动,稻秸原料、淀粉和粗甘油通过混合大桨叶16和混合小桨叶17在混合单元内充分混合,混合螺旋5再将混合后的原料输送至混合单元出口,然后进入成型单元内成型。致密成型单元的环模成型装置24为卧式放置。如需改变原料配比范围,调整液体泵23输出量以及驱动电机链轮18和粉料添加仓链轮19的组合减速比即可。In this embodiment, rice straw is used as the raw material, crushed to less than 5 mm, dried to a moisture content of about 10% after hydrothermal treatment, and transported to the raw material supply warehouse; starch is used as the added powder, and transported to the powder addition warehouse; The crude glycerin is used as the liquid additive, which is transported to the liquid raw material addition warehouse. Feeding driving sprocket 18 and powder material adding bin sprocket 19 combined reduction ratios are 9. The driving motor 9 drives the raw material bin screw shaft 2 and the powder adding bin screw shaft 4 to rotate through the raw material bin transmission chain 10 and the powder material addition bin transmission chain 11, and the rice straw raw material is sent into the mixing unit at a certain speed, and at the same time, the set deceleration is utilized. Ratio realizes the automatic addition of starch additives in proportion. The valve 22 is opened, and the liquid pump 23 starts to work at the same time, and the crude glycerol is added into the mixing unit at a certain rate through the delivery pipe 21 . The included angle between the blade of the mixing large paddle 16 and the center line of the mixing shaft 12 is 75°, the mixing drive motor 13 starts to work, and the mixing shaft 12 and the mixing screw shaft 6 are driven to rotate by the mixing drive chain 14 and the mixing screw shaft drive chain 15, The rice straw raw material, starch and crude glycerin are fully mixed in the mixing unit by mixing the large paddle 16 and the small mixing paddle 17, and the mixing screw 5 transports the mixed raw material to the outlet of the mixing unit, and then enters the molding unit for molding. The ring molding device 24 of the dense molding unit is placed horizontally. If it is necessary to change the proportioning range of raw materials, just adjust the output of the liquid pump 23 and the combined reduction ratio of the driving motor sprocket 18 and the powder adding bin sprocket 19 to get final product.
实施例2Example 2
结合图1~图5:Combined with Figure 1 to Figure 5:
在该实施例中,以锯末为原料,调制含水率10%左右,输送至原料供应仓内;以淀粉为添加粉料,输送至粉料添加仓;以石蜡液为液体添加料,输送至液体原料添加仓。In this embodiment, sawdust is used as the raw material, and the moisture content is prepared to be about 10%, which is transported to the raw material supply bin; starch is used as the powder to be added, and it is transported to the powder addition bin; Raw material addition bin.
加料驱动链轮18和粉料添加仓链轮19组合减速比为10。驱动电机9通过原料仓传动链条10和粉料添加仓传动链条11带动原料仓螺旋轴2和粉料添加仓螺旋轴4转动,锯末原料以一定速度送入混合单元,同时利用已设置的减速比实现淀粉添加料自动按比例添加。打开阀门22,同时液体泵23开始工作,通过输送管21将石蜡液以一定的速率添加至混合单元内。混合大桨叶16的叶片与混合轴12的中心线夹角为80°,混合驱动电机13开始工作,通过混合驱动链条14和混合螺旋轴驱动链条15带动混合轴12和混合螺旋轴6转动,锯末原料、淀粉和石蜡液通过混合大桨叶16和混合小桨叶17在混合单元内充分混合,混合螺旋5再将混合后的原料输送至混合单元出口,然后进入成型单元内成型。致密成型单元的环模成型装置24为卧式放置。如需改变原料配比范围,调整液体泵23输出量以及驱动电机链轮18和粉料添加仓链轮19的组合减速比即可。Feeding driving sprocket 18 and powder material adding bin sprocket 19 combined reduction ratio is 10. The driving motor 9 drives the screw shaft 2 of the raw material bin and the screw shaft 4 of the powder adding bin to rotate through the transmission chain 10 of the raw material bin and the transmission chain 11 of the powder addition bin. Realize the automatic addition of starch additives in proportion. The valve 22 is opened, and the liquid pump 23 starts to work at the same time, and the paraffin liquid is added into the mixing unit through the delivery pipe 21 at a certain rate. The included angle between the blade of the mixing large paddle 16 and the center line of the mixing shaft 12 is 80°, the mixing drive motor 13 starts to work, and the mixing shaft 12 and the mixing screw shaft 6 are driven to rotate by the mixing drive chain 14 and the mixing screw shaft drive chain 15, The sawdust raw material, starch and paraffin liquid are fully mixed in the mixing unit by mixing the large paddle 16 and the small mixing paddle 17, and the mixing screw 5 transports the mixed raw material to the outlet of the mixing unit, and then enters the molding unit for molding. The ring molding device 24 of the dense molding unit is placed horizontally. If it is necessary to change the proportioning range of raw materials, just adjust the output of the liquid pump 23 and the combined reduction ratio of the driving motor sprocket 18 and the powder adding bin sprocket 19 to get final product.
实施例3Example 3
结合图1~图6:Combined with Figure 1 to Figure 6:
在该实施例中,以稻秸为原料,破碎至5mm以下,烘焙处理后烘干至含水率10%左右,输送至原料供应仓内;以淀粉为添加粉料,输送至粉料添加仓;以废机油为液体添加料,输送至液体原料添加仓。加料驱动链轮18和粉料添加仓链轮19组合减速比为5。驱动电机9通过原料仓传动链条10和粉料添加仓传动链条11带动原料仓螺旋轴2和粉料添加仓螺旋轴4转动,稻秸原料以一定速度送入混合单元,同时利用已设置的减速比实现淀粉添加料自动按比例添加。打开阀门22,同时液体泵23开始工作,通过输送管21将废机油以一定的速率添加至混合单元内。混合大桨叶16的叶片与混合轴12的中心线夹角为70°,混合驱动电机13开始工作,通过混合驱动链条14和混合螺旋轴驱动链条15带动混合轴12和混合螺旋轴6转动,稻秸原料、淀粉和废机油过混合大桨叶16和混合小桨叶17在混合单元内充分混合,混合螺旋5再将混合后的原料输送至混合单元出口,然后进入成型单元内成型。如图6所示,致密成型单元的环模成型装置24为立式放置。如需改变原料配比范围,调整液体泵23输出量以及驱动电机链轮18和粉料添加仓链轮19的组合减速比即可。In this embodiment, rice straw is used as raw material, crushed to less than 5 mm, dried to a moisture content of about 10% after baking, and transported to the raw material supply warehouse; starch is used as the added powder, and transported to the powder added warehouse; The waste engine oil is used as the liquid additive, which is transported to the liquid raw material addition bin. Feeding driving sprocket 18 and powder material adding bin sprocket 19 combined reduction ratios are 5. The driving motor 9 drives the raw material bin screw shaft 2 and the powder adding bin screw shaft 4 to rotate through the raw material bin transmission chain 10 and the powder material addition bin transmission chain 11, and the rice straw raw material is sent into the mixing unit at a certain speed, and at the same time, the set deceleration is utilized. Ratio realizes the automatic addition of starch additives in proportion. Open the valve 22, and at the same time, the liquid pump 23 starts to work, and the waste engine oil is added into the mixing unit through the delivery pipe 21 at a certain rate. The included angle between the blade of the mixing large paddle 16 and the center line of the mixing shaft 12 is 70°, the mixing drive motor 13 starts to work, and the mixing drive chain 14 and the mixing screw shaft drive chain 15 drive the mixing shaft 12 and the mixing screw shaft 6 to rotate. The rice straw raw material, starch and waste engine oil are fully mixed in the mixing unit with the large paddle 16 and the mixing small paddle 17, and the mixing screw 5 transports the mixed raw material to the outlet of the mixing unit, and then enters the molding unit for molding. As shown in FIG. 6 , the ring molding device 24 of the dense molding unit is placed vertically. If it is necessary to change the proportioning range of raw materials, just adjust the output of the liquid pump 23 and the combined reduction ratio of the driving motor sprocket 18 and the powder adding bin sprocket 19 to get final product.
Claims (9)
- A kind of 1. compound modified biomass solid molding fuel preparation facilities, it is characterised in that:Add including raw material supply storehouse, powder Add storehouse, liquid charging stock addition storehouse, mixed cell and compact formed unit;The discharging opening in raw material supply storehouse and powder addition storehouse be located at mixed cell feeding mouth side, and by mixed cell feeding mouth and The hybrid chamber connection of mixed cell,Liquid charging stock addition bin discharge port external connects with mixed cell hybrid chamber,Compact formed unit is located at mixed cell discharge port end, and mixed cell discharging opening is connected with compact formed unit feed mouth;Wherein, raw material cabin feeding screw(1)It is distributed in raw material cabin helical axis(2)On, powder addition storehouse spiral(3)It is distributed in powder Add storehouse helical axis(4)On, mixing auger(5)It is distributed in the mixing auger axle positioned at mixed cell discharging opening one end(6)On, it is former Feed bin helical axis(2), powder addition storehouse helical axis(4)With mixing auger axle(6)It is located at raw material warehouse respectively(7), powder addition Warehouse(8)With the bottom of mixed cell hybrid chamber;Feed motor(9)Pass through raw material cabin driving chain(10)Added with powder Storehouse driving chain(11)Drive raw material cabin helical axis simultaneously respectively(2)Storehouse helical axis is added with powder(4)Rotate;Mixing paddle is equal It is distributed in mixing axle(12)On, mix axle(12)Positioned at mixing auger axle(6)Surface, hybrid drive motor(13)By mixing axle Drive chain(14)With mixing auger axle drive chain(15)Drive mixing axle simultaneously respectively(12)With mixing auger axle(6)Turn It is dynamic.
- 2. compound modified biomass solid molding fuel preparation facilities according to claim 1, it is characterised in that:It is described mixed Closing blade includes mixing big blade(16)With the small blade of mixing(17), mix big blade(16)With the small blade of mixing(17)Interval is equal Cloth is in mixing axle(12)On.
- 3. compound modified biomass solid molding fuel preparation facilities according to claim 2, it is characterised in that:It is described mixed Close big blade(16)Blade with mixing axle(12)Center line be in 70 °~80 ° angles.
- 4. the compound modified biomass solid molding fuel preparation facilities according to claim 1 or 2 or 3, it is characterised in that: The charging motor(9)On charging drive sprocket(18)Storehouse helical axis is added with powder(4)On powder addition storehouse chain Wheel(19)Combination speed reducing ratio scope be 5~10.
- 5. the compound modified biomass solid molding fuel preparation facilities according to claim 1 or 2 or 3, it is characterised in that: The liquid addition storehouse warehouse in the liquid charging stock addition storehouse(20)Pass through delivery pipe(21)With mixed cell hybrid chamber close to mixing One end connection of unit feeding mouth, and delivery pipe(21)On be provided with valve(22)And liquid pump(23).
- 6. compound modified biomass solid molding fuel preparation facilities according to claim 4, it is characterised in that:The liquid The liquid addition storehouse warehouse in body raw material addition storehouse(20)Pass through delivery pipe(21)Enter with mixed cell hybrid chamber close to mixed cell One end connection of material mouth, and delivery pipe(21)On be provided with valve(22)And liquid pump(23).
- 7. the compound modified biomass solid molding fuel preparation facilities according to claim 1 or 2 or 3 or 6, its feature exist In:The compact formed unit includes ring moulds shaped device(24), speed changer(25), it is molded motor(26)And base (27), wherein, ring moulds shaped device(24), speed changer(25), shaping motor(26)Positioned at base(27)On, ring moulds shaping Device(24)Pass through speed changer(25)With being molded motor(26)Output axis connection.
- 8. compound modified biomass solid molding fuel preparation facilities according to claim 4, it is characterised in that:The cause Close forming unit includes ring moulds shaped device(24), speed changer(25), it is molded motor(26)And base(27), wherein, Ring moulds shaped device(24), speed changer(25), shaping motor(26)Positioned at base(27)On, ring moulds shaped device(24)It is logical Cross speed changer(25)With being molded motor(26)Output axis connection.
- 9. compound modified biomass solid molding fuel preparation facilities according to claim 5, it is characterised in that:The cause Close forming unit includes ring moulds shaped device(24), speed changer(25), it is molded motor(26)And base(27), wherein, Ring moulds shaped device(24), speed changer(25), shaping motor(26)Positioned at base(27)On, ring moulds shaped device(24)It is logical Cross speed changer(25)With being molded motor(26)Output axis connection.
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