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Article Optimal Cooling System Design for Increasing the Growth Rate of Single-Crystal in the Czochralski Process Using the Simulation

Hye Jun Jeon , Hyeonwook Park, Ganesh Koyyada, Salh Alhammadi and Jae Hak Jung * Chemical Engineering Department, Yeungnam University, Gyeongsan 38541, Korea; [email protected] (H.J.J.); [email protected] (H.P.); [email protected] (G.K.); [email protected] (S.A.) * Correspondence: [email protected]; Tel.: +82-053-810-3513

 Received: 17 July 2020; Accepted: 28 August 2020; Published: 1 September 2020 

Abstract: Here, we report a successfully modified Czochralski process system by introducing the cooling system and subsequent examination of the results using crystal growth simulation analysis. Two types of cooling system models have been designed, i.e., long type and double type cooling design (LTCD and DTCD) and their production quality of was compared with that of the basic type cooling design (BTCD) system. The designed cooling system improved the uniformity of the temperature gradient in the crystal and resulted in the significant decrease of the thermal stress. Moreover, the silicon monocrystalline ingot growth rate has been enhanced to 18% by using BTCD system. The detailed simulation results have been discussed in the manuscript. The present research demonstrates that the proposed cooling system would stand as a promising technique to be applied in CZ-Si crystal growth with a large size/high pulling rate.

Keywords: silicon; cooling system design; pulling speed; crystal growth rate; Czochralski process; crystal growth simulation

1. Introduction Most single crystal silicon ingots are grown using the Czochralski process. In this process, monocrystalline silicon is manufactured by contacting a silicon from molten silicon and pulling it out slowly using a pulling system with crucible rotation [1]. The uptime of the Czochralski process is quite long and expensive. Therefore, the current industry aims to increase productivity and economic efficiency by increasing the speed of crystal growth. To improve productivity, it is necessary to reach a high crystal growth rate, but it is difficult to maintain the quality of the silicon crystal at a high crystal growth rate from a predetermined process. Furthermore, the twisting phenomenon of the crystal has limited attempts to achieve a high crystal growth rate in a given hot zone. A higher crystal growth rate than the given value can result in a distortion of the lattice inside the crystal, which causes dislocations and deteriorates the crystal quality [2–5]. Therefore, our research proposes an implementation plan to improve the growth rate of the crystal as well as internally improve the chamber. The entire process of the proceeds in the following order: dipping, necking, shouldering, body growth, and tailing. To grow high-quality silicon ingots, certain variables and von Mises stress must be considered. Moreover, the crystal defect area V/G (crystal growth rate (V)/temperature gradient (G) of the silicon melt–crystal interface region) must be considered [6,7]. The crystal growth rate must be able to pull faster while maintaining quality from the crystal’s internal temperature gradient and the free defect area of the melt–crystal interface. Improving the pulling speed of a single crystal silicon ingot will need to consider structural improvements. CG-Sim software

Processes 2020, 8, 1077; doi:10.3390/pr8091077 www.mdpi.com/journal/processes Processes 2020, 8, 1077 2 of 13 is a simulation software for growing single and polycrystals from a melt of . The software is used to achieve the optimal design, process conditions, and crystal quality improvement through heat transfer, temperature analysis, as well as gas and melt convection analysis of the crystal defects and stress calculations. The mathematical modeling represents the equations for the convection of gas flow and fluid in Czochralski furnace and the heat transfer phenomena through hot zone [8].

2. Mathematical Modeling and Experiment The Czochralski process structure is shown in Figure1. We obtained cooling system using the Crystal Growth Simulation. The geometry of the Czochralski growth system is symmetrical in the axial direction, but the nature of the growing crystal is isotropic. Therefore, it is not easy to achieve full axial symmetry since it is too complicated to match the central axis of the triple point in the growth process. Therefore, this study assumes axial symmetry by reducing the asymmetrical pattern using rotation. The Czochralski growth simulation utilizes two-dimensional cylindrical coordinates [9]. In the Czochralski process, studies on computational models, such as the Reynolds number (Re), Grashof number (Gr), and Prandtl number (Pr), have been conducted [10]. To analyze the temperature distribution and fluid flow of the Czochralski process, there are (1) continuous equations of differential equations, (2) momentum equations for each velocity component, and (3) energy equations. By assuming incompressible fluids and expressing them in tensor form in Cartesian coordinates, the explanation can be expressed as follows:

∂ρ + (ρu) = 0 (1) ∂t ∇· Du ρ = p + τ + ρg (2) Dt −∇ ∇· ∂e ρ + p( u) = (k T) + ϕ (3) ∂t ∇· ∇ ∇ where D , ρ, u, , p, and t are the convective derivative, the density, velocity, divergence, pressure, Dt ∇ and time, respectively. τ represents the deviatoric stress tensor, which has an order of two, while g is the gravitational acceleration acting on the continuum, ϕ is the viscous-dissipation function, and k is the thermal conductivity. For the dimensionless number, in this article, the rate of of silicon corresponds to heat flux, transition in crystals and melts from the following equation [11]:

 dT  dt  ρcrystal∆Hun = λ λ (4) dn melt − dn crystal where un is the average rate of partial crystallization at the melt–crystal interface, ∆H is the heat of crystallization of 1.8 106 (J/kg), and ρ is the solid silicon thermal conductivity at the melting × crystal point temperature 66.5 (W/km). The average crystallization rate υ was calculated by integrating the space S with uv representing the perpendicular crystallization rate to the partial crystallization rate un at the melt–crystal interface from following the equation: Z 1 υ = u ds (5) s v Flow due to surface tension occurs in the direction of the low-temperature part at the high-temperature part where the surface tension is small, i.e., flow occurs in the direction of the interface from the crucible wall. Therefore, flow caused by a difference in density and the flow direction due to a difference in surface tension are mutually synergistic. Hence, the overall flow occurs from the crucible to the interface at the surface portion and from the interface to the bottom at the center. Rotation of the crucible and crystal primarily produces circumferential flow. The dimensionless number that can indicate the effect of this rotation is the Reynolds number e for the rotation. If the speed of crystal and R Processes 2020, 8, 1077 3 of 13

crucible and the characteristic length are Ωx, Ωc, and h respectively, the Reynolds number for rotation is defined as follows: 2 Ωxh ex = (6) R v 2 Ωch ec = (7) Processes 2020, 8, x FOR PEER REVIEW R v 3 of 14

(a)

(b)

Figure 1. GeometryGeometry of of Czochralski Czochralski process process ( (aa),), basic basic process process of of cooling system ( b) from CrystalCrystal Growth Simulation.

WhileThe average the shape crystallization of the flow in forcedrate v convectionwas calculated depends by on integrating Re, the shape the of space the flow S inwith natural 𝑢 convectionrepresenting depends the perpendicular on Gr, which crystallizatio representsn rate the ratioto the of partial the buoyant crystallization to viscous rate forces𝑢 at actingthe melt– on thecrystal fluid. interface from following the equation: gβ∆TR3 Buoyant force Gr = = (8) v2 1 Viscous force υ = 𝑢 ds (5) where R refers to the diameter. s Pr indicates the contribution of the momentum diffusivity relative to thermal diffusivity in layer flow.Flow Thermal due ditoff usivitysurface dominatestension occu whenrs in Pr the< 1, direction and momentum of the low-temperature diffusivity dominates part whenat the Prhigh-> 1. temperature part where the surface tension is small, i.e., flow occurs in the direction of the interface from the crucible wall. Therefore, flowv causedviscous by di aff differenceusion rate in densityCpµ and the flow direction due Pr = = = (9) to a difference in surface tension area mutuallythermal syne diffusionrgistic. rate Hence, kthe overall flow occurs from the crucible to the interface at the surface portion and from the interface to the bottom at the center. In the Czochralski process, single-crystal silicon crystal growth directly interacts with the flow Rotation of the crucible and crystal primarily produces circumferential flow. The dimensionless of dissolved silicon in crucible. The impurities and gases introduced into melt–crystal number that can indicate the effect of this rotation is the Reynolds number Re for the rotation. If the interfaces, heat transfer, molten silicon convection, and temperature gradient are important parameters, speed of crystal and crucible and the characteristic length are Ω , Ω , and h respectively, the and the crystal growth rates influences the temperature gradient inside the growth determination [12]. Reynolds number for rotation is defined as follows: At the equal temperature gradient, the high rate of crystalline growth resulted in high in vacancy defect Ωℎ ℛe = (6) 𝑣

Ωℎ ℛe = (7) 𝑣

While the shape of the flow in forced convection depends on Re, the shape of the flow in natural convection depends on Gr, which represents the ratio of the buoyant to viscous forces acting on the fluid.

Processes 2020, 8, 1077 4 of 13 with the melt–crystal interface in concave form, whereby the low rate of crystalline growth appeared in high interstitial defect in convex form. Therefore, it provides information to predict the number of defects in the crystal, as it helps to determine the shape of the melt–crystal interface depending on the growth rate of the crystal. The improving in the growth rate should be carried out by considering the quality of the appropriate crystal [13–17]. The numerical simulation used for this experiment was CG-Sim® (Crystal Growth Simulation) of the STR Group in St. Petersburg, Russia. CG-Sim is a crystal growth data that is a package that collects data from real processes and combines them into a single software. The efficiency of the process can be improved by comparison with actual data. The CG-Sim (melt) software can simulate the process of growing single crystals and multicrystals from the melt of a crystal and can produce different results depending on the internal structure, size of the crystal, and shape of the quartz crucible. The simulation was carried out considering the quality determination of the crystal grown Si-ingot according to the design of a new cooling system and the method to realize a high pulling rate. Table1 lists the properties of the main substances, including the thermal properties and emissivity. The unique properties of silicon, graphite as a cooling system pipes, inert gases, such as argon, quartz crucibles (silica) and iron (), carbon felt as a thermal insulator, and water as a cooling system, which all influence the growth of the crystals, are used [18–20].

Table 1. Properties of the material.

Materials Heat Capacity (J/kg) Heat Conductivity (W/m) Emissivity Si(crystal) 1000 75.22 0.7 Si(melt) 915 66.50 0.3 Graphite 720 105.26 0.7 Ar 521 3.06 – Quartz crucible 1232 4 0.85 Steel 438 15 0.45 Carbon felt – 0.02 0.9 Water 4200 0.6 0.5

3. Results and Discussions Initially, the crystal growth simulations (CG-Sim) were performed for basic model crystal design (BTCD) of the Czochralski process (CZ-process) for clear understanding of the parameters that affect single-crystal production yield. Figure2 describes the thermal gradient in the CZ-process with di fferent crystal position (CP) heights. The growth rate and defects of the single-crystal silicon ingot were studied using CG-Sim analysis at various crystal position heights with a pulling speed of 1.0 mm/min. Figure3 illustrates the V/G ratio, von Mises stress, and power consumption with different CP heights at various crystal lengths at 1.0 mm/min of fixed pulling speed in CZ-process. The corresponding results are listed in Table2. von Mises stress has been considered as an e ffective or equivalent stress. When an object is subjected to a force or moment from outside, it would tolerate that force to some extent, but if it is beyond certain size, it would no longer support the external force, hence gets destroyed. The condition that predicts such destruction is termed as “yield criterion.” The yield criterion is a value that indicates the maximum distortion energy at each point of an object under stress. It is based on various failure theories, but the maximum distortion energy theory, which has been considered the most accurate, uses von Mises equivalent stress. Plasticity occurs when the calculated equivalent stress value is greater than the yield strength of the crystal. The simulation package of the Czochralski process would judge the stress based on the number of Re, Gr, and Pr. The amount of change in stress increased slightly from CP400 to CP800 and decreased rapidly with increasing crystal height. When the stress was high, the uniformity of the temperature gradient difference based on the diameter of the crystal was exceeded. The results suggest an increase in the crystal length and the stress in the crystal has decreased with increased cooling effect [21–23]. It indicates that the increase of cooling time would improve the crystal quality. Generally, the stress at 30 MPa or less has not lead to stress defects in the crystal Processes 2020, 8, x FOR PEER REVIEW 5 of 14

CP heights at various crystal lengths at 1.0 mm/min of fixed pulling speed in CZ-process. The corresponding results are listed in Table 2. von Mises stress has been considered as an effective or equivalent stress. When an object is subjected to a force or moment from outside, it would tolerate that force to some extent, but if it is beyond certain size, it would no longer support the external force, hence gets destroyed. The condition that predicts such destruction is termed as “yield criterion.” The yield criterion is a value that indicates the maximum distortion energy at each point of an object under stress. It is based on various failure theories, but the maximum distortion energy theory, which has been considered the most accurate, uses von Mises equivalent stress. Plasticity occurs when the Processes 2020, 8, 1077 5 of 13 calculated equivalent stress value is greater than the yield strength of the crystal. The simulation package of the Czochralski process would judge the stress based on the number of Re, Gr, and Pr. growthThe amount [24]. However,of change thein stress silicon increased crystal growth slightly conditions from CP400 are definedto CP800 based and ondecreased the critical rapidly region with in whichincreasing the interstitial crystal height. region When is transformed the stress in was the vacancyhigh, the region. uniformity The V of/G the ratio temperature identified the gradient defect dominationdifference based area of on vacancy the diameter or interstitial of the ascrystal shown wa ins Equationexceeded. (10). The The results critical suggest V/G can an beincrease determined in the bycrystal concentration length and of vacancythe stress (Cv) in theconcentration crystal has decr of interstitialeased with (Ci) increased= 0. Vacancy cooling is agglomeratedeffect [21–23]. toIt − formindicates void, that Oxidation the increase Induced of cooling Stacking time Fault would (OISF), improve Crystal the Originatedcrystal quality. Pit (COP),Generally, and the interstitial stress at agglomerate30 MPa or less to has form not a largelead to dislocation stress defects loop in [25 th].e Thecrystal obtained growth defect-free [24]. However, area indicated the silicon that crystal the vacancygrowth andconditions interstitial are are defined very low based concentrations on the critical without region COP, in OISF, which and dislocationthe interstitial loops region [26–30 is]. Therefore,transformed when in the the vacancy V/G value region. is in rangeThe V/G between ratio iden 0.00213tified and the 0.00219 defect domination (cm2/min/k) area along of withvacancy radial or andinterstitial axial direction, as shown the in crystalEquation growth (10). The is free critical of defect V/G can area be and determined shown in by Figure concentration4[31–34]. of vacancy (Cv)The − concentration V/G ratio has of initiallyinterstitial increased (Ci) = 0. fromVacancy CP400 is agglomerated to CP 800 after to form which void, it decreased Oxidation with Induced the increaseStacking inFault CP height.(OISF), Moreover,Crystal Originated the power Pit consumption (COP), and wasinterstitial decreased agglomerate from 92.12 to toform 87.75 a large kW. Thedislocation CG-Sim loop analysis [25]. resultsThe obtained for various defect-free CP heights area indicated of single crystalthat the ingot vacancy in CZ-process and interstitial suggest are very that thelow increase concentrations in the crystal without length COP, would OISF, decrease and dislocat the stression loops in the [26–30]. crystal Therefore, due to increased when the cooling V/G value time. Eventually,is in range between it indicates 0.00213 thatthe and increase 0.00219 of(cm cooling2/min/k) time along would with improve radial and the axial crystal direction, quality. the crystal growth is free of defect area and shown in Figure 4 [31–34]. V Velocity → TheG V/GTemperature ratio gradienthas initially increased from CP400 to CP 800 after which it decreased with the  V→ 2 1 1 increase in CP height.= 0.00216 Moreover,mm min− Kthe− power consumption was decreased from 92.12 to 87.75 kW. The ⇒  G Critical    CG-SimV analysis> V results= Vfor various CP heights of single crystal ingot in CZ-process suggest that(10) the ⇒ G G Critical G Interstitial  V   V   V  increaseG in< theG crystal= lengthG would decrease the stress in the crystal due to increased cooling time. ⇒   Critical Vacancy         Eventually,V it indicates that< 0.00213 the increaseV of

Figure 2. Configuration of basic model crystal design (BTCD) Czochralski process (CZ-process) with Figure 2. Configuration of basic model crystal design (BTCD) Czochralski process (CZ-process) with different CP (crystal position) 400, 800, 1200, 2000, 2400, and 3000 mm based at a 1.0 mm/min pulling rate. different CP (crystal position) 400, 800, 1200, 2000, 2400, and 3000 mm based at a 1.0 mm/min pulling rate. Table 2. Analysis result of the crystal positions.

Crystal Position V/G (cm2/min/K) (Average) von Mises Stress (MPa) (Average) Power (kW) Crystal Mass (kg)

CP400 0.00232 15.09 92.12 29.25 CP800 0.00239 15.33 89.08 62.41 CP1200 0.00236 15.07 87.56 95.77 CP2000 0.00235 15.08 86.59 162.52 CP2400 0.00236 14.99 86.31 196.60 CP3000 0.00238 14.71 87.75 246.07 Processes 2020, 8, 1077x FOR PEER REVIEW 66 of of 14 13

0.00240 V/G[cm2/min/K] 0.00239

0.00238

0.00237

0.00236 /min/K] 2 0.00235

0.00234 V/G[cm 0.00233

0.00232

0.00231 CP400 CP800 CP1200 CP2000 CP2400 CP3000 Crystal position

(a)

15.4 Von_mises_stress[MPa] 15.3

15.2

15.1

15.0

Stress[MPa] 14.9

14.8

14.7

CP400 CP800 CP1200 CP2000 CP2400 CP3000 Crystal position

(b)

93

92 Power[kW]

91

90

89

Power[kW] 88

87

86

CP400 CP800 CP1200 CP2000 CP2400 CP3000 Crystal position

(c)

Figure 3. CG-SimCG-Sim analysis analysis for for single-crystal single-crystal Si ingot at a pulling pulling rate of 1.0 1.0 (mm/min) (mm/min) with various CP heights: ( a))V V/G/G (ratio of the the growth growth rate to the the vertical vertical T T gradient), gradient), ( b)) von von Mises Mises stress, stress, and and ( (c)) power power by CP (crystal position).

Processes 2020, 8, x FOR PEER REVIEW 7 of 14

𝑉 → 𝑉𝑒𝑙𝑜𝑐𝑖𝑡𝑦

𝐺 → 𝑇𝑒𝑚𝑝𝑒𝑟𝑎𝑡𝑢𝑟𝑒 𝑔𝑟𝑎𝑑𝑖𝑒𝑛𝑡 𝑉 ⇒ = 0.00216𝑚𝑚𝑚𝑖𝑛𝐾 𝐺 𝑉 𝑉 𝑉 ⇒ = (10) 𝐺 𝐺 𝐺 𝐼𝑛𝑡𝑒𝑟𝑠𝑡𝑖𝑡𝑖𝑎𝑙 𝑉 𝑉 𝑉 ⇒ = 𝐺 𝐺 𝐺 𝑉𝑎𝑐𝑎𝑛𝑐𝑦

𝑉 𝑉 𝑉 𝑉 𝑉 Processes 2020, 8, 1077 ⇒ 0.00213 0.00213~0.00219 0.00219 7 of 13 𝐺 𝐺 𝐺 / 𝐺 𝐺

FigureFigure 4. 4.Area Area of of free-defectsfree-defects fromfrom the vacancy, interstitial,interstitial, COP, COP, OISF OISF and and dislocation dislocation loops. loops. Cooling System Length Adjustment and Dual-System Design Table 2. Analysis result of the crystal positions. In order to understand the cooling effect on the single-crystal production yield and quality, Crystal V/G (cm2/min/K) von Mises Stress (MPa) Power Crystal Mass we modified the cooling system in CZ-process with two types of designs and studied their effects Position (Average) (Average) (kW) (kg) using CG-Sim analysis. Figure5 describes the cooling system BTCD, the long type cooling design CP400 0.00232 15.09 92.12 29.25 (LTCD), and the other one is double type cooling design (DTCD) installed in the Czochralski process, CP800 0.00239 15.33 89.08 62.41 whereCP1200 LTCD was just a 10%0.00236 extended length of cooling 15.07 system compared 87.56 to that of BTCD.95.77 Figure 6 showsCP2000 the CG-Sim 2D view0.00235 of thermal gradients nearby 15.08 crystal and illustrated 86.59 point of162.52 advantage by coolingCP2400 design in CZ-process.0.00236 The decreased thermal 14.99 gradients were 86.31 observed in196.60 vertical and horizontalCP300 DTCD0 than LTCD,0.00238 due to faster cooling rate 14.71 inDTCP design, which 87.75decreased 246.07 the internal heat of the crystal, thereby maintaining the uniformity. Processes 2020, 8, x FOR PEER REVIEW 8 of 14 Cooling System Length Adjustment and Dual-System Design In order to understand the cooling effect on the single-crystal production yield and quality, we modified the cooling system in CZ-process with two types of designs and studied their effects using CG-Sim analysis. Figure 5 describes the cooling system BTCD, the long type cooling design (LTCD), and the other one is double type cooling design (DTCD) installed in the Czochralski process, where LTCD was just a 10% extended length of cooling system compared to that of BTCD. Figure 6 shows the CG-Sim 2D view of thermal gradients nearby crystal and illustrated point of advantage by cooling design in CZ-process. The decreased thermal gradients were observed in vertical and horizontal DTCD than LTCD, due to faster cooling rate in DTCP design, which decreased the internal heat of the crystal, thereby maintaining the uniformity.

FigureFigure 5.5. ModifiedModified coolingcooling systemsystem inin CzochralskiCzochralski process,process, basicbasic coolingcooling systemsystem toto extendedextended 10%10% longlong typetype coolingcooling designdesign andand doubledouble typetype coolingcooling design.design.

Figure 6. BTCD, long type cooling design (LTCD), and double type cooling design (DTCD) schematic diagram of the overall process of the water-cooling system in CG-Sim 2D view.

To clearly understand the crystal quality, the V/G ratio, von Mises stress, power consumption, and crystal mass were calculated by CG-Sim analysis. The corresponding results are displayed in Figure 7 by comparing with the BTCD model. Table 3 illustrates the comparative data of BTCD,

Processes 2020, 8, x FOR PEER REVIEW 8 of 14

ProcessesFigure2020, 85., 1077Modified cooling system in Czochralski process, basic cooling system to extended 10% long8 of 13 type cooling design and double type cooling design.

FigureFigure 6.6. BTCD,BTCD, longlong typetype coolingcooling designdesign (LTCD),(LTCD),and anddouble double typetype coolingcooling designdesign (DTCD)(DTCD)schematic schematic diagram of the overall process of the water-cooling system in CG-Sim 2D view. diagram of the overall process of the water-cooling system in CG-Sim 2D view. To clearly understand the crystal quality, the V/G ratio, von Mises stress, power consumption, To clearly understand the crystal quality, the V/G ratio, von Mises stress, power consumption, and crystal mass were calculated by CG-Sim analysis. The corresponding results are displayed in and crystal mass were calculated by CG-Sim analysis. The corresponding results are displayed in Figure7 by comparing with the BTCD model. Table3 illustrates the comparative data of BTCD, LTCD, Figure 7 by comparing with the BTCD model. Table 3 illustrates the comparative data of BTCD, and BTCD obtained in CG-Sim analysis. Based on the results obtained in the BTCD, we have designed two types of cooling systems to understand the effective cooling system on crystal quality. The CG-Sim 2d view of the Cz-process is displayed in Figure6. In addition, Figure7 depicts the V /G, von Mises stress, and power and defects in the Si-single crystal ingot by CG-Sim analysis, and the corresponding results are listed in Table3.

Table 3. Analysis result of the simulation.

Type CP400 CP800 CP1200 CP2000 CP2400 CP3000 BTCD 0.00232 0.00239 0.00236 0.00235 0.00236 0.00238 V/G (cm2/min/k) LTCD 0.00230 0.00236 0.00234 0.00234 0.00234 0.00237 DTCD 0.00222 0.00219 0.00217 0.00216 0.00217 0.00219 BTCD 15.09 15.33 15.07 15.08 14.99 14.71 von Mises stress (MPa) LTCD 14.75 14.80 14.98 14.94 15.00 14.49 DTCD 14.20 13.84 13.82 14.13 14.01 13.59 BTCD 92.12 89.08 87.56 86.59 86.31 87.75 Power (kW) LTCD 92.01 89.64 88.20 86.22 86.83 88.15 DTCD 94.04 91.51 90.58 89.45 89.09 90.86 Processes 2020, 8, x FOR PEER REVIEW 9 of 14

LTCD, and BTCD obtained in CG-Sim analysis. Based on the results obtained in the BTCD, we have designed two types of cooling systems to understand the effective cooling system on crystal quality. The CG-Sim 2d view of the Cz-process is displayed in Figure 6. In addition, Figure 7 depicts the V/G, Processesvon2020 Mises, 8, 1077stress, and power and defects in the Si-single crystal ingot by CG-Sim analysis, and the9 of 13 corresponding results are listed in Table 3.

2 CP400 2 CP400 V/G[cm /min/K] V/G[cm /min/K] CP800 CP800 0.00240 0.002390 CP1200 CP1200 0.002385 0.00238 CP2000 CP2000 0.002380 CP2400 CP2400 0.00236 0.002375 CP3000 0.002370 CP3000 0.00234 0.002365 0.002360 0.00232 0.002355 0.00230 0.002350 0.00228

0.002345 /min/K] /min/K] 2 2 0.002340 0.00226 0.002335 0.002330 0.00224

V/G[cm 0.002325 V/G[cm 0.00222 0.002320 0.002315 0.00220 0.002310 0.00218 0.002305 0.002300 0.00216 0.00214 Basic Long type Basic Double tpye Long type cooling design Double type cooling design

(a) (b)

Stress[MPa] CP400 CP400 Stress[MPa] CP800 CP800 15.35 15.4 15.30 CP1200 CP1200 CP2000 CP2000 15.25 15.2 15.20 CP2400 CP2400 15.15 CP3000 15.0 CP3000 15.10 15.05 14.8 15.00 14.95 14.6 14.90 14.85 14.4 14.80 14.2 Stress[MPa] 14.75 Stress[MPa] 14.70 14.0 14.65 14.60 13.8 14.55 14.50 13.6 14.45 Basic Long type Basic Double tpye Long type cooling design Double type cooling design

(c) (d)

Power[kW] CP400 CP800 94.0 CP1200 93.5 CP2000 93.0 CP2400 92.5 92.0 CP3000 91.5 91.0 90.5 90.0 89.5 89.0 Power[kW] 88.5 88.0 87.5 87.0 86.5 86.0 Basic Long type Double tpye Type

(e)

FigureFigure 7. Comparative 7. Comparative analysis analysis of of the the BTCD, BTCD, LTCD, LTCD, and and DTCD DTCD ( a()a) and and ( b(b)V) V/G/G results; results; ((cc)) andand ((dd)) von Misesvon stress; Mises and stress; (e) and the ( power.e) the power.

The V/G ratio, which represents the defect-free area was measured. The DTCD-based crystal showed that the DTCD has a lower V/G compared to BTCD, in which the reduction percentage was approximately 8.29%. The V/G was only decreased by 1% compared to LTCD and BTCD. Moreover, the V/G values have approached the defect-free area using DTCD design. This is due to an increase in crystal CP, which slightly decreases the V/G values, thereby approaching the defect-free area, which has been advantageous in obtaining production yield and quality crystals. Similarly, the stress effect was also compared for the DTCD, LTCD, and BTCD designs wherein the decreasing rate of stress was almost 10% for DTCD than BTCD design and 3% for LTCD than BTCD. This is due to the improvement in the cooling efficiency as the distance between the DTCD and the crystal is less, which led to a fast reduction of heat from inside the crystal. As the stress decreases, the stress required to destroy the crystal also decreases with decrease in temperature gradient. However, the power consumption was increased by approximately 3% for DTCD compared to BTCD (Figure7) because more power has been consumed in order to maintain the hot zone temperature of the molten state from the effect of cooling system inside the chamber. Processes 2020, 8, 1077 10 of 13

The obtained results indicated that each CP has improved with decreasing V/G and von Mises stress. The process was considered as a mass production since the CZ-process has required high cost and longtime operation. Therefore, the higher height of CP has the faster cooling effect, and the lower value of stress can be observed from the results. The CP3000 has been selected as a best test target since it has the best cooling effect. To further analyze the effect of cooling systems design on crystal height, the temperature distribution was analyzed at CP3000 using CG-Sim for all the cooling designs. Figure8 represents the thermal distribution and heat flux inside the chamber and crystal using BTCD, LTCD, and DTCD cooling systems at CP3000. The lowest temperature distribution was observed for DTCD design compared to the BTCD and LTCD, which was due to the increase in the cooling capacity and influence Processes 2020, 8, x FOR PEER REVIEW 11 of 14 of some region nearby. Moreover, when the temperature gradient decreases inside the crystal, the crystal growthProcesses rate 2020 would, 8, x FOR increase, PEER REVIEW simultaneously. 11 of 14

Figure 8. CG-Sim analyzed thermal gradient in crystal and the vectors indicated heat flux in Cz- Figure 8. CG-Sim analyzed thermal gradient in crystal and the vectors indicated heat flux in Cz-process processFigure using 8. CG-Sim BTCD analyzed (a), LTCD thermal (b), and gradient DTCD in(c) crystalcooling and systems, the vectors respectively, indicated at heatCP3000. flux in Cz- usingprocess BTCD using (a), BTCD LTCD (a (b), ),LTCD and DTCD(b), and (c DTCD) cooling (c) systems,cooling systems, respectively, respectively, at CP3000. at CP3000. The rapid crystal growth rate is important to produce large crystal ingot with improved The rapid crystal growth rate is important to produce large crystal ingot with improved productivity. Therefore, the simulations were conducted at pulling speeds of 1.0–2.0 mm/min at productivity.productivity. Therefore, Therefore, the the simulationssimulations were conducted at at pulling pulling speeds speeds of of 1.0–2.0 1.0–2.0 mm/min mm/min at at CP3000. The corresponding comparative plots are displayed in Figure 9. Table 4 shows the difference CP3000.CP3000. The The corresponding corresponding comparative comparative plots are disp displayedlayed in in Figure Figure 9.9 .Tabl Tablee 44 shows shows the the difference di fference between V/G and von Mises stress, which are expressed as the quality of the LTCD and DTCD betweenbetween V /GV/G and and von von Mises Mises stress, stress, which which are are expressed expressed as the as qualitythe quality of the of LTCDthe LTCD and DTCDand DTCD crystals crystals according to the pulling speed. accordingcrystals according to the pulling to the speed. pulling speed.

BTCD BTCD 2 BTCD Von_Mises_stress[Pa] BTCD V/G[cm /min/K]2 LTCD Von_Mises_stress[Pa] LTCD V/G[cm /min/K] LTCD LTCD 0.0042 DTCD 50 DTCD 0.0042 DTCD 50 DTCD 0.0040 0.0040 45 45 0.00380.0038 40 0.00360.0036 40 0.00340.0034 3535 0.00320.0032 3030 /min/K] /min/K] 2 0.00302 0.0030 2525 Stress[MPa] 0.00280.0028 Stress[MPa] V/G[cm V/G[cm 0.00260.0026 2020 0.00240.0024 1515 0.00220.0022 1010 0.00200.0020 1.01.21.41.61.82.01.01.21.41.61.82.0 1.01.0 1.2 1.2 1.4 1.4 1.6 1.6 1.8 1.8 2.0 2.0 Pulling speed[mm/min] PullingPulling speed[mm/min] speed[mm/min] Pulling speed[mm/min]

(a(a) ) (b()b ) Figure 9. Results at a high pulling speed for each CP3000 design (a) V/G and (b) von Mises stress. Figure 9. ResultsResults at at a a high pulling sp speedeed for each CP3000 design ( a))V V/G/G and (b) von Mises stress.

Table 4. CG-Sim analysis results at various pulling speeds between 1.0 and 2.0 mm/min at CP3000. Table 4. CG-Sim analysis results at various pulling speeds between 1.0 and 2.0 mm/min at CP3000. V/G (cm2/min/K) von_Mises_Stress (MPa) Pulling V/G (cm2/min/K) von_Mises_Stress (MPa) Pulling Decreasing Decreasing Speed BTCD LTCD DTCD Decreasing BTCD LTCD DTCD Decreasing Speed BTCD LTCD DTCD Rate % BTCD LTCD DTCD Rate % Rate % Rate % 1.0 0.00238 0.00237 0.00219 8.67% 14.71 14.49 13.59 8.24% 1.01.1 0.00238 0.00256 0.002370.00255 0.002190.00236 8.47%8.67% 16.87 14.71 16.64 14.49 15.09 13.59 11.79% 8.24% 1.11.2 0.00256 0.00274 0.002550.00272 0.002360.00253 8.30%8.47% 19.32 16.87 18.66 16.64 17.13 15.09 12.78% 11.79% 1.21.3 0.00274 0.00290 0.002720.00288 0.002530.00269 7.80%8.30% 21.919.32 21.36 18.66 18.79 17.13 16.55% 12.78% 1.31.4 0.00290 0.00308 0.002880.00305 0.002690.00285 8.07%7.80% 25.18 21.9 24.5 21.36 21.33 18.79 18.04% 16.55% 1.41.5 0.00308 0.00325 0.003050.00323 0.002850.00301 7.97%8.07% 28.78 25.18 27.79 24.5 24.39 21.33 17.99% 18.04% 1.51.6 0.00325 0.00341 0.003230.00338 0.003010.00316 7.91%7.97% 32.13 28.78 31.59 27.79 27.33 24.39 17.56% 17.99% 1.6 0.00341 0.00338 0.00316 7.91% 32.13 31.59 27.33 17.56%

Processes 2020, 8, 1077 11 of 13

Table 4. CG-Sim analysis results at various pulling speeds between 1.0 and 2.0 mm/min at CP3000.

V/G (cm2/min/K) von_Mises_Stress (MPa) Pulling Speed Decreasing Decreasing BTCD LTCD DTCD BTCD LTCD DTCD Rate % Rate % 1.0 0.00238 0.00237 0.00219 8.67% 14.71 14.49 13.59 8.24% 1.1 0.00256 0.00255 0.00236 8.47% 16.87 16.64 15.09 11.79% 1.2 0.00274 0.00272 0.00253 8.30% 19.32 18.66 17.13 12.78% 1.3 0.00290 0.00288 0.00269 7.80% 21.9 21.36 18.79 16.55% 1.4 0.00308 0.00305 0.00285 8.07% 25.18 24.5 21.33 18.04% 1.5 0.00325 0.00323 0.00301 7.97% 28.78 27.79 24.39 17.99% 1.6 0.00341 0.00338 0.00316 7.91% 32.13 31.59 27.33 17.56% 1.7 0.00359 0.00356 0.00332 8.13% 36.79 35.75 30.81 19.40% 1.8 0.00377 0.00374 0.00347 8.64% 40.71 39.42 35.27 15.42% 1.9 0.00396 0.00392 0.00364 8.79% 44.28 43.1 38.79 14.15% 2 0.00413 0.00411 0.00381 8.39% 48.03 46.48 42.3 13.54%

The above results illustrate that the increased pulling speed would move the V/G values towards defect area from defect-free area. However, the V/G values were lower for DTCD than BTCD and LTCD designs, suggesting a possibility to improve the crystal production by modifying the cooling system of DTCD. Furthermore, von Mises stress defects were also greatly decreased for DTCD design compared to the other designs at each pulling speed. The average stress differences between BTCD and LTCD were 1–3%, whereas the comparison of average stress difference between BTCD and DTCD was 15%. As a result, the experimental data has shown the possibility of satisfying the high crystal growth rate while improving the stress, by reducing the temperature gradient inside the crystal from the cooling system. The efficient difference between LTCD and DTCD were significantly indicated from the comparison results with BTCD. In other words, the effect of crystal growth was lower than that of the double design due to the cooling effects, and the pulling speed could be improved. The V/G value of DTCD was approximately 7.5% better than that of LTCD. Moreover, the internal thermal stress of the crystal was improved by approximately 12% because longer residence time from the cooling zone during crystal growth and deeper crystal would result in lower internal temperature gradient of the crystal. With this experience, methods to enhance the pulling speed and growth rate have been developed. This study was aimed at increasing the pulling rate of a single crystal silicon ingot by the Czochralski method using a Crystal Growth Simulation.

4. Conclusions The crystal growth rate of BTCD and LTCD does not have a large margin of error, a difference of about 0.2 mm/min between the DTCD and the range of velocities could be confirmed through this experiment. That is, the cooling effect had a great influence on the crystal growth rate, and the growth rate could be improved. From this study, the difference between the V/G and von Mises stress was shown for each cooling system design, and the defect-free area V/G value of DTCD was approximately 8% better than that of BTCD. In addition, a longer residence time and faster cooling effect from the cooling zone during crystal growth and a lower internal temperature gradient resulted in an approximately 15% decrease in the internal thermal stress of the crystal. Through this experience, one of the growth enhancement solutions was applied to achieve an improved pulling speed. The purpose of this study was to achieve a high rate of increase in single crystal silicon ingots by the Czochralski method using Crystal Growth Simulation. Although the power was slightly different from the BTCD, the crystal growth rate was improved by 18.1% or more by the modified DTCD. In other words, Processes 2020, 8, 1077 12 of 13 increasing the crystal growth rate of the single crystal silicon ingot reduces the production time of the process more than the amount of electric power consumed, thereby improving productivity. In addition, efficiencies were achieved from an economic perspective. As a result of this research, further progress was able to be completed in the development of the Czochralski process and step to secure the source technology for achieving economic efficiency and improved productivity of single crystal silicon ingots was implemented.

Author Contributions: Conceptualization, J.H.J. and H.J.J.; methodology, J.H.J.; validation, J.H.J., software and simulation H.J.J.; formal analysis and evaluation, J.H.J. and H.J.J.; investigation, H.J.J., H.P., S.A., and G.K.; resources, process system optimized Laboratory and STR Group.; data curation, process system optimized laboratory; writing—original draft preparation, H.J.J.; writing—review and editing, J.H.J., S.A., H.P., and H.J.J.; visualization, J.J.H., G.K., H.P., and H.J.J.; supervision, J.H.J.; project administration, J.H.J.; all authors contributed to writing the paper and reviewed the draft. All authors have read and agreed to the published version of the manuscript. Funding: This research was supported by the Korea Institute of Energy Technology Evaluation and Planning (KETEP), Ministry of Trade, Industry, and Energy (MOTIE) of Republic of Korea (No. 20173030018990), and by X-mind Corps program of National Research Foundation of Korea (NRF) funded by the Ministry of Science, ICT (2019H1D8A110563011). Acknowledgments: The authors would like to thank Vladimir Artemyev and colleagues from STR for useful discussions and fruitful cooperation with CG-Sim simulations. Conflicts of Interest: The authors declare no conflict of interest. Software: This work used the software CG-Sim v.20 software of STR Company (www.str-soft.com) to obtain a result. Moreover, Vladimir Artemyev from STR Group Inc. (http://str-soft.com) has supported software training.

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