CN118461022B - Perfluoro tripropylamine electrolytic tank capable of detecting liquid density - Google Patents
Perfluoro tripropylamine electrolytic tank capable of detecting liquid density Download PDFInfo
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- 239000007788 liquid Substances 0.000 title claims abstract description 43
- 229950008618 perfluamine Drugs 0.000 title claims abstract description 21
- JAJLKEVKNDUJBG-UHFFFAOYSA-N perfluorotripropylamine Chemical compound FC(F)(F)C(F)(F)C(F)(F)N(C(F)(F)C(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)F JAJLKEVKNDUJBG-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 238000002955 isolation Methods 0.000 claims abstract description 30
- 238000005192 partition Methods 0.000 claims abstract description 26
- 210000005056 cell body Anatomy 0.000 claims abstract description 24
- 210000004027 cell Anatomy 0.000 claims abstract description 20
- 230000007246 mechanism Effects 0.000 claims abstract description 17
- 238000005057 refrigeration Methods 0.000 claims abstract description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 24
- 238000007789 sealing Methods 0.000 claims description 13
- 229910052757 nitrogen Inorganic materials 0.000 claims description 12
- 239000003507 refrigerant Substances 0.000 claims description 10
- 238000013016 damping Methods 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 8
- 230000009471 action Effects 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 4
- 230000006835 compression Effects 0.000 claims description 3
- 238000007906 compression Methods 0.000 claims description 3
- 238000004821 distillation Methods 0.000 claims description 3
- 238000006073 displacement reaction Methods 0.000 claims 2
- 239000012452 mother liquor Substances 0.000 abstract description 13
- 238000000034 method Methods 0.000 description 19
- 230000008569 process Effects 0.000 description 17
- 239000000463 material Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 9
- 238000005868 electrolysis reaction Methods 0.000 description 9
- 230000000903 blocking effect Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 2
- YFTHZRPMJXBUME-UHFFFAOYSA-N tripropylamine Chemical compound CCCN(CCC)CCC YFTHZRPMJXBUME-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 1
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 1
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003682 fluorination reaction Methods 0.000 description 1
- 125000001153 fluoro group Chemical group F* 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/02—Process control or regulation
- C25B15/021—Process control or regulation of heating or cooling
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B3/00—Electrolytic production of organic compounds
- C25B3/01—Products
- C25B3/09—Nitrogen containing compounds
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B3/00—Electrolytic production of organic compounds
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- C25B3/11—Halogen containing compounds
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B3/00—Electrolytic production of organic compounds
- C25B3/20—Processes
- C25B3/27—Halogenation
- C25B3/28—Fluorination
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N9/00—Investigating density or specific gravity of materials; Analysing materials by determining density or specific gravity
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N9/00—Investigating density or specific gravity of materials; Analysing materials by determining density or specific gravity
- G01N9/36—Analysing materials by measuring the density or specific gravity, e.g. determining quantity of moisture
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Abstract
本发明公开了一种能够检测液体密度的全氟三丙胺电解槽,包括:电解槽本体;制冷换热器,包含立式换热罐,所述立式换热罐的上下侧分别固接有相应的上隔板和下隔板,所述上隔板和下隔板之间贯穿连接有多个相应的换热流通管;换热介质循环机构,包含呈夹层状态固接于所述下隔板下侧的立式换热罐外侧的换热夹套;多功能隔离机构,包含设置于循环进料管下侧的立式换热罐内的活动隔离件;隔离件驱动机构,包含设置于换热夹套底侧的驱动液压缸,所述驱动液压缸的活塞杆回缩,以驱动所述活动隔离件将贮存于其底侧的产品从产品出料管挤压输出。本发明能够有效便捷将产品进行输出,且能够明显降低产品输出时对电解母液的夹带量。
The present invention discloses a perfluorotripropylamine electrolytic cell capable of detecting liquid density, comprising: an electrolytic cell body; a refrigeration heat exchanger, comprising a vertical heat exchange tank, the upper and lower sides of the vertical heat exchange tank are respectively fixedly connected with corresponding upper and lower partitions, and a plurality of corresponding heat exchange circulation pipes are connected through the upper and lower partitions; a heat exchange medium circulation mechanism, comprising a heat exchange jacket fixedly connected to the outer side of the vertical heat exchange tank on the lower side of the lower partition in a sandwich state; a multifunctional isolation mechanism, comprising a movable isolation member arranged in the vertical heat exchange tank on the lower side of the circulating feed pipe; an isolation member driving mechanism, comprising a driving hydraulic cylinder arranged on the bottom side of the heat exchange jacket, the piston rod of the driving hydraulic cylinder is retracted to drive the movable isolation member to squeeze and output the product stored on its bottom side from the product discharge pipe. The present invention can effectively and conveniently output the product, and can significantly reduce the entrainment of the electrolytic mother liquor when the product is output.
Description
技术领域Technical Field
本发明涉及全氟三丙胺制备用设备技术领域,具体是指一种能够检测液体密度的全氟三丙胺电解槽。The invention relates to the technical field of equipment for preparing perfluorotripropylamine, in particular to a perfluorotripropylamine electrolytic cell capable of detecting liquid density.
背景技术Background Art
全氟三丙胺对人体完全无毒,而且能溶解携带大量的氧气和二氧化碳,它是构成现代医学领域应用的人造血浆的主要成分之一。同时用作仪器仪表的抗腐蚀传动液、介电绝缘液,电子元件、器件检漏液。因此,生产全氟三丙胺对于科学进步和发展意义重大。Perfluorotripropylamine is completely non-toxic to the human body and can dissolve and carry a large amount of oxygen and carbon dioxide. It is one of the main components of artificial plasma used in modern medicine. It is also used as an anti-corrosion transmission fluid, dielectric insulation fluid, and leak detection fluid for electronic components and devices. Therefore, the production of perfluorotripropylamine is of great significance to scientific progress and development.
现有制备全氟三丙胺的技术中应用最广的是采用电解氟化的方法,三丙胺和氟化氢组成的母液在电解槽中通入低压直流电,产生游离氟原子直接取代三丙胺中的氢原子,再经过简单的纯化处理,即可得到全氟三丙胺产品。该过程中,需要通过相应的制冷换热器以循环对母液和产品进行冷却,从而防止母液和产品在电解过程中因升温而导致物料气化。由于电解后的产品“全氟三丙胺”的密度会比母液高,因此,制备得到的产品和母液之间会出现明显的分层现象。目前,针对完成电解槽后的产品的采收方式,主要是将位于电解槽底侧的物料进行输出。由于电解过程中的母液需要循环经过制冷换热器,导致电解槽内的物料存在持续的波动,致使输出的产品中经常存在较大量的母液夹带,很是麻烦。针对上述问题的解决,现有的做法是停机进行产品输出,待产品输出完成后再重新进入电解作业,这样一来,无疑会大幅降低产品的生产效率。The most widely used technology for preparing perfluorotripropylamine is the electrolytic fluorination method. A mother liquor composed of tripropylamine and hydrogen fluoride is passed through a low-voltage direct current in an electrolytic cell to generate free fluorine atoms to directly replace the hydrogen atoms in tripropylamine. After a simple purification treatment, the perfluorotripropylamine product can be obtained. In this process, it is necessary to circulate the mother liquor and the product through a corresponding refrigeration heat exchanger to cool the mother liquor and the product, so as to prevent the mother liquor and the product from gasifying due to temperature rise during the electrolysis process. Since the density of the electrolytic product "perfluorotripropylamine" is higher than that of the mother liquor, there will be obvious stratification between the prepared product and the mother liquor. At present, the method for collecting the product after the electrolytic cell is completed is mainly to output the material located at the bottom side of the electrolytic cell. Since the mother liquor in the electrolysis process needs to circulate through the refrigeration heat exchanger, the material in the electrolytic cell has continuous fluctuations, resulting in a large amount of mother liquor entrainment in the output product, which is very troublesome. In order to solve the above problem, the existing practice is to stop the machine to output the product, and then re-enter the electrolysis operation after the product output is completed. This will undoubtedly greatly reduce the production efficiency of the product.
因此,在不停机,即不影响电解进程的基础上,设计一款能够有效便捷将产品进行输出,且能够明显降低产品输出时对电解母液的夹带量的能够检测液体密度的全氟三丙胺电解槽是本发明的研究目的。Therefore, the research purpose of the present invention is to design a perfluorotripropylamine electrolytic cell that can detect liquid density and can output the product effectively and conveniently without stopping the machine, that is, without affecting the electrolysis process, and can significantly reduce the amount of entrainment of the electrolytic mother liquor during product output.
发明内容Summary of the invention
针对上述现有技术存在的技术问题,本发明在于提供了一种能够检测液体密度的全氟三丙胺电解槽,该能够检测液体密度的全氟三丙胺电解槽能够有效解决上述现有技术存在的技术问题。In view of the technical problems existing in the above-mentioned prior art, the present invention provides a perfluorotripropylamine electrolytic cell capable of detecting liquid density, which can effectively solve the technical problems existing in the above-mentioned prior art.
本发明的技术方案是:The technical solution of the present invention is:
一种能够检测液体密度的全氟三丙胺电解槽,包括:A perfluorotripropylamine electrolytic cell capable of detecting liquid density, comprising:
电解槽本体,所述电解槽本体的一侧向外设置有母液进液管,所述电解槽本体1为现有电解槽,其为现有设备,针对其具体构造这里不在赘述;An electrolytic cell body, one side of which is provided with a mother liquid inlet pipe, and the electrolytic cell body 1 is an existing electrolytic cell, which is an existing device, and its specific structure is not described here;
制冷换热器,包含立式换热罐,所述立式换热罐的上下侧分别固接有相应的上隔板和下隔板,所述上隔板和下隔板之间贯穿连接有多个相应的换热流通管,所述下隔板底侧的立式换热罐通过相应的循环进料管泵接到所述电解槽本体的底部,所述上隔板上侧的立式换热罐通过相应的循环回料管连接到所述电解槽本体的上部,所述立式换热罐的底端通过相应的单向阀向外连接有相应的产品出料管;A refrigeration heat exchanger, comprising a vertical heat exchange tank, wherein the upper and lower sides of the vertical heat exchange tank are respectively fixedly connected with corresponding upper partitions and lower partitions, and a plurality of corresponding heat exchange circulation pipes are connected through the upper and lower partitions, the vertical heat exchange tank on the bottom side of the lower partition is connected to the bottom of the electrolytic cell body through a corresponding circulation feed pipe pump, the vertical heat exchange tank on the upper side of the upper partition is connected to the upper part of the electrolytic cell body through a corresponding circulation return pipe, and the bottom end of the vertical heat exchange tank is connected to the corresponding product discharge pipe through a corresponding one-way valve;
换热介质循环机构,包含呈夹层状态固接于所述下隔板下侧的立式换热罐外侧的换热夹套,所述换热夹套的上部设置有一连接到所述下隔板上侧的立式换热罐上的导通管,所述换热夹套的底侧向外连接有冷媒进入管,所述上隔板下侧的立式换热罐向外连接有冷媒排出管;The heat exchange medium circulation mechanism comprises a heat exchange jacket fixedly connected to the outer side of the vertical heat exchange tank on the lower side of the lower partition in a sandwich state, a conducting pipe connected to the vertical heat exchange tank on the upper side of the lower partition is arranged on the upper part of the heat exchange jacket, a refrigerant inlet pipe is connected to the bottom side of the heat exchange jacket, and a refrigerant discharge pipe is connected to the vertical heat exchange tank on the lower side of the upper partition;
多功能隔离机构,包含设置于所述循环进料管下侧的立式换热罐内的活动隔离件,所述活动隔离件的中部向下连接有可伸缩波纹管,所述立式换热罐与换热夹套的底部之间贯穿安装有一相应的限位管,所述可伸缩波纹管的底侧套设于所述限位管内,且所述可伸缩波纹管的底端部密封连接到所述换热夹套的底部;所述活动隔离件上呈环形阵列设置有若干个相应的安装孔,所述安装孔的周围分别设置有若干个相应的透液孔,安装孔处分别可升降安装有截面呈工字形设置的封堵件,所述封堵件的密度小于产品的密度、大于母液的密度,封堵件的底部可对所述透液孔形成封堵,封堵件的顶部不对所述透液孔形成封堵;The multifunctional isolating mechanism comprises a movable isolating member arranged in the vertical heat exchange tank at the lower side of the circulating feed pipe, a retractable bellows is connected downwardly to the middle part of the movable isolating member, a corresponding limit tube is installed between the vertical heat exchange tank and the bottom of the heat exchange jacket, the bottom side of the retractable bellows is sleeved in the limit tube, and the bottom end of the retractable bellows is sealed and connected to the bottom of the heat exchange jacket; a plurality of corresponding mounting holes are arranged in an annular array on the movable isolating member, a plurality of corresponding liquid permeable holes are arranged around the mounting holes, and plugging members with an I-shaped cross section can be lifted and installed at the mounting holes, the density of the plugging member is less than the density of the product and greater than the density of the mother liquid, the bottom of the plugging member can form a blockage for the liquid permeable hole, and the top of the plugging member does not form a blockage for the liquid permeable hole;
隔离件驱动机构,包含设置于所述换热夹套底侧的驱动液压缸,所述驱动液压缸的活塞杆端套设于所述可伸缩波纹管内、并连接到所述活动隔离件的底侧,所述活动隔离件上设置有至少一个相应的压力传感器,其中一个封堵件上浮到位后对所述压力传感器形成抵接压紧,当贮存于所述立式换热罐底部的产品高度上升至所述封堵件的顶部所在高度时,所述封堵件在其最大浮力作用下对所述压力传感器的作用力达到设定值,所述驱动液压缸的活塞杆回缩,以驱动所述活动隔离件将贮存于其底侧的产品从所述产品出料管挤压输出。The isolation member driving mechanism comprises a driving hydraulic cylinder arranged on the bottom side of the heat exchange jacket, the piston rod end of the driving hydraulic cylinder is sleeved in the retractable bellows and connected to the bottom side of the movable isolation member, and at least one corresponding pressure sensor is arranged on the movable isolation member, and one of the sealing members floats up to the position to form abutment and compression against the pressure sensor. When the height of the product stored at the bottom of the vertical heat exchange tank rises to the height of the top of the sealing member, the force exerted by the sealing member on the pressure sensor under the action of its maximum buoyancy reaches a set value, and the piston rod of the driving hydraulic cylinder retracts to drive the movable isolation member to extrude and output the product stored on its bottom side from the product discharge pipe.
所述活动隔离件内均匀填充安装有诸多相应的减振用阻尼粒子。The movable isolating member is evenly filled with a plurality of corresponding vibration-reducing damping particles.
所述单向阀外侧的产品出料管上连接有一相应的虹吸三通管,所述虹吸三通管的虹吸段连接到所述可伸缩波纹管与限位管的底部间隔处。A corresponding siphon tee is connected to the product discharge pipe outside the one-way valve, and the siphon section of the siphon tee is connected to the bottom interval between the telescopic bellows and the limiting pipe.
所述压力传感器的信号线贯穿所述可伸缩波纹管连接到外界电控制器上。The signal line of the pressure sensor passes through the retractable bellows and is connected to an external electrical controller.
所述产品出料管连接到相应的中间罐上。The product discharge pipe is connected to the corresponding intermediate tank.
所述中间罐泵接到相应的蒸馏设备的进料端。The intermediate tank pump is connected to the feed end of the corresponding distillation equipment.
所述电解槽本体的右侧上部向外连接有尾气排出管。The upper right side of the electrolytic cell body is externally connected with a tail gas exhaust pipe.
所述电解槽本体的左侧向外连接相应的氮气置换管,所述氮气置换管连接到外界氮气源。The left side of the electrolytic cell body is externally connected to a corresponding nitrogen replacement pipe, and the nitrogen replacement pipe is connected to an external nitrogen source.
本发明的优点:Advantages of the present invention:
1)本发明将产品的采收端从电解槽本体更替为制冷换热器,在不影响制冷换热器的正常运行的基础上,通过多功能隔离机构的设置,以在制冷换热器的立式换热罐的底部形成隔离区,物料于立式换热罐进行循环制冷的过程中,密度大于电解母液的产品将逐步经透液孔于活动隔离件的底侧形成贮存,当贮存于立式换热罐底部的产品高度上升至封堵件的所在位置时,封堵件开始呈漂浮状态,直至贮存于立式换热罐底部的产品高度上升至封堵件的顶部所在高度时,封堵件所受浮力最大,在其最大浮力作用下对压力传感器的作用力达到设定值时,即可检测判断出:贮存于立式换热罐底部的高密度产品的贮存量达到封堵件的顶部高度,此时,控制驱动液压缸的活塞杆回缩,以驱动活动隔离件将贮存于其底侧的产品从产品出料管挤压输出。产品输出过程中,电解进程正常进行,从而在不影响电解进程的基础上,有效便捷将产品进行输出,且能够明显降低产品输出时对电解母液的夹带量。1) The present invention replaces the product collection end from the electrolytic cell body to the refrigeration heat exchanger. On the basis of not affecting the normal operation of the refrigeration heat exchanger, an isolation area is formed at the bottom of the vertical heat exchange tank of the refrigeration heat exchanger through the setting of a multifunctional isolation mechanism. In the process of circulating refrigeration of the material in the vertical heat exchange tank, the product with a density greater than the electrolytic mother liquid will gradually be stored on the bottom side of the movable isolation part through the liquid permeable hole. When the height of the product stored at the bottom of the vertical heat exchange tank rises to the position of the plugging part, the plugging part begins to float until the height of the product stored at the bottom of the vertical heat exchange tank rises to the height of the top of the plugging part. The buoyancy of the plugging part is the largest. When the force acting on the pressure sensor under the action of its maximum buoyancy reaches the set value, it can be detected and judged that the storage amount of the high-density product stored at the bottom of the vertical heat exchange tank reaches the top height of the plugging part. At this time, the piston rod of the control driving hydraulic cylinder is retracted to drive the movable isolation part to squeeze and output the product stored on its bottom side from the product discharge pipe. During the product output process, the electrolysis process proceeds normally, so that the product can be output effectively and conveniently without affecting the electrolysis process, and the amount of entrainment of the electrolytic mother liquor during product output can be significantly reduced.
2)本发明的活动隔离件中部向下连接有可伸缩波纹管,可伸缩波纹管的底侧套设于限位管内,且其底端部密封连接到换热夹套的底部,在可伸缩波纹管、限位管的介入下,实现对隔离件驱动机构的外置安装,从而防止因活动隔离件的驱动而导致出现物料泄漏问题,以确保本发明的实用效果。2) The middle part of the movable isolator of the present invention is connected downwardly with a retractable bellows, the bottom side of the retractable bellows is sleeved in the limiting tube, and the bottom end thereof is sealed and connected to the bottom of the heat exchange jacket. With the intervention of the retractable bellows and the limiting tube, the external installation of the isolator driving mechanism is realized, thereby preventing the material leakage caused by the driving of the movable isolator, thereby ensuring the practical effect of the present invention.
3)本发明的换热介质循环机构包含呈夹层状态固接于下隔板下侧的立式换热罐外侧的换热夹套,制冷热交换过程中,冷媒预先经换热夹套进行流通,以对贮存于立式换热罐底侧的产品物料形成降温,使贮存于立式换热罐底侧的产品物料始终处于稳定的液态状态下,从而进一步确保本发明的实用效果。3) The heat exchange medium circulation mechanism of the present invention comprises a heat exchange jacket fixed to the outer side of the vertical heat exchange tank on the lower side of the lower partition in a sandwich state. During the refrigeration heat exchange process, the refrigerant is circulated through the heat exchange jacket in advance to cool the product material stored on the bottom side of the vertical heat exchange tank, so that the product material stored on the bottom side of the vertical heat exchange tank is always in a stable liquid state, thereby further ensuring the practical effect of the present invention.
4)本发明的活动隔离件内均匀填充安装有诸多相应的减振用阻尼粒子,在减振用阻尼粒子之间的摩擦耗能作用下,有效形成减振隔离层,以降低循环进液过程对贮存于立式换热罐底侧的产品的波动影响,从而降低循环的电解母液混入贮存于立式换热罐底侧的产品内的概率,以进一步降低产品输出时对电解母液的夹带量。4) The movable isolating member of the present invention is evenly filled with a plurality of corresponding vibration-reducing damping particles. Under the effect of friction energy dissipation between the vibration-reducing damping particles, a vibration-reducing isolation layer is effectively formed to reduce the fluctuation effect of the circulating liquid inlet process on the product stored at the bottom side of the vertical heat exchange tank, thereby reducing the probability of the circulating electrolyte mother liquid mixing into the product stored at the bottom side of the vertical heat exchange tank, so as to further reduce the entrainment of the electrolyte mother liquid when the product is output.
5)本发明的单向阀外侧的产品出料管上连接有一相应的虹吸三通管,虹吸三通管的虹吸段连接到可伸缩波纹管与限位管的底部间隔处。在活动隔离件下行以将贮存于其底侧的产品从产品出料管挤压输出的过程中,虹吸三通管对可伸缩波纹管与限位管的间隔处形成虹吸,以将可伸缩波纹管与限位管之间的产品抽排往产品出料管进行输出,从而对可伸缩波纹管与限位管的间隔处形成泄压,以防止可伸缩波纹管过度承压而导致出现明显的变形,从而进一步确保本发明的实用效果。5) A corresponding siphon tee is connected to the product discharge pipe on the outside of the one-way valve of the present invention, and the siphon section of the siphon tee is connected to the bottom gap between the telescopic bellows and the limit tube. When the movable isolating member moves downward to squeeze and discharge the product stored on its bottom side from the product discharge pipe, the siphon tee forms a siphon on the gap between the telescopic bellows and the limit tube to pump and discharge the product between the telescopic bellows and the limit tube to the product discharge pipe, thereby forming a pressure relief on the gap between the telescopic bellows and the limit tube to prevent the telescopic bellows from being over-pressurized and causing obvious deformation, thereby further ensuring the practical effect of the present invention.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为本发明的结构示意图。FIG1 is a schematic structural diagram of the present invention.
图2为制冷换热器的结构示意图。FIG. 2 is a schematic diagram of the structure of a refrigeration heat exchanger.
图3为活动隔离件的结构示意图。FIG. 3 is a schematic structural diagram of a movable isolating member.
附图中:电解槽本体1、母液进液管2、立式换热罐301、上隔板302、下隔板303、换热流通管304、循环进料管4、循环回料管5、单向阀6、产品出料管7、换热夹套801、导通管802、冷媒进入管803、冷媒排出管804、活动隔离件901、可伸缩波纹管902、限位管903、封堵件904、透液孔10、驱动液压缸11、压力传感器12、减振用阻尼粒子13、虹吸三通管14、中间罐15、尾气排出管16、氮气置换管17。In the accompanying drawings: electrolytic cell body 1, mother liquor inlet pipe 2, vertical heat exchange tank 301, upper partition 302, lower partition 303, heat exchange circulation pipe 304, circulation feed pipe 4, circulation return pipe 5, one-way valve 6, product discharge pipe 7, heat exchange jacket 801, conducting pipe 802, refrigerant inlet pipe 803, refrigerant discharge pipe 804, movable isolation part 901, retractable bellows 902, limit pipe 903, blocking part 904, liquid permeable hole 10, driving hydraulic cylinder 11, pressure sensor 12, damping particles for vibration reduction 13, siphon tee 14, intermediate tank 15, exhaust gas discharge pipe 16, nitrogen replacement pipe 17.
具体实施方式DETAILED DESCRIPTION
为了便于本领域技术人员理解,现将实施例结合附图对本发明的结构作进一步详细描述:In order to facilitate understanding by those skilled in the art, the structure of the present invention is further described in detail with reference to the embodiments and the accompanying drawings:
参考图1-3,一种能够检测液体密度的全氟三丙胺电解槽,包括:Referring to Figures 1-3, a perfluorotripropylamine electrolytic cell capable of detecting liquid density comprises:
电解槽本体1,所述电解槽本体1的一侧向外设置有母液进液管2,所述电解槽本体1为现有电解槽设备,其为现有设备,针对其具体构造这里不在赘述;An electrolytic cell body 1, a mother liquid inlet pipe 2 is provided outwardly on one side of the electrolytic cell body 1, and the electrolytic cell body 1 is an existing electrolytic cell device, which is an existing device and its specific structure is not described here;
制冷换热器,包含立式换热罐301,所述立式换热罐301的上下侧分别固接有相应的上隔板302和下隔板303,所述上隔板302和下隔板303之间贯穿连接有多个相应的换热流通管304,所述下隔板303底侧的立式换热罐301通过相应的循环进料管4泵接到所述电解槽本体1的底部,所述上隔板302上侧的立式换热罐301通过相应的循环回料管5连接到所述电解槽本体1的上部,所述立式换热罐301的底端通过相应的单向阀6向外连接有相应的产品出料管7;A refrigeration heat exchanger, comprising a vertical heat exchange tank 301, wherein upper and lower sides of the vertical heat exchange tank 301 are respectively fixedly connected with corresponding upper partitions 302 and lower partitions 303, and a plurality of corresponding heat exchange circulation pipes 304 are connected through the upper partitions 302 and the lower partitions 303, wherein the vertical heat exchange tank 301 on the bottom side of the lower partition 303 is connected to the bottom of the electrolytic cell body 1 through a corresponding circulation feed pipe 4 pump, and the vertical heat exchange tank 301 on the upper side of the upper partition 302 is connected to the upper part of the electrolytic cell body 1 through a corresponding circulation return pipe 5, and the bottom end of the vertical heat exchange tank 301 is connected to the corresponding product discharge pipe 7 through a corresponding one-way valve 6;
换热介质循环机构,包含呈夹层状态固接于所述下隔板303下侧的立式换热罐301外侧的换热夹套801,所述换热夹套801的上部设置有一连接到所述下隔板303上侧的立式换热罐301上的导通管802,所述换热夹套801的底侧向外连接有冷媒进入管803,所述上隔板302下侧的立式换热罐301向外连接有冷媒排出管804;The heat exchange medium circulation mechanism comprises a heat exchange jacket 801 fixedly connected to the outer side of the vertical heat exchange tank 301 on the lower side of the lower partition 303 in a sandwich state, a conducting pipe 802 connected to the vertical heat exchange tank 301 on the upper side of the lower partition 303 is provided on the upper part of the heat exchange jacket 801, a refrigerant inlet pipe 803 is connected to the bottom side of the heat exchange jacket 801, and a refrigerant outlet pipe 804 is connected to the vertical heat exchange tank 301 on the lower side of the upper partition 302;
多功能隔离机构,包含设置于所述循环进料管4下侧的立式换热罐301内的活动隔离件901,所述活动隔离件901的中部向下连接有可伸缩波纹管902,所述立式换热罐301与换热夹套801的底部之间贯穿安装有一相应的限位管903,所述可伸缩波纹管902的底侧套设于所述限位管903内,且所述可伸缩波纹管902的底端部密封连接到所述换热夹套801的底部;所述活动隔离件901上呈环形阵列设置有若干个相应的安装孔,所述安装孔的周围分别设置有若干个相应的透液孔10,安装孔处分别可升降安装有截面呈工字形设置的封堵件904,所述封堵件904的密度小于产品的密度、大于母液的密度,封堵件904的底部可对所述透液孔10形成封堵,封堵件904的顶部不对所述透液孔10形成封堵;The multifunctional isolation mechanism comprises a movable isolation member 901 disposed in the vertical heat exchange tank 301 below the circulating feed pipe 4, the middle of the movable isolation member 901 is downwardly connected with a retractable bellows 902, a corresponding limit tube 903 is installed between the vertical heat exchange tank 301 and the bottom of the heat exchange jacket 801, the bottom side of the retractable bellows 902 is sleeved in the limit tube 903, and the bottom end of the retractable bellows 902 is sealed and connected to the heat exchange jacket 801. The bottom of the sleeve 801; the movable isolating member 901 is provided with a plurality of corresponding mounting holes in an annular array, and a plurality of corresponding liquid permeable holes 10 are respectively provided around the mounting holes, and a blocking member 904 with an I-shaped cross section can be installed at the mounting holes in a lifting manner, and the density of the blocking member 904 is less than the density of the product and greater than the density of the mother liquid, and the bottom of the blocking member 904 can block the liquid permeable hole 10, and the top of the blocking member 904 does not block the liquid permeable hole 10;
隔离件驱动机构,包含设置于所述换热夹套801底侧的驱动液压缸11,所述驱动液压缸11的活塞杆端套设于所述可伸缩波纹管902内、并连接到所述活动隔离件901的底侧,所述活动隔离件901上设置有至少一个相应的压力传感器12,其中一个封堵件904上浮到位后对所述压力传感器12形成抵接压紧,当贮存于所述立式换热罐301底部的产品高度上升至所述封堵件904的顶部所在高度时,所述封堵件904在其最大浮力作用下对所述压力传感器12的作用力达到设定值,所述驱动液压缸11的活塞杆回缩,以驱动所述活动隔离件901将贮存于其底侧的产品从所述产品出料管7挤压输出。The isolation member driving mechanism includes a driving hydraulic cylinder 11 arranged on the bottom side of the heat exchange jacket 801, the piston rod end of the driving hydraulic cylinder 11 is sleeved in the retractable bellows 902 and connected to the bottom side of the movable isolation member 901, and at least one corresponding pressure sensor 12 is provided on the movable isolation member 901, and one of the sealing members 904 floats up to form abutment and compression on the pressure sensor 12. When the height of the product stored at the bottom of the vertical heat exchange tank 301 rises to the height of the top of the sealing member 904, the sealing member 904 exerts a force on the pressure sensor 12 under the action of its maximum buoyancy to reach a set value, and the piston rod of the driving hydraulic cylinder 11 retracts to drive the movable isolation member 901 to squeeze and output the product stored on its bottom side from the product discharge pipe 7.
本发明将产品的采收端从电解槽本体1更替为制冷换热器,在不影响制冷换热器的正常运行的基础上,通过多功能隔离机构的设置,以在制冷换热器的立式换热罐301的底部形成隔离区,物料于立式换热罐301进行循环制冷的过程中,密度大于电解母液的产品将逐步经透液孔10于活动隔离件901的底侧形成贮存,当贮存于立式换热罐301底部的产品高度上升至封堵件904的所在位置时,封堵件904开始呈漂浮状态,直至贮存于立式换热罐301底部的产品高度上升至封堵件904的顶部所在高度时,封堵件904所受浮力最大,在其最大浮力作用下对压力传感器12的作用力达到设定值时,即可检测判断出:贮存于立式换热罐301底部的高密度产品的贮存量达到封堵件904的顶部高度,此时,控制驱动液压缸11的活塞杆回缩,以驱动活动隔离件901将贮存于其底侧的产品从产品出料管7挤压输出。产品输出过程中,电解进程正常进行,从而在不影响电解进程的基础上,有效便捷将产品进行输出,且能够明显降低产品输出时对电解母液的夹带量。The present invention replaces the product collection end from the electrolytic cell body 1 with the refrigeration heat exchanger. On the basis of not affecting the normal operation of the refrigeration heat exchanger, the multifunctional isolation mechanism is set to form an isolation area at the bottom of the vertical heat exchange tank 301 of the refrigeration heat exchanger. During the process of circulating refrigeration of the material in the vertical heat exchange tank 301, the product with a density greater than the electrolytic mother liquid will gradually pass through the liquid permeable hole 10 to form storage on the bottom side of the movable isolation member 901. When the height of the product stored at the bottom of the vertical heat exchange tank 301 rises to the position of the blocking member 904, the blocking member 904 It starts to float until the height of the product stored at the bottom of the vertical heat exchange tank 301 rises to the height of the top of the plugging member 904. The buoyancy of the plugging member 904 is the largest. When the force acting on the pressure sensor 12 under the action of its maximum buoyancy reaches the set value, it can be detected and judged that the storage volume of the high-density product stored at the bottom of the vertical heat exchange tank 301 reaches the top height of the plugging member 904. At this time, the piston rod of the control driving hydraulic cylinder 11 is retracted to drive the movable isolation member 901 to squeeze and output the product stored at its bottom side from the product discharge pipe 7. During the product output process, the electrolysis process is carried out normally, so that the product can be effectively and conveniently output without affecting the electrolysis process, and the entrainment of the electrolytic mother liquor during the product output can be significantly reduced.
本发明在可伸缩波纹管902、限位管903的介入下,实现了对隔离件驱动机构的外置安装,从而防止因活动隔离件901的驱动而导致出现物料泄漏问题,以确保本发明的实用效果。且本发明的制冷热交换过程中,冷媒预先经换热夹套801进行流通,以对贮存于立式换热罐301底侧的产品物料形成降温,使贮存于立式换热罐301底侧的产品物料始终处于稳定的液态状态下,从而确保本发明的实用效果。The present invention realizes the external installation of the isolator drive mechanism with the intervention of the telescopic bellows 902 and the limit tube 903, thereby preventing the material leakage caused by the driving of the movable isolator 901, so as to ensure the practical effect of the present invention. In the refrigeration heat exchange process of the present invention, the refrigerant is circulated through the heat exchange jacket 801 in advance to cool the product material stored at the bottom side of the vertical heat exchange tank 301, so that the product material stored at the bottom side of the vertical heat exchange tank 301 is always in a stable liquid state, thereby ensuring the practical effect of the present invention.
所述活动隔离件901内均匀填充安装有诸多相应的减振用阻尼粒子13,本实施例中,所述减振用阻尼粒子13采用铁制球体状颗粒。在减振用阻尼粒子13之间的摩擦耗能作用下,有效形成减振隔离层,以降低循环进液过程对贮存于立式换热罐301底侧的产品的波动影响,从而降低循环的电解母液混入贮存于立式换热罐301底侧的产品内的概率,以进一步降低产品输出时对电解母液的夹带量。The movable isolating member 901 is evenly filled with a plurality of corresponding vibration damping particles 13. In this embodiment, the vibration damping particles 13 are iron spherical particles. Under the friction energy dissipation between the vibration damping particles 13, a vibration damping isolation layer is effectively formed to reduce the fluctuation effect of the circulating liquid inlet process on the product stored at the bottom of the vertical heat exchange tank 301, thereby reducing the probability of the circulating electrolytic mother liquid being mixed into the product stored at the bottom of the vertical heat exchange tank 301, so as to further reduce the entrainment of the electrolytic mother liquid when the product is output.
所述单向阀6外侧的产品出料管7上连接有一相应的虹吸三通管14,所述虹吸三通管14的虹吸段连接到所述可伸缩波纹管902与限位管903的底部间隔处。在活动隔离件901下行以将贮存于其底侧的产品从产品出料管7挤压输出的过程中,虹吸三通管14对可伸缩波纹管902与限位管903的间隔处形成虹吸,以将可伸缩波纹管902与限位管903之间的产品抽排往产品出料管7进行输出,从而对可伸缩波纹管902与限位管903的间隔处形成泄压,以防止可伸缩波纹管902过度承压而导致出现明显的变形,从而进一步确保本发明的实用效果。A corresponding siphon tee 14 is connected to the product discharge pipe 7 outside the one-way valve 6, and the siphon section of the siphon tee 14 is connected to the bottom interval between the telescopic bellows 902 and the limiting pipe 903. When the movable isolating member 901 moves downward to squeeze and output the product stored at the bottom side thereof from the product discharge pipe 7, the siphon tee 14 forms a siphon on the interval between the telescopic bellows 902 and the limiting pipe 903, so as to pump and discharge the product between the telescopic bellows 902 and the limiting pipe 903 to the product discharge pipe 7, thereby forming a pressure relief on the interval between the telescopic bellows 902 and the limiting pipe 903, so as to prevent the telescopic bellows 902 from being over-pressurized and causing obvious deformation, thereby further ensuring the practical effect of the present invention.
所述压力传感器12的信号线贯穿所述可伸缩波纹管902连接到外界电控制器上。The signal line of the pressure sensor 12 passes through the retractable bellows 902 and is connected to an external electrical controller.
所述产品出料管7连接到相应的中间罐15上。所述中间罐15泵接到相应的蒸馏设备的进料端。The product discharge pipe 7 is connected to the corresponding intermediate tank 15. The intermediate tank 15 is pumped to the feed end of the corresponding distillation equipment.
所述电解槽本体1的右侧上部向外连接有尾气排出管16。所述电解槽本体1的左侧向外连接相应的氮气置换管17,所述氮气置换管17连接到外界氮气源。在电解进程开始之前,预先通过所述氮气置换管17往电解槽本体1内通入氮气,以进行氮气置换动作。The upper right side of the electrolytic cell body 1 is connected to an exhaust gas exhaust pipe 16. The left side of the electrolytic cell body 1 is connected to a corresponding nitrogen replacement pipe 17, which is connected to an external nitrogen source. Before the electrolysis process begins, nitrogen is introduced into the electrolytic cell body 1 through the nitrogen replacement pipe 17 to perform nitrogen replacement.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention. It should be pointed out that for ordinary technicians in this technical field, several improvements and modifications can be made without departing from the principle of the present invention. These improvements and modifications should also be regarded as the scope of protection of the present invention.
Claims (8)
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CN202410916439.2A CN118461022B (en) | 2024-07-09 | 2024-07-09 | Perfluoro tripropylamine electrolytic tank capable of detecting liquid density |
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CN117740466A (en) * | 2024-02-19 | 2024-03-22 | 国网浙江省电力有限公司宁波供电公司 | An insulating oil liquid-taking device and liquid-taking method with liquid level control |
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CN117738837A (en) * | 2023-12-08 | 2024-03-22 | 华北电力大学(保定) | Longitudinal sea rotating wheel power generation hydrogen production device |
CN117740466A (en) * | 2024-02-19 | 2024-03-22 | 国网浙江省电力有限公司宁波供电公司 | An insulating oil liquid-taking device and liquid-taking method with liquid level control |
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