WO2012139362A1 - Polysilicon ingot casting furnace and polysilicon ingot casting method - Google Patents

Polysilicon ingot casting furnace and polysilicon ingot casting method Download PDF

Info

Publication number
WO2012139362A1
WO2012139362A1 PCT/CN2011/080602 CN2011080602W WO2012139362A1 WO 2012139362 A1 WO2012139362 A1 WO 2012139362A1 CN 2011080602 W CN2011080602 W CN 2011080602W WO 2012139362 A1 WO2012139362 A1 WO 2012139362A1
Authority
WO
WIPO (PCT)
Prior art keywords
furnace
polycrystalline silicon
silicon ingot
heating body
heat insulator
Prior art date
Application number
PCT/CN2011/080602
Other languages
French (fr)
Chinese (zh)
Inventor
史珺
宗卫峰
水川
佟晨
程素玲
Original Assignee
上海普罗新能源有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 上海普罗新能源有限公司 filed Critical 上海普罗新能源有限公司
Publication of WO2012139362A1 publication Critical patent/WO2012139362A1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B11/00Single-crystal growth by normal freezing or freezing under temperature gradient, e.g. Bridgman-Stockbarger method
    • C30B11/003Heating or cooling of the melt or the crystallised material
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/02Silicon
    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B29/00Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape
    • C30B29/02Elements
    • C30B29/06Silicon
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Definitions

  • the invention relates to the field of solar polycrystalline silicon ingots, in particular to a polycrystalline silicon ingot furnace, and to a polycrystalline silicon ingot casting method.
  • Polycrystalline silicon ingot technology was developed from around 2004. When people discovered that the polycrystalline silicon ingots could be sliced and made into solar cells, the polycrystalline silicon ingot furnace was started. Compared with single crystal furnaces, polycrystalline silicon ingot furnaces are characterized by low cost, large output, and easy handling. Since 2007, the global production of polycrystalline silicon photovoltaic cells has surpassed that of monocrystalline silicon. By 2010, the proportion of polycrystalline silicon has risen to more than 70%.
  • the existing polycrystalline silicon ingot furnace adopts electric resistance or induction heating to melt the polycrystalline silicon with a good ratio, and then adopts a method of solidifying from the bottom and gradually solidifying upward crystal growth to obtain a polycrystalline silicon ingot. Since 2004, the output of the existing polycrystalline silicon ingot furnace has ranged from 120 kg to 170 kg, 250 kg, 450 kg to 660 kg. Due to the larger single furnace output of the existing polycrystalline silicon ingot furnace, the higher the production efficiency and the lower the unit energy consumption, therefore, many manufacturers hope to develop a higher yield polycrystalline silicon ingot furnace.
  • the existing polysilicon ingot furnace that can be seen on the market has a maximum capacity of 660 kg, which is a single silicon ingot.
  • Some companies have tried 800 kilograms, but they have been stranded for various reasons. The main reason is that if the weight of a single silicon ingot is too large, the size must be correspondingly increased.
  • the bottom of the ingot is cooled first, and the top is cooled, so that the crystal can grow slowly from the bottom to the top. The cooling is carried out by the bottom silicon crystal carrying the heat to the bottom.
  • the technical problem to be solved by the present invention is to provide a polycrystalline silicon ingot furnace which can double the output of a single ingot furnace and ensure good quality without changing the niobium and silicon ingot access and the opening device for the ingot. Therefore, the utilization rate of the existing equipment can be improved and the investment cost of the equipment can be saved, energy saving, water saving, and solar saving can be saved, and the cost can be saved. To this end, the present invention also provides a polycrystalline silicon ingot casting method using the polycrystalline silicon ingot furnace.
  • the polycrystalline silicon ingot furnace comprises: a furnace body and a heat insulator in the furnace body, a graphite platform, four crucibles, an upper heating body and a lower heating body.
  • the furnace body includes an upper furnace cover, a furnace body and a furnace bottom, and the furnace bottom and the furnace body are hydraulically connected, and the furnace bottom can be separated or closed from the furnace body.
  • the heat insulating body is cuboidal, and the heat insulating body comprises an upper heat insulating body and a lower heat insulating body.
  • the graphite platform is located in the heat insulator and surrounded by the heat insulator, and the four crucibles are placed on the graphite platform.
  • the upper heating body and the lower heating body are both located in the heat retaining body, and the upper heating body is located below the top surface of the upper heat insulating body of the top of the crucible, and the lower heating body is located at the graphite Below the platform, the upper heating body and the upper heat retaining body are fixed together and fixed to the furnace body, and the lower heating body and the lower heat insulating body are fixed together and can be separated from the upper heat insulating body together Move Downward.
  • a further improvement is that the four crucibles are placed on the graphite platform in a field shape.
  • a further improvement is that the sides of the four turns are 720 mm to 1200 mm, respectively.
  • a further improvement is that the four crucibles are standard gauges or special gauges for solar grade polycrystalline silicon ingots.
  • a further improvement is that the upper heating body completely covers the four turns, and the outer edge of the upper heating body is larger than the outer edge of the four turns by 5% to 30%, and the four turns are The outer side surface and the heat retaining body are spaced apart by a distance, and a portion of the upper heating body outside the outer edge of the four turns is used to heat the sides of the four turns.
  • a further improvement is that a shield is placed around each of the turns.
  • a further improvement is that the upper heating body is composed of two heating circuits, which can work simultaneously and can also be hot backups to each other.
  • a further improvement is that the lower heat retaining body is connected to the lifting and lowering mechanism, and the lower heat insulating body is lowered by the lifting and lowering mechanism.
  • the polycrystalline silicon ingot method provided by the present invention comprises the following steps:
  • Step 1 Lowering and opening the bottom of the furnace with a hydraulic device and loading the silicon material into the four crucibles,
  • Step 2 Raise the bottom of the furnace to close it and start vacuuming.
  • Step 3 When the degree of vacuum of the furnace body reaches 1 Pa, the upper heating body and the lower heating body are powered, and the heating of the silicon material is started and the silicon material is completely melted.
  • Step 4 performing a crystal growth process, comprising the steps of: gradually reducing the power of the lower heating body to gradually lower the temperature of the bottom of the crucible, and when the bottom temperature of the crucible is lower than the melting point of the silicon material Crystallization starts and polysilicon is formed; when the power of the lower heating body drops to zero, the lower heat insulator and the lower heater are lowered together, so that the polysilicon continues to grow upward.
  • Step 5 lifting the lower heat insulator and the lower heat body, annealing the polysilicon, and then cooling the polysilicon.
  • Step 6 When the temperature of the polycrystalline silicon ingot formed by the polysilicon is lowered to 300 ° C or lower, the bottom of the furnace is lowered and the polycrystalline silicon ingot is taken out.
  • the polycrystalline silicon ingot furnace of the invention has four crucibles, and can realize four furnaces for producing four polycrystalline silicon ingots, thereby multiplying the output of the single ingot furnace.
  • the design of the edge of the upper heating body of the polycrystalline silicon ingot furnace of the present invention is larger than the size of the edge of the four crucibles, so that the upper heating body can be heated at the upper portion to realize the four crucibles.
  • the side heating can form a gradient gradually decreasing from the top to the bottom on the sides of the four turns during the growth of the polysilicon, so that the isothermal surface in each of the crucibles can be horizontal, and the heat dissipation on the outer side of the crucible can be solved.
  • the problem of the level of the isothermal surface is not high. A good isothermal surface can ultimately improve the quality of the polycrystalline silicon ingot.
  • the polycrystalline silicon ingot furnace of the present invention does not need to increase the size of each polycrystalline silicon ingot to increase the yield of the polycrystalline silicon ingot, and can avoid the horizontal temperature field of the crucible caused by the large-sized polycrystalline silicon ingot being difficult to maintain, and the vertical temperature difference It will be very large and the resulting crystal growth quality will be deteriorated, so that good columnar crystals can be formed and the quality of the product can be improved.
  • the polycrystalline silicon ingot furnace of the present invention does not need to change the bismuth and silicon ingot access and the opening device for the ingot, that is, the polycrystalline silicon ingot furnace of the invention can be compatible with the equipment on the existing production line, thereby saving investment cost, and Can improve production efficiency.
  • the four enamels of the present invention are placed in a field and have a certain space in the middle for placing the slabs, the ratio of the insulating cage area to the rated output or the insulation of the silicon material.
  • the specific surface area is significantly lower than that of the existing single ingot; in addition, the design of the upper heating body of the present invention can omit the side heating body, so that the furnace type of the present invention can have significant energy saving effect, and the present invention can also be used Water and solar terms can save costs.
  • FIG. 1 is a schematic cross-sectional view showing a polycrystalline silicon ingot furnace according to an embodiment of the present invention
  • FIG. 2 is a top crystal photograph of a polycrystalline silicon ingot produced by a polycrystalline silicon ingot method according to an embodiment of the present invention
  • FIG. 3 is a longitudinal cross-sectional photograph of a polycrystalline silicon ingot produced by a polycrystalline silicon ingot method according to an embodiment of the present invention
  • FIG. 4 is a top crystal photograph of a polycrystalline silicon ingot produced by the method of polycrystalline silicon ingot according to the second embodiment of the present invention.
  • Figure 5 is a longitudinal cross-sectional photograph of a polycrystalline silicon ingot produced by the method of polycrystalline silicon ingot according to the second embodiment of the present invention.
  • FIG. 6 is a top crystal photograph of a polycrystalline silicon ingot produced by the method of three polycrystalline silicon ingots according to an embodiment of the present invention.
  • Figure 7 is a longitudinal cross-sectional photograph of a polycrystalline silicon ingot produced by the third polycrystalline silicon ingot method of the embodiment of the present invention.
  • FIG. 1 it is a schematic cross-sectional view of a polycrystalline silicon ingot furnace according to an embodiment of the present invention.
  • the polycrystalline silicon ingot furnace of the embodiment of the invention comprises: a furnace body and a heat insulator in the furnace body, a graphite platform 6, four crucibles 7, an upper heating body 9 and a lower heating body 5.
  • the furnace body comprises an upper furnace cover 1, a furnace body 2 and a furnace bottom 3, and the furnace bottom 3 and the furnace body 2 are hydraulically connected, and the furnace bottom 3 and the furnace body can be passed by the hydraulic device 2 Separate or closed, used to load and unload silicon or polycrystalline silicon ingots.
  • the furnace body shell is made of a stainless steel water-cooled furnace shell.
  • the upper furnace cover 1 functions to fix the upper heating body 9, connect the heating water cable, install the top temperature measuring device, and connect the ventilation pipe.
  • the furnace body 2 is fixed with a side insulator, that is, an insulator constituting the heat insulator, and is also connected to a vacuum pipeline.
  • the furnace body 2 is supported on the ground by four brackets, the upper furnace cover 1 is directly placed on the furnace body 2 and sealed by a flange; the furnace bottom 3 is suspended by a hydraulic system On the furnace body 2, when the hydraulically controlled furnace bottom is lifted and sealed, the vacuum sealing is also performed through the flange.
  • the hearth 3 and the furnace body 2 adopt a hydraulic suspension mechanism, and the hydraulic mechanism can control the furnace bottom 3 to stop at any height within the stroke.
  • the furnace bottom 3 is provided with a plurality of temperature measuring points, which can measure the temperature of each raft and different positions, so that the bottom temperature condition in the furnace can be clearly displayed on the display and provided to Control System.
  • the heat insulating body is cuboidal, and the heat insulating body includes an upper heat insulating body 8 and a lower heat insulating body 4.
  • the graphite platform 6 is located in the heat insulator and surrounded by the heat insulator, and the four turns 7 are placed on the graphite platform 6.
  • the size of the crucible may be a standard polycrystalline silicon ingot such as 450 kg, 500 kg, 660 kg or 800 kg, and the sides of the four crucibles are respectively 720 mm to 1200 mm.
  • the four crucibles 7 are placed in a field shape with a certain space in the middle for placing the crucible guards. Due to the geometry of 4 ingots corresponding to the arrangement of the four crucibles 7, the ratio of the area of the insulating cage to the rated output or the specific surface area of the insulator used for the silicon material is significantly lower than that of the single ingot. Therefore, the furnace has a remarkable energy saving effect, and the unit energy consumption is reduced by about 20% compared to the single furnace type. At the same time, the argon consumption is reduced by about 60% relative to the single furnace type.
  • the size of the graphite platform 6 has a certain margin and may be slightly larger or slightly smaller.
  • the upper heating body 9 and the lower heating body 5 are both located in the heat retaining body, and the upper heating body 8 is located below the top surface of the upper heat insulating body 8 at the top of the crucible 7, and the lower heating
  • the body 5 is located below the graphite platform 6, the upper heating body 9 and the upper heat retaining body 8 are fixed together and fixed on the furnace body 2, and the lower heating body 5 and the lower heat insulating body 4 are fixed. Together and together with the upper insulation 8 and moving downwards.
  • the lower heat retaining body 4 is connected to the lifting and lowering mechanism, and is lowered by the lifting and lowering mechanism.
  • the lower heat retaining body 4 is lowered, and the graphite platform 6 is not lowered; when the loading and unloading are performed, the lower heat insulating body 4 and the graphite platform 6 (with four crucibles 7) are lowered together. .
  • the upper heating body 9 completely covers the four crucibles 7, and the outer edge of the upper heating body 9 has a size larger than the outer edge of the four crucibles 7 by 5% to 30%.
  • the side surface and the heat insulator are spaced apart by a distance, and a portion of the upper heating body 9 outside the outer edge of the four turns 7 is used to heat the sides of the four turns.
  • the growth quality of polycrystalline silicon used in solar photovoltaic cells has a strong relationship with the final cell efficiency. If you want to get good battery quality, you need a larger grain size and the crystal column growth direction is as vertical as possible. For this reason, it is required that the isothermal surface inside the crucible 7 is as horizontal as possible during crystal growth.
  • the invention adopts up-and-down heating and no side heating, when the crystal grows, it is easy to cause the outer sides of the four crucibles to be supercooled, and the periphery of the crucible is first cooled, so that the crystal grows from the outside to the inside. Therefore, the outer diameter of the upper heating body 9 is increased in size, and the outer side surface of the crucible 7 is kept at a certain distance from the heat insulating body, so that the outer side surface of the crucible 7 can be always used by the upper heating body 9. Heating is taking place.
  • the upper heating body 9 has a large heating to the upper portion and a lower temperature at the bottom portion, a lower temperature gradient is formed on the side surface to ensure the level of the isothermal surface inside the four crucibles 7.
  • the unique design of the upper heating body 9 not only can provide heat to the silicon material, but also maintains the top temperature when the silicon is fused and directional solidification, and can also maintain a high temperature lower than the side of the crucible during directional solidification.
  • the gradient keeps the solid-liquid interface in the crucible horizontal and ensures the quality of the crystal growth. This design not only improves the crystal growth quality, but also saves energy by eliminating the side heating body.
  • the upper heating body 9 is composed of two heating circuits, and the two circuits can work at the same time or can be hot backup each other. When one heating circuit fails to work normally, another heating circuit can ensure the melting and crystal growth of the silicon material. The completion. Since the top heating can not be interrupted during ingot casting, this design greatly improves the reliability of the equipment operation and reduces the accident rate. Both sets of graphite heating bodies are connected to the external transformer through the inner and outer water cables. This design ensures that the silicon material is melted at the fastest rate when the silicon material melts, ensuring maximum energy savings and maximum yield.
  • the lower heating body 5 works simultaneously with the upper heating body 9 when the silicon is melted, so that the silicon can be melted with the highest efficiency, which not only saves energy but also shortens the working time.
  • the power of the lower heating body 5 can be gradually reduced according to the program.
  • the power is reduced to zero, the lower thermal insulation of the bottom begins to descend, and the bottom begins to dissipate heat, and the lowering speed of the lower thermal insulation body can be according to the bottom temperature curve. Control, to ensure that the temperature of the bottom of the ingot is lowered according to the set curve, and the silicon ingot is allowed to grow at a set rate.
  • the upper and lower double temperature zone resistance heating and melting silicon material is adopted, and the thermal field method is a DSS method in which the crucible and the thermal insulation body are relatively fixed, and the bottom cooling method is used to complete the directional solidification of the crystal.
  • the polycrystalline silicon ingot method of the embodiment of the invention comprises the following steps:
  • Step 1 The hydraulic system is used to lower and open the furnace bottom 3 and the silicon material is loaded into the four crucibles 7, so that the upper thermal insulation body 8 and the lower thermal insulation body 4 are closed.
  • Step 2 Raise the bottom 3 to close it and start vacuuming.
  • Step 3 When the degree of vacuum of the furnace body reaches 1 Pa, the upper heating body 9 and the lower heating body 5 are powered, and the upper and lower heating bodies are simultaneously heated at a high power to drive the silicon at a maximum speed. The material is completely melted.
  • Step 4 performing a crystal growth process, including a sub-step: gradually reducing the power of the lower heating body, so that the temperature of the bottom of the crucible is gradually decreased, and when the temperature of the bottom of the crucible 7 is lower than the melting point of the silicon material, that is, 1410 ° C. At 1414 ° C, the bottom of the crucible 7 begins to crystallize and form polysilicon.
  • the temperature drop rate at the bottom of the crucible 7 will slow down or even stop falling, at which time crystal growth may be slowed or even stopped; thus, in the embodiment of the present invention
  • the bottom heating power is reduced to zero, the lower heat retaining body 4 and the lower heating body 5 are lowered together, so that the crucible 7 radiates heat to the periphery of the furnace bottom 3, thereby making the crucible 7
  • the temperature of the lower heat retaining body 4 is controlled according to the bottom temperature curve, and the temperature of the bottom of the polycrystalline silicon ingot formed by the polycrystalline silicon is lowered according to a set curve, so that the polycrystalline silicon ingot is crystallized at a set rate.
  • the power of the upper heating body 9 is gradually reduced.
  • Step 5 Lifting the lower heat insulator 4 and the lower heating body 5, annealing the polysilicon, and then cooling the polysilicon.
  • Step 6 When the temperature of the polycrystalline silicon ingot formed by the polycrystalline silicon is lowered to below 300 ° C, the furnace bottom 3 is lowered and the polycrystalline silicon ingot is taken out.
  • the increase in the size of the ingot requires a simultaneous increase in the size of the crucible, and at the same time, the loading of a single crucible and the removal and transportation of the ingot are greatly increased.
  • the opening and cutting of large-sized silicon ingots will also present special requirements for the corresponding equipment. This will make the procurement of equipment and equipment more difficult and costly.
  • the manner in which the four spindles are described in the present invention completely avoids the above problems.
  • the subsequent silicon ingot processing equipment can be completely universal from transportation to opening and cutting, greatly reducing the equipment input of the user and improving the utilization rate of the existing equipment.
  • the user can fully use the existing ingot opening and slicing of the existing ingots, saving a lot of equipment investment. Silicon ingots can be processed and handled using existing equipment without having to reorder.
  • the polycrystalline silicon ingot furnace has a single furnace output of 1800 kg, and uses four common 450 kg crucibles, the outer diameter of the furnace is 4 meters, and the heating power is 1200 kilowatts.
  • the polycrystalline silicon ingot furnace of the preferred embodiment of the present invention saves 20% energy, 30% water saving and more than 60% solar energy than a single 450 kg ingot furnace.
  • Table 1 is a comparison table of operating parameters of a polycrystalline silicon ingot furnace and an existing 450 kg furnace type according to a preferred embodiment of the present invention.
  • Step 1 Four 870 x 870 x 420 mm quartz crucibles 7 were placed on the graphite platform 6 in the polycrystalline silicon ingot of the embodiment of the present invention, and each of the crucibles 7 was charged with 430 kg.
  • Step 2 The outside of the crucible 7 is surrounded by a graphite shield, and then the furnace bottom 3 is raised. When the furnace bottom 3 and the furnace body 2 are completely close together, vacuuming is started.
  • Step 3 When the degree of vacuum reaches 1 Pa, the upper and lower heating bodies 5 and 9 are started to be powered to start heating the molten silicon. After about 6 hours, the silicon material began to melt. Wait another 2 hours, after the silicon material is completely melted, it is kept at a temperature of 1490 ° C for about half an hour, that is, the temperature is lowered.
  • Step 4 Perform a crystal growth process, including a sub-step: the top temperature of the crucible 7 is lowered from 1460 ° C to 1400 ° C, and the bottom of the crucible 7 is cooled from 1450 ° C to 950 ° C, and the cooling time is about 32 hours.
  • This process is a crystal growth process of a silicon ingot, that is, a polycrystalline silicon ingot.
  • the lower heat retaining body 4 needs to be lowered at about 1200 ° C, otherwise the bottom temperature cannot be lowered in time.
  • Step 5 then the top temperature is lowered to 1350 ° C in 2 hours. At this time, the lower heat retaining body 4 is lifted again to be close to the upper heat insulating body 8 . It was further reduced to 1150 ° C in 3 hours and kept at 1150 ° C for 2 hours. This process is the process of annealing the ingot. After that, cool down to 900 °C in 3 hours, turn off the heating power, and let the silicon ingot automatically cool down. This is the cooling phase.
  • Step 6 When the temperature in the furnace is lower than 300 ° C, the lower heat retaining body 4 can be lowered, and the silicon ingot and the ⁇ 7 connecting guard plate are taken out from the furnace by a forklift, and placed in a non-ventilated manner. The room is naturally cooled.
  • the photo of the top crystal is as shown in FIG.
  • the resistivity of the silicon ingot was measured, and the obtained value was between 1 ⁇ cm and 2.5 ⁇ cm, and the minority carrier lifetime was tested, both of which were 2 ⁇ sec or more.
  • the silicon ingot fully meets the standard requirements of solar cells. After the solar cell was fabricated on the silicon wafer, that is, the silicon ingot, the average conversion efficiency was 16.5%.
  • Step 1 Put four 870x870x480 quartz crucibles 7 into the ingot furnace described in the embodiment of the present invention, that is, the graphite platform 6 in the polycrystalline silicon ingot furnace, and each of the crucibles 7 is charged with 490 kg. A total of 1960 kg was charged.
  • Step 2 The outside of the crucible 7 is surrounded by a graphite shield, and then the furnace bottom 3 is raised. When the furnace bottom 3 and the furnace body 2 are completely close together, vacuuming is started.
  • Step 3 When the degree of vacuum reaches 1 Pa, the upper and lower heating bodies 5 and 9 are started to be powered to start heating the molten silicon. After about 5 hours, the silicon material began to melt. After waiting for another 3 hours, the silicon material is completely melted and maintained at a temperature of 1490 ° C for about half an hour, that is, the temperature is lowered.
  • Step 4 Perform a crystal growth process, including a sub-step: the top temperature is lowered from 1460 ° C to 1400 ° C, and the bottom is cooled from 1450 ° C to 900 ° C, and the cooling time is about 34 hours.
  • This process is a crystal growth process of a silicon ingot.
  • the lower heat retaining body 4 needs to be lowered at about 1200 ° C, otherwise the bottom temperature cannot be lowered in time.
  • Step 5 then the top temperature is cooled to 1350 ° C in 2 hours. At this time, the lower heat retaining body is lifted again to the upper heat retaining body. It was further reduced to 1150 ° C in 3 hours and kept at 1150 ° C for 2 hours. This process is the process of annealing the ingot. After that, cool down to 900 °C in 3 hours, turn off the heating power, and let the silicon ingot automatically cool down. This is the cooling phase.
  • Step 6 When the temperature in the furnace is lower than 300 °C, the lower insulation body can be lowered, and the silicon ingot and the Qilian shield are taken out from the furnace by a forklift, and placed in a non-ventilated room to be naturally cooled.
  • the cutting is performed in the longitudinal direction of the silicon ingot, and a photograph of the cross section is shown in Fig. 5. After inspection, the four silicon ingots are more uniform in crystallization, indicating that the temperature field control meets the design requirements.
  • the resistivity of the silicon ingot was tested to obtain a value between 1.2 ⁇ cm and 2.5 ⁇ cm, and the minority carrier lifetime was tested, both of which were above 2 microseconds.
  • the silicon ingot fully meets the standard requirements of solar cells. After the solar cell was fabricated on the silicon wafer, the average conversion efficiency was 16.7%.
  • Step 1 Four 1020 x 1020 x 480 mm quartz crucibles 7 were placed on the graphite platform 6 in the ingot furnace described in the examples of the present invention, and each of the crucibles 7 was charged with 660 kg, and a total of 2,640 kg was charged.
  • Step 2 The outside of the crucible 7 is surrounded by a graphite shield, and then the bottom 3 is raised. When the bottom 3 and the shaft 2 are completely closed, vacuuming is started.
  • Step 3 When the degree of vacuum reaches 1 Pa, the upper and lower heating bodies 5 and 9 are started to be powered to start heating the molten silicon. After about 7 hours, the silicon material began to melt. After waiting for another 3 hours, the silicon material is completely melted and maintained at a temperature of 1500 for about half an hour, that is, the temperature is lowered.
  • Step 4 Perform a crystal growth process, including a sub-step: when the temperature is lowered to 1460 ° C, the temperature is maintained for 1 hour. Then, the top temperature is lowered from 1460 ° C to 1400 ° C, and the bottom is cooled from the current temperature to 860 ° C, and the cooling time is about 34 hours.
  • This process is a crystal growth process of a silicon ingot. In the above process, the lower heat retaining body 4 needs to be lowered at about 1200 ° C, otherwise the bottom temperature cannot be lowered in time.
  • Step 5 then the top temperature is lowered to 1350 ° C in 2 hours. At this time, the lower heat retaining body 4 is lifted again to be close to the upper heat insulating body 8 . It was further reduced to 1150 ° C in 3 hours and kept at 1150 ° C for 2 hours. This process is an ingot annealing stage. After that, cool down to 900 °C in 3 hours, turn off the heating power, and let the silicon ingot automatically cool down. This is the silicon ingot cooling stage.
  • Step 6 When the temperature in the furnace is lower than 300 °C, the lower heat retaining body 4 can be lowered, and the silicon ingot and the ⁇ 7 connecting plate are taken out from the furnace by a forklift, and placed in a non-ventilated room to be naturally cooled.
  • the resistivity of the silicon ingot was tested to obtain a value between 1.2 ⁇ cm and 2.5 ⁇ cm, and the minority carrier lifetime was tested, both of which were above 2 microseconds.
  • the ingot fully meets the standard requirements of solar cells. After the solar cell was fabricated on the silicon wafer, the average conversion efficiency was 16.7%.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Inorganic Chemistry (AREA)
  • Silicon Compounds (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)

Abstract

Disclosed is a polysilicon ingot casting furnace. A furnace body comprises an upper furnace cover (1), a furnace stack (2) and a furnace bottom (3). The furnace bottom (3) and the furnace stack (2) are connected in a hydraulic manner. A heat insulator is cubic, and the heat insulator comprises an upper heat insulator (8) and a lower heat insulator (4). A graphite platform (6) is located in the heat insulator, and four crucibles are placed on the graphite platform (6). An upper heater (9) and a lower heater (5) are both located in the heat insulator. The upper heater (9) is located under the top surface of the upper heat insulator (8). The lower heater (5) is located under the graphite platform (6). The upper heater (9) and the upper heat insulator (8) are fixed together and fixed on the furnace stack (2). The lower heater (5) and the lower heat insulator (4) are fixed together and are capable of being separated from the upper heat insulator (8) and moving downwards. Further disclosed is a polysilicon ingot casting method. The present invention can improve the throughput of a single ingot casting furnace exponentially while ensuring desired quality, can increase the utilization of existing devices while saving the investment cost of the devices, and can save energy, water and gas.

Description

多晶硅铸锭炉和多晶硅铸锭方法  Polycrystalline silicon ingot furnace and polycrystalline silicon ingot casting method Technical FieldTechnical Field
本发明涉及太阳能多晶硅铸锭领域,特别是涉及一种多晶硅铸锭炉,本发明还涉及一种多晶硅铸锭方法。  The invention relates to the field of solar polycrystalline silicon ingots, in particular to a polycrystalline silicon ingot furnace, and to a polycrystalline silicon ingot casting method.
Background ArtBackground Art
多晶硅铸锭技术是从2004年前后发展起来的。当人们发现多晶硅铸锭后一样可以进行切片并制作太阳能电池的时候,就开始了多晶硅铸锭炉的制作。与单晶炉相比,多晶硅铸锭炉具有成本低、产量大、容易处理的特点。从2007年开始,全球多晶硅光伏电池片的产量就超过了单晶硅,到了2010年,多晶硅的比例更加上升到了70%以上。 Polycrystalline silicon ingot technology was developed from around 2004. When people discovered that the polycrystalline silicon ingots could be sliced and made into solar cells, the polycrystalline silicon ingot furnace was started. Compared with single crystal furnaces, polycrystalline silicon ingot furnaces are characterized by low cost, large output, and easy handling. Since 2007, the global production of polycrystalline silicon photovoltaic cells has surpassed that of monocrystalline silicon. By 2010, the proportion of polycrystalline silicon has risen to more than 70%.
现有多晶硅铸锭炉是采用电阻或感应加热,将配比好的多晶硅熔化后,采用从底部开始冷却,逐渐向上长晶的定向凝固的方式,得到多晶硅锭的。从2004年以来,现有多晶硅铸锭炉的单炉产量从120公斤开始,到170公斤、250公斤、450公斤到660公斤。由于现有多晶硅铸锭炉的单炉产量越大,生产效率就越高,单位能耗越低,因此,不少厂家希望能够研制产量更高的多晶硅铸锭炉。 The existing polycrystalline silicon ingot furnace adopts electric resistance or induction heating to melt the polycrystalline silicon with a good ratio, and then adopts a method of solidifying from the bottom and gradually solidifying upward crystal growth to obtain a polycrystalline silicon ingot. Since 2004, the output of the existing polycrystalline silicon ingot furnace has ranged from 120 kg to 170 kg, 250 kg, 450 kg to 660 kg. Due to the larger single furnace output of the existing polycrystalline silicon ingot furnace, the higher the production efficiency and the lower the unit energy consumption, therefore, many manufacturers hope to develop a higher yield polycrystalline silicon ingot furnace.
目前,市面上能够见到的现有多晶硅铸锭炉最大的产能是660公斤,采用的是单个硅锭的方式。有公司进行了800公斤的尝试,但因为各种原因搁浅。主要原因有,如果单个硅锭的重量过大,那么尺寸必然相应加大,而在铸锭长晶阶段,硅锭底部先冷却,顶部后冷却,这样晶体才能从底部到顶部慢慢生长,顶部的冷却是靠底部硅晶体将热量不断带到底部而进行的。而如果硅锭尺寸过大,那么,由于硅晶体的导热性并不好,因此底部和顶部的温差将会过大而产生应力,此外,晶体过长会导致晶体生长过程中变形,而且,更重要的是,过大的硅锭给坩埚的制造和硅锭的处理以及硅锭的开方带来困难,不仅需要新型的配套设备,而且,给这些配套设备的坩埚等辅件的成本带来很大的挑战。因此,加大单个硅锭的方法不仅对提高单炉产量的贡献不大,而且,已经面临瓶颈。 At present, the existing polysilicon ingot furnace that can be seen on the market has a maximum capacity of 660 kg, which is a single silicon ingot. Some companies have tried 800 kilograms, but they have been stranded for various reasons. The main reason is that if the weight of a single silicon ingot is too large, the size must be correspondingly increased. In the long crystal phase of the ingot, the bottom of the ingot is cooled first, and the top is cooled, so that the crystal can grow slowly from the bottom to the top. The cooling is carried out by the bottom silicon crystal carrying the heat to the bottom. However, if the size of the silicon ingot is too large, since the thermal conductivity of the silicon crystal is not good, the temperature difference between the bottom and the top will be too large to generate stress, and in addition, the crystal is too long to cause deformation during crystal growth, and, moreover, What is important is that too large silicon ingots bring difficulties to the manufacture of tantalum and the processing of silicon ingots and the opening of silicon ingots. Not only do new types of ancillary equipment are required, but also the cost of such accessories and the like. A big challenge. Therefore, the method of increasing the single silicon ingot not only has little contribution to the improvement of the single furnace output, but also has already faced a bottleneck.
Technical ProblemTechnical Problem
本发明所要解决的技术问题是提供一种多晶硅铸锭炉,能成倍地提高单个铸锭炉产量、并能保证质量良好,不需要改变铸锭用的坩埚和硅锭存取以及开方设备,从而提高现有设备的使用率并能节省设备投资成本,能够节能、节水和节气,能节约成本;为此,本发明还提供一种使用该多晶硅铸锭炉的多晶硅铸锭方法。 The technical problem to be solved by the present invention is to provide a polycrystalline silicon ingot furnace which can double the output of a single ingot furnace and ensure good quality without changing the niobium and silicon ingot access and the opening device for the ingot. Therefore, the utilization rate of the existing equipment can be improved and the investment cost of the equipment can be saved, energy saving, water saving, and solar saving can be saved, and the cost can be saved. To this end, the present invention also provides a polycrystalline silicon ingot casting method using the polycrystalline silicon ingot furnace.
Technical SolutionTechnical Solution
为解决上述技术问题,本发明提供的多晶硅铸锭炉包括:炉体和位于所述炉体中的一保温体、一石墨平台、四个坩埚、上加热体和下加热体。所述炉体包括上炉盖、炉身和炉底,所述炉底和所述炉身采用液压连接,所述炉底能和所述炉身分开或闭合。所述保温体为立方形,所述保温体包括上保温体和下保温体。所述石墨平台位于所述保温体中并被所述保温体包围,所述四个坩埚放置于所述石墨平台上。所述上加热体和所述下加热体都位于所述保温体中,且所述上加热体位于所述坩埚顶部的所述上保温体的顶面下方、所述下加热体位于所述石墨平台下方,所述上加热体和所述上保温体固定在一起并固定于所述炉身上,所述下加热体和所述下保温体固定在一起并能一起和所述上保温体分开并向下移动。 In order to solve the above technical problems, the polycrystalline silicon ingot furnace provided by the present invention comprises: a furnace body and a heat insulator in the furnace body, a graphite platform, four crucibles, an upper heating body and a lower heating body. The furnace body includes an upper furnace cover, a furnace body and a furnace bottom, and the furnace bottom and the furnace body are hydraulically connected, and the furnace bottom can be separated or closed from the furnace body. The heat insulating body is cuboidal, and the heat insulating body comprises an upper heat insulating body and a lower heat insulating body. The graphite platform is located in the heat insulator and surrounded by the heat insulator, and the four crucibles are placed on the graphite platform. The upper heating body and the lower heating body are both located in the heat retaining body, and the upper heating body is located below the top surface of the upper heat insulating body of the top of the crucible, and the lower heating body is located at the graphite Below the platform, the upper heating body and the upper heat retaining body are fixed together and fixed to the furnace body, and the lower heating body and the lower heat insulating body are fixed together and can be separated from the upper heat insulating body together Move Downward.
进一步的改进是,所述四个坩埚在所述石墨平台上的放置方式为呈田字形摆放。 A further improvement is that the four crucibles are placed on the graphite platform in a field shape.
进一步的改进是,所述四个坩埚的边长分别为720毫米~1200毫米。 A further improvement is that the sides of the four turns are 720 mm to 1200 mm, respectively.
进一步的改进是,所述四个坩埚为用于太阳能级多晶硅铸锭的标准规格坩埚或特殊规格的坩埚。 A further improvement is that the four crucibles are standard gauges or special gauges for solar grade polycrystalline silicon ingots.
进一步的改进是,所述上加热体完全覆盖住所述四个坩埚、且所述上加热体的外缘尺寸大于所述四个坩埚的外缘尺寸5%~30%,所述四个坩埚的外侧面和所述保温体相隔有一定的距离,所述上加热体的处于所述四个坩埚的外缘外部的部分用于对所述四个坩埚的侧面加热。 A further improvement is that the upper heating body completely covers the four turns, and the outer edge of the upper heating body is larger than the outer edge of the four turns by 5% to 30%, and the four turns are The outer side surface and the heat retaining body are spaced apart by a distance, and a portion of the upper heating body outside the outer edge of the four turns is used to heat the sides of the four turns.
进一步的改进是,在各所述坩埚的周围放置有护板。 A further improvement is that a shield is placed around each of the turns.
进一步的改进是,所述上加热体由两个加热回路组成,所述两个加热回路能同时工作、也能互为热备份。 A further improvement is that the upper heating body is composed of two heating circuits, which can work simultaneously and can also be hot backups to each other.
进一步的改进是,所述下保温体和升降传动机构连接,所述下保温体下降是通过升降传动机构实现。 A further improvement is that the lower heat retaining body is connected to the lifting and lowering mechanism, and the lower heat insulating body is lowered by the lifting and lowering mechanism.
为解决上述技术问题,本发明提供的多晶硅铸锭方法,包括如下步骤: In order to solve the above technical problem, the polycrystalline silicon ingot method provided by the present invention comprises the following steps:
步骤一、用液压装置放下并打开所述炉底并在所述四个坩埚中装入硅料, Step 1. Lowering and opening the bottom of the furnace with a hydraulic device and loading the silicon material into the four crucibles,
步骤二、上升所述炉底使其闭合,开始抽真空。 Step 2: Raise the bottom of the furnace to close it and start vacuuming.
步骤三、当所述炉体的真空度达到1Pa时,给所述上加热体和所述下加热体送电,开始加热所述硅料并使所述硅料完全熔化。 Step 3: When the degree of vacuum of the furnace body reaches 1 Pa, the upper heating body and the lower heating body are powered, and the heating of the silicon material is started and the silicon material is completely melted.
步骤四、进行长晶过程,包括分步骤:逐步降低所述下加热体的功率,使所述坩埚底部温度逐渐降低,当所述坩埚底部温度低于所述硅料的熔点时所述坩埚底部开始结晶并形成多晶硅;当所述下加热体的功率降到0时,将所述下保温体和所述下加热体一起下降,使所述多晶硅继续往上生长。 Step 4, performing a crystal growth process, comprising the steps of: gradually reducing the power of the lower heating body to gradually lower the temperature of the bottom of the crucible, and when the bottom temperature of the crucible is lower than the melting point of the silicon material Crystallization starts and polysilicon is formed; when the power of the lower heating body drops to zero, the lower heat insulator and the lower heater are lowered together, so that the polysilicon continues to grow upward.
步骤五、将所述下保温体和所述下加热体提升,对所述多晶硅进行退火,接着再对所述多晶硅进行冷却。 Step 5: lifting the lower heat insulator and the lower heat body, annealing the polysilicon, and then cooling the polysilicon.
步骤六、当所述多晶硅形成的多晶硅铸锭的温度降低到300℃以下时,放下所述炉底并将所述多晶硅铸锭取出。 Step 6. When the temperature of the polycrystalline silicon ingot formed by the polysilicon is lowered to 300 ° C or lower, the bottom of the furnace is lowered and the polycrystalline silicon ingot is taken out.
Advantageous EffectsAdvantageous Effects
本发明的有益效果为: The beneficial effects of the invention are:
1 、本发明多晶硅铸锭炉具有四个坩埚,能实现一炉生产四个多晶硅铸锭,从而能成倍地提高单个铸锭炉产量。 1 The polycrystalline silicon ingot furnace of the invention has four crucibles, and can realize four furnaces for producing four polycrystalline silicon ingots, thereby multiplying the output of the single ingot furnace.
2 、本发明多晶硅铸锭炉的所述上加热体的边缘的尺寸大于所述四个坩埚的边缘尺寸的设计,能使所述上加热体在上部加热的同时,实现对所述四个坩埚的侧面加热,在多晶硅生长过程中能在所述四个坩埚的侧面形成从顶部到底部温度逐渐降低的梯度,从而能够保证各所述坩埚内的等温面为水平状,能够解决坩埚的外侧的散热快而造成的等温面不水平的问题。良好的等温面最终能够提高多晶硅铸锭的质量。同时,本发明多晶硅铸锭炉不需要通过增大各多晶硅铸锭的尺寸方法来提高多晶硅铸锭的产量,能够避免大尺寸的多晶硅铸锭造成的坩埚的水平温场难以保持、垂直方向的温差会很大以及由此造成的晶体生长质量变差的问题,从而能形成良好的柱状晶,提高产品的质量。 2 The design of the edge of the upper heating body of the polycrystalline silicon ingot furnace of the present invention is larger than the size of the edge of the four crucibles, so that the upper heating body can be heated at the upper portion to realize the four crucibles. The side heating can form a gradient gradually decreasing from the top to the bottom on the sides of the four turns during the growth of the polysilicon, so that the isothermal surface in each of the crucibles can be horizontal, and the heat dissipation on the outer side of the crucible can be solved. The problem of the level of the isothermal surface is not high. A good isothermal surface can ultimately improve the quality of the polycrystalline silicon ingot. At the same time, the polycrystalline silicon ingot furnace of the present invention does not need to increase the size of each polycrystalline silicon ingot to increase the yield of the polycrystalline silicon ingot, and can avoid the horizontal temperature field of the crucible caused by the large-sized polycrystalline silicon ingot being difficult to maintain, and the vertical temperature difference It will be very large and the resulting crystal growth quality will be deteriorated, so that good columnar crystals can be formed and the quality of the product can be improved.
3 、本发明多晶硅铸锭炉并不需要改变铸锭用的坩埚和硅锭存取以及开方设备,即本发明多晶硅铸锭炉能够和现有生产线上的设备兼容,从而能够节约投资成本,并能提高生产效率。 3 The polycrystalline silicon ingot furnace of the present invention does not need to change the bismuth and silicon ingot access and the opening device for the ingot, that is, the polycrystalline silicon ingot furnace of the invention can be compatible with the equipment on the existing production line, thereby saving investment cost, and Can improve production efficiency.
4 、本发明的四个坩埚呈田字型放置并在中间留有一定的空间用来放置坩埚护板的放置方式,其隔热笼面积和额定产量之比或者说硅料所耗用绝热体的比表面积显著低于现有单锭的炉型;另外本发明的所述上加热体的设计能够省略侧面加热体,从而能使本发明的炉型具有显著的节能效果,同时本发明还能节水和节气,从而能节约成本。 4 The four enamels of the present invention are placed in a field and have a certain space in the middle for placing the slabs, the ratio of the insulating cage area to the rated output or the insulation of the silicon material. The specific surface area is significantly lower than that of the existing single ingot; in addition, the design of the upper heating body of the present invention can omit the side heating body, so that the furnace type of the present invention can have significant energy saving effect, and the present invention can also be used Water and solar terms can save costs.
Description of DrawingsDescription of Drawings
图1是本发明实施例多晶硅铸锭炉的剖面示意图; 1 is a schematic cross-sectional view showing a polycrystalline silicon ingot furnace according to an embodiment of the present invention;
图2是本发明实施例一多晶硅铸锭方法生产的多晶硅锭的顶部结晶照片; 2 is a top crystal photograph of a polycrystalline silicon ingot produced by a polycrystalline silicon ingot method according to an embodiment of the present invention;
图3是本发明实施例一多晶硅铸锭方法生产的多晶硅锭的纵向截面照片; 3 is a longitudinal cross-sectional photograph of a polycrystalline silicon ingot produced by a polycrystalline silicon ingot method according to an embodiment of the present invention;
图4是本发明实施例二多晶硅铸锭方法生产的多晶硅锭的顶部结晶照片; 4 is a top crystal photograph of a polycrystalline silicon ingot produced by the method of polycrystalline silicon ingot according to the second embodiment of the present invention;
图5是本发明实施例二多晶硅铸锭方法生产的多晶硅锭的纵向截面照片; Figure 5 is a longitudinal cross-sectional photograph of a polycrystalline silicon ingot produced by the method of polycrystalline silicon ingot according to the second embodiment of the present invention;
图6是本发明实施例三多晶硅铸锭方法生产的多晶硅锭的顶部结晶照片; 6 is a top crystal photograph of a polycrystalline silicon ingot produced by the method of three polycrystalline silicon ingots according to an embodiment of the present invention;
图7是本发明实施例三多晶硅铸锭方法生产的多晶硅锭的纵向截面照片。 Figure 7 is a longitudinal cross-sectional photograph of a polycrystalline silicon ingot produced by the third polycrystalline silicon ingot method of the embodiment of the present invention.
Best ModeBest Mode
Mode for InventionMode for Invention
如图1所示,是本发明实施例多晶硅铸锭炉的剖面示意图。 As shown in FIG. 1, it is a schematic cross-sectional view of a polycrystalline silicon ingot furnace according to an embodiment of the present invention.
本发明实施例多晶硅铸锭炉包括:炉体和位于所述炉体中的一保温体、一石墨平台6、四个坩埚7、上加热体9和下加热体5。 The polycrystalline silicon ingot furnace of the embodiment of the invention comprises: a furnace body and a heat insulator in the furnace body, a graphite platform 6, four crucibles 7, an upper heating body 9 and a lower heating body 5.
所述炉体包括上炉盖1、炉身2和炉底3,所述炉底3和所述炉身2采用液压连接,通过所述液压装置能将所述炉底3和所述炉身2分开或闭合,分开时用于装卸硅料或多晶硅锭。所述炉体外壳采用不锈钢水冷炉壳。所述上炉盖1起着固定所述上部加热体9、连接加热水电缆、安装顶部测温装置、连接通气管路的作用。所述炉身2固定侧面绝热体即组成所述保温体的绝缘体,同时也连接真空管路。所述炉身2通过四个支架支撑在地面上,所述上炉盖1直接放置在所述炉身2上,并通过法兰密封;所述炉底3则是通过液压系统悬挂在所述炉身2上,在液压控制炉底提升封炉时,也通过法兰进行真空密封。所述炉底3与所述炉身2采用液压悬挂机构,液压机构可以控制所述炉底3停止在行程内的任意高度。所述炉底3设有多个测温点,可以对每个坩埚的多个高度和不同的位置进行测温,使得炉内的底部温区状况能够清晰的在显示器上显示出来,并提供给控制系统。 The furnace body comprises an upper furnace cover 1, a furnace body 2 and a furnace bottom 3, and the furnace bottom 3 and the furnace body 2 are hydraulically connected, and the furnace bottom 3 and the furnace body can be passed by the hydraulic device 2 Separate or closed, used to load and unload silicon or polycrystalline silicon ingots. The furnace body shell is made of a stainless steel water-cooled furnace shell. The upper furnace cover 1 functions to fix the upper heating body 9, connect the heating water cable, install the top temperature measuring device, and connect the ventilation pipe. The furnace body 2 is fixed with a side insulator, that is, an insulator constituting the heat insulator, and is also connected to a vacuum pipeline. The furnace body 2 is supported on the ground by four brackets, the upper furnace cover 1 is directly placed on the furnace body 2 and sealed by a flange; the furnace bottom 3 is suspended by a hydraulic system On the furnace body 2, when the hydraulically controlled furnace bottom is lifted and sealed, the vacuum sealing is also performed through the flange. The hearth 3 and the furnace body 2 adopt a hydraulic suspension mechanism, and the hydraulic mechanism can control the furnace bottom 3 to stop at any height within the stroke. The furnace bottom 3 is provided with a plurality of temperature measuring points, which can measure the temperature of each raft and different positions, so that the bottom temperature condition in the furnace can be clearly displayed on the display and provided to Control System.
所述保温体为立方形,所述保温体包括上保温体8和下保温体4。所述石墨平台6位于所述保温体中并被所述保温体包围,所述四个坩埚7放置于所述石墨平台6上。所述坩埚的大小可以采用市面上标准的多晶硅铸锭坩埚如:450公斤、500公斤、660公斤或800公斤等,所述四个坩埚的边长分别为720毫米~1200毫米。 The heat insulating body is cuboidal, and the heat insulating body includes an upper heat insulating body 8 and a lower heat insulating body 4. The graphite platform 6 is located in the heat insulator and surrounded by the heat insulator, and the four turns 7 are placed on the graphite platform 6. The size of the crucible may be a standard polycrystalline silicon ingot such as 450 kg, 500 kg, 660 kg or 800 kg, and the sides of the four crucibles are respectively 720 mm to 1200 mm.
所述四个坩埚7呈田字型放置,中间留有一定的空间用来放置坩埚护板。由于4锭也即对应四个坩埚7摆放的几何结构,其隔热笼面积和额定产量之比或者说硅料所耗用绝热体的比表面积显著低于单锭的炉型。因而该炉型具有显著的节能效果,单位能耗相对单锭炉型降低约20%。同时相对于单锭炉型,氩气消耗降低了约60%。所述石墨平台6的尺寸有一定的余量,可以略大或略小。 The four crucibles 7 are placed in a field shape with a certain space in the middle for placing the crucible guards. Due to the geometry of 4 ingots corresponding to the arrangement of the four crucibles 7, the ratio of the area of the insulating cage to the rated output or the specific surface area of the insulator used for the silicon material is significantly lower than that of the single ingot. Therefore, the furnace has a remarkable energy saving effect, and the unit energy consumption is reduced by about 20% compared to the single furnace type. At the same time, the argon consumption is reduced by about 60% relative to the single furnace type. The size of the graphite platform 6 has a certain margin and may be slightly larger or slightly smaller.
所述上加热体9和所述下加热体5都位于所述保温体中,且所述上加热体8位于所述坩埚7顶部的所述上保温体8的顶面下方、所述下加热体5位于所述石墨平台6下方,所述上加热体9和所述上保温体8固定在一起并固定于所述炉身2上,所述下加热体5和所述下保温体4固定在一起并能一起和所述上保温体8分开并向下移动。所述下保温体4和升降传动机构连接,并通过所述升降传动机构实现下降。在铸锭过程中,所述下保温体4下降,所述石墨平台6不下降;在装料与卸料时,所述下保温体4、石墨平台6(连带四个坩埚7)才一起下降。 The upper heating body 9 and the lower heating body 5 are both located in the heat retaining body, and the upper heating body 8 is located below the top surface of the upper heat insulating body 8 at the top of the crucible 7, and the lower heating The body 5 is located below the graphite platform 6, the upper heating body 9 and the upper heat retaining body 8 are fixed together and fixed on the furnace body 2, and the lower heating body 5 and the lower heat insulating body 4 are fixed. Together and together with the upper insulation 8 and moving downwards. The lower heat retaining body 4 is connected to the lifting and lowering mechanism, and is lowered by the lifting and lowering mechanism. During the ingot casting process, the lower heat retaining body 4 is lowered, and the graphite platform 6 is not lowered; when the loading and unloading are performed, the lower heat insulating body 4 and the graphite platform 6 (with four crucibles 7) are lowered together. .
所述上加热体9完全覆盖住所述四个坩埚7、且所述上加热体9的外缘尺寸大于所述四个坩埚7的外缘尺寸5%~30%,所述四个坩埚的外侧面和所述保温体相隔有一定的距离,所述上加热体9的处于所述四个坩埚7的外缘外部的部分用于对所述四个坩埚的侧面加热。用于太阳能光伏电池的多晶硅的生长质量与最后的电池效率有很大的关系。如果希望能够得到好的电池质量,就需要晶粒较大,而且晶柱生长方向尽量垂直。为此,就要求在晶体生长时,所述坩埚7内部的等温面尽量呈水平状。由于本发明所采用的是上下加热,没有侧面加热,因此,在晶体生长时,很容易造成四个坩埚外侧过冷,而导致坩埚的外围先冷却,使得晶体从外向里生长。所以本发明在所述上部加热体9的外缘加大了尺寸,并使坩埚7的外侧面与保温体保持一定的距离,这样,坩埚7的外侧面就能够由所述上部加热体9一直在进行加热。而且,由于所述上部加热体9对上部的加热较大,底部的温度较低,因此,刚好在侧面形成下低上高的温度梯度,保证了四个坩埚7内部的等温面的水平。所述上部加热体9的独特设计,不仅能够向硅料提供热量,进行熔硅和在定向凝固时保持顶部温度,而且,还可以在进行定向凝固时对坩埚侧面保持一个上高下低的温度梯度,使得坩埚内的固液界面保持水平,保证长晶的质量。该设计不仅能够提高晶体生长质量,而且还由于省去了侧面加热体,大大节约了能源。 The upper heating body 9 completely covers the four crucibles 7, and the outer edge of the upper heating body 9 has a size larger than the outer edge of the four crucibles 7 by 5% to 30%. The side surface and the heat insulator are spaced apart by a distance, and a portion of the upper heating body 9 outside the outer edge of the four turns 7 is used to heat the sides of the four turns. The growth quality of polycrystalline silicon used in solar photovoltaic cells has a strong relationship with the final cell efficiency. If you want to get good battery quality, you need a larger grain size and the crystal column growth direction is as vertical as possible. For this reason, it is required that the isothermal surface inside the crucible 7 is as horizontal as possible during crystal growth. Since the invention adopts up-and-down heating and no side heating, when the crystal grows, it is easy to cause the outer sides of the four crucibles to be supercooled, and the periphery of the crucible is first cooled, so that the crystal grows from the outside to the inside. Therefore, the outer diameter of the upper heating body 9 is increased in size, and the outer side surface of the crucible 7 is kept at a certain distance from the heat insulating body, so that the outer side surface of the crucible 7 can be always used by the upper heating body 9. Heating is taking place. Moreover, since the upper heating body 9 has a large heating to the upper portion and a lower temperature at the bottom portion, a lower temperature gradient is formed on the side surface to ensure the level of the isothermal surface inside the four crucibles 7. The unique design of the upper heating body 9 not only can provide heat to the silicon material, but also maintains the top temperature when the silicon is fused and directional solidification, and can also maintain a high temperature lower than the side of the crucible during directional solidification. The gradient keeps the solid-liquid interface in the crucible horizontal and ensures the quality of the crystal growth. This design not only improves the crystal growth quality, but also saves energy by eliminating the side heating body.
所述上部加热体9由两个加热回路组成,两个回路既可以同时工作,也可以互为热备份,在一个加热回路故障不能正常工作时,另外一个加热回路能够保证硅料熔化和长晶的完成。由于铸锭时顶部加热是不能中断的,这一设计大大提高了设备工作的可靠性,减少了事故发生率,两套石墨加热体均通过内外水电缆与外部的变压器连接。这样的设计,可以保证在硅料熔化时能够以最快的速度熔化硅料,保证最大的节能和最高的产率。 The upper heating body 9 is composed of two heating circuits, and the two circuits can work at the same time or can be hot backup each other. When one heating circuit fails to work normally, another heating circuit can ensure the melting and crystal growth of the silicon material. The completion. Since the top heating can not be interrupted during ingot casting, this design greatly improves the reliability of the equipment operation and reduces the accident rate. Both sets of graphite heating bodies are connected to the external transformer through the inner and outer water cables. This design ensures that the silicon material is melted at the fastest rate when the silicon material melts, ensuring maximum energy savings and maximum yield.
所述下加热体5在熔硅时与所述上加热体9同时工作,可以保证以最高的效率进行熔硅,不仅节约能源,还可以缩短工作时间。在开始定向凝固时,所述下加热体5功率可以按照程序逐渐降低,当功率降为零时,底部的下保温体开始下降,底部开始散热,底部下保温体的下降速度根据底部温度曲线可控,保证硅锭底部的温度按照设定的曲线下降,促使硅锭按照设定的速率进行晶体的生长。 The lower heating body 5 works simultaneously with the upper heating body 9 when the silicon is melted, so that the silicon can be melted with the highest efficiency, which not only saves energy but also shortens the working time. When the directional solidification is started, the power of the lower heating body 5 can be gradually reduced according to the program. When the power is reduced to zero, the lower thermal insulation of the bottom begins to descend, and the bottom begins to dissipate heat, and the lowering speed of the lower thermal insulation body can be according to the bottom temperature curve. Control, to ensure that the temperature of the bottom of the ingot is lowered according to the set curve, and the silicon ingot is allowed to grow at a set rate.
本发明实施例多晶硅铸锭方法采用的是上下双温区电阻加热熔化硅料,采用的热场方式是坩埚和保温体均相对固定,底部降温方式来完成晶体的定向凝固的DSS方式。本发明实施例多晶硅铸锭方法包括如下步骤: In the polycrystalline silicon ingot casting method, the upper and lower double temperature zone resistance heating and melting silicon material is adopted, and the thermal field method is a DSS method in which the crucible and the thermal insulation body are relatively fixed, and the bottom cooling method is used to complete the directional solidification of the crystal. The polycrystalline silicon ingot method of the embodiment of the invention comprises the following steps:
步骤一、用液压装置放下并打开所述炉底3并在所述四个坩埚7中装入硅料,使所述上保温体8和所述下保温体4闭合。 Step 1. The hydraulic system is used to lower and open the furnace bottom 3 and the silicon material is loaded into the four crucibles 7, so that the upper thermal insulation body 8 and the lower thermal insulation body 4 are closed.
步骤二、上升所述炉底3使其闭合,开始抽真空。 Step 2: Raise the bottom 3 to close it and start vacuuming.
步骤三、当所述炉体的真空度达到1Pa时,给所述上加热体9和所述下加热体5送电,所述上下加热体同时大功率加热,以最大的速度将所述硅料完全熔化。 Step 3: When the degree of vacuum of the furnace body reaches 1 Pa, the upper heating body 9 and the lower heating body 5 are powered, and the upper and lower heating bodies are simultaneously heated at a high power to drive the silicon at a maximum speed. The material is completely melted.
步骤四、进行长晶过程,包括分步骤:逐步降低所述下加热体的功率,使所述坩埚底部温度逐渐降低,当所述坩埚7底部温度低于所述硅料的熔点即1410℃~1414℃时所述坩埚7底部开始结晶并形成多晶硅。当所述下加热体5的功率降到0时,所述坩埚7底部的温度下降速度将变慢甚至停止下降,这时,会导致晶体生长变慢甚至停止;为此,在本发明实施例中当底部加热功率降到零后,将所述下保温体4和所述下加热体5一起下降,这样,所述坩埚7会向所述炉底3四周散发热量,从而使所述坩埚7温度不断地下降;所述下保温体4的下降速度根据底部温度曲线可控,保证所述多晶硅形成的多晶硅锭底部的温度按照设定的曲线下降,促使多晶硅锭按照设定的速率进行晶体的生长。在经过计算的时间内,当所述多晶硅生长到所述坩埚7的顶部时,逐步降低所述上加热体9的功率。 Step 4: performing a crystal growth process, including a sub-step: gradually reducing the power of the lower heating body, so that the temperature of the bottom of the crucible is gradually decreased, and when the temperature of the bottom of the crucible 7 is lower than the melting point of the silicon material, that is, 1410 ° C. At 1414 ° C, the bottom of the crucible 7 begins to crystallize and form polysilicon. When the power of the lower heating body 5 drops to zero, the temperature drop rate at the bottom of the crucible 7 will slow down or even stop falling, at which time crystal growth may be slowed or even stopped; thus, in the embodiment of the present invention When the bottom heating power is reduced to zero, the lower heat retaining body 4 and the lower heating body 5 are lowered together, so that the crucible 7 radiates heat to the periphery of the furnace bottom 3, thereby making the crucible 7 The temperature of the lower heat retaining body 4 is controlled according to the bottom temperature curve, and the temperature of the bottom of the polycrystalline silicon ingot formed by the polycrystalline silicon is lowered according to a set curve, so that the polycrystalline silicon ingot is crystallized at a set rate. Growing. During the calculated time, when the polysilicon is grown to the top of the crucible 7, the power of the upper heating body 9 is gradually reduced.
步骤五、将所述下保温体4和所述下加热体5提升,对所述多晶硅进行退火,接着再对所述多晶硅进行冷却。 Step 5: Lifting the lower heat insulator 4 and the lower heating body 5, annealing the polysilicon, and then cooling the polysilicon.
步骤六、当所述多晶硅形成的多晶硅铸锭的温度降低到300℃以下时,放下所述炉底3并将所述多晶硅铸锭取出。 Step 6. When the temperature of the polycrystalline silicon ingot formed by the polycrystalline silicon is lowered to below 300 ° C, the furnace bottom 3 is lowered and the polycrystalline silicon ingot is taken out.
本发明实施例所叙述的采用一炉多锭的方式提高单炉的铸锭产量,而不是采用一味单纯地加大锭的尺寸的方法,带来了许多好处。 The method of increasing the ingot yield of a single furnace by using a multi-ingot furnace as described in the embodiment of the present invention, rather than adopting a method of simply increasing the size of the ingot, brings many advantages.
首先,如果单锭的尺寸过大过高,不仅每个坩埚内部的水平温场难以保持,垂直方向的温差也会很大,导致晶体生长质量变差。实验表明,当硅锭尺寸超过360mm时,硅锭从底部到顶部很难长成完好的柱状晶,而柱状晶是多晶硅电池硅片所必须的。 First, if the size of a single ingot is too large or too high, not only is the horizontal temperature field inside each crucible difficult to maintain, but the temperature difference in the vertical direction is also large, resulting in deterioration of crystal growth quality. Experiments have shown that when the size of the ingot exceeds 360 mm, it is difficult for the ingot to grow into a good columnar crystal from the bottom to the top, and the columnar crystal is necessary for the polycrystalline silicon wafer.
此外,硅锭尺寸的加大,需要坩埚同步加大,同时,单个坩埚的装入和硅锭的取出和运送都会增加很大的难度。此外,大尺寸的硅锭的开方和截断也会提出对相应设备的特殊需求。这会造成设备和坩埚采购的难度加大,成本增高。 In addition, the increase in the size of the ingot requires a simultaneous increase in the size of the crucible, and at the same time, the loading of a single crucible and the removal and transportation of the ingot are greatly increased. In addition, the opening and cutting of large-sized silicon ingots will also present special requirements for the corresponding equipment. This will make the procurement of equipment and equipment more difficult and costly.
因此,本发明所叙述的一炉四锭的方式完全避免了上述问题。使用本发明的铸锭炉,后续的硅锭处理设备,从运送到开方和截断,设备可以完全通用,大大减少了用户的设备投入,提高现有设备的使用率。因为采用标准尺寸和重量的硅锭,使得用户能够充分沿用现有的硅锭的破锭开方和切片的全部设备,节约大量的设备投资。硅锭的处理和搬运都可以采用现有的设备,不必重新订购。 Therefore, the manner in which the four spindles are described in the present invention completely avoids the above problems. By using the ingot furnace of the invention, the subsequent silicon ingot processing equipment can be completely universal from transportation to opening and cutting, greatly reducing the equipment input of the user and improving the utilization rate of the existing equipment. Because of the standard size and weight of the ingot, the user can fully use the existing ingot opening and slicing of the existing ingots, saving a lot of equipment investment. Silicon ingots can be processed and handled using existing equipment without having to reorder.
本发明一较佳实施例多晶硅铸锭炉的单炉产量为1800公斤的炉子,采用四个通用的450公斤坩埚,炉体外径为4米,加热功率为1200千瓦。经过试验,本发明一较佳实施例多晶硅铸锭炉比单个450公斤的铸锭炉节能20%,节水30%,节气60%以上。如表1所述为本发明一较佳实施例多晶硅铸锭炉与现有450公斤炉型的运行参数比较表。 In a preferred embodiment of the present invention, the polycrystalline silicon ingot furnace has a single furnace output of 1800 kg, and uses four common 450 kg crucibles, the outer diameter of the furnace is 4 meters, and the heating power is 1200 kilowatts. After testing, the polycrystalline silicon ingot furnace of the preferred embodiment of the present invention saves 20% energy, 30% water saving and more than 60% solar energy than a single 450 kg ingot furnace. Table 1 is a comparison table of operating parameters of a polycrystalline silicon ingot furnace and an existing 450 kg furnace type according to a preferred embodiment of the present invention.
表1 Table 1
项目 project 本发明一较佳实施例多晶硅铸锭炉 Polycrystalline silicon ingot furnace according to a preferred embodiment of the present invention 现有450公斤炉型 Existing 450 kg furnace type
单炉产量 Single furnace output 1800 公斤~2000公斤 1800 kg to 2000 kg 450 公斤~500公斤 450 kg to 500 kg
单个硅锭重量 Single ingot weight 450 公斤~500公斤 450 kg to 500 kg 450 公斤~500公斤 450 kg to 500 kg
单炉最大年产硅锭数量 The maximum annual output of silicon ingots in a single furnace 576 锭 576 spindles 144 锭 144 spindles
单炉最大年产量 Maximum annual output of single furnace 288 吨 288 tons 72 吨 72 tons
100MW 硅片所需设备台数 Number of equipment required for 100MW silicon wafer ≤4 ≤4 ≤16 ≤16
硅锭成品规格 Silicon ingot finished product specifications 840×840×(≥260)mm 840×840×(≥260)mm 840×840×(≥260)mm 840×840×(≥260)mm
单次加工周期 Single processing cycle 58 小时 58 hours 58 小时 58 hours
装机功率 Installed power 1200KVA 1200KVA 三组加热,单组最大350 KVA Three groups of heating, single group up to 350 KVA
单位电耗* Unit power consumption* ≤8kwh/kg ≤8kwh/kg ≤10kwh/kg ≤10kwh/kg
循环水流量 Circulating water flow 560L /min 560L / min 200L /min 200L / min
气耗 Gas consumption <80m3 <80m 3 <58m3 <58m 3
* 两种炉型电耗值均是在采用普通硬毡做隔热层时测量所得。 * The power consumption values of both furnace types are measured when using ordinary hard felt as insulation layer.
本发明实施例一多晶硅铸锭方法的步骤如下: The steps of the polycrystalline silicon ingot method of the embodiment of the present invention are as follows:
步骤一、将四个870x870x420mm的石英坩埚7放入本发明实施例多晶硅铸锭内的所述石墨平台6上,每个所述坩埚7装料430公斤。 Step 1. Four 870 x 870 x 420 mm quartz crucibles 7 were placed on the graphite platform 6 in the polycrystalline silicon ingot of the embodiment of the present invention, and each of the crucibles 7 was charged with 430 kg.
步骤二、所述坩埚7外面用石墨护板包围保护,然后上升所述炉底3,当所述炉底3与所述炉身2完全并拢后,开始抽真空。 Step 2: The outside of the crucible 7 is surrounded by a graphite shield, and then the furnace bottom 3 is raised. When the furnace bottom 3 and the furnace body 2 are completely close together, vacuuming is started.
步骤三、当真空度达到1Pa时,开始给所述上下加热体5和9送电,开始加热熔硅。大约6小时后,硅料开始融化。再等2小时,硅料全部熔化后,在温度1490℃处保持大约半小时,即开始降温。 Step 3: When the degree of vacuum reaches 1 Pa, the upper and lower heating bodies 5 and 9 are started to be powered to start heating the molten silicon. After about 6 hours, the silicon material began to melt. Wait another 2 hours, after the silicon material is completely melted, it is kept at a temperature of 1490 ° C for about half an hour, that is, the temperature is lowered.
步骤四、进行长晶过程,包括分步骤:所述坩埚7的顶部温度从1460℃向1400℃降温,所述坩埚7的底部则从1450℃向950℃降温,降温时间大约32小时。本过程为硅锭即多晶硅锭的长晶过程。在上述过程中,所述下保温体4在大约1200℃时需要下降,否则底部温度无法按照时间下降。 Step 4: Perform a crystal growth process, including a sub-step: the top temperature of the crucible 7 is lowered from 1460 ° C to 1400 ° C, and the bottom of the crucible 7 is cooled from 1450 ° C to 950 ° C, and the cooling time is about 32 hours. This process is a crystal growth process of a silicon ingot, that is, a polycrystalline silicon ingot. In the above process, the lower heat retaining body 4 needs to be lowered at about 1200 ° C, otherwise the bottom temperature cannot be lowered in time.
步骤五、然后顶部温度用2小时降温到1350℃,此时,将所述下保温体4再次提升到与所述上保温体8并拢。再用3小时降低到1150℃,并在1150℃保温2小时。本过程为硅锭退火的过程。之后,用3小时降温到900℃,关闭加热电源,让硅锭自动降温。此为冷却阶段。 Step 5, then the top temperature is lowered to 1350 ° C in 2 hours. At this time, the lower heat retaining body 4 is lifted again to be close to the upper heat insulating body 8 . It was further reduced to 1150 ° C in 3 hours and kept at 1150 ° C for 2 hours. This process is the process of annealing the ingot. After that, cool down to 900 °C in 3 hours, turn off the heating power, and let the silicon ingot automatically cool down. This is the cooling phase.
步骤六、当所述炉内温度低于300℃时,即可降下所述下保温体4,将硅锭与所述坩埚7连护板一起用叉车从所述炉内取出,放置在不通风的房间内自然冷却。 Step 6. When the temperature in the furnace is lower than 300 ° C, the lower heat retaining body 4 can be lowered, and the silicon ingot and the 坩埚 7 connecting guard plate are taken out from the furnace by a forklift, and placed in a non-ventilated manner. The room is naturally cooled.
对采用本发明实施例一多晶硅铸锭方法生产的上述硅锭的外表面去除后,可见顶部的结晶照片如图2所示。 After the outer surface of the above silicon ingot produced by the polycrystalline silicon ingot method of the embodiment of the present invention is removed, the photo of the top crystal is as shown in FIG.
沿所述硅锭的纵向进行切割,截面的照片如图3所示。经过检验,四个硅锭结晶较均匀,表明温场控制达到设计要求。 Cutting is performed in the longitudinal direction of the silicon ingot, and a photograph of the cross section is shown in FIG. After inspection, the four silicon ingots are more uniform in crystallization, indicating that the temperature field control meets the design requirements.
测试所述硅锭的电阻率,得到的值在1Ω·cm~2.5Ω·cm之间,测试少子寿命,均在2微秒以上。 The resistivity of the silicon ingot was measured, and the obtained value was between 1 Ω·cm and 2.5 Ω·cm, and the minority carrier lifetime was tested, both of which were 2 μsec or more.
所述硅锭完全满足太阳能电池的标准要求。后经过对该硅片即所述硅锭制作太阳能电池,得到的平均转换效率为16.5%。 The silicon ingot fully meets the standard requirements of solar cells. After the solar cell was fabricated on the silicon wafer, that is, the silicon ingot, the average conversion efficiency was 16.5%.
本发明实施例二多晶硅铸锭方法的步骤如下: The steps of the method for ingot casting polycrystalline silicon according to the second embodiment of the present invention are as follows:
步骤一、将四个870x870x480的石英坩埚7放入本发明实施例所叙述的铸锭炉即所述多晶硅铸锭炉内的所述石墨平台6上,每个所述坩埚7装料490公斤,共装料1960公斤。 Step 1. Put four 870x870x480 quartz crucibles 7 into the ingot furnace described in the embodiment of the present invention, that is, the graphite platform 6 in the polycrystalline silicon ingot furnace, and each of the crucibles 7 is charged with 490 kg. A total of 1960 kg was charged.
步骤二、所述坩埚7外面用石墨护板包围保护,然后上升所述炉底3,当所述炉底3与所述炉身2完全并拢后,开始抽真空。 Step 2: The outside of the crucible 7 is surrounded by a graphite shield, and then the furnace bottom 3 is raised. When the furnace bottom 3 and the furnace body 2 are completely close together, vacuuming is started.
步骤三、当真空度达到1Pa时,开始给所述上下加热体5和9送电,开始加热熔硅。大约5小时后,硅料开始融化。再等3小时,硅料全部熔化后,在温度1490℃处保持大约半小时,即开始降温。 Step 3: When the degree of vacuum reaches 1 Pa, the upper and lower heating bodies 5 and 9 are started to be powered to start heating the molten silicon. After about 5 hours, the silicon material began to melt. After waiting for another 3 hours, the silicon material is completely melted and maintained at a temperature of 1490 ° C for about half an hour, that is, the temperature is lowered.
步骤四、进行长晶过程,包括分步骤:顶部温度从1460℃向1400℃降温,底部则从1450℃向900℃降温,降温时间大约34小时。本过程为硅锭的长晶过程。在上述过程中,下保温体4在大约1200℃时需要下降,否则底部温度无法按照时间下降。 Step 4: Perform a crystal growth process, including a sub-step: the top temperature is lowered from 1460 ° C to 1400 ° C, and the bottom is cooled from 1450 ° C to 900 ° C, and the cooling time is about 34 hours. This process is a crystal growth process of a silicon ingot. In the above process, the lower heat retaining body 4 needs to be lowered at about 1200 ° C, otherwise the bottom temperature cannot be lowered in time.
步骤五、然后顶部温度用2小时降温到1350℃,此时,将下保温体再次提升到与上保温体并拢。再用3小时降低到1150℃,并在1150℃保温2小时。本过程为硅锭退火的过程。之后,用3小时降温到900℃,关闭加热电源,让硅锭自动降温。此为冷却阶段。 Step 5, then the top temperature is cooled to 1350 ° C in 2 hours. At this time, the lower heat retaining body is lifted again to the upper heat retaining body. It was further reduced to 1150 ° C in 3 hours and kept at 1150 ° C for 2 hours. This process is the process of annealing the ingot. After that, cool down to 900 °C in 3 hours, turn off the heating power, and let the silicon ingot automatically cool down. This is the cooling phase.
步骤六、当炉内温度低于300℃时,即可降下下保温体,将硅锭与坩埚连护板一起用叉车从炉内取出,放置在不通风的房间内自然冷却。 Step 6. When the temperature in the furnace is lower than 300 °C, the lower insulation body can be lowered, and the silicon ingot and the Qilian shield are taken out from the furnace by a forklift, and placed in a non-ventilated room to be naturally cooled.
对采用本发明实施例二多晶硅铸锭方法生产的上述硅锭的外表面去除后,可见顶部的结晶照片如图4所示。 After the outer surface of the above silicon ingot produced by the method of the polycrystalline silicon ingot of the second embodiment of the present invention is removed, the photo of the top crystal is as shown in FIG.
沿所述硅锭的纵向进行切割,截面的照片如图5所示。经过检验,四个所述硅锭结晶较均匀,表明温场控制达到设计要求。 The cutting is performed in the longitudinal direction of the silicon ingot, and a photograph of the cross section is shown in Fig. 5. After inspection, the four silicon ingots are more uniform in crystallization, indicating that the temperature field control meets the design requirements.
测试所述硅锭的电阻率,得到的值在1.2Ω·cm~2.5Ω·cm之间,测试少子寿命,均在2微秒以上。 The resistivity of the silicon ingot was tested to obtain a value between 1.2 Ω·cm and 2.5 Ω·cm, and the minority carrier lifetime was tested, both of which were above 2 microseconds.
所述硅锭完全满足太阳能电池的标准要求。后经过对该硅片制作太阳能电池,得到的平均转换效率为16.7%。 The silicon ingot fully meets the standard requirements of solar cells. After the solar cell was fabricated on the silicon wafer, the average conversion efficiency was 16.7%.
本发明实施例三多晶硅铸锭方法的步骤如下: The steps of the third polycrystalline silicon ingot method of the embodiment of the present invention are as follows:
步骤一、将四个1020x1020x480mm的石英坩埚7放入本发明实施例所叙述的铸锭炉内的石墨平台6上,每个所述坩埚7装料660公斤,共装料2640公斤。 Step 1. Four 1020 x 1020 x 480 mm quartz crucibles 7 were placed on the graphite platform 6 in the ingot furnace described in the examples of the present invention, and each of the crucibles 7 was charged with 660 kg, and a total of 2,640 kg was charged.
步骤二、所述坩埚7外面用石墨护板包围保护,然后上升炉底3,当所述炉底3与所述炉身2完全并拢后,开始抽真空。 Step 2: The outside of the crucible 7 is surrounded by a graphite shield, and then the bottom 3 is raised. When the bottom 3 and the shaft 2 are completely closed, vacuuming is started.
步骤三、当真空度达到1Pa时,开始给所述上下加热体5和9送电,开始加热熔硅。大约7小时后,硅料开始融化。再等3小时,硅料全部熔化后,在温度1500处保持大约半小时,即开始降温。 Step 3: When the degree of vacuum reaches 1 Pa, the upper and lower heating bodies 5 and 9 are started to be powered to start heating the molten silicon. After about 7 hours, the silicon material began to melt. After waiting for another 3 hours, the silicon material is completely melted and maintained at a temperature of 1500 for about half an hour, that is, the temperature is lowered.
步骤四、进行长晶过程,包括分步骤:降温到1460℃时,保温1小时。然后,顶部温度从1460℃向1400℃降温,底部则从当前温度向860℃降温,降温时间大约34小时。本过程为硅锭的长晶过程。在上述过程中,所述下保温体4在大约1200℃时需要下降,否则底部温度无法按照时间下降。 Step 4: Perform a crystal growth process, including a sub-step: when the temperature is lowered to 1460 ° C, the temperature is maintained for 1 hour. Then, the top temperature is lowered from 1460 ° C to 1400 ° C, and the bottom is cooled from the current temperature to 860 ° C, and the cooling time is about 34 hours. This process is a crystal growth process of a silicon ingot. In the above process, the lower heat retaining body 4 needs to be lowered at about 1200 ° C, otherwise the bottom temperature cannot be lowered in time.
步骤五、然后顶部温度用2小时降温到1350℃,此时,将所述下保温体4再次提升到与上保温体8并拢。再用3小时降低到1150℃,并在1150℃保温2小时。本过程为硅锭退火阶段。之后,用3小时降温到900℃,关闭加热电源,让硅锭自动降温。此为硅锭冷却阶段。 Step 5, then the top temperature is lowered to 1350 ° C in 2 hours. At this time, the lower heat retaining body 4 is lifted again to be close to the upper heat insulating body 8 . It was further reduced to 1150 ° C in 3 hours and kept at 1150 ° C for 2 hours. This process is an ingot annealing stage. After that, cool down to 900 °C in 3 hours, turn off the heating power, and let the silicon ingot automatically cool down. This is the silicon ingot cooling stage.
步骤六、当炉内温度低于300℃时,即可降下所述下保温体4,将硅锭与坩埚7连护板一起用叉车从炉内取出,放置在不通风的房间内自然冷却。 Step 6. When the temperature in the furnace is lower than 300 °C, the lower heat retaining body 4 can be lowered, and the silicon ingot and the 坩埚7 connecting plate are taken out from the furnace by a forklift, and placed in a non-ventilated room to be naturally cooled.
对采用本发明实施例二多晶硅铸锭方法生产的上述硅锭的外表面去除后,可见顶部的结晶照片如图6所示。 After the outer surface of the above silicon ingot produced by the method of the polycrystalline silicon ingot of the second embodiment of the present invention is removed, the photo of the top crystal is shown in Fig. 6.
沿所述硅锭的纵向进行切割,截面的照片如图7所示。经过检验,四个所述硅锭结晶较均匀,表明温场控制达到设计要求。 Cutting is performed in the longitudinal direction of the silicon ingot, and a photograph of the cross section is shown in FIG. After inspection, the four silicon ingots are more uniform in crystallization, indicating that the temperature field control meets the design requirements.
测试所述硅锭的电阻率,得到的值在1.2Ω·cm~2.5Ω·cm之间,测试少子寿命,均在2微秒以上。 The resistivity of the silicon ingot was tested to obtain a value between 1.2 Ω·cm and 2.5 Ω·cm, and the minority carrier lifetime was tested, both of which were above 2 microseconds.
该锭完全满足太阳能电池的标准要求。后经过对该硅片制作太阳能电池,得到的平均转换效率为16.7%。 The ingot fully meets the standard requirements of solar cells. After the solar cell was fabricated on the silicon wafer, the average conversion efficiency was 16.7%.
以上通过具体实施例对本发明进行了详细的说明,但这些并非构成对本发明的限制。在不脱离本发明原理的情况下,本领域的技术人员还可做出许多变形和改进,这些也应视为本发明的保护范围。 The present invention has been described in detail by way of specific examples, but these are not intended to limit the invention. Many modifications and improvements can be made by those skilled in the art without departing from the principles of the invention.
Industrial ApplicabilityIndustrial Applicability
Sequence List TextSequence List Text

Claims (1)

1 、一种多晶硅铸锭炉,其特征在于,包括:炉体和位于所述炉体中的一保温体、一石墨平台、四个坩埚、上加热体和下加热体;1 a polycrystalline silicon ingot furnace, comprising: a furnace body and a heat retaining body located in the furnace body, a graphite platform, four crucibles, an upper heating body and a lower heating body;
所述炉体包括上炉盖、炉身和炉底,所述炉底和所述炉身采用液压连接,所述炉底能和所述炉身分开或闭合;The furnace body includes an upper furnace cover, a furnace body and a furnace bottom, and the furnace bottom and the furnace body are hydraulically connected, and the furnace bottom can be separated or closed from the furnace body;
所述保温体为立方形,所述保温体包括上保温体和下保温体;The heat insulating body is cuboidal, and the heat insulating body comprises an upper heat insulating body and a lower heat insulating body;
所述石墨平台位于所述保温体中并被所述保温体包围,所述四个坩埚放置于所述石墨平台上;The graphite platform is located in the heat insulator and surrounded by the heat insulator, and the four crucibles are placed on the graphite platform;
所述上加热体和所述下加热体都位于所述保温体中,且所述上加热体位于所述坩埚顶部的所述上保温体的顶面下方、所述下加热体位于所述石墨平台下方,所述上加热体和所述上保温体固定在一起并固定于所述炉身上,所述下加热体和所述下保温体固定在一起并能一起和所述上保温体分开并向下移动。The upper heating body and the lower heating body are both located in the heat retaining body, and the upper heating body is located below the top surface of the upper heat insulating body of the top of the crucible, and the lower heating body is located at the graphite Below the platform, the upper heating body and the upper heat retaining body are fixed together and fixed to the furnace body, and the lower heating body and the lower heat insulating body are fixed together and can be separated from the upper heat insulating body together Move Downward.
2 、如权利要求1所述多晶硅铸锭炉,其特征在于:所述四个坩埚在所述石墨平台上的放置方式为呈田字形摆放。2 The polycrystalline silicon ingot furnace according to claim 1, wherein the four crucibles are placed on the graphite platform in a field shape.
3 、如权利要求1所述多晶硅铸锭炉,其特征在于:所述四个坩埚的边长分别为720毫米~1200毫米。3 The polycrystalline silicon ingot furnace according to claim 1, wherein the four sides have a side length of 720 mm to 1200 mm.
4 、如权利要求1所述多晶硅铸锭炉,其特征在于:所述上加热体完全覆盖住所述四个坩埚、且所述上加热体的外缘尺寸大于所述四个坩埚的外缘尺寸5%~30%,所述四个坩埚的外侧面和所述保温体相隔有一定的距离,所述上加热体的处于所述四个坩埚的外缘外部的部分用于对所述四个坩埚的侧面加热。4 The polycrystalline silicon ingot furnace according to claim 1, wherein said upper heating body completely covers said four turns, and said outer heating body has an outer edge size larger than an outer edge size of said four turns %~30%, the outer sides of the four turns are separated from the heat insulating body by a certain distance, and the portion of the upper heating body outside the outer edge of the four turns is used for the four turns The side is heated.
5 、如权利要求1所述多晶硅铸锭炉,其特征在于:在各所述坩埚的周围放置有护板。5. A polycrystalline silicon ingot furnace according to claim 1, wherein a shield is placed around each of said weirs.
6 、如权利要求1所述多晶硅铸锭炉,其特征在于:所述上加热体由两个加热回路组成,所述两个加热回路能同时工作、也能互为热备份。6 The polycrystalline silicon ingot furnace according to claim 1, wherein the upper heating body is composed of two heating circuits, and the two heating circuits can work simultaneously and can also be hot backups to each other.
7 、一种多晶硅铸锭方法,其特征在于,包括如下步骤:7. A method of ingot casting polysilicon, comprising the steps of:
步骤一、用液压装置放下并打开所述炉底并在所述四个坩埚中装入硅料;Step 1: using a hydraulic device to lower and open the furnace bottom and loading silicon material into the four crucibles;
步骤二、上升所述炉底使其闭合,开始抽真空;Step two, raising the bottom of the furnace to close it, and starting to vacuum;
步骤三、当所述炉体的真空度达到1Pa时,给所述上加热体和所述下加热体送电,开始加热所述硅料并使所述硅料完全熔化;Step 3: when the degree of vacuum of the furnace body reaches 1 Pa, the upper heating body and the lower heating body are powered, and the heating of the silicon material is started and the silicon material is completely melted;
步骤四、进行长晶过程,包括分步骤:逐步降低所述下加热体的功率,使所述坩埚底部温度逐渐降低,当所述坩埚底部温度低于所述硅料的熔点时所述坩埚底部开始结晶并形成多晶硅;当所述下加热体的功率降到0时,将所述下保温体和所述下加热体一起下降,使所述多晶硅继续往上生长;Step 4, performing a crystal growth process, comprising the steps of: gradually reducing the power of the lower heating body to gradually lower the temperature of the bottom of the crucible, and when the bottom temperature of the crucible is lower than the melting point of the silicon material Starting to crystallize and form polysilicon; when the power of the lower heating body drops to 0, the lower heat insulator and the lower heating body are lowered together, so that the polysilicon continues to grow upward;
步骤五、将所述下保温体和所述下加热体提升,对所述多晶硅进行退火,接着再对所述多晶硅进行冷却;Step 5: lifting the lower heat insulator and the lower heating body, annealing the polysilicon, and then cooling the polysilicon;
步骤六、当所述多晶硅形成的多晶硅铸锭的温度降低到300℃以下时,放下所述炉底并将所述多晶硅铸锭取出。Step 6. When the temperature of the polycrystalline silicon ingot formed by the polysilicon is lowered to 300 ° C or lower, the bottom of the furnace is lowered and the polycrystalline silicon ingot is taken out.
PCT/CN2011/080602 2011-04-11 2011-10-10 Polysilicon ingot casting furnace and polysilicon ingot casting method WO2012139362A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201110089125.2 2011-04-11
CN2011100891252A CN102732959A (en) 2011-04-11 2011-04-11 Polysilicon ingot furnace and polysilicon ingot casting method

Publications (1)

Publication Number Publication Date
WO2012139362A1 true WO2012139362A1 (en) 2012-10-18

Family

ID=46989234

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2011/080602 WO2012139362A1 (en) 2011-04-11 2011-10-10 Polysilicon ingot casting furnace and polysilicon ingot casting method

Country Status (2)

Country Link
CN (1) CN102732959A (en)
WO (1) WO2012139362A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107805841A (en) * 2017-12-04 2018-03-16 江苏高照新能源发展有限公司 A kind of controllable G7 polycrystalline silicon ingot or purifying furnaces DS blocks bottom attemperator
CN108179467A (en) * 2018-03-07 2018-06-19 深圳市石金科技股份有限公司 A kind of Novel fender component for polysilicon ingot crucible
CN109082706A (en) * 2018-10-30 2018-12-25 浙江羿阳太阳能科技有限公司 Energy-saving polysilicon ingot casting device
CN109097830A (en) * 2018-10-30 2018-12-28 浙江羿阳太阳能科技有限公司 Polycrystalline silicon ingot casting energy saving furnace
CN110438564A (en) * 2019-08-26 2019-11-12 大同新成新材料股份有限公司 A kind of more product silicon thermal field crucible split type heat-proof device and its application methods
CN113753884A (en) * 2021-09-28 2021-12-07 福建科华石墨科技有限公司 Graphitization system

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102978687B (en) * 2012-12-21 2015-06-10 英利集团有限公司 Crystal growth method of polycrystalline silicon ingot
CN103409790B (en) * 2013-08-01 2016-02-03 安徽大晟新能源设备科技有限公司 The lower well heater hoisting appliance of accurate single-crystal ingot casting furnace
CN103409791A (en) * 2013-08-01 2013-11-27 安徽大晟新能源设备科技有限公司 Six-sided thermal field structure in thermal insulators of quasi-single crystal silicon ingot furnace
CN104502826A (en) * 2014-12-03 2015-04-08 东莞市长安东阳光铝业研发有限公司 Polycrystalline silicon ingot casting rapid test method
CN108004589A (en) * 2018-01-12 2018-05-08 无锡惠郡科技有限公司 A kind of manufacture method and its manufacturing equipment of octagon polycrystalline silicon ingot casting
CN109448800B (en) * 2018-12-24 2022-12-06 内蒙古神舟硅业有限责任公司 Method for judging mass gliding time of refined trichlorosilane
CN111506456B (en) * 2020-04-20 2023-04-28 哈尔滨科友半导体产业装备与技术研究院有限公司 Multiple backup method for crystal growth data of furnace body
CN113279059A (en) * 2020-09-28 2021-08-20 晶海洋半导体材料(东海)有限公司 Novel polycrystalline silicon ingot casting device and ingot casting method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006335582A (en) * 2005-05-31 2006-12-14 Daiichi Kiden:Kk Crystalline silicon manufacturing unit and its manufacturing method
CN101089233A (en) * 2006-06-13 2007-12-19 赵荣相 Manufacturing equipment for polysilicon ingot
WO2007148988A1 (en) * 2006-06-23 2007-12-27 Rec Scanwafer As Crystallization furnace
CN201133766Y (en) * 2007-11-30 2008-10-15 上海普罗新能源有限公司 Polycrystalline silicon fine ingot furnace adopting gradient temperature reduction
CN101323972A (en) * 2008-07-14 2008-12-17 大连理工大学 Polysilicon directional freezing equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102007026298A1 (en) * 2007-06-06 2008-12-11 Freiberger Compound Materials Gmbh Arrangement and method for producing a crystal from the melt of a raw material and single crystal
CN201473324U (en) * 2009-07-27 2010-05-19 管悦 Overhead type polysilicon furnace with upper heater and lower heater

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006335582A (en) * 2005-05-31 2006-12-14 Daiichi Kiden:Kk Crystalline silicon manufacturing unit and its manufacturing method
CN101089233A (en) * 2006-06-13 2007-12-19 赵荣相 Manufacturing equipment for polysilicon ingot
WO2007148988A1 (en) * 2006-06-23 2007-12-27 Rec Scanwafer As Crystallization furnace
CN201133766Y (en) * 2007-11-30 2008-10-15 上海普罗新能源有限公司 Polycrystalline silicon fine ingot furnace adopting gradient temperature reduction
CN101323972A (en) * 2008-07-14 2008-12-17 大连理工大学 Polysilicon directional freezing equipment

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107805841A (en) * 2017-12-04 2018-03-16 江苏高照新能源发展有限公司 A kind of controllable G7 polycrystalline silicon ingot or purifying furnaces DS blocks bottom attemperator
CN108179467A (en) * 2018-03-07 2018-06-19 深圳市石金科技股份有限公司 A kind of Novel fender component for polysilicon ingot crucible
CN109082706A (en) * 2018-10-30 2018-12-25 浙江羿阳太阳能科技有限公司 Energy-saving polysilicon ingot casting device
CN109097830A (en) * 2018-10-30 2018-12-28 浙江羿阳太阳能科技有限公司 Polycrystalline silicon ingot casting energy saving furnace
CN110438564A (en) * 2019-08-26 2019-11-12 大同新成新材料股份有限公司 A kind of more product silicon thermal field crucible split type heat-proof device and its application methods
CN113753884A (en) * 2021-09-28 2021-12-07 福建科华石墨科技有限公司 Graphitization system

Also Published As

Publication number Publication date
CN102732959A (en) 2012-10-17

Similar Documents

Publication Publication Date Title
WO2012139362A1 (en) Polysilicon ingot casting furnace and polysilicon ingot casting method
WO2021008159A1 (en) Coil-movable temperature field structure suitable for czochralski method, and single crystal growth method
KR100861412B1 (en) Manufacturing equipment for poly silicon ingot
WO2011136479A2 (en) High-output apparatus for manufacturing a polycrystal silicon ingot for a solar cell
CN103813983B (en) Directional solidification system and method
WO2016082525A1 (en) Device for moving small heat insulating plate at bottom of polycrystalline silicon ingot furnace and polycrystalline silicon ingot furnace
CN102127809A (en) Polycrystalline silicon ingot furnace
CN103343387B (en) A kind of polycrystalline silicon ingot or purifying furnace and casting ingot method thereof
CN113638048B (en) Method for growing indium phosphide single crystal by VGF method
CN103966657A (en) Ingotting furnace for polycrystalline silicon and quasi single crystal silicon and application method for ingotting furnace
CN102701213B (en) Solar polycrystalline silicon purification equipment employing directional solidification metallurgical method
WO2010118692A1 (en) Method and device for metallurgical purification using liquid dross filter and method for purifying polysilicon
US20110129404A1 (en) System and process for the production of polycrystalline silicon for photovoltaic use
US9410266B2 (en) Process for producing multicrystalline silicon ingots by the induction method, and apparatus for carrying out the same
CN102758245A (en) Deoxidizing type single crystal furnace
CN106048718B (en) A kind of polysilicon fritting ingot casting sundries discharging method
KR101249808B1 (en) Device and method for manufacturing high-purity polycrystalline silicon for solar cell
CN106119956B (en) A kind of polysilicon fritting casting ingot method
CN213113600U (en) Square silicon core ingot furnace thermal field structure
CN110106546B (en) High-yield casting monocrystalline silicon growth method and thermal field structure
CN115198350A (en) Thermal field system capable of reducing oxygen content of silicon crystal and process method
CN206783821U (en) A kind of heating control system for casting polysilicon top side and being separately controlled
CN210458426U (en) Polycrystal ingot furnace heater
CN106087045B (en) A kind of polysilicon fritting ingot casting melt and crystal growing technology
JPH0848598A (en) Silicon melting device

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 11863525

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 11863525

Country of ref document: EP

Kind code of ref document: A1