CN204307566U - A kind of acid bath blending equipment - Google Patents
A kind of acid bath blending equipment Download PDFInfo
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- CN204307566U CN204307566U CN201420820922.2U CN201420820922U CN204307566U CN 204307566 U CN204307566 U CN 204307566U CN 201420820922 U CN201420820922 U CN 201420820922U CN 204307566 U CN204307566 U CN 204307566U
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- tank body
- acid
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- acid bath
- zinc sulfate
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- 239000002253 acid Substances 0.000 title claims abstract description 48
- 238000002156 mixing Methods 0.000 title claims abstract description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 30
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 claims abstract description 23
- 229960001763 zinc sulfate Drugs 0.000 claims abstract description 23
- 229910000368 zinc sulfate Inorganic materials 0.000 claims abstract description 23
- 239000000919 ceramic Substances 0.000 claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- 238000003756 stirring Methods 0.000 claims description 12
- 239000003788 bath preparation Substances 0.000 claims description 9
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 abstract description 13
- 229910052938 sodium sulfate Inorganic materials 0.000 abstract description 13
- 235000011152 sodium sulphate Nutrition 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 9
- 238000002425 crystallisation Methods 0.000 abstract description 2
- 230000008025 crystallization Effects 0.000 abstract description 2
- 238000001704 evaporation Methods 0.000 abstract description 2
- 230000008020 evaporation Effects 0.000 abstract description 2
- 238000002474 experimental method Methods 0.000 abstract description 2
- 238000011112 process operation Methods 0.000 abstract description 2
- 238000009987 spinning Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 238000005485 electric heating Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000008234 soft water Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 229920000297 Rayon Polymers 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Manufacture And Refinement Of Metals (AREA)
Abstract
本实用新型涉及一种酸浴调配设备,包括罐体,所述罐体的上部设置有斗式加料器、硫酸锌高位槽和浓硫酸高位槽,所述罐体的下部设置有出酸管,所述斗式加料器、硫酸锌高位槽和浓硫酸高位槽分别通过管道与罐体连接,所述罐体上设置有蒸汽进管,所述罐体的外部沿周向设置有陶瓷加热板;硫酸锌、硫酸钠、硫酸能够根据实际需要进行灵活调节;工艺流程短,操作人员少,便于维护;本设备减少了酸站蒸发、结晶等复杂工艺操作,占地面积小;本设备温度可以实现自动调节,可以保证实验的正常运行;本设备最大的优点在于实现了三组分的连续补加,有效避免了以前间歇补加所造成的浓度波动。
The utility model relates to an acid bath blending equipment, which comprises a tank body. The upper part of the tank body is provided with a bucket feeder, a zinc sulfate high-level tank and a concentrated sulfuric acid high-level tank, and the lower part of the tank body is provided with an acid outlet pipe. The bucket feeder, the zinc sulfate head tank and the concentrated sulfuric acid head tank are respectively connected to the tank body through pipelines, the tank body is provided with a steam inlet pipe, and the outside of the tank body is provided with a ceramic heating plate along the circumference; Zinc sulfate, sodium sulfate, and sulfuric acid can be flexibly adjusted according to actual needs; the process flow is short, the number of operators is small, and it is easy to maintain; this equipment reduces complex process operations such as evaporation and crystallization in acid stations, and occupies a small area; the temperature of this equipment can achieve Automatic adjustment can ensure the normal operation of the experiment; the biggest advantage of this equipment is that it realizes the continuous addition of the three components, effectively avoiding the concentration fluctuation caused by the previous intermittent addition.
Description
技术领域technical field
本实用新型涉及一种化纤行业用设备,具体的说涉及一种酸浴调配设备。The utility model relates to equipment used in the chemical fiber industry, in particular to an acid bath mixing equipment.
背景技术Background technique
酸站在粘胶整个体系中占有十分重要的位置,它为纺丝机提供了透明度高,三组分稳定的酸浴,其中三组分为硫酸、硫酸钠和硫酸锌,只有酸浴稳定且指标合格,才能生产出合格的粘胶纤维。在试验新品种的过程中,我们纺丝是在实验室中实现的,酸浴量大约在400L左右,由于新品种的开发需要不断调整浓度和温度,我们不能直接采用大生产线的酸浴,需要自己使用调配设备进行调配,如果调配设备置完全按照大生产线配置来的话,流程很长,且操作人员很多,浪费太大,现在没有专用的调配设备共技术开发人员使用。The acid station occupies a very important position in the whole viscose system. It provides the spinning machine with a high transparency and three-component stable acid bath, of which the three components are sulfuric acid, sodium sulfate and zinc sulfate. Only the acid bath is stable and Only when the index is qualified can qualified viscose fiber be produced. In the process of testing new varieties, our spinning is realized in the laboratory, and the acid bath volume is about 400L. Because the development of new varieties requires constant adjustment of concentration and temperature, we cannot directly use the acid bath of a large production line. Use the deployment equipment for deployment by yourself. If the deployment equipment is configured according to the configuration of the large production line, the process will be very long, and there will be a lot of operators, which will cause too much waste. Now there is no dedicated deployment equipment for technical developers to use.
实用新型内容Utility model content
本实用新型要解决的问题是针对以上问题,提供一种工艺流程短、操作人员少、便于维护的酸浴调配设备。The problem to be solved by the utility model is to provide an acid bath blending equipment with short process flow, few operators and easy maintenance for the above problems.
为解决上述问题,本实用新型所采用的技术方案是:一种酸浴调配设备,包括罐体,所述罐体的上部设置有斗式加料器、硫酸锌高位槽和浓硫酸高位槽,所述罐体的下部设置有出酸管,所述斗式加料器、硫酸锌高位槽和浓硫酸高位槽分别通过管道与罐体连接,所述罐体上设置有蒸汽进管,所述罐体的外部沿周向设置有陶瓷加热板。In order to solve the above problems, the technical solution adopted by the utility model is: an acid bath blending equipment, including a tank body, the upper part of the tank body is provided with a bucket feeder, a zinc sulfate elevated tank and a concentrated sulfuric acid elevated tank, the The lower part of the tank body is provided with an acid outlet pipe, the bucket feeder, the zinc sulfate head tank and the concentrated sulfuric acid head tank are respectively connected to the tank body through pipelines, the tank body is provided with a steam inlet pipe, and the tank body The outside is provided with a ceramic heating plate along the circumference.
本设备可以通过斗式加料器、硫酸锌高位槽和浓硫酸高位槽向罐体内加入硫酸钠、硫酸锌和硫酸,硫酸锌、硫酸钠、硫酸能够根据实际需要进行灵活调节,工艺流程短,操作人员少,便于维护。This equipment can add sodium sulfate, zinc sulfate and sulfuric acid into the tank through bucket feeder, zinc sulfate high level tank and concentrated sulfuric acid high level tank. Zinc sulfate, sodium sulfate and sulfuric acid can be flexibly adjusted according to actual needs. The process is short and easy to operate. Less personnel, easy to maintain.
作为一种优化方案,所述陶瓷加热板的数量为两个。As an optimized solution, the number of the ceramic heating plates is two.
作为一种优化方案,所述罐体的上部设置有回流管。As an optimized solution, a return pipe is arranged on the upper part of the tank body.
作为一种优化方案,所述回流管上设置有热电偶。As an optimized solution, a thermocouple is arranged on the return pipe.
作为一种优化方案,还包括控制箱,所述陶瓷加热板和热电偶与控制箱电连接。As an optimized solution, a control box is also included, and the ceramic heating plate and the thermocouple are electrically connected to the control box.
作为一种优化方案,所述罐体内设置有搅拌轴,所述罐体的上部设置有电机,所述电机与搅拌轴传动连接,所述搅拌轴上设置有搅拌叶片。As an optimized solution, a stirring shaft is provided in the tank body, a motor is provided on the upper part of the tank body, the motor is connected to the stirring shaft by transmission, and stirring blades are provided on the stirring shaft.
作为一种优化方案,所述蒸汽进管位于罐体内的部分上设置有多个通孔。As an optimized solution, the part of the steam inlet pipe located in the tank body is provided with a plurality of through holes.
作为一种优化方案,所述蒸汽进管上设置有阀门。As an optimized solution, the steam inlet pipe is provided with a valve.
作为一种优化方案,所述罐体的下部设置有排酸管。As an optimized solution, an acid discharge pipe is provided at the lower part of the tank body.
本实用新型采取以上技术方案,具有以下优点:The utility model adopts the above technical scheme and has the following advantages:
硫酸锌、硫酸钠、硫酸能够根据实际需要进行灵活调节;工艺流程短,操作人员少,便于维护;本设备减少了酸站蒸发、结晶等复杂工艺操作,占地面积小;本设备温度可以实现自动调节,可以保证实验的正常运行;本设备最大的优点在于实现了三组分的连续补加,有效避免了以前间歇补加所造成的浓度波动。Zinc sulfate, sodium sulfate, and sulfuric acid can be flexibly adjusted according to actual needs; the process flow is short, the number of operators is small, and it is easy to maintain; this equipment reduces complex process operations such as evaporation and crystallization in acid stations, and occupies a small area; Automatic adjustment can ensure the normal operation of the experiment; the biggest advantage of this equipment is that it realizes the continuous addition of the three components, effectively avoiding the concentration fluctuation caused by the previous intermittent addition.
下面结合附图和实施例对本实用新型作进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is further described.
附图说明Description of drawings
附图1为本实用新型实施例中一种酸浴调配设备的结构示意图。Accompanying drawing 1 is the structure diagram of an acid bath preparation equipment in the embodiment of the utility model.
具体实施方式Detailed ways
实施例:如附图1所示,一种酸浴调配设备,包括罐体5,所述罐体5的上部设置有斗式加料器1、硫酸锌高位槽2和浓硫酸高位槽3,所述罐体5的下部设置有出酸管11和排酸管12,出酸管11和排酸管12上设置有阀门,所述斗式加料器1、硫酸锌高位槽2和浓硫酸高位槽3分别通过管道与罐体5连接,所述罐体5上设置有蒸汽进管13,所述蒸汽进管13位于罐体5内的部分上设置有多个通孔,所述蒸汽进管13上设置有阀门4,所述罐体5的外部沿周向设置有陶瓷加热板7。Embodiment: as shown in accompanying drawing 1, a kind of acid bath deployment equipment comprises tank body 5, and the top of described tank body 5 is provided with bucket feeder 1, zinc sulfate head tank 2 and concentrated sulfuric acid head tank 3, so The bottom of the tank body 5 is provided with an acid discharge pipe 11 and an acid discharge pipe 12, and the acid discharge pipe 11 and the acid discharge pipe 12 are provided with valves, the bucket feeder 1, the zinc sulfate head tank 2 and the concentrated sulfuric acid head tank 3 are respectively connected to the tank body 5 through pipelines, the tank body 5 is provided with a steam inlet pipe 13, and the part of the steam inlet pipe 13 located in the tank body 5 is provided with a plurality of through holes, and the steam inlet pipe 13 A valve 4 is arranged on the top, and a ceramic heating plate 7 is arranged on the outside of the tank body 5 along the circumferential direction.
所述陶瓷加热板7的数量为两个,可以根据需要增加或减少陶瓷加热板7的数量。The number of the ceramic heating plates 7 is two, and the number of the ceramic heating plates 7 can be increased or decreased as required.
所述罐体5的上部设置有回流管10,所述回流管10上设置有热电偶6。A return pipe 10 is arranged on the upper part of the tank body 5 , and a thermocouple 6 is arranged on the return pipe 10 .
还包括控制箱9,所述陶瓷加热板7和热电偶6与控制箱9电连接。A control box 9 is also included, and the ceramic heating plate 7 and the thermocouple 6 are electrically connected to the control box 9 .
所述罐体5内设置有搅拌轴14,所述罐体5的上部设置有电机8,所述电机8与搅拌轴14传动连接,所述搅拌轴14上设置有搅拌叶片15。A stirring shaft 14 is arranged inside the tank body 5 , and a motor 8 is arranged on the upper part of the tank body 5 , the motor 8 is connected to the stirring shaft 14 by transmission, and the stirring shaft 14 is provided with a stirring blade 15 .
在进行小试线纺丝前,我们需要对酸浴进行提前调配并升温完毕,准备纺丝,首先是进行酸浴的调配工作。Before spinning on a small test line, we need to prepare the acid bath in advance and heat it up to prepare for spinning. First, we need to prepare the acid bath.
酸浴的调配是在罐体5中进行的,罐体5为不锈钢904材质,壁厚5mm,直径600mm,溶剂280L,首先使用小试线中的现有软水管加入软化水,并开启酸泵循环,待软水加入量达到玻璃管标定刻度时停止加入。The deployment of the acid bath is carried out in the tank body 5, the tank body 5 is made of stainless steel 904, the wall thickness is 5mm, the diameter is 600mm, and the solvent is 280L. First, use the existing soft water pipe in the small test line to add softened water, and turn on the acid pump Circulate, and stop adding when the amount of soft water added reaches the calibration scale of the glass tube.
打开阀门4,通过蒸汽进管13内的蒸汽对桶中的软水进行加热,温度升至指定温度,如65度,具体温度需要根据纺丝开始时间及工艺要求而定。蒸汽进管13为PP材质,表面布满直径为2mm的小孔,可以大量喷射蒸汽,使软化水温度在0.5h内达到指定温度。Open the valve 4, the steam in the steam inlet pipe 13 heats the soft water in the bucket, and the temperature rises to a specified temperature, such as 65 degrees, and the specific temperature needs to be determined according to the spinning start time and process requirements. The steam inlet pipe 13 is made of PP material, and the surface is covered with small holes with a diameter of 2mm, which can spray a large amount of steam, so that the temperature of the softened water reaches the specified temperature within 0.5h.
升温完毕后,通过浓硫酸高位槽3、斗式加料器1和硫酸锌高位槽2依次加入浓硫酸、元明粉、硫酸锌,三者的加入量根据工艺计算而得。After the temperature rise is completed, concentrated sulfuric acid, sodium sulfate, and zinc sulfate are sequentially added through the concentrated sulfuric acid head tank 3, bucket feeder 1 and zinc sulfate head tank 2, and the addition amount of the three is calculated according to the process.
浓硫酸的加入通过浓硫酸高位槽3实现。开启浓硫酸高位槽3底部的阀门,让浓硫酸缓慢流入罐体5中,此时观测浓硫酸高位槽3上自带的液位,防止过量,加入时,操作工要带防护面罩,防止硫酸溅出伤人。Adding of the concentrated sulfuric acid is realized by the concentrated sulfuric acid head tank 3. Open the valve at the bottom of the concentrated sulfuric acid head tank 3 to allow the concentrated sulfuric acid to slowly flow into the tank body 5. At this time, observe the liquid level on the concentrated sulfuric acid head tank 3 to prevent excess. When adding, the operator should wear a protective mask to prevent sulfuric acid Splash hurts.
硫酸锌的加入通过硫酸锌高位槽2实现,由于硫酸锌容易吸水和结块,并且加入量很小,我们需要将硫酸锌用酸浴提前溶解好再用,溶解的酸浴来源为大生产线,同样,硫酸锌高位槽2上面也有液位,可以控制其加入量。The addition of zinc sulfate is realized through the zinc sulfate high tank 2. Since zinc sulfate is easy to absorb water and agglomerate, and the amount added is very small, we need to dissolve zinc sulfate in an acid bath in advance before using it. The source of the dissolved acid bath is a large production line. Equally, also liquid level is arranged above the zinc sulfate head tank 2, can control its addition.
硫酸钠的加入不能像硫酸锌加入那样使用酸浴提前溶解,因为硫酸钠初始加入量大,斗式加料器1体积有限,硫酸钠溶解度不是很高,我们不能使用溶液。我们通过斗式加料器1进行加粉操作,直接将元明粉加入罐体5中,罐体5的表面一样带有液位。The addition of sodium sulfate cannot be dissolved in advance using an acid bath like the addition of zinc sulfate, because the initial addition of sodium sulfate is large, the volume of the bucket feeder 1 is limited, and the solubility of sodium sulfate is not very high, so we cannot use the solution. We carry out the powder adding operation through the bucket feeder 1, and directly add the Yuanming Powder into the tank body 5, and the surface of the tank body 5 also has a liquid level.
三者加入时,需要注意,在浓硫酸加入完毕后应该打开电机8,速度调为80r/min。加硫酸钠的速度不能太快,加入速度要跟酸浴循环的速度基本一致,防止硫酸钠加入太急堵塞出酸管11。When the three are added, it should be noted that the motor 8 should be turned on after the concentrated sulfuric acid is added, and the speed should be adjusted to 80r/min. The speed of adding sodium sulfate can not be too fast, and the speed of adding will be basically consistent with the speed of acid bath circulation, prevents sodium sulfate from adding too quickly to block the acid pipe 11.
初始酸浴调配完毕后,循环30分钟,然后观测此时控制箱9的示数,根据实际需要再次调整酸温,此后时间内测试酸浓,进行微调使浓度达到要求,最后盖上罐体5盖板,使罐体5处于密封状态循环。After the initial acid bath is prepared, circulate it for 30 minutes, then observe the display of the control box 9 at this time, adjust the acid temperature again according to actual needs, test the acid concentration within a period of time thereafter, make fine adjustments to make the concentration meet the requirements, and finally cover the tank body 5 The cover plate makes the tank body 5 circulate in a sealed state.
开启陶瓷加热板7和控制箱9,进行保温操作,陶瓷电加热板7功率为20kw,绕罐体5两周,陶瓷电加热板7是间歇保温加热的,热电偶6的安装位置在回流管10上,测试回酸温度,将信号反馈到控制箱9,陶瓷电加热板7与控制箱9形成连锁,通过控制箱9控制陶瓷电加热板7的开停。Turn on the ceramic heating plate 7 and the control box 9 to carry out the heat preservation operation. The power of the ceramic electric heating plate 7 is 20kw, and it goes around the tank body 5 for two weeks. The ceramic electric heating plate 7 is intermittently heat-preserved and heated. 10, test the acid back temperature, feed back the signal to the control box 9, the ceramic electric heating plate 7 and the control box 9 form a chain, and control the start and stop of the ceramic electric heating plate 7 through the control box 9.
纺丝开始后,由于三组分不断变化,需要对三者不断补加,此时,浓硫酸、硫酸锌的调整量不是通过液位变化来看,因为需要补加的量较小,短时间内看不出液位的变化,无法计量。此时我们是通过秒表和量筒来计量的,计量时间为20s,通过公式换算可得到此时二者的瞬时加入量,硫酸钠的加入量,是通过秒表、烧杯和天平来计量的,通过公式换算后,同样可得到瞬时加入量,计量时间为20s。After the spinning starts, due to the constant changes of the three components, the three components need to be added continuously. At this time, the adjustment amount of concentrated sulfuric acid and zinc sulfate is not judged by the change of liquid level, because the amount to be added is small, and the short-term There is no visible change in the liquid level, and it cannot be measured. At this time, we measure through a stopwatch and a measuring cylinder, and the measurement time is 20s. The instantaneous addition amount of the two at this time can be obtained through the conversion of the formula. The addition amount of sodium sulfate is measured through a stopwatch, a beaker and a balance. Through the formula After conversion, the instantaneous addition amount can also be obtained, and the metering time is 20s.
纺丝完毕后,我们不能将酸浴长时间放置,因为硫酸钠容易结晶堵塞过滤器和管道,我们需要将酸浴通过排酸管12排掉。After spinning, we cannot place the acid bath for a long time, because sodium sulfate is easy to crystallize and block the filter and pipeline, so we need to drain the acid bath through the acid discharge pipe 12.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110093669A (en) * | 2019-05-28 | 2019-08-06 | 新乡化纤股份有限公司 | A kind of viscose glue continuously spins acid bath groove band pressure spinning process |
CN111803995A (en) * | 2020-07-31 | 2020-10-23 | 北京神州瑞霖环境技术研究院有限公司 | Natural evaporation crystallization system for acid bath discharge liquid reflux removal part and application |
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2014
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110093669A (en) * | 2019-05-28 | 2019-08-06 | 新乡化纤股份有限公司 | A kind of viscose glue continuously spins acid bath groove band pressure spinning process |
CN111803995A (en) * | 2020-07-31 | 2020-10-23 | 北京神州瑞霖环境技术研究院有限公司 | Natural evaporation crystallization system for acid bath discharge liquid reflux removal part and application |
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