CN-224207980-U - Novel continuous reactor device
Abstract
The utility model discloses a novel continuous reactor device which comprises a tube array reactor, wherein a first feeding pipe is communicated and connected to the top of the tube array reactor near the left side, a second feeding pipe is communicated and connected to the bottom of the tube array reactor near the left side and the right side respectively, SK mixers are respectively communicated and connected to the top of the first feeding pipe and the bottom of the two second feeding pipes, a combined SK mixer is arranged in the tube array reactor, and a heat exchange medium inlet is communicated and connected to the left side of the tube array reactor near the bottom. According to the technical scheme, through mutual matching among components such as the tubular reactor, the SK mixer, the combined SK mixer and the like, various materials can be added at different time and continuously produced, the SK mixer group is connected in parallel inside the tubular reactor, so that the solution mixing and reaction efficiency is higher, the heat exchange efficiency is higher, the local temperature rise is avoided, the reaction heat can be effectively utilized, and the heat supply is carried out on two-stage reactions.
Inventors
- WU DECAI
- LIU FANGYU
- Lv ao
- DONG JIXUAN
- LI ZHENFANG
Assignees
- 山东远联化工股份有限公司
Dates
- Publication Date
- 20260508
- Application Date
- 20250529
Claims (5)
- 1. The novel continuous reactor device is characterized by comprising a tube array reactor (1), wherein a first feeding pipe (7) is communicated and connected to the top of the tube array reactor (1) near the left side, a second feeding pipe (8) is respectively communicated and connected to the bottom of the tube array reactor (1) near the left side and the right side, and SK mixers (2) are respectively communicated and connected to the top of the first feeding pipe (7) and the bottom of the two second feeding pipes (8).
- 2. The novel continuous reactor device according to claim 1, wherein a combined SK mixer (3) is arranged in the tubular reactor (1), and a heat exchange medium inlet (4) is connected to the left side of the tubular reactor (1) near the bottom.
- 3. A novel continuous reactor device according to claim 2, characterized in that the right side of the shell-and-tube reactor (1) is connected in communication with a heat exchange medium outlet (5) near the top, and the top of the shell-and-tube reactor (1) is connected in communication with an outlet E (6) near the right side.
- 4. A novel continuous reactor device according to claim 3, characterized in that the combined SK mixer (3) is arranged inside the tubular reactor (1) near the top and the heat exchange medium outlet (5) is located near the bottom on the right side of the combined SK mixer (3).
- 5. The novel continuous reactor device according to claim 1, characterized in that the SK mixer (2) located above is located above the tubular reactor (1) near the left side, and the SK mixer (2) located below is located below the tubular reactor (1) near the right side.
Description
Novel continuous reactor device Technical Field The utility model relates to the technical field of reactors, in particular to a novel continuous reactor device. Background A reactor apparatus is an engineering device for carrying out chemical, physical or biological reactions whose core function is to provide the reaction with appropriate conditions (e.g. temperature, pressure, mixing regime, etc.) to promote substance conversion or energy exchange. However, the reactor device in the prior art cannot realize the addition and continuous production of various materials at different times when in use, so that the solution mixing and reaction efficiency is reduced, the heat exchange efficiency is lower, and the local temperature rise cannot be avoided, so that the reactor device cannot effectively utilize the reaction heat and perform heat supply on two-stage reactions, and therefore, a novel continuous reactor device is provided. Disclosure of utility model The utility model aims to at least solve one of the technical problems in the prior art, and provides a novel continuous reactor device which is applicable to continuous reaction, can realize addition and continuous production of various materials at different time, and is internally connected with an SK mixer group in parallel in a tubular reactor, so that the solution mixing and reaction efficiency is higher, the heat exchange efficiency is higher, the local temperature rise is avoided, the reaction heat can be effectively utilized, and the heat supply is carried out on two-stage reactions. In order to achieve the purpose, the novel continuous reactor device comprises a tube array reactor, wherein a first feeding pipe is connected to the top of the tube array reactor near the left side in a communicated manner, a second feeding pipe is connected to the bottom of the tube array reactor near the left side and the right side in a communicated manner respectively, and SK mixers are connected to the top of the first feeding pipe and the bottom of the two second feeding pipes in a communicated manner respectively. According to the novel continuous reactor device, a combined SK mixer is arranged in the tubular reactor, and a heat exchange medium inlet is communicated and connected to the left side of the tubular reactor close to the bottom. According to the novel continuous reactor device, the right side of the tubular reactor is communicated and connected with a heat exchange medium outlet near the top, and the top of the tubular reactor is communicated and connected with an outlet E near the right side. According to the novel continuous reactor device, the combined SK mixer is arranged in the tubular reactor near the top, and the heat exchange medium outlet is positioned at the right side of the combined SK mixer near the bottom. According to the novel continuous reactor device, the SK mixer positioned above is positioned above the tubular reactor and near the left side, and the SK mixer positioned below is positioned below the tubular reactor and near the right side. The technical scheme has at least one beneficial effect that through the mutual coordination among the components such as the tube array reactor, the SK mixer, the combined SK mixer and the like, the tube array reactor can realize the addition and continuous production of various materials at different time, the SK mixer group is connected in parallel inside the tube array reactor, so that the solution mixing and reaction efficiency is higher, the heat exchange efficiency is higher, the local heating is avoided, the reaction heat can be effectively utilized, and the heat supply is carried out on two-stage reactions. Additional aspects and advantages of the utility model will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the utility model. Drawings The utility model is further described below with reference to the drawings and examples; FIG. 1 is a schematic diagram of a front view of the present utility model; FIG. 2 is a schematic partial structural view of the components of the combination SK mixer and SK mixer of FIG. 1; Fig. 3 is an enlarged view of F in fig. 1. Legend description: 1. The system comprises a shell-and-tube reactor, a 2-SK mixer, a 3-combined SK mixer, a 4-heat exchange medium inlet, a 5-heat exchange medium outlet, and a 6-outlet E. Detailed Description Reference will now be made in detail to the present embodiments of the present utility model, examples of which are illustrated in the accompanying drawings, wherein the accompanying drawings are used to supplement the description of the written description so that one can intuitively and intuitively understand each technical feature and overall technical scheme of the present utility model, but not to limit the scope of the present utility model. Referring to fig. 1 to 3, the novel continuous reactor device according to the embodiment