CN115595443A - Recycling method for bell jar coating of reduction furnace, auxiliary device for recycling, and solution circulation system for recycling - Google Patents
Recycling method for bell jar coating of reduction furnace, auxiliary device for recycling, and solution circulation system for recycling Download PDFInfo
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- 230000009467 reduction Effects 0.000 title claims abstract description 266
- 238000000576 coating method Methods 0.000 title claims abstract description 204
- 239000011248 coating agent Substances 0.000 title claims abstract description 197
- 238000000034 method Methods 0.000 title claims abstract description 50
- 238000004064 recycling Methods 0.000 title claims abstract description 10
- 239000000243 solution Substances 0.000 claims abstract description 179
- 239000002184 metal Substances 0.000 claims abstract description 89
- 229910052751 metal Inorganic materials 0.000 claims abstract description 89
- 239000012266 salt solution Substances 0.000 claims abstract description 34
- 238000004090 dissolution Methods 0.000 claims abstract description 33
- 239000007789 gas Substances 0.000 claims description 80
- 238000000197 pyrolysis Methods 0.000 claims description 33
- 150000003839 salts Chemical class 0.000 claims description 33
- 238000011084 recovery Methods 0.000 claims description 32
- 230000008569 process Effects 0.000 claims description 26
- 239000007788 liquid Substances 0.000 claims description 16
- 230000007246 mechanism Effects 0.000 claims description 14
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 11
- 229910017604 nitric acid Inorganic materials 0.000 claims description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 238000002425 crystallisation Methods 0.000 claims description 3
- 230000008025 crystallization Effects 0.000 claims description 3
- 229910021420 polycrystalline silicon Inorganic materials 0.000 abstract description 17
- 229920005591 polysilicon Polymers 0.000 abstract description 17
- 239000000463 material Substances 0.000 abstract description 16
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 239000007769 metal material Substances 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 4
- 238000006722 reduction reaction Methods 0.000 description 236
- 230000006872 improvement Effects 0.000 description 31
- 229910052709 silver Inorganic materials 0.000 description 24
- 239000004332 silver Substances 0.000 description 24
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 23
- 238000009434 installation Methods 0.000 description 18
- 239000000725 suspension Substances 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 9
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 9
- 101710134784 Agnoprotein Proteins 0.000 description 7
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical group [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 6
- 229910052737 gold Inorganic materials 0.000 description 5
- 239000010931 gold Substances 0.000 description 5
- 239000006166 lysate Substances 0.000 description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- 229910052802 copper Inorganic materials 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
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- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- 230000003373 anti-fouling effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000004377 microelectronic Methods 0.000 description 1
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- 238000005549 size reduction Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- ZDHXKXAHOVTTAH-UHFFFAOYSA-N trichlorosilane Chemical compound Cl[SiH](Cl)Cl ZDHXKXAHOVTTAH-UHFFFAOYSA-N 0.000 description 1
- 239000005052 trichlorosilane Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/006—Wet processes
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F1/00—Etching metallic material by chemical means
- C23F1/08—Apparatus, e.g. for photomechanical printing surfaces
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- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F1/00—Etching metallic material by chemical means
- C23F1/10—Etching compositions
- C23F1/14—Aqueous compositions
- C23F1/16—Acidic compositions
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F1/00—Etching metallic material by chemical means
- C23F1/46—Regeneration of etching compositions
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Abstract
本发明公开了一种还原炉钟罩涂层回收方法、回收用辅助装置及回收用溶解液循环系统,涉及多晶硅生产领域,具体包括如下步骤:向还原炉钟罩内输送溶解还原炉钟罩内壁涂层的溶解液,溶解液对还原炉钟罩内壁涂层进行溶解,溶解后产生的涂层金属盐溶液、气体和H2O送出还原炉钟罩;对生成的涂层金属盐溶液进行热解,涂层金属盐溶液热解后生成金属和气体。本发明溶解液对还原炉钟罩内壁的涂层进行溶解,最终生成涂层金属盐溶液、气体和H2O,并对生成的涂层金属盐溶液进行热解,从而得到金属和气体,即实现对涂层材料的回收,避免了对金属材料的浪费,降低了企业生产成本。
The invention discloses a method for recovering a coating of a reducing furnace bell jar, an auxiliary device for recycling and a recycling system for a solution solution, and relates to the field of polysilicon production, specifically comprising the following steps: transporting the dissolved inner wall of the reducing furnace bell jar The solution of the coating, the solution dissolves the coating on the inner wall of the bell jar of the reduction furnace, and the coating metal salt solution, gas and H 2 O generated after the dissolution are sent out to the bell jar of the reduction furnace; the resulting coating metal salt solution is heated solution, the coating metal salt solution pyrolyzes to generate metal and gas. The dissolving solution of the present invention dissolves the coating on the inner wall of the bell jar of the reduction furnace, finally generates coating metal salt solution, gas and H2O , and pyrolyzes the generated coating metal salt solution to obtain metal and gas, namely Realize the recycling of coating materials, avoid the waste of metal materials, and reduce the production cost of enterprises.
Description
技术领域technical field
本发明涉及多晶硅生产领域,具体而言,涉及一种还原炉钟罩涂层回收方法、回收用辅助装置及回收用溶解液循环系统。The invention relates to the field of polysilicon production, in particular to a method for recovering the bell jar coating of a reduction furnace, an auxiliary device for recovery, and a solution circulation system for recovery.
背景技术Background technique
多晶硅是光伏行业和微电子行业的基础材料,改良西门子法是当前制备多晶硅的主流方法。改良西门子法的特点是:在钟罩式化学气相沉积(CVD)反应器(行业术语为多晶硅还原炉)中,以通电自加热至温度为950℃-1150℃的细硅芯为沉积载体,通入多晶硅还原炉的三氯氢硅与氢气在热硅芯表面发生氢还原反应,被还原的硅沉积在硅芯表面,随着氢还原反应的进行,硅芯的直径逐渐变大,直至达到规定的尺寸,最终以多晶硅棒的形式采出。Polysilicon is the basic material for the photovoltaic industry and microelectronics industry, and the modified Siemens method is currently the mainstream method for preparing polysilicon. The characteristic of the improved Siemens method is: in a bell-type chemical vapor deposition (CVD) reactor (the industry term is a polysilicon reduction furnace), the fine silicon core that is self-heated to a temperature of 950°C-1150°C is used as a deposition carrier. The trichlorosilane and hydrogen gas entering the polysilicon reduction furnace undergo a hydrogen reduction reaction on the surface of the hot silicon core, and the reduced silicon is deposited on the surface of the silicon core. With the progress of the hydrogen reduction reaction, the diameter of the silicon core gradually increases until it reaches the specified The size is finally mined in the form of polysilicon rods.
多晶硅还原炉的主要材质为不锈钢,为了避免出现多晶硅还原炉运行过程中因内壁温度过高而使不锈钢材料蠕变失效的问题,通常在多晶硅还原炉外壁和多晶硅还原炉内壁间的夹套内通入低温水进行冷却,使多晶硅还原炉内壁温度保持在300℃以下。在多晶硅还原炉运行过程中,硅棒表面发射出大量近红外段电磁波,到达内壁表面的近红外电磁波大部分被低反射率的不锈钢内壁所吸收,并转化为多晶硅还原炉内壁的内热能,然后传导至高热容的低温冷却水。据统计,夹套冷却水带走的热量约占多晶硅还原炉总输入能量的60%以上。The main material of the polysilicon reduction furnace is stainless steel. In order to avoid the problem of creep failure of the stainless steel material due to the high temperature of the inner wall during the operation of the polysilicon reduction furnace, it is usually passed through the jacket between the outer wall of the polysilicon reduction furnace and the inner wall of the polysilicon reduction furnace. Enter low-temperature water for cooling, so that the temperature of the inner wall of the polysilicon reduction furnace is kept below 300°C. During the operation of the polysilicon reduction furnace, a large number of near-infrared electromagnetic waves are emitted from the surface of the silicon rod, and most of the near-infrared electromagnetic waves reaching the inner wall surface are absorbed by the stainless steel inner wall with low reflectivity, and converted into internal heat energy of the inner wall of the polysilicon reduction furnace, and then Conduction to low temperature cooling water with high heat capacity. According to statistics, the heat taken away by the jacket cooling water accounts for more than 60% of the total input energy of the polysilicon reduction furnace.
为了减少还原炉钟罩水带走的热能损失和多晶硅还原炉内壁不锈钢杂质的析出,还原炉内壁通常设置一层高近红外电磁波反射涂层来实现生产过程节能和防污的目的,诸如金、银、铜等,该涂层具有一定的服役寿命,当寿命到达后,需要移除旧涂层,制备新涂层,而金、银、铜等金属都价格昂贵。In order to reduce the loss of heat energy taken away by the bell jar water of the reduction furnace and the precipitation of stainless steel impurities on the inner wall of the polysilicon reduction furnace, a layer of high near-infrared electromagnetic wave reflective coating is usually provided on the inner wall of the reduction furnace to achieve the purpose of energy saving and antifouling in the production process, such as gold, Silver, copper, etc., the coating has a certain service life. When the service life is reached, the old coating needs to be removed to prepare a new coating, while gold, silver, copper and other metals are expensive.
因此,现急需开发一种还原炉钟罩涂层回收方法、回收用辅助装置及回收用溶解液循环系统。Therefore, there is an urgent need to develop a recovery furnace bell jar coating recovery method, an auxiliary device for recovery and a solution circulation system for recovery.
发明内容Contents of the invention
本发明的目的在于提供一种还原炉钟罩涂层回收用辅助装置、回收系统及回收用溶解液循环系统,能有效实现对还原炉钟罩内壁的涂层材料的回收。The object of the present invention is to provide an auxiliary device for recovery of the bell jar coating of the reduction furnace, a recovery system and a solution circulation system for recovery, which can effectively realize the recovery of the coating material on the inner wall of the bell jar of the reduction furnace.
为实现本发明目的,采用的技术方案为:For realizing the object of the present invention, the technical scheme that adopts is:
一种还原炉钟罩涂层回收方法,具体包括如下步骤:A method for recovering the coating of a reduction furnace bell jar, specifically comprising the steps of:
向还原炉钟罩内输送溶解还原炉钟罩内壁涂层的溶解液,溶解液对还原炉钟罩内壁涂层进行溶解,溶解后产生的涂层金属盐溶液、气体和H2O送出还原炉钟罩;Transport the solution to dissolve the coating on the inner wall of the bell jar of the reduction furnace to the bell jar of the reduction furnace. The solution dissolves the coating on the inner wall of the bell jar of the reduction furnace, and the resulting coating metal salt solution, gas and H 2 O are sent out of the reduction furnace bell jar;
对生成的涂层金属盐溶液进行蒸发结晶,结晶后热解,涂层金属盐热解后生成金属和气体。Evaporate and crystallize the resulting coating metal salt solution, pyrolyze after crystallization, and generate metal and gas after pyrolysis of the coating metal salt.
进一步的,将热解生成的气体回收后溶解于水,用以制备溶解液。Further, the gas generated by pyrolysis is recovered and dissolved in water to prepare a solution.
进一步的,涂层金属盐的热解温度为400℃~1200℃。Further, the pyrolysis temperature of the coating metal salt is 400°C-1200°C.
进一步的,还原炉钟罩可根据回收方法需求进行放置,如卧式放置、立式放置。Furthermore, the reduction furnace bell jar can be placed according to the requirements of the recovery method, such as horizontal placement or vertical placement.
进一步的,溶解液在对还原炉钟罩内壁涂层进行溶解过程中,还原炉钟罩同步旋转。Further, when the dissolving solution dissolves the coating on the inner wall of the reduction furnace bell, the reduction furnace bell rotates synchronously.
进一步的,所述溶解液为盐酸、硝酸中的一种或多种。Further, the dissolving solution is one or more of hydrochloric acid and nitric acid.
进一步的,所述溶解液浓度为1wt%~70wt%。Further, the concentration of the solution is 1wt%-70wt%.
进一步的,送入到还原炉钟罩内的溶解液体积不大于还原炉钟罩内部体积的一半。Further, the volume of the solution sent into the bell jar of the reduction furnace is no more than half of the internal volume of the bell jar of the reduction furnace.
进一步的,送入到还原炉钟罩内的溶解液体积是还原炉钟罩内部体积的使1/4~1/2。Further, the volume of the solution sent into the bell jar of the reduction furnace is 1/4 to 1/2 of the internal volume of the bell jar of the reduction furnace.
进一步的,溶解液在对还原炉钟罩内壁涂层进行溶解过程中,对还原炉钟罩内部加热。Further, the solution heats the inside of the reduction furnace bell during the process of dissolving the coating on the inner wall of the reduction furnace bell.
进一步的,还原炉钟罩内部的加热温度为30℃~200℃,且还原炉钟罩内部的氮气保压在0.1MPa~1MPa。Further, the heating temperature inside the bell jar of the reduction furnace is 30° C. to 200° C., and the pressure of nitrogen inside the bell jar of the reduction furnace is maintained at 0.1 MPa to 1 MPa.
一种还原炉钟罩涂层回收用辅助装置,包括卧式机架和驱动卧式机架旋转的驱动机构,卧式机架包括用于固定钟罩法兰的旋转底座和固定钟罩吊环的吊环连接件,且旋转底座和吊环连接件之间支撑有多个支撑杆,旋转底座上还开设有通孔,且旋转底座上还设置有进料管。An auxiliary device for recovering the bell jar coating of a reduction furnace, including a horizontal frame and a drive mechanism for driving the horizontal frame to rotate, and the horizontal frame includes a rotating base for fixing the bell jar flange and a ring for fixing the bell jar A ring connector, a plurality of support rods are supported between the rotating base and the ring connecting member, a through hole is opened on the rotating base, and a feeding pipe is also arranged on the rotating base.
进一步的,所述进料管上设有加热器。Further, a heater is provided on the feed pipe.
进一步的,所述驱动机构包括主动驱动结构和从动驱动结构,主动驱动结构和从动驱动结构分别位于卧式机架的两端。Further, the driving mechanism includes a driving driving structure and a driven driving structure, and the driving driving structure and the driven driving structure are respectively located at two ends of the horizontal frame.
进一步的,所述旋转底座为圆形,主动驱动结构包括固定件和驱动件,驱动件为两个,两个驱动件均转动支承在固定件上,且旋转底座共同支撑在两个驱动件上,且固定件上还安装有可调节转速并能够驱动驱动件转动的驱动电机。Further, the rotating base is circular, and the active driving structure includes a fixing part and a driving part, and there are two driving parts, both of which are rotatably supported on the fixing part, and the rotating base is jointly supported on the two driving parts , and a drive motor with adjustable speed and capable of driving the drive to rotate is installed on the fixed part.
进一步的,所述驱动件和旋转底座上均设置有啮合齿,驱动件上的啮合齿与旋转底座上的啮合齿相互啮合。Further, the driving part and the rotating base are both provided with engaging teeth, and the engaging teeth on the driving part and the engaging teeth on the rotating base mesh with each other.
进一步的,所述支撑杆为可伸缩结构。Further, the support rod is a telescopic structure.
进一步的,所述吊环连接件为环形,从动驱动结构包括可沿支撑杆长度方向往复运动的移动件,移动件上支承有可转动的从动轮,从动轮为两个,吊环连接件共同支撑在两个从动轮上。Further, the lifting ring connector is ring-shaped, and the driven driving structure includes a moving part that can reciprocate along the length direction of the support rod. The moving part supports a rotatable driven wheel. There are two driven wheels, and the lifting ring connecting part supports together on the two driven wheels.
进一步的,所述从动驱动结构还包括导轨,移动件为在导轨上往复滑动的滑块。Further, the driven driving structure further includes a guide rail, and the moving part is a slider reciprocatingly sliding on the guide rail.
进一步的,所述旋转底座和吊环连接件上还开设有多个安装孔组,多个安装孔组沿旋转底座的半径方向间隔排布,且每个安装孔组均包括以旋转底座中心圆周周向间隔排布的安装孔。Further, multiple mounting hole groups are provided on the rotating base and the suspension ring connector, and the multiple mounting hole groups are arranged at intervals along the radial direction of the rotating base, and each mounting hole group includes a center circumference of the rotating base. Mounting holes arranged at intervals.
一种还原炉钟罩涂层回收用溶解液循环系统,包括如上任意一项所述的辅助装置,还包括与进料管连接的溶解液容器、与通孔连接的涂层金属盐收集器。A solution circulation system for recycling bell jar coatings of a reduction furnace, comprising any one of the auxiliary devices described above, a solution container connected to a feed pipe, and a coating metal salt collector connected to a through hole.
进一步的,所述涂层金属盐收集器的出口端还连接有热解反应器,热解反应器出口端还连接有用于收集热解后气体的气体收集器。Further, the outlet end of the coating metal salt collector is also connected to a pyrolysis reactor, and the outlet end of the pyrolysis reactor is also connected to a gas collector for collecting pyrolysis gas.
进一步的,所述气体收集器上还连接有将气体输送至溶解液容器内的第一输送管路。Further, the gas collector is also connected with a first delivery pipeline for delivering the gas into the solution container.
进一步的,所述涂层金属盐收集器与气体收集器之间还连接有用于输送涂层溶解过程中产生的气体的第二输送管道。Further, a second delivery pipeline for delivering the gas generated during the coating dissolution process is also connected between the coating metal salt collector and the gas collector.
进一步的,所述溶解液容器上还连接有用于置换其内部气体的置换气体容器。Further, the dissolving solution container is also connected with a replacement gas container for replacing the gas inside it.
本发明的有益效果是,The beneficial effect of the present invention is,
本发明通过向还原炉钟罩内输送溶解液,通过溶解液对还原炉钟罩内壁的涂层进行溶解,最终生成涂层金属盐溶液、气体和H2O,并对生成的涂层金属盐溶液蒸发结晶后得到的涂层金属盐进行热解,从而得到金属和气体,即实现对涂层材料的回收,避免了对金属材料的浪费,降低了企业生产成本。In the present invention, the coating on the inner wall of the bell jar of the reduction furnace is dissolved by the solution by delivering the solution to the bell jar of the reduction furnace, and finally a coating metal salt solution, gas and H2O are generated, and the resulting coating metal salt The coating metal salt obtained after the solution is evaporated and crystallized is pyrolyzed to obtain metal and gas, which realizes the recovery of the coating material, avoids the waste of metal materials, and reduces the production cost of the enterprise.
本发明中通过设置气体收集器,并使气体收集器收集器与溶解液容器连接,使气体与水溶解后可以得到新的溶解液,实现了溶解液的全流程回收再利用。In the present invention, a gas collector is provided, and the gas collector is connected to a solution container, so that a new solution can be obtained after dissolving the gas and water, and the whole-process recovery and reuse of the solution is realized.
本发明中通过提供辅助装置,使钟罩内壁的涂层金属在需要回收时,不仅可使钟罩呈卧式安装,且使钟罩在卧式安装后还可进行旋转,使钟罩的完整性得到保证,使涂层金属回收时无需钟罩自身进行拆装,使回收效率更高。In the present invention, by providing an auxiliary device, when the coated metal on the inner wall of the bell jar needs to be recycled, not only the bell jar can be installed horizontally, but also the bell jar can be rotated after the horizontal installation, so that the bell jar is completely intact. The safety is guaranteed, so that the bell jar itself does not need to be disassembled and assembled when the coated metal is recycled, so that the recycling efficiency is higher.
附图说明Description of drawings
附图示出了本发明的示例性实施方式,并与其说明一起用于解释本发明的原理,其中包括了这些附图以提供对本发明的进一步理解,并且附图包括在本说明书中并构成本说明书的一部分。The accompanying drawings illustrate exemplary embodiments of the invention and, together with the description, serve to explain the principles of the invention, are included to provide a further understanding of the invention, and are incorporated in and constitute the present specification. part of the manual.
图1是本发明实施例3提供的还原炉钟罩涂层回收用辅助装置的结构示意图;Fig. 1 is the structural representation of the auxiliary device for recovery of the reduction furnace bell jar coating provided by the embodiment of the present invention 3;
图2是图1中还原炉钟罩的结构示意图;Fig. 2 is the structural representation of reduction furnace bell jar among Fig. 1;
图3是图1中卧式机架的结构示意图;Fig. 3 is the structural representation of horizontal frame among Fig. 1;
图4是旋转底座与驱动件配合的结构示意图;Fig. 4 is a structural schematic diagram of the cooperation between the rotating base and the driving member;
图5是钟罩吊环与从动轮配合的结构示意图;Fig. 5 is a schematic diagram of the structure of the cooperation of the bell ring and the driven wheel;
图6是本发明实施例4提供的还原炉钟罩涂层回收用溶解液循环系统的结构示意图。Fig. 6 is a schematic structural diagram of a solution circulation system for recovering the bell jar coating of the reduction furnace provided in Example 4 of the present invention.
附图中标记及相应的零部件名称:Marks and corresponding component names in the attached drawings:
1、还原炉钟罩,2、卧式机架,3、驱动机构,4、溶解液容器,5、涂层金属盐收集器,6、热解反应器,7、气体收集器,8、置换气体容器;1. Reduction furnace bell jar, 2. Horizontal rack, 3. Driving mechanism, 4. Solution container, 5. Coating metal salt collector, 6. Pyrolysis reactor, 7. Gas collector, 8. Replacement gas container;
101、钟罩法兰,102、钟罩吊环;101, bell jar flange, 102, bell jar suspension ring;
201、旋转底座,202、支撑杆,203、吊环连接件,204、啮合齿,205、通孔,206、进料管,207、加热器,208、安装孔;201, rotating base, 202, support rod, 203, ring connector, 204, meshing teeth, 205, through hole, 206, feed pipe, 207, heater, 208, mounting hole;
301、固定件,302、驱动件,303、导轨,304、移动件,305、从动轮。301, fixed part, 302, driving part, 303, guide rail, 304, moving part, 305, driven wheel.
具体实施方式detailed description
下面结合附图和实施方式对本发明作进一步的详细说明。可以理解的是,此处所描述的具体实施方式仅用于解释相关内容,而非对本发明的限定。另外还需要说明的是,为了便于描述,附图中仅示出了与本发明相关的部分。The present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments. It can be understood that the specific implementation manners described here are only used to explain relevant content, rather than to limit the present invention. In addition, it should be noted that, for the convenience of description, only the parts related to the present invention are shown in the drawings.
需要说明的是,在不冲突的情况下,本发明中的实施方式及实施方式中的特征可以相互组合。下面将参考附图并结合实施方式来详细说明本发明。It should be noted that, in the case of no conflict, the embodiments and features in the embodiments of the present invention can be combined with each other. The present invention will be described in detail below with reference to the drawings and in combination with embodiments.
实施例1Example 1
本发明提供的一种还原炉钟罩涂层回收方法,具体包括如下步骤:A kind of reduction furnace bell jar coating recovery method provided by the invention specifically comprises the following steps:
将还原炉钟罩1密封,使还原炉钟罩1内部形成一个密闭的空间,向还原炉钟罩1内输送溶解还原炉钟罩1内壁涂层的溶解液,在保证溶解液能对还原炉钟罩1内壁涂层溶解的情况下,由于还原炉钟罩1内壁涂层有金、银、铜等金属,因此,根据还原炉内壁涂层的材料不同,溶解液也可选用不同材料,溶解原理如下:The
涂层金属+溶解液→涂层金属盐溶液+气体+H2OCoating metal + solution → coating metal salt solution + gas + H 2 O
即,溶解液对还原炉钟罩1内壁涂层进行溶解后得到涂层金属盐溶液、气体和H2O,需要说明的是,此处的涂层金属盐溶液是指得到的金属盐溶液为含涂层金属离子的盐溶液,如还原炉钟罩1内壁涂层有金、银、铜等高近红外电磁波反射涂层,则形成的涂层金属盐溶液即为含金离子的盐溶液、含银离子的盐溶液、含铜离子的盐溶液等。That is, the solution dissolves the coating on the inner wall of the reduction
将溶解后生成的涂层金属盐溶液、气体和H2O从还原炉钟罩1内送出,并对得到的涂层金属盐溶液蒸发结晶后进行热解反应,热解反应原理如下:The coating metal salt solution, gas and H 2 O generated after dissolution are sent out from the
涂层金属盐→金属+气体Coating Metal Salt → Metal + Gas
即,涂层金属盐热解后得到金属和气体,此处的金属即为涂层金属材料,实现了对涂层材料的回收,避免了对金属材料的浪费,降低了企业生产成本。That is, metal and gas are obtained after pyrolysis of the coating metal salt, and the metal here is the coating metal material, which realizes the recovery of the coating material, avoids the waste of the metal material, and reduces the production cost of the enterprise.
作为本实施例更进一步的改进,涂层金属盐在热解后,对得到的气体进行收集,并将收集的气体溶解于水中,气体与水溶解后得到新的溶解液,该溶解液收集后可用溶解还原炉钟罩1内壁涂层的溶解液,实现了对溶解液的回收和闭环利用,大大降低了涂层金属的回收成本。As a further improvement of this embodiment, after the coating metal salt is pyrolyzed, the obtained gas is collected, and the collected gas is dissolved in water, and a new solution is obtained after the gas and water are dissolved. After the solution is collected, The solution that can be used to dissolve the coating on the inner wall of the
作为本实施例更进一步的改进,涂层金属盐的热解温度为400℃~1200℃,使涂层金属盐的热解效率更高,而涂层金属盐的最优热解温度可根据实际情况进行选择。As a further improvement of this embodiment, the pyrolysis temperature of the coating metal salt is 400°C to 1200°C, so that the pyrolysis efficiency of the coating metal salt is higher, and the optimal pyrolysis temperature of the coating metal salt can be determined according to the actual situation. situation to choose.
作为本实施例更进一步的改进,还原炉钟罩1呈卧式放置,使溶解液能一次性对还原炉钟罩1整个高度的内壁涂层进行溶解,使溶解液与涂层的接触面积更大,不仅方便对涂层的溶解,且能大大减小溶解液的用量,使涂层的溶解效率大大提高。As a further improvement of this embodiment, the reduction
作为本实施例更进一步的改进,溶解液在对还原炉钟罩1内壁涂层进行溶解的过程中,为了保证在采用少量溶解液的情况下能对还原炉钟罩1内壁所有的涂层进行溶解,可使还原炉钟罩1进行旋转,还原炉钟罩1的旋转速度为1r/h到1r/s之间,且还原炉钟罩1在旋转时,送入到还原炉钟罩1内的溶解液随着还原炉钟罩1的旋转对还原炉钟罩1内壁的所有涂层进行溶解,使还原炉钟罩1内壁的涂层能全部被回收。As a further improvement of this embodiment, in the process of dissolving the coating on the inner wall of the reduction
作为本实施例更进一步的改进,所述溶解液为盐酸、硝酸中的一种或多种,当溶解液为盐酸和硝酸盐两种时,盐酸和硝酸盐可按照一定比例混合配置,在实际操作过程中,溶解液的具体采用的种类可根据涂层的材料种类来选择,在保证不伤害涂层本质的情况下,使涂层的溶解效率得到保证。As a further improvement of this embodiment, the dissolving liquid is one or more of hydrochloric acid and nitric acid. When the dissolving liquid is hydrochloric acid and nitrate, the hydrochloric acid and nitrate can be mixed according to a certain proportion. During the operation, the specific type of dissolving solution can be selected according to the type of coating material, so as to ensure the dissolution efficiency of the coating without damaging the essence of the coating.
作为本实施例更进一步的改进,所述溶解液浓度为1wt%~70wt%,溶解液浓度的具体选择可根据涂层的材料种类、涂层的厚度等进行决定,在保证溶解效率的情况下,溶解液的浓度可随意选择。As a further improvement of this embodiment, the concentration of the solution is 1wt% to 70wt%. The specific choice of the concentration of the solution can be determined according to the material type of the coating, the thickness of the coating, etc. In the case of ensuring the dissolution efficiency , the concentration of the solution can be chosen arbitrarily.
作为本实施例更进一步的改进,为了方便溶解液在对涂层溶解后排出还原炉钟罩1,还原炉钟罩1上必然具有一个用于排放涂层金属盐溶液的通孔205,为了避免溶解液在对涂层溶解过程中从该通孔205泄漏,因此,送入到还原炉钟罩1内的溶解液体积不大于还原炉钟罩1内部体积的一半,使溶解液一次溶解的涂层面积不大于还原炉钟罩1内壁的一半,在避免溶解液从还原炉钟罩1内泄漏的情况下,保证溶解液一次溶解的涂层面积达到最大化。在本发明中,在不考虑溶解液用量和溶解液泄漏的情况下,此时还原炉钟罩1可呈立式放置,还原炉钟罩1也无需旋转,且溶解液的体积也可大于还原炉钟罩1内部体积的一半,甚至溶解液的体积可直接为还原炉钟罩1内部体积;同时,当还原炉钟罩1呈立式放置情况下,为了减少溶解液的使用量,溶解液也可以采用喷淋的方式作用到还原炉钟罩1内壁上,也能实现溶解液与还原炉钟罩1内壁的金属涂层进行接触并实现溶解。As a further improvement of this embodiment, in order to facilitate the dissolving solution to discharge the reduction
作为本实施例更进一步的改进,送入到还原炉钟罩1内的溶解液体积是还原炉钟罩1内部体积的使1/4~1/2,在保证溶解效率的同时避免溶解液从还原炉钟罩1内泄漏,溶解液的体积可随意选择。As a further improvement of this embodiment, the volume of the solution sent into the
作为本实施例更进一步的改进,溶解液在对还原炉钟罩1内壁涂层进行溶解过程中,对还原炉钟罩1内部加热,提高溶解液的温度,使溶解液的溶解效率大大提高。As a further improvement of this embodiment, the dissolution solution heats the interior of the reduction
作为本实施例更进一步的改进,还原炉钟罩1内部的加热温度为30℃~200℃,在不破坏溶解液的溶解质量下,还原炉钟罩1内部的加热温度可随意选择;同时,避免溶解液在对涂层溶解过程中其他气体进入还原炉钟罩1内对溶解造成影响,还原炉钟罩1内部还充入有氮气进行保压,使还原炉钟罩1内部的压力保持在0.1MPa~1MPa。As a further improvement of this embodiment, the heating temperature inside the reduction
实施例2Example 2
还原炉钟罩内壁涂层为银,还原炉钟罩涂层回收方法具体包括如下步骤:The inner wall coating of the bell jar of the reduction furnace is silver, and the method for recovering the bell jar coating of the reduction furnace specifically includes the following steps:
将还原炉钟罩1密封,使还原炉钟罩1内部形成一个密闭的空间,向还原炉钟罩1内输送溶解还原炉钟罩1内壁银涂层的溶解液HNO3,溶解液HNO3对还原炉钟罩1内壁银涂层溶解的溶解原理如下:The
Ag+HNO3→AgNO3+NOx+H2OAg+HNO 3 →AgNO 3 +NO x +H 2 O
即,溶解液对还原炉钟罩1内壁涂层进行溶解后得到AgNO3溶液、气体NOx和H2O。That is, the AgNO 3 solution, gas NO x and H 2 O are obtained after the solution dissolves the coating on the inner wall of the reduction
将溶解后生成的AgNO3溶液、气体NOx和H2O从还原炉钟罩1内送出,并对得到的AgNO3溶液蒸发结晶后进行热解反应,热解反应原理如下: The dissolved AgNO3 solution, gas NOx and H2O are sent out from the bell jar 1 of the reduction furnace, and the obtained AgNO3 solution is evaporated and crystallized for pyrolysis reaction. The principle of the pyrolysis reaction is as follows:
2AgNO3→2Ag+2NO2+O2 2AgNO 3 →2Ag+2NO 2 +O 2
即,AgNO3热解后得到Ag和气体NO2,实现了对涂层材料的回收,避免了对银材料的浪费,降低了企业生产成本。That is, Ag and gas NO 2 are obtained after AgNO 3 is pyrolyzed, which realizes the recovery of coating materials, avoids the waste of silver materials, and reduces the production cost of enterprises.
作为本实施例更进一步的改进,AgNO3在热解后,对得到的气体NO2和溶解Ag得到的气体NOX进行收集,并将收集的气体NOX溶解于水中,其反应为:As a further improvement of this embodiment, after AgNO3 is pyrolyzed, the obtained gas NO2 and gas NOx obtained by dissolving Ag are collected, and the collected gas NOx is dissolved in water, and the reaction is:
NOX+O2+H2O→HNO3 NO X +O 2 +H 2 O→HNO 3
NOX与水溶解后得到新的溶解液HNO3,该溶解液HNO3收集后可用溶解还原炉钟罩1内壁的银涂层,实现了对溶解液HNO3的回收和闭环利用,大大降低了银涂层的回收成本。After NO X is dissolved with water, a new solution HNO 3 is obtained. After the solution HNO 3 is collected, it can be used to dissolve the silver coating on the inner wall of the reduction
作为本实施例更进一步的改进,AgNO3的热解温度为400℃~1200℃,使AgNO3的热解效率更高,而AgNO3的最优热解温度可根据实际情况进行选择。As a further improvement of this embodiment, the pyrolysis temperature of AgNO 3 is 400° C. to 1200° C., so that the pyrolysis efficiency of AgNO 3 is higher, and the optimal pyrolysis temperature of AgNO 3 can be selected according to the actual situation.
作为本实施例更进一步的改进,还原炉钟罩1呈卧式放置,使溶解液HNO3能一次性对还原炉钟罩1整个高度的银涂层进行溶解,使溶解液HNO3与银涂层的接触面积更大,不仅方便对银的溶解,且能大大减小溶解液HNO3的用量,使银涂层的溶解效率大大提高。As a further improvement of this embodiment, the reduction
作为本实施例更进一步的改进,溶解液HNO3在对还原炉钟罩1内壁的银涂层进行溶解的过程中,为了保证在采用少量溶解液HNO3的情况下能对还原炉钟罩1内壁所有的银涂层进行溶解,可使还原炉钟罩1进行旋转,还原炉钟罩1的旋转速度为1r/h到1r/s之间,且还原炉钟罩1在旋转时,送入到还原炉钟罩1内的溶解液HNO3随着还原炉钟罩1的旋转对还原炉钟罩1内壁的所有银涂层进行溶解,使还原炉钟罩1内壁的银涂层能全部被回收。As a further improvement of this embodiment, in the process of dissolving the silver coating on the inner wall of the reduction
作为本实施例更进一步的改进,所述溶解液HNO3浓度为1wt%~70wt%,溶解液HNO3浓度的具体选择可根据银涂层的厚度等进行决定,在保证溶解效率的情况下,溶解液HNO3的浓度可随意选择。As a further improvement of this embodiment, the HNO3 concentration of the dissolving solution is 1wt% to 70wt%, and the specific selection of the HNO3 concentration of the dissolving solution can be determined according to the thickness of the silver coating. In the case of ensuring the dissolution efficiency, The concentration of the dissolving solution HNO 3 can be chosen arbitrarily.
作为本实施例更进一步的改进,为了方便溶解液HNO3在对银涂层溶解后排出还原炉钟罩1,还原炉钟罩1上必然具有一个用于排放AgNO3溶液的通孔205,为了避免溶解液HNO3在对银涂层溶解过程中从该通孔205泄漏,因此,送入到还原炉钟罩1内的溶解液体积不大于还原炉钟罩1内部体积的一半,使溶解液一次溶解的银涂层面积不大于还原炉钟罩1内壁的一半,在避免溶解液HNO3从还原炉钟罩1内泄漏的情况下,保证溶解液HNO3一次溶解的涂层面积达到最大化。在本发明中,在不考虑溶解液HNO3用量和溶解液HNO3泄漏的情况下,此时还原炉钟罩1可呈立式放置,还原炉钟罩1也无需旋转,且溶解液的体积也可大于还原炉钟罩1内部体积的一半,甚至溶解液的体积可直接为还原炉钟罩1内部体积;同时,当还原炉钟罩1呈立式放置情况下,为了减少溶解液的使用量,溶解液也可以采用喷淋的方式作用到还原炉钟罩1内壁上,也能实现溶解液与还原炉钟罩1内壁的金属涂层进行接触并实现溶解。As a further improvement of this embodiment, in order to make it easier for the solution HNO to discharge the reduction furnace bell jar 1 after dissolving the silver coating, the reduction furnace bell jar 1 must have a through
作为本实施例更进一步的改进,送入到还原炉钟罩1内的溶解液HNO3体积是还原炉钟罩1内部体积的使1/4~1/2,在保证溶解效率的同时避免溶解液HNO3从还原炉钟罩1内泄漏,溶解液HNO3的体积可随意选择。As a further improvement of this embodiment, the volume of the solution HNO3 that is sent into the reduction
作为本实施例更进一步的改进,溶解液在对还原炉钟罩1内壁涂层进行溶解过程中,对还原炉钟罩1内部加热,提高溶解液的温度,使溶解液的溶解效率大大提高。As a further improvement of this embodiment, the dissolution solution heats the interior of the reduction
作为本实施例更进一步的改进,还原炉钟罩1内部的加热温度为30℃~200℃,在不破坏溶解液HNO3的溶解质量下,还原炉钟罩1内部的加热温度可随意选择;同时,避免溶解液HNO3在对银涂层溶解过程中其他气体进入还原炉钟罩1内对溶解造成影响,还原炉钟罩1内部还充入有氮气进行保压,使还原炉钟罩1内部的压力保持在0.1MPa~1MPa。As a further improvement of this embodiment, the heating temperature inside the
实施例3Example 3
在本实施方式中,为了实施实施例1中的回收方法,本实施例3中还提供了一种还原炉钟罩涂层回收用辅助装置,该辅助装置用于对还原炉钟罩1固定安装,具体的,辅助装置包括卧式机架2和驱动机构3,卧式机架2即为呈卧式放置的机架,机架的轴线方向水平延伸,而驱动机构3能驱动卧式机架2进行旋转;所述卧式机架2包括旋转底座201和吊环连接件203,旋转底座201与吊环连接架之间具有一定间距,由于还原炉钟罩1下端具有钟罩法兰101,还原炉钟罩1上端具有钟罩吊环102,且钟罩法兰101为环形,钟罩吊环102为多个,多个钟罩吊环102沿还原炉钟罩1外壁圆周周向均匀间隔排布,而卧式机架2上的旋转底座201用于固定钟罩法兰101,吊环连接件203用于固定钟罩吊环102;为了保证吊环连接件203与旋转底座201之间的连接,旋转底座201与吊环连接件203之间还支撑有支撑杆202,同时,为了保持旋转底座201与吊环连接件203之间的平稳性,支撑杆202至少为两个,多个支撑杆202沿吊环连接件203的中心圆周周向均匀间隔排布。In this embodiment, in order to implement the recovery method in Example 1, an auxiliary device for recovering the coating of the reduction furnace bell jar is also provided in this embodiment 3, and the auxiliary device is used for fixed installation of the reduction
在实际使用过程中,将还原炉钟罩1下端的钟罩法兰101固定在旋转底座201上,此时旋转底座201对还原炉钟罩1下端进行封闭,使还原炉钟罩1内部形成密封腔室,为了将溶解液送入或送出还原炉钟罩1,旋转底座201还开设有供溶解液送出还原炉钟罩1的通孔205,为了避免还原炉钟罩1内的溶解液不足钟罩二分之一的情况下溶解液从通孔205内溢出,可优先将通孔205设置在旋转底座201中心,使还原炉钟罩1内溶解液的最高液面高度可达到还原炉钟罩1内部半径减去通孔205半径的差;同时,旋转底座201上还设置有延伸至还原炉钟罩1内的进料管206,使溶解液可通过进料管206加入到还原炉钟罩1内。In the actual use process, the
在本发明中,为了避免因进料管206偏心安装在旋转底座201上而导致还原炉钟罩1在旋转过程中连接进料管206的管道受到甩动,还可扩大通孔205孔径,将进料管206安装在通孔205内,且为了避免进料管206对通孔205封堵,进料管206的外壁直径小于通孔205孔径,使进料管206外壁与通孔205孔壁之间具有间隙,使还原炉钟罩1内的溶解液可通过该间隙排出还原炉钟罩1。在本发明中,由于进料管206安装在通孔205内的同时不能对通孔205进行封堵,因此,进料管206在安装时,可在通孔205内固定多个向通孔205中心的加强杆,将进料管206共同固定在多个加强杆上,从而实现对进料管206的固定安装。In the present invention, in order to avoid that the pipe connecting the
在需要对还原炉钟罩1内壁涂层进行回收时,可先将卧式机架2呈竖直放置,采用吊装设备对还原炉钟罩1呈竖直吊装,在吊装过程中使还原炉钟罩1下端的钟罩法兰101穿过吊环连接件203,使还原炉钟罩1放置在旋转底座201上,钟罩吊环102支撑在吊环连接件203上,而还原炉钟罩1放置在旋转底座201上的同时进料管206伸入至还原炉钟罩1内,最后采用螺钉将钟罩法兰101固定在旋转底座201上,并采用螺钉将钟罩吊环102固定在吊环连接件203上,使还原炉钟罩1固定在卧式机架2上。When it is necessary to reclaim the coating on the inner wall of the
对安装好还原炉钟罩1的卧式机架2进行吊装,使安装好还原炉钟罩1的卧式机架2呈卧式放置并与驱动机构3传动,不仅实现还原炉钟罩1的卧式安装,且实现对还原炉钟罩1的驱动,使还原炉钟罩1在呈卧式状态时进行旋转,从而满足还原炉钟罩1内壁涂层回收时使用。Hoist the
作为本实施例更进一步的改进,所述进料管206上设有加热器207,该加热器207可以为电加热器207,加热器207不仅能对通过进料管206送入的溶解液进行加热,还能对还原炉钟罩1内部环境进行加热,使溶解液在对涂层材料进行溶解时的溶解效率更高。As a further improvement of this embodiment, the
作为本实施例更进一步的改进,所述驱动机构3包括主动驱动结构和从动驱动结构,主动驱动结构为主动对卧式机架2驱动的驱动结构,从动驱动结构为受主动驱动结构带动而使卧式机架2从动驱动的驱动结构,且主动驱动结构和从动驱动结构分别位于卧式机架2的两端,使卧式机架2的一端通过主动驱动结构驱动,卧式机架2的另一端随主动驱动结构的驱动进行从动转动,使卧式机架2的转动更加平稳。此处需要说明的是,在本实施例中,从动驱动结构也可为多个,此时,多个从动驱动结构与主动驱动结构共同沿卧式机架2的轴线方向均匀间隔排布,不仅使卧式机架2能受到足够的支撑,且保证了卧式机架2在旋转时更加平稳。As a further improvement of this embodiment, the driving mechanism 3 includes an active driving structure and a driven driving structure, the active driving structure is a driving structure that actively drives the
作为本实施例更进一步的改进,所述旋转底座201为圆形,通孔205位于旋转底座201的中心,使还原炉钟罩1安装完毕后,最多可向还原炉钟罩1内注入溶解液的液面高度为还原炉钟罩1内壁半径减去通孔205半径,使还原炉钟罩1内注入溶解液能达到最大量,从而使注入还原炉钟罩1内的溶解液用量的选择范围更大,在保证溶解效率的同时可使用最少的溶解液。所述主动驱动结构包括固定件301和驱动件302,固定架可直接固定在地面上或基座上,驱动件302的轴线沿水平方向延伸,且驱动件302为两个,两个驱动件302之间具有一定间距,卧式机架2呈卧式状态放置时,旋转底座201的外圆面共同支撑在两个驱动件302上,通过驱动件302与旋转底座201外圆面的配合,在实现对旋转底座201支撑的同时不影响旋转底座201和驱动件302的转动。As a further improvement of this embodiment, the rotating
为了驱动旋转底座201转动,固定件301上还安装有用于驱动驱动件302转动的驱动电机(图中未示出),该驱动电机为一个,且该驱动电机可驱动任意一个驱动件302转动即可;同时,驱动电机输出端可通过联轴器直接与驱动件302的轮轴连接,且为了降低驱动件302的转速,还可设置减速器,使驱动电机输出端与减速器输入端连接,减速器输出端与驱动件302的轮轴连接;当然,在未设置减速器的情况下,驱动电机也可采用变频电机,通过调节驱动电机的频率来调节驱动电机的转速,从而调节驱动件302的转速。In order to drive the rotating
作为本实施例更进一步的改进,所述驱动件302和旋转底座201上均设置有啮合齿204,即驱动件302为小齿轮,旋转底座201为大齿轮,且驱动件302上的啮合齿204与旋转底座201上的啮合齿204相互啮合,有效避免驱动件302与旋转底座201之间打滑,使驱动件302与旋转底座201之间的相互转动更加平稳,避免安装在卧式机架2上的还原炉钟罩1在涂层回收过程中产生震动,使溶解液对涂层的溶解得到保证。As a further improvement of this embodiment, the driving
作为本实施例更进一步的改进,所述支撑杆202为可伸缩结构,支撑杆202可直接采用液压杆、气缸或电子伸缩件等自动伸缩元件,通过支撑杆202的伸缩,使旋转底座201与吊环连接件203之间的间距可进行调节,从而满足不同高度的还原炉钟罩1的安装,使辅助装置适用范围更广。As a further improvement of this embodiment, the
作为本实施例更进一步的改进,所述吊环连接件203为环形,吊环连接件203的内径大于还原炉钟罩1上的钟罩法兰101直径,保证还原炉钟罩1安装在卧式机架2上时钟罩法兰101能穿过吊环连接件203与旋转底座201抵拢;同时,由于吊环连接件203内径大于钟罩法兰101直径,因此,还原炉钟罩1上的钟罩吊环102长度需大于钟罩法兰101的宽度,优选的,钟罩吊环102的延伸端与吊环连接件203的外圆面平齐。所述从动驱动结构包括可沿支撑杆202长度方向往复运动的移动件304,移动件304的移动方向与支撑杆202的伸缩方向一致,且还原炉钟罩1安装时,移动件304的移动方向、移动距离与支撑杆202的伸缩方向、伸缩距离相同;所述移动件304上还支承有两个从动轮305,以吊环连接件203的圆心为圆心,两个从动轮305均位于以该圆心所形成的圆环上,从而使两个从动轮305的轮面均与吊环连接件203的外圆面配合,使卧式机架2呈卧式状态放置时,吊环连接件203的外圆面共同支撑在两个从动轮305上,通过从动轮305外圆面与吊环连接件203外圆面的配合,在实现对吊环连接件203支撑的同时不影响从动轮305与吊环连接件203的转动。As a further improvement of this embodiment, the
通过驱动电机驱动驱动件302转动,并通过驱动件302外圆面与旋转底座201啮合,使驱动件302在转动的同时带动旋转底座201转动,且由于吊环连接件203与旋转底座201通过支撑杆202连接,吊环连接件203与从动轮305配合,使旋转底座201在转动的同时吊环连接件203与驱动件302相对转动,使卧式机架2和安装在卧式机架2上的还原炉钟罩1同步转动,使注入到还原炉钟罩1内溶解液对涂层进行溶解。The driving
作为本实施例更进一步的改进,所述从动驱动结构还包括导轨303,导轨303的长度方向与支撑杆202的轴线方向一致,且导轨303上具有滑槽,滑槽的横截面呈矩形或┻型,移动件304为在滑槽内可往复滑动的滑块,移动件304的横截面呈T型,移动件304可沿滑槽往复滑动,为了使移动件304滑动至滑槽的固定位置后不会继续滑动,还可在移动件304上设置螺钉,当移动件304滑动至固定位置后,拧紧螺钉,使螺钉抵紧在导轨303上,而当移动件304需要滑动时,松动螺钉即可。在本实施例中,导轨303的横截面还可以为“工”型,此时,可在移动件304下表面开设T型槽,并使移动件304通过T型槽滑动卡设在导轨303上,同时,为了防止移动件304从导轨303上脱落,还可在导轨303的两端设置对移动件304限制的挡块。As a further improvement of this embodiment, the driven driving structure further includes a
作为本实施例更进一步的改进,所述旋转底座201和吊环连接件203上还开设有多个安装孔组,旋转底座201上的多个安装孔组沿旋转底座201的半径方向间隔排布,旋转底座201上每个安装孔组均包括以旋转底座201中心圆周周向间隔排布的安装孔208,而吊环连接件203上的多个安装孔组沿吊环连接件203的半径方向间隔排布,吊环连接件203上每个安装孔组均包括以吊环连接件203中心圆周周向间隔排布的安装孔208。通过旋转底座201上设置的安装孔208和吊环连接件203上设置的安装孔208配合,使卧式机架2上可安装不同尺寸的还原炉钟罩1。As a further improvement of this embodiment, the rotating
为了避免将大尺寸还原炉钟罩1安装在辅助装置上时,因还原炉钟罩1上钟罩法兰101的直径大于靠近旋转底座201中心安装孔组所形成的圆的直径,而导致还原炉钟罩1安装在辅助装置上后,送入到还原炉钟罩1内的溶解液会直接通过靠近旋转底座201中心部分的安装孔组流出,因此,当还原炉钟罩1安装在辅助装置上后,可采用木质封堵头或橡胶封堵头将旋转底座201上其余的安装孔208进行堵塞;当然,也可在还原炉钟罩1未安装在辅助装置上之前将旋转底座201上所有的安装孔208均采用木质封堵头或橡胶封堵头进行封堵,在需要安装还原炉钟罩1时,将与钟罩法兰101上螺栓孔对应的安装孔208中的木质封堵头或橡胶封堵头取出即可。因此,在旋转底座201上开设多个安装孔组,并使多个安装孔组沿旋转底座的半径方向间隔排布,在满足安装不同尺寸还原炉钟罩1的情况下,并不影响溶解液对还原炉钟罩1内壁金属涂层的溶解。In order to avoid the large-size
当还原炉钟罩1内壁的涂层在回收之前需要使还原炉钟罩1在呈卧式状态的同时进行旋转,此时,还原炉钟罩1则可安装在辅助装置,使还原炉钟罩1在卧式状态下进行旋转,具体如下:When the coating on the inner wall of the reduction
通过吊装工具对卧式机架2进行吊装,使卧式机架2与驱动机构3脱离呈竖直放置,接着,伸缩杆收缩,伸缩杆带动吊环连接件203向旋转底座201靠近,采用吊装工具对还原炉钟罩1进行吊取,吊装工具在吊取过程中,吊取的还原炉钟罩1下端的钟罩法兰101穿过吊环连接件203向下放置在旋转底座201上,并使还原炉钟罩1中心轴线与旋转底座201中心在同一直线上,而在还原炉钟罩1放置在旋转底座201上的同时,安装在通孔205内的进料管206伸入到还原炉钟罩1内部,接着,采用螺钉将钟罩法兰101与旋转底座201固定,伸缩杆伸长,伸缩杆带动吊环连接件203靠近钟罩吊环102,在吊环连接件203与钟罩吊环102抵拢时,伸缩杆停止伸长,采用螺钉将钟罩吊环102与吊环连接件203固定,使还原炉钟罩1固定在卧式机架2上。The
松动移动件304,手动推动移动件304沿轨道滑动,当移动件304上的从动轮305与固定件301上的驱动件302之间的间距与旋转底座201与吊环连接件203之间的间距相等时,将移动件304与导轨303固定;通过吊装工具将安装有还原炉钟罩1的卧式机架2呈卧式放倒,并通过吊装工具对放倒的卧式机架2进行吊装,在吊装过程中,将旋转底座201共同放置在两个驱动件302上,将吊环连接件203共同放置在两个从动轮305上,使固定有还原炉钟罩1的卧式机架2放置在驱动机构3上。Loosen the moving
将溶解液通过进料管206送入到还原炉钟罩1内,当溶解涂层用的溶解液在通过进料管206送入到还原炉钟罩1后,启动驱动电机,驱动电机带动其中一个驱动件302转动,通过驱动件302与旋转底座201啮合,使驱动件302在转动时带动旋转底座201转动,并通过吊环连接件203与从动轮305的配合,从而使卧式机架2和安装在卧式机架2上的还原炉钟罩1同步转动,使还原炉钟罩1在卧式状态下进行旋转,通过还原炉钟罩1的旋转,溶解液与涂层接触,溶解液对涂层进行溶解,实现了对涂层的回收;而在溶解液输送和溶解液溶解涂层过程中,加热器207对溶解液和还原炉钟罩1内部环境进行加热。The solution is sent into the reduction
当溶解液对涂层溶解后需排出还原炉钟罩1时,吊装工具对卧式机架2进行吊取,使其处于立式状态,此时,还原炉钟罩1内的生成的涂层金属盐溶液可通过通孔205孔壁与进料管206之间的间隙排出,加热器207停止加热。When the solution needs to be discharged from the reduction
在本实施例中,为了使操作更加简单,还可设置一个翻转架,并将固定件301和轨道均安装在翻转架上,而为了避免卧式机架2在通过翻转架翻转过程中旋转底座201与驱动件302脱离、吊环连接件203与从动轮305脱离,还可在翻转架上固定一个用于对卧式机架2绑固和解绑方便的绑定结构,使翻转架在对卧式机架2翻转过程中绑定结构能将卧式机架2绑固在翻转架上,使还原炉钟罩1在需要安装在卧式机架2上时或还原炉钟罩1在需要从卧式机架2上拆下时或还原炉钟罩1内的涂层金属盐溶液在需要排出时,翻转架能对卧式机架2进行翻转使其处于竖立状态,从而使还原炉钟罩1在安装或拆取过程中均无需再将卧式机架2从驱动机构3上吊转,使还原炉钟罩1的安装、拆卸更加方便。In this embodiment, in order to make the operation easier, a flip frame can also be set, and the fixing
实施例4Example 4
在实施例1中的回收方法和实施例2中的辅助装置的基础上,为了使送入到还原炉钟罩1内的溶解液能进行循环使用,本实施例3还提供了一种还原炉钟罩涂层回收用溶解液循环系统,除了包括如实施例2中所述的辅助装置以外,还包括溶解液容器4和涂层金属盐收集器5,溶解液容器4用于对溶解涂层的溶解液进行储存,涂层金属盐收集器5用于对涂层溶解后形成的涂层金属盐溶液进行收集,具体的,溶解液容器4出口端与进料管206进口端连接,由于还原炉钟罩1安装在卧式机架2上后需要进行旋转,因此,为了避免卧式机架2在带动还原炉钟罩1旋转过程中连接进料管206与溶解液容器4的管道缠绕,其管道出口端与进料管206进口端之间通过旋转接头连接;同理,为了避免卧式机架2在带动还原炉钟罩1旋转过程中连接通孔205与涂层金属盐收集器5的管道缠绕,该管道进口端与通孔205之间也通过旋转接头连接。On the basis of the recovery method in
当还原炉钟罩1安装在卧式机架2上后需要对涂层进行溶解时,将溶解液容器4内的溶解液通过进料管206送入到还原炉钟罩1内,当送入到还原炉钟罩1内的溶解液的量达到要求时,停止向还原炉钟罩1内输送溶解液;启动驱动电机,驱动电机带动其中一个驱动件302转动,通过旋转底座201与驱动件302啮合,使驱动件302在转动时带动旋转底座201转动,并通过吊环连接件203与从动轮305的配合,从而使卧式机架2和安装在卧式机架2上的还原炉钟罩1同步转动,使还原炉钟罩1在卧式状态下进行旋转,通过还原炉钟罩1的旋转,溶解液与涂层接触,溶解液对涂层进行溶解。When the reduction
当溶解液与涂层完全溶解生成涂层金属盐溶液时,吊装工具对卧式机架2进行吊取,使其处于立式状态,此时,还原炉钟罩1内的生成的涂层金属盐溶液可通过通孔205孔壁与进料管206之间的间隙排出送入到涂层金属盐收集器5内,完成了对涂层的回收。When the solution and the coating are completely dissolved to generate a coating metal salt solution, the hoisting tool lifts the
作为本实施例更进一步的改进,所述涂层金属盐收集器5的出口端还连接有热解反应器6,热解反应器6用于使收集的涂层金属盐溶液进行蒸发结晶并在结晶后进行热解反应,从而还原得到金属和气体,且热解反应器6出口端还连接有气体收集器7,气体收集器7用于对热解反应过程中生成的气体进行收集。通过对气体和金属分开收集,使气体后续可进行循环使用,使金属后续可继续制备多晶硅还原炉钟罩1内壁的涂层,实现了涂层的回收和闭环利用。As a further improvement of this embodiment, the outlet end of the coating
作为本实施例更进一步的改进,所述气体收集器7上还连接有将热解产生的气体输送至溶解液容器4内的第一输送管路,使后期得到的气体可溶解于溶解液中继续用于涂层回收,实现了溶解液的回收和闭环利用。As a further improvement of this embodiment, the
作为本实施例更进一步的改进,由于涂层与溶解液反应过程中除了生成涂层金属盐溶液之外还会生成气体,因此,涂层金属盐收集器5与气体收集器7之间还连接有第二输送管道(图中未示出),第二输送管道能将涂层溶解过程中产生的气体直接由涂层金属盐收集器5输送到气体收集器7内。As a further improvement of this embodiment, since the coating and the solution react in addition to generating the coating metal salt solution, gas will also be generated, therefore, the coating
作为本实施例更进一步的改进,由于溶解液与涂层金属在反应过程中需对还原炉钟罩1内进行保压,因此,溶解液容器4上还连接有置换气体容器8,置换气体容器8内填充有用于对还原炉钟罩1内保压的氮气,通过将其并联在溶解液容器4出口端,使置换气体容器8内的氮气通过进料管206送入到还原炉钟罩1内,使还原炉钟罩1内溶解液与涂层金属在反应过程中产生的气体通过通孔205依次送入到金属盐收集器5和气体收集器7内,最终置换到气体收集器7内。As a further improvement of this embodiment, since the solution and the coating metal need to maintain the pressure in the reduction
当本系统与辅助装置配合使用时,具体工作原理如下:When the system is used in conjunction with auxiliary devices, the specific working principle is as follows:
当需要对还原炉钟罩1内壁的涂层进行回收时,先对还原炉钟罩1进行安装,还原炉钟罩1的安装方式如下:When the coating on the inner wall of the reduction
通过吊装工具对卧式机架2进行吊装,使卧式机架2与驱动机构3脱离呈竖直放置,接着,伸缩杆收缩,伸缩杆带动吊环连接件203向旋转底座201靠近,采用吊装工具对还原炉钟罩1进行吊取,吊装工具在吊取过程中,吊取的还原炉钟罩1下端的钟罩法兰101穿过吊环连接件203向下放置在旋转底座201上,并使还原炉钟罩1中心轴线与旋转底座201中心在同一直线上,而在还原炉钟罩1放置在旋转底座201上的同时,安装在通孔205内的进料管206伸入到还原炉钟罩1内部,接着,采用螺钉将钟罩法兰101与旋转底座201固定,伸缩杆伸长,伸缩杆带动吊环连接件203靠近钟罩吊环102,在吊环连接件203与钟罩吊环102抵拢时,伸缩杆停止伸长,采用螺钉将钟罩吊环102与吊环连接件203固定,使还原炉钟罩1固定在卧式机架2上。The
松动移动件304,手动推动移动件304沿轨道滑动,当移动件304上的从动轮305与固定件301上的驱动件302之间的间距与旋转底座201与吊环连接件203之间的间距相等时,将移动件304与导轨303固定;通过吊装工具将安装有还原炉钟罩1的卧式机架2呈卧式放倒,并通过吊装工具对放倒的卧式机架2进行吊装,在吊装过程中,将旋转底座201共同放置在两个驱动件302上,将吊环连接件203共同放置在两个从动轮305上,使固定有还原炉钟罩1的卧式机架2放置在驱动机构3上。Loosen the moving
接着,对原炉钟罩内壁的涂层进行溶解、回收,溶解、回收方式如下:Then, the coating on the inner wall of the bell jar of the former furnace is dissolved and recovered, and the dissolution and recovery methods are as follows:
将溶解液容器4出口端与进料管206进口端通过旋转接头和管道连接,并将通孔205与涂层金属盐收集器5进口端通过旋转接头和管道连接,使溶解液容器4内的溶解液通过进料管206送入到还原炉钟罩1内,当送入到还原炉钟罩1内的溶解液的量达到要求时,停止向还原炉钟罩1内输送溶解液;启动驱动电机,驱动电机带动其中一个驱动件302转动,通过驱动件302与旋转底座201啮合,使驱动件302在转动时带动旋转底座201转动,并通过吊环连接件203与从动轮305的配合,从而使卧式机架2和安装在卧式机架2上的还原炉钟罩1同步转动,使还原炉钟罩1在卧式状态下进行旋转,通过还原炉钟罩1的旋转,溶解液与涂层接触,溶解液对涂层进行溶解。The outlet end of the solution container 4 is connected with the inlet end of the
接着,打开置换气体容器8,置换气体容器8内的氮气通过进料管206送入到还原炉钟罩1内,使溶解液在溶解涂层金属过程中产生的气体通过通孔205排出并进入到涂层金属盐收集器5内,进入到涂层金属盐收集器5内的气体通过第二输送管道送入到气体收集器7内,最终使溶解液在溶解涂层金属过程中产生的气体被置换到气体收集器7。Then, the
当溶解液与涂层完全溶解生成涂层金属盐溶液时,吊装工具对卧式机架2进行吊取,使卧式机架2处于立式状态,此时,还原炉钟罩1内的生成的涂层金属盐溶液和气体可通过通孔205孔壁与进料管206之间的间隙排出并送入到涂层金属盐收集器5内,进入涂层金属盐收集器5内的气体通过输送管道直接送入到气体收集器7内,而进入涂层金属盐收集器5内的涂层金属盐溶液送入到热解反应器6内进行热解,涂层金属盐溶液热解生成金属和气体,生成的金属直接送出热解反应器6,生成的气体送入到气体收集器7内,收集在气体收集器7内的气体送入到溶解液容器4内,溶解液容器4内的溶解液对气体进行吸收得到新的溶解液,用于下一次涂层回收。When the solution and the coating are completely dissolved to generate a coating metal salt solution, the hoisting tool lifts the
在本说明书的描述中,参考术语“一个实施例/方式”、“一些实施例/方式”、“示例”、“具体示例”、或“一些示例”等的描述意指结合该实施例/方式或示例描述的具体特征、结构、材料或者特点包含于本申请的至少一个实施例/方式或示例中。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/方式或示例。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/方式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/方式或示例以及不同实施例/方式或示例的特征进行结合和组合。In the description of this specification, descriptions referring to the terms "one embodiment/mode", "some embodiments/modes", "examples", "specific examples", or "some examples" mean that the embodiments/modes are combined The specific features, structures, materials or characteristics described in or examples are included in at least one embodiment/mode or example of the present application. In this specification, the schematic representations of the above terms do not necessarily refer to the same embodiment/mode or example. Moreover, the described specific features, structures, materials or characteristics may be combined in any one or more embodiments/modes or examples in an appropriate manner. In addition, those skilled in the art may combine and combine different embodiments/modes or examples and features of different embodiments/modes or examples described in this specification without conflicting with each other.
此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括至少一个该特征。在本申请的描述中,“多个”的含义是至少两个,例如两个,三个等,除非另有明确具体的限定。In addition, the terms "first" and "second" are used for descriptive purposes only, and cannot be interpreted as indicating or implying relative importance or implicitly specifying the quantity of indicated technical features. Thus, the features defined as "first" and "second" may explicitly or implicitly include at least one of these features. In the description of the present application, "plurality" means at least two, such as two, three, etc., unless otherwise specifically defined.
本领域的技术人员应当理解,上述实施方式仅仅是为了清楚地说明本发明,而并非是对本发明的范围进行限定。对于所属领域的技术人员而言,在上述公开的基础上还可以做出其它变化或变型,并且这些变化或变型仍处于本发明的范围内。It should be understood by those skilled in the art that the above embodiments are only for clearly illustrating the present invention, rather than limiting the scope of the present invention. For those skilled in the art, other changes or modifications can be made on the basis of the above disclosure, and these changes or modifications are still within the scope of the present invention.
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CN111408503A (en) * | 2020-04-07 | 2020-07-14 | 亚洲硅业(青海)股份有限公司 | Spraying equipment |
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CN207957778U (en) * | 2018-02-08 | 2018-10-12 | 亚洲硅业(青海)有限公司 | A kind of reduction furnace bell jar rotating device |
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