WO2020228550A1 - 一种便于排料的蒸发结晶装置 - Google Patents

一种便于排料的蒸发结晶装置 Download PDF

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WO2020228550A1
WO2020228550A1 PCT/CN2020/088350 CN2020088350W WO2020228550A1 WO 2020228550 A1 WO2020228550 A1 WO 2020228550A1 CN 2020088350 W CN2020088350 W CN 2020088350W WO 2020228550 A1 WO2020228550 A1 WO 2020228550A1
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crystallization
tank
discharging
crystallization tank
filter screen
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PCT/CN2020/088350
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English (en)
French (fr)
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树晓荣
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江苏嘉泰蒸发设备股份有限公司
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Publication of WO2020228550A1 publication Critical patent/WO2020228550A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D9/00—Crystallisation
    • B01D9/02—Crystallisation from solutions

Definitions

  • the invention relates to the technical field of evaporative crystallization equipment, in particular to an evaporative crystallization device that is convenient for discharging.
  • Evaporation refers to the phase change process of a substance from a liquid to a gaseous state
  • crystallization refers to a substance that forms a crystal from a liquid or gaseous state.
  • evaporation refers to the process in which a certain substance in a solution reaches the boiling point and volatilizes by heating
  • crystallization refers to the process in which the solute in the solution reaches supersaturation to precipitate crystals.
  • evaporation and crystallization are often together, because the purpose of evaporation is generally to volatilize the solution in the solution, so that a certain solute in the solution is supersaturated and crystallized.
  • the existing evaporative crystallization device still has shortcomings: firstly, there is no discharging mechanism inside, which is not convenient for discharging the crystals after crystallization, and is not convenient for the daily processing and use of the operators. Secondly, there is no heat utilization mechanism inside. The heat of the high-temperature steam generated during evaporation cannot be used, and the direct discharge will easily lead to the loss of heat energy. Finally, there is no self-cleaning structure inside, and the filter cannot be cleaned, which will easily cause the filter to block and affect the crystallization of the solution. And filtering treatment.
  • the purpose of the present invention is to solve the problem of inconvenient discharging treatment of crystals after crystallization, inability to utilize the heat of high-temperature steam generated during evaporation, and inability to clean the filter screen, and proposes a convenient discharging process The evaporation crystallization device.
  • An evaporative crystallization device convenient for discharging including a crystallization tank, a sealed top cover installed on the top of the crystallization tank, a mixer installed at the center of the top of the sealed top cover, a stirring rod installed at the bottom of the mixer and located inside the crystallization tank, and An electric heating plate on the inside of the tank, the inside of the crystallization tank is located on the outside of the stirring rod, and a heat release box with a ring structure is installed.
  • the crystallization tank is connected with the heat release box through an air inlet pipe, and the outside of the heat release box is horizontal Connected with an exhaust pipe penetrating the crystallizing tank, the inner side of the crystallizing tank is located below the heat release box and horizontally installed with a filter screen, and the outer end surface of the stirring rod is located above the filter screen with a plurality of sets of brushes installed at equal intervals
  • a discharge hopper is fixedly connected to the bottom of the crystallization tank, and the outer end surface of the stirring rod is located between the discharge hopper and the filter screen.
  • a plurality of groups of scrapers with a right-angle trapezoidal structure are installed on the outer end surface of the stirring rod. The wall and the inner surface of the discharge hopper are attached to each other.
  • the outside of the crystallization tank is located on one side of the filter screen and is horizontally connected with a slag collecting pipe, and the outside of the open end of the slag collecting pipe is connected with a sealing screw cap by screwing.
  • the bottom opening of the discharge hopper is vertically fixedly connected with a discharge pipe, and a control valve is arranged inside the open end of the discharge pipe.
  • the outer surface walls of the multiple sets of brush plates and the outer surface walls of the filter mesh are attached to each other.
  • the bottom end of the outer end surface of the stirring rod is located inside the discharge pipe and is fixedly connected with a spiral blade, and the spiral blade and the discharge pipe are in transitional fit.
  • the outer end surface of the heat release box is fixedly connected with a plurality of groups of bumps in an annular and equidistant manner with respect to the vertical center line of the heat release box.
  • a discharging mechanism is provided inside, and multiple sets of scrapers are provided on the inside of the discharge hopper outside the stirring rod, and the outer walls of the multiple sets of scrapers are attached to the outer surface of the discharge hopper, and at the same time
  • the bottom end of the stirring rod is located inside the discharge pipe with spiral blades.
  • a heat utilization mechanism is provided inside, a heat release box is provided inside the crystallization tank, and the heat release box is connected to the crystallization tank through an air inlet pipe, and an exhaust pipe that penetrates the crystallization tank is connected to the outside of the heat release box.
  • the high-temperature steam When high-temperature steam is generated in the crystallization tank, the high-temperature steam will enter the heat sink through the air inlet pipe under the action of the pressure. When the high-temperature steam contacts the heat sink, it will transfer the high-temperature heat to the heat sink.
  • the heat release box can transfer and heat the solution inside the crystallization tank, and the used steam will be discharged through the exhaust pipe.
  • This structure can utilize the heat of the high-temperature steam during evaporation, which improves This improves the efficiency of the evaporation crystallization treatment in the crystallization tank, and also improves the energy saving of the crystallization device.
  • a self-cleaning structure is arranged inside, and multiple sets of brush plates are arranged on the outside of the stirring rod above the filter screen, and at the same time, a slag collecting pipe and a sealing screw are arranged on the side of the filter screen outside the crystallization tank. Cover, when the stirring rod rotates, multiple sets of brush plates will rotate and scrub the outer surface of the filter screen. The impurities from the brush will be discharged into the slag collecting pipe under the rotation of the brush plate.
  • the structure can realize the self-cleaning treatment of the filter screen, which not only reduces the occurrence of clogging of the filter screen, but also improves the functionality of the crystallization device.
  • FIG. 1 is a schematic diagram of the structure of an evaporation crystallization device that facilitates discharging proposed by the present invention
  • FIG. 2 is a schematic diagram of the internal structure of the crystallization tank of the present invention.
  • Fig. 3 is a schematic cross-sectional structure diagram at A-A in the present invention.
  • an evaporative crystallization device that facilitates discharging, including a crystallization tank 1, a sealing top cover installed on the top of the crystallization tank 1, 2, and a top center of the sealing top cover 2.
  • Agitator 3 at the bottom of the agitator 3 a stirring rod 11 located inside the crystallizer 1 and an electric heating plate 16 mounted on the inside of the crystallizer 1.
  • the inside of the crystallizer 1 is located outside the stirring rod 11 and a ring structure is installed.
  • Heat box 14 crystallizing tank 1 is connected to heat radiating tank 14 through inlet pipe 4, the outside of heat radiating tank 14 is horizontally connected with an exhaust pipe 5 that penetrates crystallizing tank 1, and the inner side of crystallizing tank 1 is located below heat radiating tank 14.
  • a filter screen 12 is installed horizontally, and the outer end surface of the stirring rod 11 is located above the filter screen 12, and a plurality of sets of brush plates 13 are installed in an annular and equidistant manner.
  • the bottom of the crystallizing tank 1 is fixedly connected with a discharge hopper 8 and the outer end surface of the stirring rod 11
  • a plurality of groups of scrapers 17 having a right-angle trapezoidal structure are installed in an annular and equidistant manner, and the outer surface of the scraper 17 and the inner surface of the discharging hopper 8 are attached to each other to facilitate the scraping of crystals. Material processing, thereby reducing the phenomenon of crystals remaining inside the crystallization tank 1.
  • the outside of the crystallizing tank 1 is located on the side of the filter screen 12 and is horizontally connected with a slag collecting pipe 6, and the outside of the open end of the slag collecting pipe 6 is connected with a sealing screw by screwing.
  • the cover 7 and the slag collecting pipe 6 are arranged to facilitate the centralized collection and treatment of solid impurities.
  • the sealing screw cap 7 is arranged to facilitate the sealing treatment at the opening of the slag collecting pipe 6 and the discharge treatment of the slag collecting pipe 6
  • the bottom opening of the discharge hopper 8 is vertically and fixedly connected with a discharge pipe 9, and the opening end of the discharge pipe 9 is provided with a control valve 10 inside.
  • the setting facilitates the opening and closing control processing of the discharge pipe 9.
  • the outer surface walls of the multiple sets of brush plates 13 and the outer surface walls of the filter screen 12 are attached to each other.
  • the bottom end of the outer end surface of the stirring rod 11 is located inside the discharge pipe 9 and is fixedly connected with a spiral blade 18, and the spiral blade 18 and the discharge pipe 9 are in transitional fit.
  • the crystals entering the inside of the discharge pipe 9 can be screw-extruded out of the discharge pipe 9, thereby improving the efficiency of crystal discharge processing.
  • the outer end surface of the heat radiating box 14 is fixedly connected to the vertical center line of the heat radiating box 14 in a ring shape and equidistantly with a plurality of sets of bumps 15.
  • the arrangement of the plurality of sets of bumps 15 improves the heat dissipation.
  • the contact area of the outer wall of the box 14 improves the heat exchange efficiency between the heat release box 14 and the solution.
  • the brush plate 13 When the stirring rod 11 rotates, the brush plate 13 will rotate the outer wall of the filter screen 12, and the impurities from the brush will be discharged into the inside of the slag collecting pipe 6 under the rotation of the brush plate 13.
  • the sealing screw cap 7 can be unscrewed to flush out the impurities inside the slag collecting pipe 6.
  • the solvent evaporates to a crystalline state, it will adhere to the inner surface of the discharge hopper 8.
  • the scraper 17 can be driven to rotate, so that the crystals adhering to the inner wall of the discharge hopper 8 are scraped into the discharge pipe 9.
  • the rotating spiral blade 18 will discharge the crystals inside the discharge pipe 9. Spiral conveying out of the discharge pipe 9 completes the evaporation and crystallization treatment of the solution.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

一种便于排料的蒸发结晶装置，包括结晶罐（1）、安装在结晶罐（1）顶部的密封顶盖（2）、安装在密封顶盖（2）顶部中心处的搅拌机（3）、安装在搅拌机（3）底部位于结晶罐（1）内侧的搅拌杆（11）和安装在结晶罐（1）内侧的电加热板（16）。蒸发结晶装置内部设置有排料机构，便于结晶后晶体的排料处理；设置有热利用机构，可将蒸发时高温蒸汽的热量进行利用处理，提升结晶罐蒸发结晶处理的效率，同时也提升了结晶装置的节能性；设置有自清洁结构，这种结构可实现滤网的自清洁处理，降低了滤网堵塞现象的产生。

Description

一种便于排料的蒸发结晶装置 技术领域
本发明涉及蒸发结晶设备技术领域，尤其涉及一种便于排料的蒸发结晶装置。
背景技术
蒸发是指物质从液态转化为气态的相变过程，结晶是指物质从液态或气态形成晶体。在化学中，蒸发是指通过加热使溶液中的某种物质达到沸点并挥发出来的过程，结晶是指溶液中的溶质达到过饱和而析出晶体的过程。在化学中蒸发和结晶经常是在一起的，因为蒸发的目的一般就是让溶液中溶液挥发出来，从而使溶液中某种溶质达到过饱和，从而使其结晶。
然而现有的蒸发结晶装置仍存在不足之处：首先，内部无设置排料机构，不便于结晶后晶体的排料处理，不便于操作人员的日常加工使用，其次，内部无设置热利用机构，无法将蒸发时产生的高温蒸汽的热量进行利用，直接排出易导致热能的损耗，最后，内部无设置自清洁结构，无法将滤网进行清洁处理，易导致滤网的堵塞，从而影响溶液的结晶和过滤处理。
发明内容
本发明的目的在于：为了解决不便于结晶后晶体的排料处理，无法将蒸发时产生的高温蒸汽的热量进行利用，且无法将滤网进行清洁处理的问题，而提出的一种便于排料的蒸发结晶装置。
为了实现上述目的，本发明采用了如下技术方案：
一种便于排料的蒸发结晶装置，包括结晶罐、安装在结晶罐顶部的密封顶盖、安装在密封顶盖顶部中心处的搅拌机、安装在搅拌机底部位于结晶罐内侧的搅拌 杆和安装在结晶罐内侧的电加热板，所述结晶罐的内部位于搅拌杆的外侧安装有呈环形结构的放热箱，所述结晶罐通过进气管与放热箱连通，所述放热箱的外侧呈水平连通有贯穿结晶罐的排气管，所述结晶罐的内侧位于放热箱的下方呈水平安装有过滤网，所述搅拌杆的外端面位于过滤网的上方呈环形等距安装有多组刷板，所述结晶罐的底部固定连接有排料斗，所述搅拌杆的外端面位于排料斗和过滤网之间呈环形等距安装有多组呈直角梯形结构的刮板，且刮板的外表壁与排料斗的内表壁相互贴合。
作为上述技术方案的进一步描述：
所述结晶罐的外部位于过滤网的一侧呈水平连通有集渣管，且集渣管的开口端外侧通过螺纹旋合连接有密封旋盖。
作为上述技术方案的进一步描述：
所述排料斗的底端开口处呈竖直固定连接有排料管，且排料管的开口端内部设置有控制阀。
作为上述技术方案的进一步描述：
所述多组刷板的外表壁与过滤网的外表壁相互贴合。
作为上述技术方案的进一步描述：
所述搅拌杆的外端面底端位于排料管的内侧固定连接有螺旋叶片，且螺旋叶片的和排料管呈过渡配合。
作为上述技术方案的进一步描述：
所述放热箱的外端面关于放热箱的竖直中线呈环形等距固定连接有多组凸块。
综上所述，由于采用了上述技术方案，本发明的有益效果是：
1、本发明中，内部设置有排料机构，在搅拌杆外部位于排料斗的内侧设置有多组刮板，且多组刮板的外表壁均与排料斗的外表壁相互贴合，同时在搅拌杆的底端位于排料管的内侧设置有螺旋叶片，当溶液蒸发至晶体状态后，会粘附在排料斗的内表壁，当搅拌机工作时，便可带动刮板进行转动，从而将粘附排料斗内壁的晶体刮入到排料管内，同时搅拌杆上转动的螺旋叶片，会将排入到排料管内部的结晶螺旋输送出排料管，这种结构便于结晶后晶体的排料处理，既便于操作人员的日常操作使用，同时也提升了结晶装置排料处理的效率。
2、本发明中，内部设置有热利用机构，在结晶罐的内侧设置有放热箱，且放热箱通过进气管与结晶罐连通，同时放热箱外部连通有贯穿结晶罐的排气管，当结晶罐内产生高温蒸汽时，高温蒸汽在气压的作用下，便会通过进气管进入到放热箱的内部，当高温蒸汽接触到放热箱时，便会将高温热量流动传递至放热箱的内部，放热箱便可将结晶罐内部的溶液进行传递加热处理，利用后的蒸汽便会通过排气管排出，这种结构可将蒸发时高温蒸汽的热量进行利用处理，既提升了结晶罐蒸发结晶处理的效率，同时也提升了结晶装置的节能性。
3、本发明中，内部设置有自清洁结构，在搅拌杆的外部位于过滤网的上方设置有多组刷板，同时在结晶罐的外部位于滤网的一侧设置有集渣管和密封旋盖，当搅拌杆转动时，多组刷板便会将过滤网的外表壁进行旋转洗刷处理，刷洗下的杂质在刷板的旋转作用下，便会排入到集渣管的内部，这种结构可实现滤网的自清洁处理，既降低了滤网堵塞现象的产生，同时也提升了结晶装置的功能性。
附图说明
图1为本发明提出的一种便于排料的蒸发结晶装置的结构示意简图；
图2为本发明中结晶罐的内部结构示意图；
图3为本发明中A-A处的剖面结构示意图。
图例说明：
1、结晶罐；2、密封顶盖；3、搅拌机；4、进气管；5、排气管；6、集渣管；7、密封旋盖；8、排料斗；9、排料管；10、控制阀；11、搅拌杆；12、过滤网；13、刷板；14、放热箱；15、凸块；16、电加热板；17、刮板；18、螺旋叶片。
具体实施方式
下面将结合本发明实施例中的附图，对本发明实施例中的技术方案进行清楚、完整地描述，显然，所描述的实施例仅仅是本发明一部分实施例，而不是全部的实施例。基于本发明中的实施例，本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其它实施例，都属于本发明保护的范围。
请参阅图1-3，本发明提供一种技术方案：一种便于排料的蒸发结晶装置，包括结晶罐1、安装在结晶罐1顶部的密封顶盖2、安装在密封顶盖2顶部中心处的搅拌机3、安装在搅拌机3底部位于结晶罐1内侧的搅拌杆11和安装在结晶罐1内侧的电加热板16，结晶罐1的内部位于搅拌杆11的外侧安装有呈环形结构的放热箱14，结晶罐1通过进气管4与放热箱14连通，放热箱14的外侧呈水平连通有贯穿结晶罐1的排气管5，结晶罐1的内侧位于放热箱14的下方呈水平安装有过滤网12，搅拌杆11的外端面位于过滤网12的上方呈环形等距安装有多组刷板13，结晶罐1的底部固定连接有排料斗8，搅拌杆11的外端面位于排料斗8和过滤网12之间呈环形等距安装有多组呈直角梯形结构的刮板17，且刮板17的外表壁与排料斗8的内表壁相互贴合，便于晶体的刮料处理，从而降低了晶体残留在结晶罐1内部现象的产生。
具体的，如图1和图2所示，结晶罐1的外部位于过滤网12的一侧呈水平 连通有集渣管6，且集渣管6的开口端外侧通过螺纹旋合连接有密封旋盖7，集渣管6的设置，便于固体杂质的集中收集处理，同时密封旋盖7的设置，便于集渣管6开口处的密封处理，同时也便于集渣管6的排料处理
具体的，如图1和图2所示，排料斗8的底端开口处呈竖直固定连接有排料管9，且排料管9的开口端内部设置有控制阀10，控制阀10的设置，便于排料管9的开合控制处理。
具体的，如图2所示，多组刷板13的外表壁与过滤网12的外表壁相互贴合。
具体的，如图2所示，搅拌杆11的外端面底端位于排料管9的内侧固定连接有螺旋叶片18，且螺旋叶片18的和排料管9呈过渡配合，螺旋叶片18的设置，可将进入到排料管9内部的晶体，螺旋挤压排出排料管9，从而提升了晶体排料处理的效率。
具体的，如图3所示，放热箱14的外端面关于放热箱14的竖直中线呈环形等距固定连接有多组凸块15，多组凸块15的设置，提升了放热箱14外壁的接触面积，从而提升了放热箱14和溶液的热交换效率。
工作原理：使用时，打开密封顶盖2，将溶液加入到结晶罐1的内部，并接通电源，搅拌机3会带动搅拌杆11将溶液进行搅拌处理，同时电加热板16会将溶液进行加热处理，结晶罐1内溶液蒸发时产生的高温蒸汽，会在气压的作用下，通过进气管4进入到放热箱14的内部，当高温蒸汽接触到放热箱14时，可对放热箱14内部进行传递加热处理，从而将结晶罐1内部的溶液进行传递加热处理，利用后的蒸汽便会通过排气管5排出，同时结晶罐1内侧的过滤网12，可将溶液进行过滤处理，当搅拌杆11转动时，刷板13便会将过滤网12的外壁，进行旋转洗刷处理，刷洗下的杂质在刷板13的旋转作用下，便会排入到集渣管6的内 部，当杂质过多时，便可旋开密封旋盖7将集渣管6内侧的杂质冲洗排出，当溶剂蒸发至晶体状态时，会粘附在排料斗8的内表壁，当搅拌杆11工作时，便可带动刮板17进行转动，从而将粘附排料斗8内壁上的晶体，刮入到排料管9内，同时转动的螺旋叶片18，会将排入到排料管9内部的晶体，螺旋输送出排料管9，便完成了溶液的蒸发结晶处理。
以上所述，仅为本发明较佳的具体实施方式，但本发明的保护范围并不局限于此，任何熟悉本技术领域的技术人员在本发明揭露的技术范围内，根据本发明的技术方案及其发明构思加以等同替换或改变，都应涵盖在本发明的保护范围之内。

Claims (6)

  1. 一种便于排料的蒸发结晶装置，包括结晶罐(1)、安装在结晶罐(1)顶部的密封顶盖(2)、安装在密封顶盖(2)顶部中心处的搅拌机(3)、安装在搅拌机(3)底部位于结晶罐(1)内侧的搅拌杆(11)和安装在结晶罐(1)内侧的电加热板(16)，其特征在于，所述结晶罐(1)的内部位于搅拌杆(11)的外侧安装有呈环形结构的放热箱(14)，所述结晶罐(1)通过进气管(4)与放热箱(14)连通，所述放热箱(14)的外侧呈水平连通有贯穿结晶罐(1)的排气管(5)，所述结晶罐(1)的内侧位于放热箱(14)的下方呈水平安装有过滤网(12)，所述搅拌杆(11)的外端面位于过滤网(12)的上方呈环形等距安装有多组刷板(13)，所述结晶罐(1)的底部固定连接有排料斗(8)，所述搅拌杆(11)的外端面位于排料斗(8)和过滤网(12)之间呈环形等距安装有多组呈直角梯形结构的刮板(17)，且刮板(17)的外表壁与排料斗(8)的内表壁相互贴合。
  2. 根据权利要求1所述的一种便于排料的蒸发结晶装置，其特征在于，所述结晶罐(1)的外部位于过滤网(12)的一侧呈水平连通有集渣管(6)，且集渣管(6)的开口端外侧通过螺纹旋合连接有密封旋盖(7)。
  3. 根据权利要求1所述的一种便于排料的蒸发结晶装置，其特征在于，排料斗(8)的底端开口处呈竖直固定连接有排料管(9)，且排料管(9)的开口端内部设置有控制阀(10)。
  4. 根据权利要求1所述的一种便于排料的蒸发结晶装置，其特征在于，所述多组刷板(13)的外表壁与过滤网(12)的外表壁相互贴合。
  5. 根据权利要求1或3所述的一种便于排料的蒸发结晶装置，其特征在于，所述搅拌杆(11)的外端面底端位于排料管(9)的内侧固定连接有螺旋叶片(18)， 且螺旋叶片(18)的和排料管(9)呈过渡配合。
  6. 根据权利要求1所述的一种便于排料的蒸发结晶装置，其特征在于，所述放热箱(14)的外端面关于放热箱(14)的竖直中线呈环形等距固定连接有多组凸块(15)。
PCT/CN2020/088350 2019-05-12 2020-04-30 一种便于排料的蒸发结晶装置 WO2020228550A1 (zh)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007049736A1 (ja) * 2005-10-28 2007-05-03 Kyowa Hakko Kogyo Co., Ltd. 濃縮晶析装置および方法
CN205948411U (zh) * 2016-08-18 2017-02-15 田军 一种移动式带废气处理装置的化工物料蒸发结晶罐
CN108837548A (zh) * 2018-06-25 2018-11-20 郑州仁宏医药科技有限公司 一种医药技术开发用药品蒸发结晶装置
CN208525886U (zh) * 2018-07-25 2019-02-22 广东永青生物科技有限公司 一种结晶果糖生产用蒸发设备
CN209952275U (zh) * 2019-05-12 2020-01-17 江苏嘉泰蒸发设备股份有限公司 一种便于排料的蒸发结晶装置

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007049736A1 (ja) * 2005-10-28 2007-05-03 Kyowa Hakko Kogyo Co., Ltd. 濃縮晶析装置および方法
CN205948411U (zh) * 2016-08-18 2017-02-15 田军 一种移动式带废气处理装置的化工物料蒸发结晶罐
CN108837548A (zh) * 2018-06-25 2018-11-20 郑州仁宏医药科技有限公司 一种医药技术开发用药品蒸发结晶装置
CN208525886U (zh) * 2018-07-25 2019-02-22 广东永青生物科技有限公司 一种结晶果糖生产用蒸发设备
CN209952275U (zh) * 2019-05-12 2020-01-17 江苏嘉泰蒸发设备股份有限公司 一种便于排料的蒸发结晶装置

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