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CN109078442A - A kind of crystal pulling furnace richness argon tail gas oil removing system - Google Patents

A kind of crystal pulling furnace richness argon tail gas oil removing system Download PDF

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Publication number
CN109078442A
CN109078442A CN201811086354.7A CN201811086354A CN109078442A CN 109078442 A CN109078442 A CN 109078442A CN 201811086354 A CN201811086354 A CN 201811086354A CN 109078442 A CN109078442 A CN 109078442A
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tail gas
argon
filter
oil
crystal pulling
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杜大艳
袁有录
杨涛
焦文艺
刘隆益
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HUBEI HEYUAN GASES Co Ltd
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HUBEI HEYUAN GASES Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of methods or devices for separating particles from gases or vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0003Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
    • B01D5/0012Vertical tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/0072Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/002Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

本发明涉及一种拉晶炉富氩尾气除油系统,包括沿尾气进气方向依次设置的至少一台与富氩尾气管道连接的真空泵、与真空泵连接的丝网过滤器、至少一台与丝网过滤器连接的风机、与风机连接的冷却器、至少一台与冷却器连接的滤芯过滤器、与滤芯过滤器连接的静电除油装置、至少一台与静电除油装置连接的脱油吸附筒以及与脱油吸附筒连接的气柜;本发明使用多种组合方式,逐级将富氩尾气中油去除,达到后续低温净化的要求,同时减少了风机数量,只使用了三台风机,减少了动设备,从而减少了故障率。

The invention relates to an argon-rich tail gas degreasing system of a crystal pulling furnace, which comprises at least one vacuum pump connected to the argon-rich tail gas pipeline, a wire mesh filter connected to the vacuum pump, at least one A fan connected to the mesh filter, a cooler connected to the fan, at least one element filter connected to the cooler, an electrostatic degreasing device connected to the filter element filter, at least one degreasing adsorption device connected to the electrostatic degreasing device cylinder and a gas cabinet connected to the deoiling adsorption cylinder; the present invention uses a variety of combinations to remove the oil in the argon-rich tail gas step by step to meet the requirements for subsequent low-temperature purification, and at the same time reduces the number of fans. Only three fans are used, reducing the The equipment is activated, thereby reducing the failure rate.

Description

一种拉晶炉富氩尾气除油系统A crystal pulling furnace argon-rich tail gas degreasing system

技术领域technical field

本发明涉及油气分离技术领域,尤其涉及一种拉晶炉富氩尾气除油系统。The invention relates to the technical field of oil and gas separation, in particular to an argon-rich tail gas deoiling system of a crystal pulling furnace.

背景技术Background technique

单晶硅的太阳能企业,在生产过程中,需要将大量高纯氩气充入多晶硅生产炉或单晶硅生产炉,作为保护气体,防止空气进入。含氩气的尾气被真空泵抽出排入大气,造成了浪费。单晶硅生产过程中排出的富氩气尾气中氩气的含量高达98%,具有很高的提取价值。同时排放的富氩尾气中含有CO、CH4、烃类、油、灰尘等对空气造成污染、对人体有伤害的物质。Monocrystalline silicon solar energy companies need to fill a large amount of high-purity argon into the polysilicon production furnace or monocrystalline silicon production furnace during the production process as a protective gas to prevent air from entering. The tail gas containing argon is pumped out by the vacuum pump and discharged into the atmosphere, resulting in waste. The content of argon in the argon-rich tail gas discharged during the production of monocrystalline silicon is as high as 98%, which has a high extraction value. At the same time, the argon-rich tail gas discharged contains CO, CH 4 , hydrocarbons, oil, dust and other substances that pollute the air and are harmful to the human body.

同时富氩尾气中含有油和灰尘,油尘难于去除,容易增加系统阻力甚至阻塞管道。油污的存在会大大降低除尘设备的效率甚至失效,而灰尘的存在又会降低除油设备效率甚至堵塞除油设备,油和灰尘同时高效去除技术是当前面临的技术难题。At the same time, the argon-enriched tail gas contains oil and dust, which is difficult to remove, and it is easy to increase the system resistance and even block the pipeline. The existence of oil pollution will greatly reduce the efficiency or even failure of the dust removal equipment, and the existence of dust will reduce the efficiency of the oil removal equipment or even block the oil removal equipment. The efficient removal of oil and dust at the same time is currently a technical problem.

目前国内文献关于富氩尾气回收处理研究很少,实际将富氩尾气回收并提纯高纯氩的项目还没有,国内文献集中在理论上利用低温方式把富氩尾气中杂质去除得到高纯氩,或简单一笔带过说需要把油尘去除,并没有考虑其中的技术难度。经过实际调试发现,富氩尾气中含油量非常大。At present, there are few domestic literatures on the recovery and treatment of argon-rich tail gas. There is no actual project to recover argon-rich tail gas and purify high-purity argon. Or simply mention that the oil and dust need to be removed, without considering the technical difficulty. After actual debugging, it is found that the oil content in the argon-rich tail gas is very large.

申请号为CN201721189615.9的发明专利中使用简单的H型管加除油吸附桶模式无法将油净化到工艺要求的效果。In the invention patent with the application number CN201721189615.9, the simple H-shaped tube plus oil removal adsorption bucket mode cannot purify the oil to the effect required by the process.

拉晶厂家一般都有成百上千台拉晶炉,这些拉晶炉分布在多个车间,要将这些尾气除油后回收,申请号为CN201721189615.9的发明专利中是采用在每个车间安装风机,将该车间的尾气通过管道送入风机,每个车间的风机再汇合集中到总管中,这种方案的缺点在于风机数量太多,风机属于用电的动设备,一旦一台风机故障,其它风机的气体就会经过故障风机倒流,从而使得气体无法回收。Crystal pulling manufacturers generally have hundreds of crystal pulling furnaces. These crystal pulling furnaces are distributed in multiple workshops. To recover these exhaust gases after degreasing, the invention patent with application number CN201721189615.9 is used in each workshop Install the fan, send the tail gas of the workshop into the fan through the pipeline, and then gather the fans of each workshop into the main pipe. The disadvantage of this solution is that there are too many fans, and the fans are dynamic equipment that consumes electricity. Once a fan fails , the gas of other fans will flow back through the faulty fan, so that the gas cannot be recovered.

基于此,针对现有技术中的不足,需要一种能够将富氩尾气中的油处理干净、同时减少风机数量降低风险的拉晶炉富氩尾气除油系统被设计出来。Based on this, in view of the deficiencies in the prior art, it is necessary to design a crystal pulling furnace argon-rich tail gas oil removal system that can clean the oil in the argon-rich tail gas and reduce the number of fans and reduce the risk.

发明内容Contents of the invention

本发明的目的是为了克服现有技术的不足,得到一种能够将富氩尾气中的油处理干净、同时减少风机数量降低风险的拉晶炉富氩尾气除油系统。The purpose of the present invention is to overcome the deficiencies of the prior art and obtain a crystal pulling furnace argon-rich tail gas deoiling system that can clean the oil in the argon-rich tail gas while reducing the number of fans and reducing the risk.

本发明是通过以下技术方案实现:The present invention is realized through the following technical solutions:

一种拉晶炉富氩尾气除油系统,包括沿尾气进气方向依次设置的至少一台与富氩尾气管道连接的真空泵、与真空泵连接的丝网过滤器、至少一台与丝网过滤器连接的风机、与风机连接的冷却器、至少一台与冷却器连接的滤芯过滤器、与滤芯过滤器连接的静电除油装置、至少一台与静电除油装置连接的脱油吸附筒以及与脱油吸附筒连接的气柜;其中,A crystal pulling furnace argon-rich tail gas deoiling system, comprising at least one vacuum pump connected to the argon-rich tail gas pipeline, a wire mesh filter connected to the vacuum pump, at least one wire mesh filter arranged in sequence along the tail gas inlet direction A fan connected to the fan, a cooler connected to the fan, at least one element filter connected to the cooler, an electrostatic degreasing device connected to the filter element filter, at least one deoiling adsorption cylinder connected to the electrostatic degreasing device, and The gas cabinet connected to the deoiling adsorption cylinder; among them,

真空泵与丝网过滤器组成系统内的预处理除油部分,风机与冷却器组成系统内的再处理除油部分,滤芯过滤器组成系统内过滤除油部分,静电除油装置组成系统内的静电除油部分,脱油吸附筒组成系统内的脱油吸附部分。Vacuum pump and wire mesh filter constitute the pretreatment and degreasing part of the system, fans and coolers constitute the reprocessing and degreasing part of the system, filter element filters constitute the filtering and degreasing part of the system, and electrostatic degreasing devices constitute the electrostatic degreasing part of the system. The deoiling part and the deoiling adsorption cartridge form the deoiling and adsorbing part of the system.

进一步地,所述丝网过滤器内设置有若干个钢丝球,所述丝网过滤器底部设置有排油管道。Further, several steel wool balls are arranged in the wire mesh filter, and an oil discharge pipe is arranged at the bottom of the wire mesh filter.

进一步地,所述冷却器包括多排冷却流程管、设置在冷却流程管外的翅片、套接在翅片外以容纳冷却流程管和翅片的套管、隔板以及箱体;所述隔板具有上隔板和下隔板,以形成夹持套管两端的夹持空间,所述上隔板和下隔板上设置有与套管相适配的通孔;所述箱体内形成有容纳隔板的工作区域,具有设置在箱体上壁的排气孔和设置在箱体侧壁底部的进气孔;每排冷却流程管包括正反交替折弯的多个U型折弯管,每排冷却流程管具有首端和末端,每排冷却流程管的首端延伸出下隔板外端并连接至出液管,所述出液管穿出对应箱体的侧壁,每排冷却流程管的末端延伸出上隔板外端并连接至进液管,所述进液管穿出对应箱体的侧壁。Further, the cooler includes multiple rows of cooling process tubes, fins arranged outside the cooling process tubes, sleeves sleeved outside the fins to accommodate the cooling process tubes and fins, partitions and boxes; The baffle has an upper baffle and a lower baffle to form a clamping space for clamping the two ends of the casing, and the upper baffle and the lower baffle are provided with through holes adapted to the casing; There is a working area for accommodating partitions, with exhaust holes set on the upper wall of the box and air inlet holes set at the bottom of the side walls of the box; each row of cooling process tubes includes multiple U-shaped bends that are bent alternately in front and back Each row of cooling process tubes has a head end and an end. The head end of each row of cooling process tubes extends out of the outer end of the lower partition and is connected to the liquid outlet pipe. The liquid outlet pipe passes through the side wall of the corresponding box. The ends of the row cooling process pipes extend out from the outer end of the upper partition and are connected to the liquid inlet pipe, and the liquid inlet pipe passes through the side wall of the corresponding box body.

更进一步地,所述冷却流程管外缘设置有沿管子轴线延伸的若干翅片,所述翅片呈环形阵列均匀分布。Furthermore, the outer edge of the cooling process tube is provided with several fins extending along the axis of the tube, and the fins are evenly distributed in an annular array.

更进一步地,所述箱体的下壁倾斜设置,并在在下壁的最低处侧设置有排油管道,所述排油管道上设置有排油阀。Furthermore, the lower wall of the box is inclined, and an oil discharge pipe is provided on the lowest side of the lower wall, and an oil discharge valve is provided on the oil discharge pipe.

进一步地,所述滤芯过滤器内设置有滤芯,所述滤芯具有若干孔隙。Further, a filter element is arranged inside the filter element, and the filter element has several pores.

进一步地,所述静电除油装置外加有14KV-16KV的高压直流电以形成二个极性相反的电场。Further, the electrostatic degreasing device is externally supplied with a high-voltage direct current of 14KV-16KV to form two electric fields with opposite polarities.

进一步地,所述脱油吸附筒内设置有硅酸盐吸附剂。Further, a silicate adsorbent is arranged in the deoiling adsorption cylinder.

进一步地,所述风机并联设置有三台。Further, there are three fans arranged in parallel.

进一步地,所述冷却器与风机之间的管道上还设置有冷却水夹套,所述冷却水夹套上设置有冷冻水管道。Further, a cooling water jacket is provided on the pipeline between the cooler and the fan, and a chilled water pipeline is provided on the cooling water jacket.

与现有的技术相比,本发明的有益效果是:本发明使用多种组合方式,逐级将富氩尾气中油去除,达到后续低温净化的要求,同时减少了风机数量,只使用了三台风机,减少了动设备,从而减少了故障率。Compared with the existing technology, the beneficial effect of the present invention is: the present invention uses a variety of combination methods to remove the oil in the argon-rich tail gas step by step, so as to meet the requirements of subsequent low-temperature purification, and at the same time reduce the number of fans, only three are used The fan reduces the number of moving equipment, thereby reducing the failure rate.

附图说明Description of drawings

图1是本发明一个实施例的系统结构示意图;Fig. 1 is a schematic diagram of the system structure of an embodiment of the present invention;

图2是本发明一个实施例中冷却器6的立体结构示意图(去除掉了箱体66的两个侧壁);Fig. 2 is the three-dimensional structure schematic diagram of cooler 6 in one embodiment of the present invention (two sidewalls of casing 66 have been removed);

图3是图2的右视图;Fig. 3 is the right view of Fig. 2;

图4是图2的主视图;Fig. 4 is the front view of Fig. 2;

图5是图4中A-A向剖视图;Fig. 5 is A-A direction sectional view among Fig. 4;

图6是图4的后视图;Fig. 6 is the back view of Fig. 4;

图7是本发明一个实施例中冷却器6去除掉箱体66的立体结构示意图;FIG. 7 is a schematic perspective view of the cooler 6 without the box 66 in one embodiment of the present invention;

图8是图7的一个正向视图;Fig. 8 is a front view of Fig. 7;

图9是图7的另一侧的立体结构示意图;Fig. 9 is a schematic perspective view of the other side of Fig. 7;

图10是图9的俯视结构示意图;Fig. 10 is a top view structural schematic diagram of Fig. 9;

图11是本发明一个实施例中单排冷却流程管61与翅片62配合在一起的结构示意图;Fig. 11 is a structural schematic view of the cooperation of single row of cooling process tubes 61 and fins 62 in one embodiment of the present invention;

图12是本发明一个实施例中单排冷却流程管61的结构示意图。FIG. 12 is a schematic structural view of a single row of cooling process tubes 61 in an embodiment of the present invention.

附图标记如下:The reference signs are as follows:

1、富氩尾气管道,2、真空泵,3、丝网过滤器,4、风机,5、冷却水夹套,6、冷却器,61、冷却流程管,62、翅片,63、套管,64、上隔板,65、下隔板,66、箱体,66-1、排气孔,66-2、进气孔,67、出液管,68、进液管,69、排油管道,7、滤芯过滤器,8、静电除油装置,9、脱油吸附筒。1. Argon-rich tail gas pipeline, 2. Vacuum pump, 3. Screen filter, 4. Fan, 5. Cooling water jacket, 6. Cooler, 61. Cooling process tube, 62. Fins, 63. Sleeve, 64, upper partition, 65, lower partition, 66, box body, 66-1, exhaust hole, 66-2, air intake hole, 67, liquid outlet pipe, 68, liquid inlet pipe, 69, oil discharge pipe , 7, filter element filter, 8, electrostatic degreasing device, 9, degreasing adsorption cylinder.

具体实施方式Detailed ways

为了使本发明的目的、技术方案及优点更加清楚明白,以下结合附图及实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.

如图1所示,一种拉晶炉富氩尾气除油系统,包括沿尾气进气方向依次设置的至少一台与富氩尾气管道1连接的真空泵2、与真空泵2连接的丝网过滤器3、至少一台与丝网过滤器3连接的风机4、与风机4连接的冷却器6、至少一台与冷却器6连接的滤芯过滤器7、与滤芯过滤器7连接的静电除油装置8、至少一台与静电除油装置8连接的脱油吸附筒9以及与脱油吸附筒9连接的气柜;其中,As shown in Figure 1, a crystal pulling furnace argon-rich tail gas degreasing system includes at least one vacuum pump 2 connected to the argon-rich tail gas pipeline 1 and a wire mesh filter connected to the vacuum pump 2 arranged in sequence along the tail gas inlet direction 3. At least one fan 4 connected to the wire mesh filter 3, a cooler 6 connected to the fan 4, at least one element filter 7 connected to the cooler 6, and an electrostatic degreasing device connected to the element filter 7 8. At least one deoiling adsorption cylinder 9 connected to the electrostatic degreasing device 8 and a gas cabinet connected to the deoiling adsorption cylinder 9; wherein,

真空泵2与丝网过滤器3组成系统内的预处理除油部分,风机4与冷却器6组成系统内的再处理除油部分,滤芯过滤器7组成系统内过滤除油部分,静电除油装置8组成系统内的静电除油部分,脱油吸附筒9组成系统内的脱油吸附部分。Vacuum pump 2 and wire mesh filter 3 form the pretreatment oil removal part in the system, fan 4 and cooler 6 form the reprocessing oil removal part in the system, filter element filter 7 forms the filter oil removal part in the system, and electrostatic oil removal device 8 forms the electrostatic oil removal part in the system, and the deoiling adsorption cylinder 9 forms the deoiling adsorption part in the system.

具体实施时,所述丝网过滤器3内设置有若干个钢丝球,所述丝网过滤器3底部设置有排油管道69。During specific implementation, several steel wool balls are arranged inside the wire mesh filter 3 , and an oil discharge pipe 69 is arranged at the bottom of the wire mesh filter 3 .

具体实施时,如图2至图12所示,所述冷却器6包括多排冷却流程管61、设置在冷却流程管61外的翅片62、套接在翅片62外以容纳冷却流程管61和翅片62的套管63、隔板以及箱体66;所述隔板具有上隔板64和下隔板65,以形成夹持套管63两端的夹持空间,所述上隔板64和下隔板65上设置有与套管63相适配的通孔;所述箱体66内形成有容纳隔板的工作区域,具有设置在箱体66上壁的排气孔66-1和设置在箱体66侧壁底部的进气孔66-2;每排冷却流程管61包括正反交替折弯的多个U型折弯管,每排冷却流程管61具有首端和末端,每排冷却流程管61的首端延伸出下隔板65外端并连接至出液管67,所述出液管67穿出对应箱体66的侧壁,每排冷却流程管61的末端延伸出上隔板64外端并连接至进液管68,所述进液管68穿出对应箱体66的侧壁。During specific implementation, as shown in FIGS. 2 to 12, the cooler 6 includes multiple rows of cooling process tubes 61, fins 62 arranged outside the cooling process tubes 61, and sleeved outside the fins 62 to accommodate the cooling process tubes. 61 and the sleeve pipe 63 of fin 62, dividing plate and casing 66; Said dividing plate has upper dividing plate 64 and lower dividing plate 65, to form the clamping space of clamping sleeve pipe 63 two ends, said upper dividing plate 64 and the lower partition 65 are provided with through holes that are compatible with the sleeve 63; the box body 66 is formed with a working area for accommodating the partition board, and has an exhaust hole 66-1 arranged on the upper wall of the box body 66 And the air inlet 66-2 arranged at the bottom of the side wall of the box body 66; each row of cooling process tubes 61 includes a plurality of U-shaped bending tubes that are bent alternately forward and reverse, and each row of cooling process tubes 61 has a head end and an end, The head end of each row of cooling process pipes 61 extends out of the outer end of the lower partition 65 and is connected to the liquid outlet pipe 67, which passes through the side wall of the corresponding box body 66, and the end of each row of cooling process pipes 61 extends Out of the outer end of the upper partition 64 and connected to the liquid inlet pipe 68 , the liquid inlet pipe 68 passes through the side wall of the corresponding box body 66 .

具体实施时,所述冷却流程管61外缘设置有沿管子轴线延伸的若干翅片62,所述翅片62呈环形阵列均匀分布。During specific implementation, the outer edge of the cooling process tube 61 is provided with several fins 62 extending along the axis of the tube, and the fins 62 are evenly distributed in an annular array.

具体实施时,所述箱体66的下壁倾斜设置,并在在下壁的最低处侧设置有排油管道69,所述排油管道69上设置有排油阀。During specific implementation, the lower wall of the box body 66 is arranged obliquely, and an oil discharge pipe 69 is arranged on the lowest side of the lower wall, and an oil discharge valve is arranged on the oil discharge pipe 69 .

在上述技术方案中,本发明使用时,较低压力气体通过进气管道进入箱体66,然后通过套管63与翅片62接触,再进入箱体66上部,然后通过排气管道进入后续系统。而冷却水从进液管68进入,进入冷却流程管61,然后从出液管67排出。在套管63中,铝制水管内的水与翅片62外的气体换热,将气体温度降低。气体下进上出,水上进下出实现逆流换热。箱体66的下壁设置一定的倾斜角度,含油的气体被冷却后部分油雾冷凝成液体,依靠自身重力流到箱体66的下壁,因箱体66的下壁有一定倾斜,油会流到最低处,再最低处设置排油空,排油孔接一根排油管和排油阀,当油积累到一定程度,打开排油阀将液态油排出。In the above technical solution, when the present invention is used, the lower pressure gas enters the box body 66 through the intake pipe, then contacts the fins 62 through the sleeve 63, then enters the upper part of the box body 66, and then enters the follow-up system through the exhaust pipe . The cooling water enters from the liquid inlet pipe 68 , enters the cooling process pipe 61 , and then discharges from the liquid outlet pipe 67 . In the casing 63, the water in the aluminum water pipe exchanges heat with the gas outside the fins 62 to reduce the temperature of the gas. The gas enters from the bottom and exits from the top, and the water enters and exits from the top to realize countercurrent heat exchange. The lower wall of the box 66 is set at a certain angle of inclination. After the oil-containing gas is cooled, part of the oil mist condenses into a liquid, which flows to the lower wall of the box 66 by its own gravity. Because the lower wall of the box 66 has a certain inclination, the oil will Flow to the lowest point, and then install an oil discharge hole at the lowest point. The oil discharge hole is connected with an oil discharge pipe and an oil discharge valve. When the oil accumulates to a certain extent, open the oil discharge valve to discharge the liquid oil.

具体实施时,所述滤芯过滤器7内设置有滤芯,所述滤芯具有若干孔隙。During specific implementation, the filter element filter 7 is provided with a filter element, and the filter element has several pores.

具体实施时,所述静电除油装置8外加有14KV-16KV的高压直流电以形成二个极性相反的电场。During specific implementation, the electrostatic degreasing device 8 is externally supplied with a high-voltage direct current of 14KV-16KV to form two electric fields with opposite polarities.

具体实施时,所述脱油吸附筒9内设置有硅酸盐吸附剂。During specific implementation, the deoiling adsorption cylinder 9 is provided with a silicate adsorbent.

具体实施时,所述风机4并联设置有三台。During specific implementation, there are three blowers 4 arranged in parallel.

具体实施时,所述冷却器6与风机4之间的管道上还设置有冷却水夹套5,所述冷却水夹套5上设置有冷冻水管道。During specific implementation, a cooling water jacket 5 is also provided on the pipeline between the cooler 6 and the fan 4 , and a chilled water pipeline is provided on the cooling water jacket 5 .

本发明的工作原理为:Working principle of the present invention is:

在具体实施时,从每个车间真空泵2抽出的富氩尾气首先进入丝网过滤器3,丝网过滤器3中装满钢丝球,气体中油与钢丝碰撞部分凝结成液体,液态的油依靠自身重力流到过滤器桶的底部,底部设置排油的管道,当油量累积到一定程度,打开排油阀将油排出。In specific implementation, the argon-rich tail gas extracted from each workshop vacuum pump 2 first enters the wire mesh filter 3, which is filled with steel wire balls, and the oil in the gas collides with the steel wire to condense into liquid, and the liquid oil relies on itself Gravity flows to the bottom of the filter barrel, and an oil discharge pipeline is set at the bottom. When the oil accumulates to a certain extent, the oil discharge valve is opened to discharge the oil.

经过以上一步骤,除掉了一部分气体中的油,之后依靠风机4的抽力将每个车间的富氩尾气管道1汇合吸入风机4,风机4增压后一方面气体压力增加使得其中的饱和含油量降低,从而部分油变成液态油,另一方面气体加压后温度上升(经计算上升约13℃),这使得部分液态油会挥发成气态。因此,在风机4后增加一套针对设计的翅片式冷却器6。After the above steps, a part of the oil in the gas is removed, and then the argon-rich tail gas pipeline 1 of each workshop is merged and sucked into the fan 4 by the suction of the fan 4. After the fan 4 is pressurized, the gas pressure increases on the one hand to make the gas in it saturated. The oil content decreases, so that part of the oil becomes liquid oil. On the other hand, the temperature of the gas increases after pressurization (by calculation, it rises by about 13°C), which makes part of the liquid oil volatilize into a gaseous state. Therefore, a set of designed finned cooler 6 is added behind the blower fan 4 .

在冷却器6中,富氩尾气温度降低,从而使得部分气态油被重新液化成液态,流到冷却器6底部,在底部设置排油管道69和排油阀,定时排出其中的液态油。In the cooler 6, the temperature of the argon-rich tail gas is lowered, so that part of the gaseous oil is re-liquefied into a liquid state and flows to the bottom of the cooler 6. An oil discharge pipe 69 and an oil discharge valve are arranged at the bottom to discharge the liquid oil therein regularly.

通过以上几个步骤,大颗粒的液态油基本已清除干净,之后富氩尾气进入滤芯过滤器7,滤芯过滤器7原理为:气体通过有着大量小孔的滤芯,较小颗粒的油无法通过滤芯小孔,从而被拦截,累积之后流到滤芯过滤器7底部,通过排油的管道排出。Through the above steps, the large particles of liquid oil have basically been removed, and then the argon-rich exhaust gas enters the filter element filter 7. The principle of the filter element filter 7 is: the gas passes through the filter element with a large number of small holes, and the oil with smaller particles cannot pass through the filter element The small holes are thus intercepted, and flow to the bottom of the cartridge filter 7 after accumulating, and are discharged through the oil discharge pipe.

由于富氩尾气中油含量太多,以上几个步骤还是不能达到除油要求,还有较多气态的油混在富氩尾气中,因此之后富氩尾气进入静电除油装置8进一步除油,利用外加高压(14KV-16KV)直流电而形成二个极性相反的电场,在库仑力的作用下,使油烟粒子带电后向收集板移动排斥的力量附在收集板上,此步骤去除了大部分气态的油雾。之后将气体通入装有硅酸盐吸附剂的脱油吸附筒9,硅酸盐吸附剂利用其多孔特性,其中的微孔能够吸附很小分子的气态油,从而去除富氩尾气中剩余的小分子油雾,之后气体进入气柜。Because the oil content in the argon-rich tail gas is too much, the above steps still cannot meet the oil removal requirements, and there is still more gaseous oil mixed in the argon-rich tail gas, so the argon-rich tail gas enters the electrostatic oil removal device 8 for further oil removal, and uses external High-voltage (14KV-16KV) direct current forms two electric fields with opposite polarities. Under the action of Coulomb force, the soot particles are charged and then move to the collection plate. The repulsive force is attached to the collection plate. This step removes most of the gaseous oil mist. Afterwards, the gas is passed into the deoiling adsorption cylinder 9 equipped with a silicate adsorbent. The silicate adsorbent utilizes its porous characteristics, and the micropores therein can absorb very small molecules of gaseous oil, thereby removing the residual argon-rich tail gas. Small molecule oil mist, after which the gas enters the gas cabinet.

经过以上多个方式的组合除油,最终才能将油除干净达到后续净化的要求。After the combination of the above multiple methods to remove oil, the oil can finally be removed to meet the requirements of subsequent purification.

以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present invention should be included in the protection of the present invention. within range.

Claims (10)

1. The utility model provides a crystal pulling furnace rich argon tail gas deoiling system which characterized in that: the device comprises at least one vacuum pump (2) connected with an argon-rich tail gas pipeline (1), a silk screen filter (3) connected with the vacuum pump (2), at least one fan (4) connected with the silk screen filter (3), a cooler (6) connected with the fan (4), at least one filter element filter (7) connected with the cooler (6), an electrostatic oil removal device (8) connected with the filter element filter (7), at least one oil removal adsorption cylinder (9) connected with the electrostatic oil removal device (8) and an air cabinet connected with the oil removal adsorption cylinder (9), which are sequentially arranged along the tail gas inlet direction; wherein,
the vacuum pump (2) and the silk screen filter (3) form a pretreatment oil removing part in the system, the fan (4) and the cooler (6) form a retreatment oil removing part in the system, the filter element filter (7) forms a filtration oil removing part in the system, the electrostatic oil removing device (8) forms an electrostatic oil removing part in the system, and the deoiling adsorption cylinder (9) forms a deoiling adsorption part in the system.
2. The argon-rich tail gas oil removal system for the crystal pulling furnace as claimed in claim 1, wherein: the wire mesh filter is characterized in that a plurality of steel wire balls are arranged in the wire mesh filter (3), and an oil discharge pipeline (69) is arranged at the bottom of the wire mesh filter (3).
3. The argon-rich tail gas oil removal system for the crystal pulling furnace as claimed in claim 1, wherein: the cooler (6) comprises a plurality of rows of cooling process pipes (61), fins (62) arranged outside the cooling process pipes (61), sleeves (63) sleeved outside the fins (62) to accommodate the cooling process pipes (61) and the fins (62), partition plates and a box body (66); the partition plate is provided with an upper partition plate (64) and a lower partition plate (65) to form clamping spaces for clamping two ends of the sleeve (63), and through holes matched with the sleeve (63) are formed in the upper partition plate (64) and the lower partition plate (65); a working area for accommodating the partition plate is formed in the box body (66), and the box body is provided with an exhaust hole (66-1) arranged on the upper wall of the box body (66) and an air inlet hole (66-2) arranged at the bottom of the side wall of the box body (66); every row of cooling process pipe (61) is including a plurality of U type pipes of bending of positive and negative alternative, and every row of cooling process pipe (61) has head end and end, and the head end of every row of cooling process pipe (61) extends baffle (65) outer end down and connects to drain pipe (67), the lateral wall that corresponds box (66) is worn out in drain pipe (67), and the end of every row of cooling process pipe (61) extends baffle (64) outer end and connects to feed liquor pipe (68), the lateral wall that corresponds box (66) is worn out in feed liquor pipe (68).
4. A low resistance oil removal cooler (6) according to claim 3, characterized in that: the outer edge of the cooling process pipe (61) is provided with a plurality of fins (62) extending along the axis of the pipe, and the fins (62) are uniformly distributed in an annular array.
5. A low resistance oil removal cooler (6) according to claim 3, characterized in that: the lower wall of the box body (66) is obliquely arranged, an oil discharge pipeline (69) is arranged on the lowest side of the lower wall, and an oil discharge valve is arranged on the oil discharge pipeline (69).
6. The argon-rich tail gas oil removal system for the crystal pulling furnace as claimed in claim 1, wherein: and a filter element is arranged in the filter element filter (7), and the filter element is provided with a plurality of pores.
7. The argon-rich tail gas oil removal system for the crystal pulling furnace as claimed in claim 1, wherein: the static oil removing device (8) is externally added with high-voltage direct current of 14KV-16KV to form two electric fields with opposite polarities.
8. The argon-rich tail gas oil removal system for the crystal pulling furnace as claimed in claim 1, wherein: a silicate adsorbent is arranged in the deoiling adsorption cylinder (9).
9. The argon-rich tail gas oil removal system for the crystal pulling furnace as claimed in claim 1, wherein: three fans (4) are connected in parallel.
10. The argon-rich tail gas oil removal system for the crystal pulling furnace as claimed in claim 1, wherein: and a cooling water jacket (5) is also arranged on the pipeline between the cooler (6) and the fan (4), and a chilled water pipeline is arranged on the cooling water jacket (5).
CN201811086354.7A 2018-09-18 2018-09-18 A kind of crystal pulling furnace richness argon tail gas oil removing system Pending CN109078442A (en)

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Application publication date: 20181225