WO2021008160A1 - 一种反应装置 - Google Patents

一种反应装置 Download PDF

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Publication number
WO2021008160A1
WO2021008160A1 PCT/CN2020/080713 CN2020080713W WO2021008160A1 WO 2021008160 A1 WO2021008160 A1 WO 2021008160A1 CN 2020080713 W CN2020080713 W CN 2020080713W WO 2021008160 A1 WO2021008160 A1 WO 2021008160A1
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WIPO (PCT)
Prior art keywords
pipeline
valve
circulation
feeding
discharging
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PCT/CN2020/080713
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English (en)
French (fr)
Inventor
孟静
韦志龙
魏会
李玉博
Original Assignee
佳化化学科技发展（上海）有限公司
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Application filed by 佳化化学科技发展（上海）有限公司 filed Critical 佳化化学科技发展（上海）有限公司
Priority to EP20839736.4A priority Critical patent/EP3964282A4/en
Priority to US17/617,149 priority patent/US11772064B2/en
Publication of WO2021008160A1 publication Critical patent/WO2021008160A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/008—Feed or outlet control devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1868—Stationary reactors having moving elements inside resulting in a loop-type movement
    • B01J19/1881—Stationary reactors having moving elements inside resulting in a loop-type movement externally, i.e. the mixture leaving the vessel and subsequently re-entering it
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
    • B01F25/51—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7176—Feed mechanisms characterised by the means for feeding the components to the mixer using pumps
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/75—Discharge mechanisms
    • B01F35/754—Discharge mechanisms characterised by the means for discharging the components from the mixer
    • B01F35/7547—Discharge mechanisms characterised by the means for discharging the components from the mixer using valves, gates, orifices or openings
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/0066—Stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2203/00—Processes utilising sub- or super atmospheric pressure
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
    • B01J2204/002—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the feeding side being of particular interest
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
    • B01J2204/005—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the outlet side being of particular interest
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743—Feeding or discharging of solids
    • B01J2208/00769—Details of feeding or discharging
    • B01J2208/00787—Bringing the solid in the form of a slurry before feeding it to the reactor

Definitions

  • This application relates to the technical field of chemical production equipment, in particular to a reaction device.
  • Chinese patent CN204768663U discloses a reaction kettle, which includes a kettle body, a pipeline assembly, a circulating pump, a feeding hopper and a valve assembly.
  • the two ends of the kettle body are respectively provided with an upper head and a lower head; the feeding end and the discharging end of the circulating pump are both connected with the feeding pipe; the feeding hopper is connected with the feeding pipe, and the feeding hopper is used to input the reaction raw materials.
  • the reaction raw materials can be transported from the feeding hopper to the kettle body through the flow pipe, the branch pipe, the guide pipe and the overflow pipe.
  • the feeding hopper can be installed on the floor of the factory building or on an external bracket, and can also be adjusted and installed according to the actual situation.
  • the valve assembly includes a discharging valve, a feeding valve and a circulation valve.
  • the discharging valve is arranged on the flow pipe, and the first end of the discharging valve is in communication with the lower head.
  • the feeding valve is arranged in the flow pipe, and the first end of the feeding valve is communicated with the feeding hopper, and the second end of the feeding valve is respectively communicated with the second end of the discharging valve and the feeding end of the circulating pump.
  • the circulation valve is arranged in the flow pipe, and the first end of the circulation valve is in communication with the discharge end of the circulation pump, and the second end of the circulation valve is in communication with the upper head.
  • reaction materials need to be put into the kettle body, first, close the discharge valve, open the feeding valve and the circulation valve, and control the circulation pump to work normally, then put the reaction materials into the feeding hopper, and the reaction materials can be removed from the feeding hopper through the circulation pump.
  • the feeding is completed, first, close the feeding valve and open the discharge valve.
  • the circulating pump can transport the reaction raw materials from the bottom of the kettle body to the top of the kettle body. In the process of circulating transportation, it can play the role of mixing raw materials. .
  • the process steps of circulation and feeding are realized through a circulating pump and multiple control valves.
  • reaction kettle still has the following defects: 1.
  • the method of feeding at the top of the kettle requires a circulating pump to pump materials from the bottom to feeding at the top of the kettle. 2. If the raw material is a solid-liquid mixture or a viscous liquid, wall hanging on the draft tube will occur during the feeding process, and the overflow tube may be blocked.
  • the technical problem to be solved by this application is to overcome the above-mentioned defects in the prior art, thereby providing a reaction device.
  • a reaction device characterized in that it comprises: a reaction kettle;
  • Circulation loop including a circulation pipeline and a circulation pump arranged on the circulation pipeline, the discharge end of the circulation pump is connected to the top of the reactor through a circulation valve, and the feeding end of the circulation pump is connected to the top of the reactor via a blocking valve The bottom of the reactor is connected;
  • Feeding circuit including a feeding pipeline and a bypass pipeline, the feeding pipeline is arranged between the blocking valve and the circulating pump, and is connected to the circulating pipeline; the bypass pipeline is provided with a control valve, and one end of the bypass pipeline is connected to the circulating pump The discharge end is connected, and the other end is connected to the bottom of the reactor;
  • Discharging circuit including a discharging pipeline, which is arranged between the circulation pump and the circulation valve, and is in communication with the circulation pipeline.
  • the discharging pipeline is provided with a discharging valve.
  • the position of the discharge pipeline is higher than the position of the bypass pipeline.
  • the bottom of the reaction kettle is provided with a two-way flow valve.
  • the feeding pipeline is connected with the raw material container.
  • the discharge pipeline is connected to the storage tank.
  • the upper part of the reaction kettle is provided with a vacuum pump.
  • a stirring paddle is arranged inside the reaction kettle.
  • the top of the reactor is provided with a driving device for driving the stirring blade.
  • the reaction device provided by this application realizes the bottom feeding of the kettle by setting the bypass pipeline, the feeding pipeline and the corresponding control valve and feeding valve, which not only overcomes the process of the circulation pump pumping the material from the bottom to the top feeding of the kettle
  • the generated head does work to reduce energy consumption; and it avoids the phenomenon that when the raw material is a solid-liquid mixture or a viscous liquid, it is easy to hang on the draft tube and the overflow tube is easily blocked.
  • the bypass pipeline, the feeding pipeline, the discharging pipeline and the corresponding valves by setting the bypass pipeline, the feeding pipeline, the discharging pipeline and the corresponding valves, the process steps of feeding, circulating and feeding can be carried out through the same circulating pump only by switching the valve switch.
  • the operation is simple and greatly improved. Improved production efficiency, promoted production standardization operation requirements, and made production more standardized and efficient.
  • FIG. 1 is a schematic structural diagram of a reaction device provided in the first embodiment of this application;
  • FIG. 2 is a schematic structural diagram of an improved reaction device provided in the first embodiment of this application.
  • connection should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral Ground connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium, and it can be a connection between two components.
  • connection should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral Ground connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium, and it can be a connection between two components.
  • an embodiment of a reaction device includes: a reaction vessel 1;
  • Circulation loop includes a circulation pipeline 2 and a circulation pump 4 arranged on the circulation pipeline 2.
  • the discharge end of the circulation pump 4 communicates with the top of the reactor 1 through a circulation valve 3, and the circulation pump 4
  • the feed end is communicated with the bottom of the reactor 1 through a blocking valve 9;
  • Feeding circuit includes a feeding pipeline 7 and a bypass pipeline 5.
  • the feeding pipeline 7 is arranged between the blocking valve 9 and the circulating pump 4, and is connected to the circulating pipeline 2;
  • the bypass pipeline 5 is provided with a control valve 6 and One end of the pipeline 5 is connected with the discharge end of the circulating pump 4, and the other end is connected with the bottom of the reactor 1;
  • Discharging circuit includes a discharging pipeline 10, which is arranged between the circulation pump 4 and the circulation valve 3, and is connected to the circulation pipeline 2, and the discharging pipeline 10 is provided with a discharging valve 11.
  • the position of the discharge pipeline 10 is higher than the position of the bypass pipeline 5.
  • the feeding line 7 is connected to the raw material container 13.
  • the discharge pipeline 10 is connected to a storage tank 14.
  • the upper part of the reaction kettle 1 is provided with a vacuum pump 15.
  • a stirring paddle 17 is provided inside the reactor 1.
  • the top of the reactor 1 is provided with a driving device 16 for driving the stirring blade 17.
  • a two-way flow valve 12 is provided on the circulation line 2 between the bottom of the reactor 1 and the bypass line 5.
  • the materials can flow from the bottom of the kettle into the kettle; when circulating and discharging, the materials can flow out of the kettle from the kettle, so that the flow direction of the materials is not restricted.
  • the feeding pipeline 7 is connected to a raw material container 13, and the raw material container 13 can be any one of a storage tank, a ton barrel, or an iron barrel, which is fixed or unfixed.
  • the raw material container 13 can be any one of a storage tank, a ton barrel, or an iron barrel, which is fixed or unfixed.
  • the discharge pipeline 10 is connected to a storage tank 14, and the storage tank 14 may be any fixed or unfixed container among a reaction kettle, a ton barrel, or an iron barrel.
  • the product can be quickly poured into the next reaction kettle or the container that can contain the product through the circulating pump to improve production efficiency.
  • the upper part of the reactor 1 is provided with a vacuum pump 15; when the reaction requires gas replacement, the vacuum pump 15 can be started to replace the gas in the reactor 1.
  • the reaction kettle 1 is provided with a stirring paddle 17 inside; the top of the reaction kettle 1 is provided with a driving device 16 for driving the stirring paddle 17; after the feeding is completed, the driving device 16 is started, and the stirring paddle 17 starts to affect the reaction kettle 1
  • the internal materials are stirred to make the materials fully mixed.

Abstract

一种反应装置，包括：反应釜（1），循环回路：包括循环管线（2）和设置于循环管线（2）上的循环泵（4），循环泵（4）的出料端通过循环阀（3）与反应釜（1）的顶部连通，循环泵（4）的进料端通过隔断阀（9）与反应釜（1）的底部连通；投料回路：包括投料管线（7）和旁通管线（5），投料管线（7）设置于隔断阀（9）和循环泵（4）之间，与循环管线（2）连通；旁通管线（5）上设置有控制阀（6），旁通管线（5）的一端与循环泵（3）的出料端连通，另一端与反应釜（1）的底部连通；出料回路：包括出料管线（10），设置于循环泵（4）与循环阀（3）之间，与循环管线（2）连通，出料管线（10）上设置有出料阀（11）。

Description

一种反应装置 技术领域
本申请涉及化工生产设备技术领域，具体涉及一种反应装置。
背景技术
目前，在化工产品的合成制备过程中，反应装置的使用非常常见。
中国专利CN204768663U公开了一种反应釜，包括釜体，管路组件，循环泵，投料斗和阀门组件。其中釜体两端分别设有上封头和下封头；循环泵的进料端及出料端均与送流管连通；投料斗与送流管连通，投料斗用于投入反应原料，之后再通过送流管、分流管、导流管及溢流管，可以将反应原料从投料斗运送至釜体内。投料斗可以安装在厂房的地面上，也可以安装在外部的支架上，还可以根据实际情况进行调整和安装。
阀门组件包括出料阀、投料阀及循环阀，出料阀设置于送流管，且出料阀的第一端与下封头连通。投料阀设置于送流管，且投料阀的第一端与投料斗连通，投料阀的第二端分别与出料阀的第二端及循环泵的进料端连通。循环阀设置于送流管，且循环阀的第一端与循环泵的出料端连通，循环阀的第二端与上封头连通。
当需要向釜体投入反应原料时，首先，关闭出料阀，打开投料阀和循环阀，并控循环泵正常工作，然后，向投料斗投入反应原料，通过循环泵可以将反应原料从投料斗中送入釜体内。当投料完毕时，首先，关闭投料阀，并打开出料阀，通过循环泵可以将反应原料从釜体的底部运送至釜体的顶部，在循环运送的过程中，可以起到混合原料的作用。从而通过一个循环泵和多个控制阀实现循环与投料的工艺步骤。
但是，上述反应釜依然存在如下缺陷：1、采用釜顶投料的方式需要循环泵从底部抽料到釜顶投料这个过程中产生的扬程做功能耗大。2、如果原料是 固液混合物或者粘稠液体时，在投料过程中会在导流管上产生挂壁，以及在溢流管可能出现堵塞。
申请内容
因此，本申请要解决的技术问题在于克服现有技术中的上述缺陷，从而提供一种反应装置。
为实现上述目的，本申请采用如下技术方案：
一种反应装置，其特征在于，包括：反应釜；
循环回路：包括循环管线和设置于所述循环管线上的循环泵，所述循环泵的出料端通过循环阀与所述反应釜的顶部连通，所述循环泵的进料端通过隔断阀与反应釜的底部连通；
投料回路：包括投料管线和旁通管线，所述投料管线设置于隔断阀和循环泵之间，与循环管线连通；所述旁通管线上设置有控制阀，旁通管线的一端与循环泵的出料端连通，另一端与反应釜的底部连通；
出料回路：包括出料管线，设置于循环泵与循环阀之间，与循环管线连通，所述出料管线上设置有出料阀。
其中，所述出料管线的位置高于旁通管线的位置。
所述反应釜的底部设有双向流动阀。
所述投料管线与原料容器相连。
所述出料管线与储罐相连。
所述反应釜的上部设有真空泵。
所述反应釜内部设置有搅拌桨。
所述反应釜的顶部设置有用于驱动所述搅拌桨的驱动装置。
关闭隔断阀、出料阀、和循环阀，打开投料阀和双向流动阀，然后调节控制阀和循环泵，实现投料。
关闭出料阀、投料阀、和控制阀，打开双向流动阀、循环阀、隔断阀和循环泵，实现循环。
关闭循环阀、投料阀、和控制阀，打开双向流动阀、出料阀、隔断阀和循环泵，实现出料。
本申请技术方案，具有如下优点：
1.本申请提供的一种反应装置，通过设置旁通管线，投料管线和相应的控制阀、投料阀的设置实现釜底投料，不仅克服了循环泵从底部抽料到釜顶投料这个过程中产生的扬程做功，降低能耗；而且避免了原料为固液混合物或者粘稠液体时，容易在导流管上挂壁以及在溢流管易堵塞的现象。本申请通过设置旁通管线、投料管线和出料管线以及相应的阀门，实现通过同一个循环泵只需要切换阀门的开关就可以进行投料、循环和打料的工艺步骤，操作简便，大幅度提高了生产效率，促进了生产标准化的作业要求，使生产更加规范高效。
附图说明
为了更清楚地说明本申请具体实施方式或现有技术中的技术方案，下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍，显而易见地，下面描述中的附图是本发明的一些实施方式，对于本领域普通技术人员来讲，在不付出创造性劳动的前提下，还可以根据这些附图获得其他的附图。
图1为本申请第一种实施方式中提供的一种反应装置的结构示意图；
图2为本申请第一种实施方式中提供的一种改进的反应装置的结构示意图；
附图标记说明：
1-反应釜；2-循环管线；3-循环阀；4-循环泵；5-旁通管线；6-控制阀；7-投料管线；8-投料阀；9-隔断阀；10-出料管线；11-出料阀；12-双向流动阀；13-原料容器；14-储罐；15-真空泵；16-驱动装置；17-搅拌桨。
具体实施方式
下面将结合附图对本申请的技术方案进行清楚、完整地描述，显然，所描述的实施例是本申请一部分实施例，而不是全部的实施例。基于本申请中的实施例，本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例，都属于本申请保护的范围。
在本申请的描述中，需要说明的是，除非另有明确的规定和限定，术语“相连”、“连接”应做广义理解，例如，可以是固定连接，也可以是可拆卸连接，或一体地连接；可以是机械连接，也可以是电连接；可以是直接相连，也可以通过中间媒介间接相连，可以是两个元件内部的连通。对于本领域的普通技术人员而言，可以具体情况理解上述术语在本申请中的具体含义。
此外，下面所描述的本申请不同实施方式中所涉及的技术特征只要彼此之间未构成冲突就可以相互结合。
实施例1
如图1所示一种反应装置的实施方式，包括：反应釜1；
循环回路：包括循环管线2和设置于所述循环管线2上的循环泵4，所述循环泵4的出料端通过循环阀3与所述反应釜1的顶部连通，所述循环泵4的进料端通过隔断阀9与反应釜1的底部连通；
投料回路：包括投料管线7和旁通管线5，所述投料管线7设置于隔断阀9和循环泵4之间，与循环管线2连通；所述旁通管线5上设置有控制阀6，旁 通管线5的一端循环泵4的出料端连通，另一端与反应釜1的底部连通；
出料回路：包括出料管线10，设置于循环泵4与循环阀3之间，与循环管线2连通，所述出料管线10上设置有出料阀11。
其中，所述出料管线10的位置高于旁通管线5的位置。
所述投料管线7与原料容器13相连。
所述出料管线10与储罐14相连。
所述反应釜1的上部设有真空泵15。
所述反应釜1内部设置有搅拌桨17。所述反应釜1的顶部设置有用于驱动所述搅拌桨17的驱动装置16。
上述反应釜1,通过设置旁通管线5，投料管线7和相应的控制阀6、投料阀8实现釜底投料，与现有技术相比，克服了循环泵4从底部抽料到釜顶投料这个过程中产生的扬程做功，降低能耗。通过采用上述反应釜1，关闭隔断阀9、出料阀11、和循环阀3，打开投料阀8，然后调节控制阀6和循环泵4，实现投料；关闭出料阀11、投料阀8、和控制阀6，打开循环阀3、隔断阀9和循环泵4，实现循环；关闭循环阀3、投料阀8、和控制阀6，打开出料阀11、隔断阀9和循环泵4，实现出料；即通过同一个循环泵4只需切换阀门的开关就可以实现投料、循环和出料的工艺步骤，操作简便。
作为一种改进实施方式，参见图2，在所述反应釜1底部与旁通管线5之间的循环管线2上设有双向流动阀12。投料时，物料可从釜底流入釜内；循环和出料时，物料又可从釜内流出釜外，使得物料的流动方向不受限制。
投料管线7与原料容器13相连，原料容器13可以为储罐、吨桶、或铁桶中任意一种固定或者不固定的容器。在投料时，可以节约人力成本，提高生产 效率。
出料管线10与储罐14相连，所述储罐14可以为反应釜、吨桶、或铁桶中任意一种固定或者不固定的容器。可快速将产品通过循环泵倒入下一反应釜内或者可盛装产品的容器内，提高生产效率。
所述反应釜1的上部设有真空泵15；当反应需要置换气体时，可启动真空泵15对反应釜1内气体进行置换。
所述反应釜1内部设置有搅拌桨17；所述反应釜1的顶部设置有用于驱动所述搅拌桨17的驱动装置16；投料完毕后，启动驱动装置16，搅拌桨17开始对反应釜1内物料进行搅拌，使物料充分混合。
显然，上述实施例仅仅是为清楚地说明所作的举例，而并非对实施方式的限定。对于所属领域的普通技术人员来说，在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。而由此所引申出的显而易见的变化或变动仍处于本发明创造的保护范围之中。

Claims (8)

  1. 一种反应装置，其特征在于，包括：反应釜；
    循环回路：包括循环管线和设置于所述循环管线上的循环泵，所述循环泵的出料端通过循环阀与所述反应釜的顶部连通，所述循环泵的进料端通过隔断阀与反应釜的底部连通；
    投料回路：包括投料管线和旁通管线，所述投料管线设置于隔断阀和循环泵之间，与循环管线连通；所述旁通管线上设置有控制阀，旁通管线的一端与循环泵的出料端连通，另一端与反应釜的底部连通；
    出料回路：包括出料管线，设置于循环泵与循环阀之间，与循环管线连通，所述出料管线上设置有出料阀。
  2. 根据权利要求1所述的反应装置，其特征在于，所述出料管线的位置高于旁通管线的位置。
  3. 根据权利要求1所述的反应装置，其特征在于，在所述反应釜的底部设有双向流动阀。
  4. 根据权利要求1所述的反应装置，其特征在于，所述投料管线与原料容器相连。
  5. 根据权利要求1所述的反应装置，其特征在于，所述出料管线与储罐相连。
  6. 根据权利要求1-5中任一项所述的反应装置，其特征在于，所述反应釜的上部设有真空泵。
  7. 根据权利要求1-5中任一项所述的反应装置，其特征在于，所述反应釜内部设置有搅拌桨。
  8. 根据权利要求7所述的反应装置，其特征在于，所述反应釜的顶部设置有用于驱动所述搅拌桨的驱动装置。
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112755951A (zh) * 2021-01-29 2021-05-07 福建未来药业有限公司 一种酶催化医药中间体制备用反应釜
CN115090247A (zh) * 2022-07-28 2022-09-23 重庆鑫盛通化工有限公司 2,5-二甲基-3-己炔-2,5-二醇溶液的中和装置

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101422717A (zh) * 2008-11-21 2009-05-06 中国蓝星（集团）股份有限公司 一种气液混合进料分布器以及采用该分布器的聚苯醚反应装置
US8152356B2 (en) * 2009-07-12 2012-04-10 Tzer-Huang Guo Spray blended emulsifier
CN103406045A (zh) * 2013-08-02 2013-11-27 杭州新亚石油化工有限公司 一种润滑脂的制备装置和制备工艺
CN204768663U (zh) 2015-05-29 2015-11-18 惠州市建科实业有限公司 反应釜
CN207722785U (zh) * 2017-11-28 2018-08-14 山东汇通利华生物科技有限公司 一种乙基麦芽酚反应釜循环搅拌装置

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011097566A1 (en) 2010-02-08 2011-08-11 Renewable Process Technologies Llc System and method for producing biomaterials
CN205886847U (zh) 2016-08-11 2017-01-18 浙江盛汇化工有限公司 一种搪玻璃反应釜防止热应力损坏装置
CN107937012B (zh) * 2017-11-10 2020-02-14 清华大学 废弃轮胎的临界水解处理装置及方法
CN108704586B (zh) 2018-05-16 2020-03-17 浙江工业大学 一种液固反应器

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101422717A (zh) * 2008-11-21 2009-05-06 中国蓝星（集团）股份有限公司 一种气液混合进料分布器以及采用该分布器的聚苯醚反应装置
US8152356B2 (en) * 2009-07-12 2012-04-10 Tzer-Huang Guo Spray blended emulsifier
CN103406045A (zh) * 2013-08-02 2013-11-27 杭州新亚石油化工有限公司 一种润滑脂的制备装置和制备工艺
CN204768663U (zh) 2015-05-29 2015-11-18 惠州市建科实业有限公司 反应釜
CN207722785U (zh) * 2017-11-28 2018-08-14 山东汇通利华生物科技有限公司 一种乙基麦芽酚反应釜循环搅拌装置

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112755951A (zh) * 2021-01-29 2021-05-07 福建未来药业有限公司 一种酶催化医药中间体制备用反应釜
CN115090247A (zh) * 2022-07-28 2022-09-23 重庆鑫盛通化工有限公司 2,5-二甲基-3-己炔-2,5-二醇溶液的中和装置
CN115090247B (zh) * 2022-07-28 2023-07-14 重庆鑫盛通化工有限公司 2,5-二甲基-3-己炔-2,5-二醇溶液的中和装置

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