Chapter 3Rice Threshing and Separation Method The threshing unit is a key device of combine harvester,which determines the working performance of the other devices. Straw characteristics of movement in the threshing process are an important way to improve threshing performance of combine harvester. The thorough investigation of both grain threshing and grain separating processes is also a crucial consideration for effective structural design and variable optimization of threshing unit. 3ª±1Threshing and Separate Model of Rice Grain Three types of threshing and separation units have reached common use over the last century of innovation and development of combine harvesters within the agricultural industry. The first is a single or multiple transverselyª²arranged threshing cylinder unit. The second is a single or multiple vertically arranged threshing cylinder unit. The third type is the combined structure of transverselyª²arranged threshing cylinders and vertical arranged threshing cylinders. The combined threshing and separation structure of single transverselyª²arranged threshing cylinders and single verticallyª²arranged threshing cylinders was proven suitable for Asian small combine harvesters,due to its simple structure,small size,and flexibility. As of now,the combined threshing and separation structure of single transverselyª²arranged threshing cylinders and single verticallyª²arranged threshing cylinders is the primary mechanical structure of combine harvesters in the Asian region. In this book,we attempt to deduce and develop theoretical models of the threshing and separation process of both tangential or longitudinal flow threshing cylinder for the threshing teeth of a knife bar,trapezoidal tooth,spike tooth,rasp bar and rectangular bar. The main structure of the rice crawler combine harvester used is as shown in Figure 3ª±1. Figure 3ª±1Rice crawler combine harvester 1ª²reel cutting table£» 2ª²control panel£» 3ª²feeder conveyor£» 4ª²tangential flow threshing cylinder (TFC unit)£» 5ª²vibrating and cleaning sieve£» 6ª²longitudinal axial flow threshing cylinder (LFC unit)£» 7ª²transmission£» 8ª²engine£» 9ª²crawler chassis There are two main categories of threshing and separation models£º regression models,which do not describe the threshing and separation process but instead summarize and build statistics of test results£» and theoretical models,which create assumptions and simplifications of the threshing and separation process,based on a theoretical basis of the threshing and separation mechanism. Regression models are more easily determined,as they are only applicable to specific test apparatus. Theoretical models,conversely,can be used to design several threshing and separation units,but these theoretical models are very rare. Also,though widely accepted,some theoretical models are not completely correct. Rice crawler combine harvester was typical in structure,consisting primarily of a reel cutting table,control panel,feeder conveyor,tangential flow threshing cylinder,vibrating and cleaning sieve,longitudinal axial flow threshing cylinder,transmission,engine,and crawler chassis. The TFC unit was laid out horizontally,perpendicular to the longitudinal axial forward direction of the combine harvester. The LFC unit had a longitudinal axial layout,parallel to the longitudinal axial forward direction of the combine harvester. The axis of the LFC unit corresponded to the crossª²section centerline of the TFC unit. The main structure of the TLFC unit is as shown in Figure 3ª±2. Figure 3ª±2Combined transverse and axial flow threshing unit 1ª²TFC unit£» 2ª²tangential flow threshing tooth£» 3ª²spiral feed head£» 4ª²longitudinal axial flow threshing tooth£» 5ª²LFC unit The diameter of the TFC unit was 490 mm and its length was 1125 mm. The threshing teeth were arranged in a four head spiral,and bar spacing between any two adjacent threshing bars was 55 mm. The height of the threshing tooth was 70 mm. The concave clearance at the entrance was 40 mm and 30 mm at the output concave clearance. The speed of the TFC unit was set to 24ª±47 m¡¤s-1. There were four kinds of tangential threshing tooth£º the knife bar,rectangular bar,spike tooth,and rasp bar. The four threshing teeth on the TFC unit are as shown in Figure 3ª±3. Figure 3ª±3Structural diagram of four threshing tooth TFC unit (a) Spike tooth£» (b) Knife bar£» (c) Rectangular bar£» (d) Rasp bar There were four kinds of LFC unit threshing tooth£º the trapezoidal tooth,rectangular bar,spike tooth,and rasp bar. The spike tooth on the LFC unit is as shown in Figure 3ª±4. Figure 3ª±4Schematic diagram of LFC unit and threshing and separation cell (a) Spike tooth LFC unit£» (b) Threshing and separation cell The diameter of the LFC unit was 500 mm,and its total length was 3390 mm. There were helical blades of 170 mm in length in front of the LFC unit,2740 mm trapezoidal teeth within its center,and a discharge plate of 480 mm in length at the rear of the unit. The coordinate origin (the starting point of grain separation) was a point of 960 mm from the top of the unit. The concave clearance of the LFC unit was 30 mm,and the concave wrap angle was 180¡ã. Six lines of threshing bars were evenly arranged on the circumference of the LFC unit,and the space between any two adjacent threshing bars was 150 mm. The LFC unit speed was 21ª±95 m/s. 3ª±1ª±1Grain threshing and separation model The threshing and separation method described in this chapter was validated through a series of experiments,for the TFC unit and LFC unit both. In the threshing unit that consisted of threshing cylinder,grid concave and cylinder cover,the grains were removed from the ears and separated,for the most part,through the grid concave and into the grain box. To model the grain threshing and separation process as Peter I. Miu£Û9ª²13£Ý,the following general assumptions were taken into consideration£º (a)the material throughput is constant,where material moves through the threshing space as a continuous stream£» (b)the material to be processed is homogeneous,i.e.,the ears are uniformly distributed within the straw mass£» (c)in the TFC unit,the material is homogeneous in any crossª²section (perpendicular to the longitudinal axis direction) of the threshing space£» (d)in the LFC unit,the material is homogeneous in any cross section of the threshing space£» (e)the mass of the material is continuously distributed throughout the threshing space and its volumetric density is a continuous function of position and time. (1) Tangential flow threshing cylinder Based on these assumptions,the grain threshing and separation of the TFC unit was as dydl=k(1-y) (3ª±1) dzdl=u(y-z) (3ª±2) where y is the rate of accumulative threshed grain£» z is the rate of accumulative separated grain£» l is the arc length of the grid concave. Coefficients k (primary threshing coefficient) and u (primary separation coefficient) were affected by the material properties,structural variables,and operating variables of the threshing unit. When the rice is at the entrance of the TFC unit,l=0. Assuming the threshed grain=0,the y is also zero. Thus,Equation (3ª±1) can be solved as y=1-e-kl (3ª±3) When the rice is at the entrance of the TFC unit,l=0. Assuming the separated grain=0,the z is also zero. Thus,according to Equation (3ª±3),Equation (3ª±2) can be solved as dzdl+uz= u(1-e-kl) (3ª±4) Equation (3ª±4) is a nonª²homogeneous linear equation. In order to obtain the general solution of Equation (3ª±4),both a general answer of a homogeneous version of Equation (3ª±4) and a particular answer of a nonª²homogenous version must be solved. The homogeneous equation of Equation (3ª±4) is as dzdl+uz=0 (3ª±5) The solution to the homogeneous equation of Equation (3ª±4) is obtained by z=C(l)e-ul (3ª±6) where C(l) is the function of the arc length of grid concave l. In order to express C(l),Equation (3ª±6) must be solved first£º dzdl=C¡ä(l) e-ul-uC(l) e-ul (3ª±7) By substituting Equation (3ª±7) and Equation (3ª±6) for Equation (3ª±4),Equation (3ª±4) can then be solved. C¡ä(l)= ueul- ue(u-k)l (3ª±8) Equation (3ª±8) is as follows£º C(l)=eul-uu-ke(u-k)l+C0(3ª±9) where C0 is a coefficient. Both the general and particular versions of Equation (3ª±4) combined can be written as z=e-uleul-uu-ke(u-k)l+C0(3ª±10) When the rice is at the entrance of the TFC unit,l=0. Assuming that the separated grain was zero,z=0. So,Equation (3ª±10) could be solved as z=1+uk-ue-kl-kk-ue-ul(3ª±11) According to Equation (3ª±1) and Equation (3ª±2),Equation (3ª±4) can be expressed as dzdl=u(1-e-kl-z)(3ª±12) Equation (3ª±12) is then written as dzdl(1-z)=u1-e-kl1-z=¦Ì-u1-ze-kl (3ª±13) Because the rate of accumulative threshed grain y is greater than the rate of accumulative separated grain z,k is far greater than l. When the arc length of the grid concave l is over 300 mm,e-kl¡Ö0 and could be ignored. According to Equation (3ª±11) and Equation (3ª±12),the separated experimental coefficients u can be written as u=-ln(1-z)l (3ª±14) The threshed experimental coefficients k is provided by Equation (3ª±15). k=1+uzz+e-ul (3ª±15) If ddl dzdl=0 ,then dzdl is the maximum. Based on Equation (3ª±12),the minimum arc length of grid concave lm is expressed. lm=lnkuk-u (3ª±16) When the difference between the rate of threshed grain y and the rate of separated grain z was at its maximum,the differential result of dz/dl was maximum,and lm was the minimum arc length. When llm,the threshed rate capacity was much lower than the separated rate capacity,and the result of (y-z) shrank. The threshing and separating capability of the TFC unit was then stable and reliable£Û14£Ý. (2) Longitudinal flow threshing cylinder The straw was threshed and separated preliminarily by the TFC unit. Next,the straw was transported to the LFC unit so as to be threshed and separated again. The mixture in the LFC unit contained both unª²threshed grain (sj) and unª²separated grain (si). The total grain rate in the LFC unit is then qj,described as£º qj=si+sj (3ª±17) Assuming that ¦Äx is an arbitrary infinitely small distance,which is one point of the LFC,¦Ë is the reª²threshed coefficient,and ¦Â is the reª²separated coefficient£» i and j are natural numbers (i=0,1,2,3£¬¡­£» j=1,2,3,¡­). Threshed grain probability density f(x) is described as f(x)£Û1-F(x)£Ý=¦Ë (3ª±18) where x is one point of the LFC,and F(x) is the cumulative total rate of threshed grain through the concave grid. Equation (3ª±18) is then written as F(x)=¡Òx0f(¦Æ)d¦Æ(3ª±19) where ¦Æ is a variable. Equation (3ª±18) and Equation (3ª±19) can be merged into£º dF(x)1-F(x)=¦Ëdx(3ª±20) The cumulative total rate of threshed grain from the concave grid of the LFC is F(x)=1-e-¦Ëx(3ª±21) Threshed grain probability density is expressed as f(x)=sj¦Ëe-¦Ëx(3ª±22) Similarly,the separated grain probability density is expressed as g(x)=¦Âe-¦Âx(3ª±23) The total rate of unª²threshed grain can be described sn(x)=sj1-¡Òx0¦Ëe-¦Ë¦Æd¦Æ=sje-¦Ëx (3ª±24) where x=L ,and L is the effective threshing and separation length of the LFC unit. Thus,the unª²threshed grain discharged from the tail hole of the LFC unit is considered as lost grain. The unª²threshed grain rate Sn(L) is expressed as sn(L)=sje-¦ËL(3ª±25) According to probability theory,independent constant random variables with the densities f(x) and sn(x) for sum variables convolute Equation (3ª±26) with these density functions h¡ä(x)£º h¡ä(x)=f(¦Î)g(x-¦Î)=¡Òx0f(x)g(x-¦Î)d¦Î(3ª±26) where ¦Î is a variable. Based on Equation (3ª±26),Equation (3ª±27) is written as h¡ä(x)=¦Ë¦Â¦Ë-¦Â(e-¦Âx-e-¦Ëx)(3ª±27) The grain separation probability density h(x) is expressed as h(x)=sjh¡ä(x)+sig(x)=sj¦Ë¦Â¦Ë-¦Â(e-¦Âx-e-¦Ëx)+si¦Âe-¦Âx (3ª±28) The rate of cumulative separated grain through the LFC unit¬ðs concave grid is writtenas H(x)=sj¦Âe-¦Ëx-¦Ëe-¦Âx¦Ë-¦Â+sj+si(1-e-¦Âx) (3ª±29) In every crossª²section of the LFC unit at a current position x of the threshing length,the mass balance for grain can be obtained£º H(x)+sn(x)+sf(x)=qj(3ª±30) To this effect,the total rate of unª²separated grain in the LFC unit is obtained£º sf(x)=qj-Hj(x)-sn(x)(3ª±31) where x=L ,and the unª²separated grain discharged from the tail hole of the LFC unit is lost grain. The unª²separated grain rate of the LFC unit is expressed as sf(L)=sie-¦ÂL-sje-¦ËL+¦Âe-¦ËL-¦Ëe-¦ÂL¦Ë-¦Â (3ª±32) 3ª±1ª±2Threshing and separation test of model The separated grain z measured using the four different types of tangential flow threshing teeth (knife bar,rectangular bar,spike tooth and rasp bar) are shown in Table 3ª±1ª± Table 3ª±1Coefficients and parameters of primary threshing and separation using different threshing teeth Serial numberCoefficients and parameters Threshing teeth of TFC unit Spike toothKnife barRectangular barRasp bar 1Arc length of grid concave l/mm676ª±67676ª±67676ª±67676ª±67 2Rate of accumulative separation grain z/%44ª±7647ª±7141ª±4146ª±32 3Rate of accumulative threshing grain y/%85ª±0487ª±0482ª±3386ª±14 4Primary separation coefficient u/m-11ª±831ª±921ª±741ª±88 5Primary threshing coefficient k/m-12ª±813ª±022ª±562ª±92 6Minimum arc length lm/mm437ª±74411ª±94470ª±34423ª±78 Based on the rate of cumulative threshed grain y and separated grain z,primary separated coefficient u,and primary threshing coefficient k can be calculated by Equation (3ª±14) and Equation (3ª±15),respectively. The rate of cumulative threshed grain y can also be obtained by Equation (3ª±3). The minimum arc length of grid concave lm can be determined by Equation (3ª±16). All the calculation results are shown in Table 3ª±1. In the TFC unit,y and z were a function of l. Assuming that k=2,2ª±5,3,3ª±5,and 4 m-1 (these scopes represent the test values),u=1,1ª±5,2,2ª±5,and 3 m-1 (again,because these scopes were test values),y and z were calculated. The results are shown in Table 3ª±2. Table 3ª±2The primary threshed coefficient k,primary separated coefficient u,cumulative threshed grain rate y,and cumulative separated grain rate z No.k/m-1y/%u/m-1z/% 1274ª±16124ª±18 22ª±581ª±581ª±537ª±03 3386ª±87248ª±75 43ª±590ª±642ª±558ª±94 5493ª±32367ª±49 6386ª±87130ª±32 7386ª±871ª±540ª±65 8386ª±87248ª±75 9386ª±872ª±555ª±14 10386ª±873ª±161ª±09 11274ª±16240ª±35 122ª±581ª±58244ª±50 13386ª±87248ª±75 143ª±590ª±64252ª±20 15493ª±32255ª±00 The rate of accumulative threshed grain y and the rate of accumulative separated grain z were then drawn using MATLAB software. The results are shown in Figure 3ª±5. Figure 3ª±5Cumulative threshing and separating rates of the TFC unit with different threshing bars (a) Cumulative threshing rate£» (b) Cumulative separating rates The rice straw was first threshed and separated preliminarily by the TFC unit. Next,the straw with grain was moved to the LFC unit so as to be threshed and separated again. The unª²threshed grains needed to be reª²threshed,and the unª²separated grain and threshed grain needed to be reª²separated. The knife bar was used in the TFC unit. The trapezoidal tooth,rectangular bar,spike tooth,and rasp bar were installed,respectively,in the LFC unit to perform the threshing and separation tests. The separated grains from the LFC unit were divided into 13 parts,perpendicular to the axial direction. The percentage of the total grain in every part,the unª²threshed grain rate,and the unª²separated grain rate were measured for the four longitudinal axial flow threshing teeth. All the test results are shown in Table 3ª±3. Table 3ª±3Accumulative separation grain percentages. means¡Àstandard errors under LFC unit Packet sequence numberRectangular barRasp barSpike toothTrapezoidal tooth 16ª±19¡À0ª±384ª±81¡À0ª±324ª±67¡À0ª±295ª±40¡À0ª±28 29ª±91¡À0ª±8713ª±21¡À0ª±6714ª±55¡À0ª±6210ª±66¡À0ª±74 311ª±42¡À1ª±4511ª±29¡À1ª±2312ª±75¡À1ª±0614ª±01¡À1ª±36 46ª±59¡À0ª±325ª±51¡À0ª±325ª±81¡À0ª±296ª±56¡À0ª±27 55ª±51¡À0ª±274ª±67¡À0ª±235ª±13¡À0ª±225ª±46¡À0ª±28 63ª±40¡À0ª±242ª±87¡À0ª±263ª±10¡À0ª±233ª±22¡À0ª±19 72ª±40¡À0ª±232ª±04¡À0ª±171ª±90¡À0ª±132ª±34¡À0ª±26 81ª±94¡À0ª±212ª±28¡À0ª±231ª±33¡À0ª±221ª±34¡À0ª±22 91ª±50¡À0ª±171ª±57¡À0ª±160ª±86¡À0ª±181ª±10¡À0ª±23 101ª±13¡À0ª±161ª±14¡À0ª±160ª±72¡À0ª±120ª±63¡À0ª±18 110ª±91¡À0ª±090ª±77¡À0ª±090ª±58¡À0ª±070ª±43¡À0ª±12 120ª±66¡À0ª±040ª±62¡À0ª±030ª±28¡À0ª±040ª±32¡À0ª±02 130ª±19¡À0ª±010ª±47¡À0ª±040ª±16¡À0ª±040ª±22¡À0ª±02 Unª²separated rate/%0ª±46¡À0ª±040ª±91¡À0ª±050ª±44¡À0ª±040ª±58¡À0ª±03 Unª²threshed rate/%0ª±08¡À0ª±010ª±14¡À0ª±010ª±02¡À0ª±010ª±04¡À0ª±01 The reª²threshing coefficient ¦Ë was then obtained by Equation (3ª±22),and the reseparation coefficient ¦Â could be obtained by Equation (3ª±23). The results are as shown in Table 3ª±4. Table 3ª±4Threshing and separation coefficient of LFC unit ParametersRectangular barRasp barSpike toothTrapezoidal tooth Unª²threshed grain rate/%0ª±080ª±140ª±020ª±04 Unª²separated grain rate/%0ª±460ª±910ª±440ª±58 Rethreshing coefficient ¦Ë/m-12ª±592ª±313ª±312ª±95 Reseparation coefficient ¦Â/m-12ª±872ª±432ª±712ª±60 The threshing probability density equation f(x) of the LFC unit and separation probability density equation h(x) of the LFC unit were drawn using MATLAB. The results are shown in Figure 3ª±6. Figure 3ª±6Grain threshing and separation probabilities density curves of the LFC unit (a) Cumulative threshing rate£» (b) Cumulative separating rates The accumulative threshed grain rate (y) and the accumulative separated grain rate (z) increased with increasing the arc length of the grid concave. The threshing and separation capacity of the knife bar in the TFC unit was stronger than other threshing teeth. The maximum primary threshing rate of the knife bar is 87ª±04%£¬and the maximum primary separation rate is 47ª±71%. In order to ensure that the separation capacity is stronger than the threshing capacity of the knife bar,the minimum arc length of the grid concave screen was set to 411ª±90 mm. After being primarily threshed and separated by the TFC unit,the unª²threshed rate was 12ª±60%,and the unª²separated grain rate was 39ª±33% at the entrance of the TFC unit. At a length of 0ª±96ª²1ª±31 m,the grain threshing probability density of the spike tooth used in the LFC unit was stronger than other threshing teeth. At a length of 1ª±48ª²2ª±91 m,the grain separation probability density of the trapezoidal tooth used in the LFC unit was stronger than other threshing teeth. 3ª±2Rice Stalk Movement during Rice Threshing 3ª±2ª±1Numerical model of threshing unit In order to present the movement parameters of the rice straw which was threshed by combine harvester£¬the threshing unit model was modeled by Pro/E software with the scale of 1¡Ã1,and then the process of threshing was simulated on EDEM software. The relationship of movement velocity and trajectory with the simulation time can be obtained by EDEM,which also can be verified by the experimental result. Straw movement condition in threshing unit is very complicated£Û15£Ý. The threshing device of tangential and axial threshing unit in a combine harvester mainly includes the tangential threshing unit,the auxiliary feeding unit and the axial threshing unit. The tangential and axial threshing unit solid modeling of a combine