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帶直揚(yáng)料板回轉(zhuǎn)筒內(nèi)秸稈碎料運(yùn)動與混合機(jī)理研究
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國家重點(diǎn)研發(fā)計劃項目(2017YFC0210303,、2016YFB0601305)


Movement and Mixing of Crushed Straw Material in Rotary Drum with Straight Plates
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    摘要:

    為研究揚(yáng)料板對實(shí)驗室級回轉(zhuǎn)筒內(nèi)秸稈碎料發(fā)酵熱均勻化速度的影響,需研究筒內(nèi)二元秸稈碎料顆粒的混合速度,。基于圖像分析,,建立了研究二元秸稈碎料顆?;旌隙菼mix及完全混合時間Tc的方法,并用Visual Studio編寫了分析軟件,。依據(jù)實(shí)驗室級回轉(zhuǎn)筒設(shè)計實(shí)驗臺,,采用完全實(shí)驗、分析軟件和正交分析法,,研究了直揚(yáng)料板對Tc的影響,。結(jié)果表明:對實(shí)驗室級回轉(zhuǎn)筒而言,在對Tc的影響上,,板長大于板數(shù),,兩者數(shù)量級相同,均表現(xiàn)顯著,,并相互耦合,;宏觀效應(yīng)曲線上,Tc隨板長增加類余弦函數(shù)規(guī)律變化,,隨板數(shù)增加類指數(shù)函數(shù)規(guī)律變化,;Tc向“單+長板”和“多+中長板”兩級化降低,向“多+短板”和“多+長板”兩級化升高,,4塊板55%筒體半徑長度揚(yáng)料板情況下混合最快,。不當(dāng)?shù)膿P(yáng)料板選擇,反而會降低筒內(nèi)料發(fā)酵熱的均勻化速度,,選用揚(yáng)料板時,,應(yīng)采用“多+中長板”方案。最后,,基于攝像結(jié)果分析了顆粒的運(yùn)動模式,、揚(yáng)料板的作用過程、揚(yáng)料板作用下的物料混合機(jī)理,,歸納總結(jié)了不同長度/數(shù)量的揚(yáng)料板作用下的顆粒運(yùn)動模式,,完成實(shí)驗室級回轉(zhuǎn)筒內(nèi)物料運(yùn)動模式的分解、定性研究,。對于工業(yè)級回轉(zhuǎn)筒,,可參考本文所提出方法進(jìn)行實(shí)驗研究。

    Abstract:

    Annual production of straw is 600 to 800 million tons in China.Dr.LI Shizhong solid-state fermented crushed straw material to acquire ethanol.However, the fermentation heat in bed often over accumulate and kill the yeast,as crushed straw material has low heat conductivity.Dr.Li use rotary drum with straight plates as fermentation drum to solve the problem. The length of plates and the number of plateshasgreat influence on movementand mixing of crushed straw material. However, there is less study in this area. In order to study the influence, section test platform was designed referred to laboratory level rotary drum. The drum can connect 1/2/4 plates andthe length of plates can adjust to 15%/35%/55%/75% ratio of drum (R). The material filling ratio and rotary speed is the same as laboratory level rotary drum: 50%, 1r/min. Some of the material was colored black while the other remains uncolored. They are laid in drum orderly to form acolored and an uncolored material layer.The two layers will mix with drum rotation, and the bed section color will change at the same time. Therefore, the section color can measure the mixing degree of colored and uncolored material. The faster the section color turn uniform grey, the faster thematerial totally mixed. The faster the material totally mixed, the greater the promoting effect of plates on averaging bed’s fermentation heat.The method to measure mixing degree was built based on image analysis, as shown in figure 2.Mesh the bit-mapped picture and calculate the number of uncolored material grids (N0) and all material grids (N) as the black pixeldensity interval between them are different. The quotient (Imix) of N0 divided by N is dimension less and will turn to 0 from 0.5 along with mixing and can mark the mixing degree. The time Imix- time fitting line turn 0 is the complete mixing time of colored and uncolored material (Tc).Data analysis resultshows that: Imix is the most accurate in the case of grid size 8mm;black pixel density [0.1,0.7] marks the uncolored material grid, [0.1,1] marksall material grid. The software to calculate Imix was programmed with Visual Studio. Thirteen section-mixing tests were done: 1/2/4 plate(s) with length 15%/35%/55%/75% ratio of drum.The control group is 0 plate. Each test were done 5 times to obtained the average Tc.The results show that: (1)The length of plates has greater influence on Tc than the number of plates, they are in the same order of magnitude and have strong coupling effects. (2) Tc is the smallest under influence of 4×0.55R plates. (3) Synthetically, Tc change like cos function along with longer plates, change like exponential function along with more plates. (4) Tcdecrease under influence of single long plate or multi middle-length plates, increase under influence of multishort plates or multilong plates. The movement modes of material were studied. From 0 to 4 plates, 0.15R to 0.75R, there is no one unique mode for every test condition. All the movement modes,the influence of plates on mixing and the mixing mechanismhave been analyzed and classified which is shown in table 2.The research can guide designing of plates of laboratory level rotary drums. It can also deepen the understanding of complex movement of crushed straw material in rotary drum with plates. However, for industrial level rotary drums, the conclusions above can not be used uncritically as the drums become much bigger. Tests need to be done on industrial level drums with methods above to acquire conclusions of bigger drums.Furthermore, two important conclusionsfor any kind of mixing process were put forward.(1)There are only two ways to mix material A and B. The first way is to let material group that totally comprised of Aleaves Amaterial layer and embed in B material layer. The second way is to break and mix material group which contains both material A and B. The first can happen in any part of the material bed, while the second can only happen in interface of material A and B. (2) If there is no permanently blocking area, the more material falling areas the material bed has, the faster the colored and uncolored material mix.

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周敬之,馮俊小,周知星,李十中.帶直揚(yáng)料板回轉(zhuǎn)筒內(nèi)秸稈碎料運(yùn)動與混合機(jī)理研究[J].農(nóng)業(yè)機(jī)械學(xué)報,2017,48(12):86-97. ZHOU Jingzhi, FENG Junxiao, ZHOU Zhixing, LI Shizhong. Movement and Mixing of Crushed Straw Material in Rotary Drum with Straight Plates[J]. Transactions of the Chinese Society for Agricultural Machinery,2017,48(12):86-97.

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  • 收稿日期:2017-03-30
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  • 在線發(fā)布日期: 2017-12-10
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