CN114769219A - Method for cleaning electronic grade polysilicon with dry ice - Google Patents
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 70
- 235000011089 carbon dioxide Nutrition 0.000 title claims abstract description 70
- 229910021420 polycrystalline silicon Inorganic materials 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 49
- 238000004140 cleaning Methods 0.000 title claims abstract description 43
- 229920005591 polysilicon Polymers 0.000 title claims abstract description 38
- 238000010926 purge Methods 0.000 claims abstract description 76
- 238000012216 screening Methods 0.000 claims abstract description 38
- 239000000463 material Substances 0.000 claims abstract description 33
- 230000008569 process Effects 0.000 claims abstract description 24
- 239000012159 carrier gas Substances 0.000 claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 15
- 230000001681 protective effect Effects 0.000 claims abstract description 5
- 239000002210 silicon-based material Substances 0.000 claims description 48
- 238000007873 sieving Methods 0.000 claims description 29
- 239000000428 dust Substances 0.000 claims description 9
- 238000007664 blowing Methods 0.000 claims description 7
- 239000011148 porous material Substances 0.000 claims 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract description 65
- 239000002245 particle Substances 0.000 abstract description 41
- 229910052710 silicon Inorganic materials 0.000 abstract description 38
- 239000010703 silicon Substances 0.000 abstract description 38
- 239000011863 silicon-based powder Substances 0.000 abstract description 27
- 239000004519 grease Substances 0.000 abstract description 10
- 239000003344 environmental pollutant Substances 0.000 abstract description 5
- 231100000719 pollutant Toxicity 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 5
- 239000002253 acid Substances 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 18
- 238000012360 testing method Methods 0.000 description 8
- 230000003749 cleanliness Effects 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 238000005554 pickling Methods 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000013078 crystal Substances 0.000 description 3
- 238000005202 decontamination Methods 0.000 description 3
- 230000003588 decontaminative effect Effects 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 150000002825 nitriles Chemical class 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000000859 sublimation Methods 0.000 description 3
- 230000008022 sublimation Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 241000979122 Bembrops anatirostris Species 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
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- 238000005092 sublimation method Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B7/00—Cleaning by methods not provided for in a single other subclass or a single group in this subclass
- B08B7/0064—Cleaning by methods not provided for in a single other subclass or a single group in this subclass by temperature changes
- B08B7/0092—Cleaning by methods not provided for in a single other subclass or a single group in this subclass by temperature changes by cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B13/00—Accessories or details of general applicability for machines or apparatus for cleaning
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/02—Silicon
- C01B33/037—Purification
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- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
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Abstract
Description
技术领域technical field
本发明涉及多晶硅生产技术领域,尤其涉及利用干冰对电子级多晶硅进行清洗的方法。The invention relates to the technical field of polycrystalline silicon production, in particular to a method for cleaning electronic grade polycrystalline silicon by using dry ice.
背景技术Background technique
电子级多晶硅在生产破碎过程中,破碎台的附近会产生大量的硅粉,这些硅粉会附着于硅块的表面,硅块进入酸洗机后,增加带入酸洗机内的污染物的几率,影响酸洗的清洗效果。此外,在破碎过程中,存在人员进行挑拣的情况,但由于硅块的边缘较为锋利,会导致人员穿戴的丁腈手套被划破并掉落些许碎片附着在硅块表面,附着的丁腈碎片是一种高碳污染物,被带入拉晶炉后,会引发单晶棒局部缺陷,甚至会导致拉晶失败。During the production and crushing of electronic grade polysilicon, a large amount of silicon powder will be produced near the crushing table, and these silicon powder will adhere to the surface of the silicon block. The probability will affect the cleaning effect of pickling. In addition, in the process of crushing, there are cases where people pick and choose, but because the edge of the silicon block is relatively sharp, the nitrile gloves worn by the personnel will be scratched and some fragments will fall off and adhere to the surface of the silicon block, and the attached nitrile fragments will It is a kind of high-carbon pollutant. After being brought into the crystal pulling furnace, it will cause local defects of the single crystal rod, and even lead to the failure of crystal pulling.
因此,现有的电子级多晶硅的清洗方法仍有待进一步改进。Therefore, the existing cleaning methods for electronic grade polysilicon still need to be further improved.
发明内容SUMMARY OF THE INVENTION
本发明旨在至少在一定程度上解决相关技术中的技术问题之一。为此,本发明的一个目的在于提出一种利用干冰对电子级多晶硅进行清洗的方法,以达到有效去除各个处理过程中可能引入的油脂,实现附着在硅块表面的硅粉、非硅物与硅块的有效分离,减少硅块表面的颗粒物,进而减少被带入酸洗机内的污染物。The present invention aims to solve one of the technical problems in the related art at least to a certain extent. To this end, an object of the present invention is to propose a method for cleaning electronic grade polysilicon using dry ice, so as to effectively remove the grease that may be introduced in each treatment process, and to realize that the silicon powder, non-silicon matter and The effective separation of the silicon block reduces the particles on the surface of the silicon block, thereby reducing the pollutants brought into the pickling machine.
在本发明的一个方面,本发明提出了一种利用干冰对电子级多晶硅进行清洗的方法,根据本发明的实施例,该方法包括:在对破碎得到的多晶硅料进行筛分的过程中,以保护气或压缩空气为载气,利用干冰对所述多晶硅料进行吹扫清洗,其中:吹扫的压力为6~8公斤力,吹扫的流速为0.8~1.2m/s。发明人发现,干冰在常压、高于-78.5℃(尤其是高于0摄氏度以上的温度环境,如室温)的条件下可以直接从固态升华至气态,将高速干冰喷射在多晶硅料的表面,干冰的升华会带走硅料表面附近大量的热量,降低硅料表面附着的油脂温度,使之被冷冻、脆化,由于硅的热膨胀系数与油脂的热膨胀系数不同,油脂在脆化后,会发生蜷曲现象,局部开裂,在高速气体的吹扫下,加速脱落,从而起到去污作用。另外,在对破碎得到的多晶硅料进行筛分的过程中,产生的硅粉会被干冰融化携带的水汽加湿,加重,同时硅块表面的颗粒、PE丝、丁腈手套等非硅物会急速的被冷冻,进行脱落,在筛分过程中硅粉颗粒及非硅物通过筛孔划出,从而起到去除硅粉及非硅物的效果。由此,该方法操作简单、方便,无需任何湿化学处理,不仅可以有效去除各个处理过程中可能引入的油脂,还能实现附着在硅块表面的硅粉、非硅物与硅块的有效分离,减少硅块表面的颗粒物,进而减少被带入酸洗机内的污染物。In one aspect of the present invention, the present invention proposes a method for cleaning electronic-grade polysilicon using dry ice. According to an embodiment of the present invention, the method includes: in the process of screening the polysilicon material obtained by crushing, Protective gas or compressed air is used as carrier gas, and dry ice is used to purge and clean the polysilicon material, wherein the purge pressure is 6-8 kgf, and the purge flow rate is 0.8-1.2 m/s. The inventor found that dry ice can be directly sublimated from solid state to gaseous state under the conditions of normal pressure and higher than -78.5°C (especially a temperature environment above 0°C, such as room temperature), and high-speed dry ice can be sprayed on the surface of polycrystalline silicon material, The sublimation of dry ice will take away a lot of heat near the surface of the silicon material, reduce the temperature of the grease attached to the surface of the silicon material, and cause it to be frozen and embrittled. The phenomenon of curling occurs and local cracking occurs. Under the purging of high-speed gas, the falling off is accelerated, thereby playing a role in decontamination. In addition, in the process of sieving the polysilicon material obtained by crushing, the generated silicon powder will be humidified and aggravated by the water vapor carried by the melting of dry ice. During the sieving process, the silicon powder particles and non-silicon materials are drawn out through the sieve holes, so as to remove the silicon powder and non-silicon materials. Therefore, the method is simple and convenient to operate, and does not require any wet chemical treatment. It can not only effectively remove the grease that may be introduced in each treatment process, but also realize the effective separation of silicon powder, non-silicon substances and silicon blocks attached to the surface of the silicon block. , reducing the particles on the surface of the silicon block, thereby reducing the pollutants brought into the pickling machine.
另外,根据本发明上述实施例的利用干冰对电子级多晶硅进行清洗的方法还可以具有如下附加的技术特征:In addition, the method for cleaning electronic-grade polysilicon with dry ice according to the above embodiments of the present invention may also have the following additional technical features:
根据本发明的实施例,对破碎得到的多晶硅料进行预筛分除尘;对预筛分除尘得到的多晶硅料进行再次筛分,在再次筛分过程中利用干冰对所述多晶硅料进行吹扫清洗。According to the embodiment of the present invention, the polycrystalline silicon material obtained by crushing is subjected to pre-screening and dust removal; the polycrystalline silicon material obtained by pre-screening and dust removal is screened again, and the polycrystalline silicon material is purged and cleaned with dry ice during the re-screening process. .
根据本发明的实施例,所述载气为压缩空气。According to an embodiment of the present invention, the carrier gas is compressed air.
根据本发明的实施例,利用筛分机对破碎得到的多晶硅料进行筛分,利用干冰吹扫机对所述多晶硅料进行吹扫清洗,在开启所述筛分机前,预先开启所述干冰吹扫机;在关闭所述筛分机后,再关闭所述干冰吹扫机。According to the embodiment of the present invention, the polysilicon material obtained by crushing is screened by a screening machine, the polycrystalline silicon material is blown and cleaned by a dry ice blower, and the dry ice blower is opened in advance before the screening machine is turned on. machine; after shutting down the screening machine, shut down the dry ice blower.
根据本发明的实施例,所述干冰吹扫机包括干冰投放孔、载气进气管线和混合气出气管线,所述干冰投放孔位于所述干冰吹扫机上部,所述载气进气管线和所述混合气出气管线分别独立地能承受6~10公斤力的压缩空气。According to an embodiment of the present invention, the dry ice blower includes a dry ice injection hole, a carrier gas inlet line and a mixed gas outlet line, the dry ice injection hole is located on the upper part of the dry ice blower, and the carrier gas inlet line and the mixed gas outlet pipeline can withstand 6-10 kilograms of compressed air independently.
根据本发明的实施例,所述吹扫清洗的温度不低于17℃,优选于17℃至室温的温度区间内进行。According to an embodiment of the present invention, the temperature of the purging and cleaning is not lower than 17°C, preferably performed in a temperature range from 17°C to room temperature.
根据本发明的实施例,所述吹扫清洗的时间为5~10min。According to an embodiment of the present invention, the purging and cleaning time is 5-10 minutes.
根据本发明的实施例,对破碎得到的多晶硅料进行筛分的过程中,采用的筛板与水平方向呈倾斜设置,在从高到底的方向上,所述筛板上的筛孔孔径逐渐变大。According to the embodiment of the present invention, in the process of sieving the polycrystalline silicon material obtained by crushing, the sieve plate used is inclined to the horizontal direction. big.
根据本发明的实施例,所述筛板与水平方向的夹角为10~25度;和/或,所述吹扫清洗方向与所述筛板设置方向的夹角为90±10度,优选90度。According to an embodiment of the present invention, the included angle between the sieve plate and the horizontal direction is 10 to 25 degrees; and/or the included angle between the purging and cleaning direction and the setting direction of the sieve plate is 90±10 degrees, preferably 90 degrees.
根据本发明的实施例,利用筛分机对破碎得到的多晶硅料进行筛分时,先开启所述筛分机工作一段时间,再对所述多晶硅料进行筛分处理;According to an embodiment of the present invention, when using a screening machine to screen the polysilicon material obtained by crushing, the screening machine is first turned on to work for a period of time, and then the polysilicon material is screened;
根据本发明的实施例,所述吹扫清洗于清洁环境中进行。According to an embodiment of the present invention, the purge cleaning is performed in a clean environment.
本发明的附加方面和优点将在下面的描述中部分给出,部分将从下面的描述中变得明显,或通过本发明的实践了解到。Additional aspects and advantages of the present invention will be set forth, in part, from the following description, and in part will be apparent from the following description, or may be learned by practice of the invention.
附图说明Description of drawings
本发明的上述和/或附加的方面和优点从结合下面附图对实施例的描述中将变得明显和容易理解,其中:The above and/or additional aspects and advantages of the present invention will become apparent and readily understood from the following description of embodiments taken in conjunction with the accompanying drawings, wherein:
图1是根据本发明一个实施例的干冰吹扫机的平面示意图。FIG. 1 is a schematic plan view of a dry ice blower according to an embodiment of the present invention.
具体实施方式Detailed ways
下面详细描述本发明的实施例,所述实施例的示例在附图中示出,其中自始至终相同或类似的标号表示相同或类似的元件或具有相同或类似功能的元件。下面通过参考附图描述的实施例是示例性的,旨在用于解释本发明,而不能理解为对本发明的限制。The following describes in detail the embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein the same or similar reference numerals refer to the same or similar elements or elements having the same or similar functions throughout. The embodiments described below with reference to the accompanying drawings are exemplary, and are intended to explain the present invention and should not be construed as limiting the present invention.
在本发明的一个方面,本发明提出了一种利用干冰对电子级多晶硅进行清洗的方法,根据本发明的实施例,该方法包括:在对破碎得到的多晶硅料进行筛分的过程中,以保护气或压缩空气为载气,利用干冰对所述多晶硅料进行吹扫清洗,其中:吹扫的压力为6~8公斤力,吹扫的流速为0.8~1.2m/s。发明人发现,干冰在常压、高于-78.5℃(尤其是高于0摄氏度以上的温度环境,如室温)的条件下可以直接从固态升华至气态,将高速干冰喷射在多晶硅料的表面,干冰的升华会带走硅料表面附近大量的热量,降低硅料表面附着的油脂温度,使之被冷冻、脆化,由于硅的热膨胀系数与油脂的热膨胀系数不同,油脂在脆化后,会发生蜷曲现象,局部开裂,在高速气体的吹扫下,加速脱落,从而起到去污作用。另外,在对破碎得到的多晶硅料进行筛分的过程中,产生的硅粉会被干冰融化携带的水汽加湿,加重,同时硅块表面的颗粒、PE丝、丁腈手套等非硅物会急速的被冷冻,进行脱落,在筛分过程中硅粉颗粒及非硅物通过筛孔划出,从而起到去除硅粉及非硅物的效果。由此,该方法操作简单、方便,无需任何湿化学处理,不仅可以有效去除各个处理过程中可能引入的油脂,还能实现附着在硅块表面的硅粉、非硅物与硅块的有效分离,减少硅块表面的颗粒物,进而减少被带入酸洗机内的污染物。In one aspect of the present invention, the present invention proposes a method for cleaning electronic-grade polysilicon using dry ice. According to an embodiment of the present invention, the method includes: in the process of screening the polysilicon material obtained by crushing, Protective gas or compressed air is used as carrier gas, and dry ice is used to purge and clean the polysilicon material, wherein the purge pressure is 6-8 kgf, and the purge flow rate is 0.8-1.2 m/s. The inventor found that dry ice can be directly sublimated from solid state to gaseous state under the conditions of normal pressure and higher than -78.5°C (especially a temperature environment above 0°C, such as room temperature), and high-speed dry ice can be sprayed on the surface of polycrystalline silicon material, The sublimation of dry ice will take away a lot of heat near the surface of the silicon material, reduce the temperature of the grease attached to the surface of the silicon material, and cause it to be frozen and embrittled. The phenomenon of curling occurs and local cracking occurs. Under the purging of high-speed gas, the falling off is accelerated, thereby playing a role in decontamination. In addition, in the process of sieving the polysilicon material obtained by crushing, the generated silicon powder will be humidified and aggravated by the water vapor carried by the melting of dry ice. During the sieving process, the silicon powder particles and non-silicon materials are drawn out through the sieve holes, so as to remove the silicon powder and non-silicon materials. Therefore, the method is simple and convenient to operate, and does not require any wet chemical treatment. It can not only effectively remove the grease that may be introduced in each treatment process, but also realize the effective separation of silicon powder, non-silicon substances and silicon blocks attached to the surface of the silicon block. , reducing the particles on the surface of the silicon block, thereby reducing the pollutants brought into the pickling machine.
根据本发明的实施例,载气吹扫的压力为6~8公斤力,例如可以为6公斤力、7公斤力、8公斤力等,吹扫的流速为0.8~1.2m/s,例如可以为0.8m/s、0.9m/s、1.0m/s、1.2m/s等,发明人发现,若载气吹扫的压力或吹扫的流速过小,难以获得有效的干冰吹扫力度,吹扫清洗的效果差;随着载气吹扫的压力或吹扫的流速增大,吹扫清洗的效果也会得到提升,但当载气吹扫的压力或吹扫的流速增大到一定程度后,继续增加载气吹扫的压力或吹扫的流速,对吹扫清洗效果进一步的改善的作用并不明显,同时还会显著增加对块状硅料吹扫清洗的成本;而通过控制载气吹扫的压力为6~8公斤力,吹扫的流速为0.8~1.2m/s,可以更好的兼顾对块状硅料的吹扫清洗效果及吹扫清洗的成本,实现块状硅料洁净度和经济成本的双赢。According to the embodiment of the present invention, the purging pressure of the carrier gas is 6-8 kgf, for example, it can be 6 kgf, 7 kgf, 8 kgf, etc., and the purging flow rate is 0.8-1.2 m/s, for example, it can be It is 0.8m/s, 0.9m/s, 1.0m/s, 1.2m/s, etc. The inventors found that if the carrier gas purging pressure or the purging flow rate is too small, it is difficult to obtain an effective dry ice purging force, The effect of purging and cleaning is poor; as the pressure of carrier gas purging or the flow rate of purging increases, the effect of purging and cleaning will also be improved, but when the pressure of carrier gas purging or the flow rate of purging increases to a certain level After the purging pressure of the carrier gas or the flow rate of the purging continues to increase, the effect of further improving the purging and cleaning effect is not obvious, and at the same time, the cost of purging and cleaning the bulk silicon material will be significantly increased; The purging pressure of the carrier gas is 6-8 kgf, and the purging flow rate is 0.8-1.2 m/s, which can better take into account the purging and cleaning effect of the bulk silicon material and the cost of purging and cleaning, and realize the block-shaped silicon material. A win-win for silicon cleanliness and economical cost.
根据本发明的实施例,当破碎得到的多晶硅料表面的硅粉或非硅物杂质较多时,可以先对破碎得到的多晶硅料进行预筛分除尘;再对预筛分除尘得到的多晶硅料进行再次筛分,在再次筛分过程中利用干冰对所述多晶硅料进行吹扫清洗,由此,可以预先除去多晶硅料的部分硅粉或非硅物杂质,从而不仅可以避免硅料中的硅粉或非硅物杂质太多影响后续对多晶硅料进行吹扫清洗的效率及效果,同时还能节约干冰用量,降低整体吹扫清洗成本,实现块状硅料洁净度和经济成本的双赢。According to the embodiment of the present invention, when there are many silicon powder or non-silicon impurities on the surface of the polysilicon material obtained by crushing, the polysilicon material obtained by crushing can be pre-screened and dedusted first; Screening again, in the process of re-screening, the polycrystalline silicon material is purged and cleaned with dry ice, so that part of the silicon powder or non-silicon impurities in the polycrystalline silicon material can be removed in advance, so as to not only avoid the silicon powder in the silicon material Too much or non-silicon impurities will affect the efficiency and effect of subsequent purging and cleaning of polysilicon materials, and at the same time, it can save the amount of dry ice, reduce the overall purging and cleaning costs, and achieve a win-win between the cleanliness of bulk silicon materials and economic costs.
根据本发明的实施例,吹扫清洗时,既可以以保护气(如惰性气体或氮气)作为干冰吹扫的载气,也可以采用结净度较高的压缩空气作为干冰吹扫的载气,由此,可以避免引入新的杂质。优选地,可以采用压缩空气作为干冰吹扫的载气,发明人发现,干冰在常压下沸点为-78.5℃,即当温度高于-78.5℃干冰就会升华,并吸收周围物体的热量,使它们的温度降低到接近-78.5℃,干冰在升华过程中,可以使压缩空气中的水汽冷凝,进而有利于硅料中的硅粉以及非硅物凝结,进行脱落,由此结合筛分能够更好地去除硅粉及非硅物。According to the embodiment of the present invention, when purging and cleaning, either protective gas (such as inert gas or nitrogen) can be used as the carrier gas for dry ice purging, or compressed air with higher degree of purity can be used as the carrier gas for dry ice purging , thereby avoiding the introduction of new impurities. Preferably, compressed air can be used as the carrier gas for dry ice purging. The inventors found that the boiling point of dry ice is -78.5°C under normal pressure, that is, when the temperature is higher than -78.5°C, dry ice will sublimate and absorb the heat of surrounding objects, Reduce their temperature to close to -78.5°C. During the sublimation process of dry ice, the water vapor in the compressed air can be condensed, which is conducive to the condensation and shedding of silicon powder and non-silicon materials in the silicon material. Better removal of silicon powder and non-silicon.
根据本发明的实施例,可以利用筛分机对破碎得到的多晶硅料进行筛分,利用干冰吹扫机对所述多晶硅料进行吹扫清洗,在开启所述筛分机前,可以预先开启所述干冰吹扫机;在关闭所述筛分机后,再关闭所述干冰吹扫机。由此,在对电子级多晶硅进行筛分的整个过程中能够保证均有干冰进行吹扫清洗,由此可以更彻底的实现对多晶硅料的吹扫清洗,进而获得洁净度更高的块状硅料。According to the embodiment of the present invention, the polycrystalline silicon material obtained by crushing can be screened by a screening machine, and the polycrystalline silicon material can be blown and cleaned by a dry ice blower. Before turning on the screening machine, the dry ice can be turned on in advance. blower; after shutting down the sieving machine, shut down the dry ice blower. Therefore, in the whole process of sieving electronic grade polysilicon, it can be ensured that dry ice is used for purging and cleaning, so that the purging and cleaning of polysilicon material can be more thoroughly achieved, thereby obtaining block silicon with higher cleanliness. material.
根据本发明的实施例,参照图1,所述干冰吹扫机可以包括干冰投放孔10、载气进气管线20和混合气出气管线30,所述干冰投放孔10可以位于所述干冰吹扫机上部,所述载气进气管线20和所述混合气出气管线30可以分别独立地能承受6~10公斤力的压缩空气。具体的,干冰吹扫机可以安装在筛分机的头部,将硅料倒入筛分机中,开启干冰吹扫机,将高速干冰喷射在多晶硅料的表面,干冰的升华会带走硅料表面附近大量的热量,降低硅料表面附着的油脂温度,使之被冷冻、脆化,由于硅的热膨胀系数与油脂的热膨胀系数不同,油脂在脆化后,会发生蜷曲现象,局部开裂,在高速气体的吹扫下,加速脱落,从而起到去污作用;另外,筛分机在抖动过程中产生的硅粉会被干冰融化携带的水汽加湿,加重,同时硅块表面的PE丝、丁腈手套等非硅物会急速的被冷冻,进行脱落,从筛分机孔径较小的筛孔划出,起到有效分离硅粉、非硅物与硅块的效果,由此,采用冰吹扫机不仅可以有效去除过程中引入的油脂,同时还可以将附着在硅块表面的硅粉、非硅物与硅块有效分离,减少硅块表面的颗粒数,进而减少被带入酸洗机内的颗粒物量。根据本发明的一些示例,载气进气管线和混合气出气管线的管径可以为DN25,且可以选用鸭嘴扁头的喷头,由此,可以进一步保证干冰和载气的混合气喷出后能够保持较高的吹扫压力及吹扫流速。According to an embodiment of the present invention, referring to FIG. 1 , the dry ice blower may include a dry
根据本发明的实施例,所述吹扫清洗的温度可以不低于17℃,例如可以是17℃、19℃、25℃、30℃等,发明人发现,在该温度条件下,既无需刻意控制环境温度,在常温常压下即可进行,而且干冰可以更快地直接从固态升华至气态,能更迅速地降低硅料表面温度,进而更有利于提高对硅料进行吹扫清洗的效率及效果。优选地,吹扫清洗可以于17℃至室温的温度区间内进行,由此,可以更好的兼顾吹扫清洗的效率及效果和经济成本。According to the embodiment of the present invention, the temperature of the purging and cleaning may not be lower than 17°C, for example, it may be 17°C, 19°C, 25°C, 30°C, etc. Control the ambient temperature, it can be carried out under normal temperature and pressure, and the dry ice can sublime directly from the solid state to the gaseous state more quickly, which can reduce the surface temperature of the silicon material more quickly, which is more conducive to improving the efficiency of purging and cleaning the silicon material. and effect. Preferably, the purging cleaning can be performed in a temperature range from 17° C. to room temperature, so that the efficiency and effect of the purging cleaning and the economic cost can be better taken into account.
根据本发明的实施例,所述吹扫清洗的时间可以为5~10min,具体可以是5min、6min、7min、8min、9min、10min等,由此,可以确保能够获得较好的吹扫清洗效果。According to the embodiment of the present invention, the time of the purging and cleaning can be 5-10 minutes, specifically 5 minutes, 6 minutes, 7 minutes, 8 minutes, 9 minutes, 10 minutes, etc., thus, it can be ensured that a good cleaning effect can be obtained .
根据本发明的实施例,对破碎得到的多晶硅料进行筛分的过程中,采用的筛板可以与水平方向呈倾斜设置,在从高到底的方向上,所述筛板上的筛孔孔径可以逐渐变大,其中该倾斜设置的筛板更有利于多晶硅料在筛板上的移动和分级筛分。由此,在筛分的过程中通过筛板振动和多级筛孔筛分,可以先去除小颗粒,如硅粉及非硅物,再去除粒径较小的硅块,最后得到符合粒径要求的硅块,由此可以进一步提高对硅粉及非硅物等小颗粒物杂质的吹扫效果,显著减少硅块表面的颗粒数,获得洁净度更高的块状硅料。According to the embodiment of the present invention, in the process of sieving the polysilicon material obtained by crushing, the sieve plate used may be inclined to the horizontal direction. Gradually become larger, wherein the inclined sieve plate is more conducive to the movement and classification and screening of polycrystalline silicon material on the sieve plate. Therefore, in the sieving process, through the sieve plate vibration and multi-stage sieve sieving, small particles such as silicon powder and non-silicon can be removed first, and then the silicon blocks with smaller particle size can be removed, and finally a suitable particle size can be obtained. The required silicon block can further improve the purging effect of small particulate impurities such as silicon powder and non-silicon material, significantly reduce the number of particles on the surface of the silicon block, and obtain block silicon material with higher cleanliness.
根据本发明的实施例,所述筛板与水平方向的夹角可以为10~25度,具体可以是10度、15度、20度、22度、25度等,由此,不仅可以方便颗粒下落,同时还可以控制颗粒的下落速率,保证筛分中的颗粒有适当的停留,避免出现因颗粒难以保持足够的筛分时间进而影响分离效果的问题;另外,所述吹扫清洗方向与所述筛板设置方向的夹角可以为90±10度,由此,可以进一步提高对块状硅料的吹扫清洗。优选地,吹扫清洗方向与所述筛板设置方向的夹角可以为90度,可以使得吹扫清洗的效果更佳。According to the embodiment of the present invention, the angle between the sieve plate and the horizontal direction may be 10 to 25 degrees, specifically 10 degrees, 15 degrees, 20 degrees, 22 degrees, 25 degrees, etc., thus, not only can the particle size be convenient At the same time, the falling rate of the particles can also be controlled to ensure that the particles in the screening have a proper stay, avoiding the problem that the particles are difficult to maintain for a sufficient screening time and thus affect the separation effect; The included angle of the setting direction of the sieve plate can be 90±10 degrees, thereby, the purging and cleaning of the bulk silicon material can be further improved. Preferably, the included angle between the purging and cleaning direction and the setting direction of the sieve plate can be 90 degrees, which can make the purging and cleaning effect better.
根据本发明的实施例,利用筛分机对破碎得到的多晶硅料进行筛分时,可以先开启所述筛分机工作一段时间,再对所述多晶硅料进行筛分处理,即对多晶硅料进行筛分前可以先使筛分机预热,使得筛分机达到正常工作状态,从而能够进一步保证筛分效果。According to the embodiment of the present invention, when using a screening machine to screen the polysilicon material obtained by crushing, the screening machine can be turned on for a period of time, and then the polysilicon material is screened, that is, the polysilicon material is screened. The screening machine can be preheated first, so that the screening machine can reach the normal working state, so as to further ensure the screening effect.
根据本发明的一些示例,所述吹扫清洗可以于清洁环境中进行,由此,可以有效避免引入新的杂质,其中清洁环境中可以设有增加装置,以方便对清洁环境中的洁净空气进行增压获得清洁度更高的压缩空气。According to some examples of the present invention, the purging and cleaning can be performed in a clean environment, thereby effectively avoiding the introduction of new impurities, wherein an increasing device can be provided in the clean environment to facilitate the cleaning of the clean air in the clean environment. Boost for cleaner compressed air.
下面参考具体实施例,对本发明进行描述,需要说明的是,这些实施例仅仅是描述性的,而不以任何方式限制本发明。The present invention will be described below with reference to specific embodiments. It should be noted that these embodiments are merely illustrative and do not limit the present invention in any way.
下述实施例中涉及的预筛分过程如下:The pre-screening process involved in the following examples is as follows:
人员戴好防尘呼吸器、消音耳塞。调试好颗粒度测试仪,测试环境的颗粒度空白值;另外,筛分机中的筛板倾斜设置,在从高到底的方向上,筛分机中的筛板上的筛孔孔径逐渐变大,筛孔孔径为30~200mm,开启筛分机5min后,向筛分机中倒入500公斤多晶硅料;筛分10min后,回收筛上硅料;将筛上硅料平均分成5份,分别为样品1、样品2、样品3、样品4、样品5。Personnel wear dust respirators and sound-absorbing earplugs. Debug the particle size tester, and test the particle size blank value of the environment; in addition, the sieve plate in the sieving machine is set inclined, and in the direction from the top to the bottom, the sieve hole diameter of the sieve plate in the sieving machine gradually becomes larger, and the screen The hole diameter is 30-200mm. After opening the sieving machine for 5 minutes, pour 500 kg of polysilicon material into the sieving machine; Sample 2, Sample 3, Sample 4, Sample 5.
实施例1Example 1
将样品1再次倒入筛分机中,开启干冰吹扫机,将吹扫压力指示调到6公斤,筛分5min后,停止筛分机。在筛分机30~200mm筛孔和筛板上方200~300mm处用颗粒度测试仪测试,分别记下1min之前、1min之后颗粒数的数据,记为数据1、数据2。Pour sample 1 into the sieving machine again, turn on the dry ice blower, adjust the purging pressure indicator to 6 kg, and stop the sieving machine after sieving for 5 minutes. Test with a particle size tester at the 30-200mm sieve hole of the sieving machine and 200-300mm above the sieve plate, and record the number of particles before 1min and after 1min, and record them as data 1 and data 2.
实施例2Example 2
与实施例1区别在于:将样品2再次倒入筛分机中,开启干冰吹扫机,将吹扫压力指示调到7公斤。The difference from Example 1 is that: the sample 2 is poured into the sieving machine again, the dry ice blowing machine is turned on, and the purging pressure indication is adjusted to 7 kg.
实施例3Example 3
与实施例1区别在于:将样品3再次倒入筛分机中,开启干冰吹扫机,将吹扫压力指示调到8公斤。The difference from Example 1 is: Pour the sample 3 into the sieving machine again, turn on the dry ice blowing machine, and adjust the blowing pressure indication to 8 kg.
实施例4Example 4
与实施例1区别在于:将样品4再次倒入筛分机中,开启干冰吹扫机,将吹扫压力指示调到9公斤。The difference from Example 1 is that: the sample 4 is poured into the sieving machine again, the dry ice blowing machine is turned on, and the purging pressure indication is adjusted to 9 kg.
对比例Comparative ratio
将样品5再次倒入筛分机中,筛分5min后,停止筛分机。在筛孔孔径为200~300mm的筛板上方用颗粒度测试仪测试,分别记下1min之前、1min之后颗粒数的数据,记为数据1、数据2。Pour sample 5 into the sieving machine again, and after sieving for 5 minutes, stop the sieving machine. Use a particle size tester on the top of the sieve plate with a sieve aperture of 200-300 mm, and record the data of the number of particles before and after 1min, which are recorded as data 1 and data 2.
表1为本发明实施例1~4和对比例1的不大于0.5μm的颗粒数总和的测试结果。其中,空白值为检测环境中不大于0.5μm的颗粒数。Table 1 is the test results of the total number of particles not larger than 0.5 μm in Examples 1 to 4 of the present invention and Comparative Example 1. Among them, the blank value is the number of particles not larger than 0.5 μm in the detection environment.
表1 0.5μm颗粒数的实验记录表(counts/ft3)Table 1 Experimental record of the number of 0.5μm particles (counts/ft 3 )
由表1可知,对比例测得的颗粒数分别为498713counts/ft3、327915counts/ft3,而实施例1~4测得的颗粒数显著降低,即采用干冰吹扫机,可以将附着在硅块表面的硅粉与硅块有效分离,进而可以大幅度降低硅料表面的颗粒。其中,随着吹扫压力增大,最终获得的块状硅料表面的颗粒数在总体上是呈下降趋势,实施例2和实施例3中测得的1min后颗粒数相对于实施例1更大的原因在于,干冰吹扫机是设在筛分机头部的,吹扫方向是自上而下的,而颗粒度测试仪是设在筛分机下游的筛板上方来进行颗粒测试的,包括两个测试点,硅料在两个测试点之间的振动下落时间为1min,干冰吹扫机开始吹扫时就对硅块表面有去硅粉粒作用,硅料越过干冰吹扫机,震动往后走,通过测试的两个点,在这两个测试点震动产生的颗粒数被颗粒度测试仪检测到,也就是说,颗粒度测试仪是通过测量环境中的颗粒数来间接获得硅料表面的颗粒数,测得的是硅料下落方向上方的颗粒数,环境中被测到的颗粒数越多,说明往下游走的粉尘数量越少,获得的硅料洁净度越高;另外,在筛分机头部,干冰吹扫机提供的剧烈气流方向是往下的,对粉尘颗粒有下压的效果,吹扫压力越大,对粉尘的下压效果也越明显;此外,干冰打在硅料上后其实硅料表面有回潮现象,可以起到降尘效果,筛板上有些地方会有潮湿硅粉,在一定的吹扫压力范围内,回潮现象随干冰吹扫压力增大也相对更明显,但从肉眼来看很难分别出来,而硅料留在筛板上的潮湿硅粉虽然可以降低往下游走的粉尘数量,但这部分硅粉被位于筛板上方200~300mm处的颗粒度测试仪检测到的概率较低,由此,导致实施例3和4获得的硅料洁净度虽然更高,但出现了测得的1min后颗粒数相对于实施例2更大的现象。综上所述,综合经济成本和吹扫清洗效果,可以选择吹扫清洗的压力为6~8公斤。It can be seen from Table 1 that the particle numbers measured in the comparative example are 498,713 counts/ft 3 and 327,915 counts/ft 3 respectively, while the particle numbers measured in Examples 1 to 4 are significantly reduced. The silicon powder on the surface of the block is effectively separated from the silicon block, which can greatly reduce the particles on the surface of the silicon material. Among them, with the increase of the purging pressure, the number of particles on the surface of the finally obtained bulk silicon material generally showed a downward trend. The big reason is that the dry ice blower is located at the head of the sieving machine, and the purging direction is from top to bottom, while the particle size tester is located above the sieve plate downstream of the sieving machine for particle testing, including Two test points, the vibration drop time of the silicon material between the two test points is 1min. When the dry ice blower starts to blow, it has the effect of removing the silicon powder on the surface of the silicon block. The silicon material passes over the dry ice blower and vibrates. Going back, through the two points of the test, the number of particles generated by vibration at these two test points is detected by the particle size tester, that is to say, the particle size tester indirectly obtains silicon by measuring the number of particles in the environment. The number of particles on the surface of the material is measured as the number of particles above the falling direction of the silicon material. The more the number of particles measured in the environment, the less the amount of dust going downstream, and the higher the cleanliness of the obtained silicon material; In addition, at the head of the screening machine, the strong airflow direction provided by the dry ice blower is downward, which has a downward pressure on the dust particles. The higher the blowing pressure, the more obvious the downward pressure effect on the dust; After being hit on the silicon material, the surface of the silicon material actually has moisture regain, which can play a role in dust reduction. There will be wet silicon powder in some places on the sieve plate. Within a certain purging pressure range, the moisture regain will also increase with the increase of the dry ice purging pressure. It is relatively more obvious, but it is difficult to distinguish it from the naked eye. Although the wet silicon powder left on the sieve plate can reduce the amount of dust going downstream, this part of the silicon powder is located 200-300mm above the sieve plate. The probability of detection by the particle size tester is low, thus, although the cleanliness of the silicon material obtained in Examples 3 and 4 is higher, the number of particles measured after 1min is larger than that in Example 2. Phenomenon. To sum up, considering the economic cost and the effect of purging and cleaning, the pressure of purging and cleaning can be selected to be 6-8 kg.
在本说明书的描述中,参考术语“一个实施例”、“一些实施例”、“示例”、“具体示例”、或“一些示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本发明的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不必须针对的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任一个或多个实施例或示例中以合适的方式结合。此外,在不相互矛盾的情况下,本领域的技术人员可以将本说明书中描述的不同实施例或示例以及不同实施例或示例的特征进行结合和组合。In the description of this specification, description with reference to the terms "one embodiment," "some embodiments," "example," "specific example," or "some examples", etc., mean specific features described in connection with the embodiment or example , structure, material or feature is included in at least one embodiment or example of the present invention. In this specification, schematic representations of the above terms are not necessarily directed to the same embodiment or example. Furthermore, the particular features, structures, materials or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, those skilled in the art may combine and combine the different embodiments or examples described in this specification, as well as the features of the different embodiments or examples, without conflicting each other.
尽管上面已经示出和描述了本发明的实施例,可以理解的是,上述实施例是示例性的,不能理解为对本发明的限制,本领域的普通技术人员在本发明的范围内可以对上述实施例进行变化、修改、替换和变型。Although the embodiments of the present invention have been shown and described above, it should be understood that the above-mentioned embodiments are exemplary and should not be construed as limiting the present invention. Embodiments are subject to variations, modifications, substitutions and variations.
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102383194A (en) * | 2010-08-25 | 2012-03-21 | 瓦克化学股份公司 | Polycrystalline silicon and method for production thereof |
CN103658177A (en) * | 2012-08-31 | 2014-03-26 | 宝山钢铁股份有限公司 | Method for producing high-strength thin strip steel in short process |
US20160214149A1 (en) * | 2014-12-24 | 2016-07-28 | Boe Technology Group Co., Ltd. | Mask cleaning apparatus and mask cleaning method |
CN106794992A (en) * | 2014-10-14 | 2017-05-31 | 株式会社德山 | Breaking polycrystalline silicon thing, the manufacture method of breaking polycrystalline silicon thing and polysilicon block breaker |
CN107530737A (en) * | 2015-04-16 | 2018-01-02 | 瓦克化学股份公司 | For being classified to polycrysalline silcon and the apparatus and method of dedusting |
CN211100177U (en) * | 2019-10-15 | 2020-07-28 | 东莞市成铭胶粘剂有限公司 | A kind of hot melt adhesive finished product classification device |
-
2022
- 2022-03-28 CN CN202210313946.8A patent/CN114769219A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102383194A (en) * | 2010-08-25 | 2012-03-21 | 瓦克化学股份公司 | Polycrystalline silicon and method for production thereof |
CN103658177A (en) * | 2012-08-31 | 2014-03-26 | 宝山钢铁股份有限公司 | Method for producing high-strength thin strip steel in short process |
CN106794992A (en) * | 2014-10-14 | 2017-05-31 | 株式会社德山 | Breaking polycrystalline silicon thing, the manufacture method of breaking polycrystalline silicon thing and polysilicon block breaker |
US20160214149A1 (en) * | 2014-12-24 | 2016-07-28 | Boe Technology Group Co., Ltd. | Mask cleaning apparatus and mask cleaning method |
CN107530737A (en) * | 2015-04-16 | 2018-01-02 | 瓦克化学股份公司 | For being classified to polycrysalline silcon and the apparatus and method of dedusting |
CN211100177U (en) * | 2019-10-15 | 2020-07-28 | 东莞市成铭胶粘剂有限公司 | A kind of hot melt adhesive finished product classification device |
Non-Patent Citations (1)
Title |
---|
国家环境保护总局清洗行业淘汰ODS特别工作组组织: "《清洗技术基础教程》", 中国环境科学出版社, pages: 229 - 230 * |
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