Convenient-to-discharge hydrolysis kettle for OB acid production and processing
By setting staggered side discharge ports and rotating sleeves on the side wall of the hydrolysis reactor for OB acid production, combined with a rotating drive mechanism, the problems of slow and inaccurate material discharge caused by material stratification in OB acid production are solved, achieving fast and accurate material discharge and improving production efficiency.
Patent Information
- Application Number
- CN202520190183.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-02-07
- Publication Date
- 2026-02-03
- Estimated Expiration
- 2035-02-07
AI Technical Summary
In the current OB acid production and processing process, the reaction materials are separated into layers, resulting in slow and inaccurate discharge speed, which affects production efficiency.
Multiple side discharge ports staggered from top to bottom are set on the side wall of the vertical reactor body, and equipped with a rotating sleeve and a side discharge pipe. The opening and closing of the side discharge ports are controlled by a rotating drive mechanism, and the material is discharged accurately and quickly in combination with the bottom discharge valve.
It enables rapid and precise discharge of materials from any layer during the OB acid production process, thereby improving production efficiency.
Smart Images

Figure CN223861803U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model relates to the technical field of OB acid production technology, specifically to a hydrolysis kettle for OB acid production and processing convenient for discharging. BACKGROUND
[0002] OB acid is mainly used for preparing fluorescent whitening agent, especially fluorescent whitening agent EBF. This whitening agent can be used for the whitening of synthetic fibers such as nylon, polyester, polypropylene, chlorofiber and triacetate fiber. In addition, OB acid is also used for the whitening of plastic film, compression molding material and injection molding material. The preparation method of OB acid comprises the following steps: adding adipic acid and thionyl chloride according to a weight ratio of 1:5-12 into a reaction kettle, adding a catalyst and heating to 75-95 DEG C for reaction to generate acyl chloride. Hydrolyze the acyl chloride to be completely solid, adjust the pH value to 9-12, heat to 81-85 DEG C for 2-2.5 hours, and then carry out decolorization treatment. Add hydrochloric acid to the filtrate, stir and centrifuge to obtain a crude product. Heat the crude product to reflux, filter to obtain a refined product. Dry, crush and package the refined product to obtain the product. In the processing process, for the reaction kettle, after the hydrolysis reaction, the reacted material is generally discharged from the bottom, and the reactants and raw materials participating in the reaction are generally also layered. Therefore, during the discharging process, the material in each layer needs to be discharged one by one. This way, the discharging speed is slow, and the material in the upper layer cannot be discharged. Therefore, the utility model provides a hydrolysis kettle for OB acid production and processing convenient for discharging, which can conveniently discharge any layer, has high discharging accuracy and fast speed, and further improves the efficiency of OB acid production. SUMMARY
[0003] (I) Technical problem solved
[0004] In view of the defects in the prior art, the utility model provides a hydrolysis kettle for OB acid production and processing convenient for discharging, which can conveniently discharge any layer, has high discharging accuracy and fast speed, and further improves the efficiency of OB acid production.
[0005] (II) Technical scheme
[0006] To achieve the above-mentioned purpose, the utility model provides the following technical scheme: a hydrolysis kettle for OB acid production and processing convenient for discharging, comprising a vertical reaction kettle body, a bottom discharging valve is installed at the bottom of the vertical reaction kettle body, a plurality of side discharging ports are formed in the side wall of the vertical reaction kettle body, the side discharging ports are sequentially and staggeredly arranged from top to bottom, a rotating sleeve is arranged on the vertical reaction kettle body and circumferentially sealed outside the side discharging ports, a plurality of side discharging pipes are fixedly connected to the rotating sleeve and in one-to-one correspondence with the side discharging ports, and a side discharging valve is fixedly installed on each side discharging pipe.
[0007] Preferably, a rotating driving mechanism for adjusting the rotation of the rotating sleeve is further included, the rotating driving mechanism comprises a gear ring fixedly installed at the bottom of the rotating sleeve through a rotating frame, a supporting ring frame is fixedly installed at the bottom of the vertical reaction kettle body, a gear meshing with the gear ring is rotatably connected to the supporting ring frame, a driving motor is fixedly installed on the supporting ring frame, and the output shaft gear of the driving motor is fixedly connected to the output end.
[0008] Preferably, the gear is provided in three groups, and the output shaft of the driving motor is fixedly connected to any one of the gears.
[0009] Preferably, the vertical reaction kettle body comprises a kettle body, a kettle cover and a kettle bottom are fixedly installed at the top and the bottom of the kettle body respectively, the bottom discharge valve is fixedly communicated at the bottom of the kettle bottom, the supporting ring frame is fixedly connected to the bottom of the kettle bottom, and the plurality of side discharge ports are formed in the kettle body and the rotating sleeve is sealingly and rotatably slidably connected to the kettle body.
[0010] Preferably, the rotating frame is rotatably and slidably connected to the supporting ring frame.
[0011] Preferably, the plurality of side discharge ports are sequentially and staggeredly arranged in a circumferential direction.
[0012] (Three) beneficial effects
[0013] Compared with the prior art, the hydrolysis kettle for OB acid production and processing has the following beneficial effects:
[0014] The hydrolysis kettle for OB acid production and processing has the following beneficial effects: the plurality of side discharge ports are sequentially and staggeredly arranged on the side wall of the vertical reaction kettle body, so that the material in any layer can be conveniently discharged after the hydrolysis reaction; the rotating sleeve is arranged, so that the material leakage through the side discharge ports can be avoided during the reaction; after the reaction is completed, the plurality of side discharge pipes are communicated with the plurality of side discharge ports when the rotating sleeve is rotated; the side discharge pipe and the side discharge valve are arranged, so that the material in any layer can be conveniently and accurately discharged; the bottom discharge valve can be used to discharge the material in the bottom layer; the hydrolysis kettle for OB acid production and processing can conveniently discharge the material in any layer, has high and fast discharging accuracy, and further improves the production efficiency of OB acid. BRIEF DESCRIPTION OF DRAWINGS
[0015] Figure 1 It is a structure schematic view of the whole decomposition of the utility model;
[0016] Figure 2 It is a structure schematic view of the whole of the utility model;
[0017] Figure 3 It is a structure schematic view of the whole decomposition of the utility model from other angles;
[0018] Figure 4 The whole other view structural schematic view of the utility model.
[0019] The marks in the drawing: 1, kettle body; 2, kettle cover; 3, kettle bottom; 4, rotating sleeve; 5, bottom discharge valve; 6, side discharge pipe; 7, side discharge valve; 8, side discharge port; 9, limiting ring; 10, support ring frame; 11, gear; 12, driving motor; 13, rotating frame; 14, gear ring. DETAILED DESCRIPTION
[0020] The technical solutions in the embodiments of the utility model will be clearly and completely described below with reference to the drawings in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by those skilled in the art without creative labor fall within the protection scope of the utility model.
[0021] Embodiment:
[0022] Please refer to Figures 1-4 An OB acid production and processing hydrolysis kettle convenient for discharging, which comprises a vertical reaction kettle body, a bottom discharge valve 5 is installed at the bottom of the vertical reaction kettle body, a plurality of side discharge ports 8 are arranged on the side wall of the vertical reaction kettle body, the plurality of side discharge ports 8 are sequentially staggered from top to bottom, a rotating sleeve 4 is arranged on the vertical reaction kettle body in a sealing circumferential manner outside the plurality of side discharge ports 8, a plurality of side discharge pipes 6 are fixedly connected to the rotating sleeve 4 outside, a side discharge valve 7 is fixedly installed on each of the plurality of side discharge pipes 6.
[0023] Specifically, the rotating sleeve 4 further comprises a rotating driving mechanism for adjusting the rotation of the rotating sleeve 4, the rotating driving mechanism comprises a gear ring 14 fixedly installed at the bottom of the rotating sleeve 4 through a rotating frame 13, a support ring frame 10 is fixedly installed at the bottom of the vertical reaction kettle body, a gear 11 engaged with the gear ring 14 is rotatably connected to the support ring frame 10, a driving motor 12 is fixedly installed on the support ring frame 10, the output shaft gear 11 of the driving motor 12 is fixedly connected to the output end, the driving motor 12 is started, the output shaft of the driving motor 12 rotates clockwise or counterclockwise, so that the gear 11 can be driven to rotate clockwise or counterclockwise, through the engagement between the gear 11 and the gear ring 14, the rotating frame 13 can be driven to rotate counterclockwise or clockwise by a certain angle, so that the plurality of side discharge pipes 6 can be synchronously rotated counterclockwise or clockwise by a certain angle.
[0024] Specifically, the gear 11 is arranged in three groups, and the output shaft of the driving motor 12 is fixedly connected with any one of the gears 11, and the other two groups of gears 11 can be used as the support tooth ring 14 to support the stability of the overall rotation of the rotating frame 13 and the rotating sleeve 4.
[0025] Specifically, the vertical reaction kettle body includes a kettle body 1, a kettle cover 2 and a kettle bottom 3 are fixedly installed at the top and bottom of the kettle body 1 respectively, a bottom discharge valve 5 is fixedly communicated at the bottom of the kettle bottom 3, and a support ring frame 10 is fixedly connected with the bottom of the kettle bottom 3, and a plurality of side discharge ports 8 are all arranged on the kettle body 1 and the rotating sleeve 4 is sealingly and slidingly matched with the kettle body 1, further, the top of the kettle cover 2 is fixedly communicated with a feeding pipe, and the feeding pipe is provided with a feeding valve, and the top of the kettle cover 2 is provided with a discharge valve, through the arrangement of the kettle body 1, the kettle cover 2 and the kettle bottom 3, the vertical reaction kettle body is more stable, further, the top and bottom of the kettle body 1 are both fixedly installed with a limiting ring 9 slidingly matched with the rotating sleeve 4, which facilitates the limiting of the rotating sleeve 4.
[0026] Specifically, the rotating frame 13 is slidingly matched with the support ring frame 10, and through the arrangement of the rotating frame 13 and the support ring frame 10, the stability of the rotating frame 13 is increased.
[0027] Specifically, the plurality of side discharge ports 8 are arranged in a circumferential staggered manner, which improves the convenience of discharging.
[0028] It should be noted that the "one embodiment", "embodiment", "exemplary embodiment", "some embodiments" and the like mentioned in the specification represent that the described embodiment can include a specific feature, structure or characteristic, but not necessarily every embodiment includes the specific feature, structure or characteristic. In addition, such phrases do not necessarily refer to the same embodiment. In addition, when a specific feature, structure or characteristic is described in connection with an embodiment, it is within the knowledge of those skilled in the art to realize such feature, structure or characteristic in connection with other embodiments described explicitly or implicitly.
[0029] It should be readily understood that "on", "above" and "over" in the present disclosure should be interpreted in the broadest way, so that "on" not only means "directly on", but also includes the meaning of "on" with intermediate features or layers therebetween, and "above" or "over" not only includes the meaning of "above" or "over", but also includes the meaning of "above" or "over" without intermediate features or layers therebetween (i.e. directly on).
[0030] Moreover, spatially relative terms, such as "beneath", "below", "lower", "above", "upper", and the like, can be used herein for ease of description to describe one element or feature's relationship to another element(s) or feature(s) as illustrated in the figures. The spatially relative terms are intended to encompass different orientations of the device in use or operation in addition to the orientations depicted in the figures. The devices can be otherwise oriented (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.
[0031] Note that, in the present document, the terms "first", "second", and the like, merely identify content distinctions, but do not necessarily require or imply any actual relationship or order between the entities or actions so identified. Also, the terms "comprises", "comprising", or any other variations thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but can include other elements not expressly listed or inherent to such process, method, article, or apparatus. An element proceeded by "comprises... a" does not, without more constraints, exclude the existence of additional identical elements in the process, method, article, or apparatus that comprises the element.
[0032] Finally, it should be noted that the above-described embodiments are merely intended for describing and illustrating, but not limiting, the technical solutions of the present application; even though the present application has been described in detail with reference to the above embodiments, those of ordinary skill in the art should understand that they can still modify the technical solutions recorded in the above embodiments, or equivalently replace some or all of the technical features thereof; and such modifications or replacements do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of the embodiments of the present application.
Claims
1. A hydrolysis reactor for OB acid production and processing that facilitates material discharge, characterized in that: The reactor includes a vertical reactor body, a bottom discharge valve (5) installed at the bottom of the reactor body, and multiple side discharge ports (8) arranged staggered from top to bottom on the side wall of the reactor body. A rotating sleeve (4) that seals and surrounds the reactor body is provided on the outside of the multiple side discharge ports (8). Multiple side discharge pipes (6) that can be connected one by one with the multiple side discharge ports (8) are fixedly connected to the outside of the rotating sleeve (4). A side discharge valve (7) is fixedly installed on each of the multiple side discharge pipes (6).
2. The hydrolysis reactor for OB acid production and processing with easy discharge as described in claim 1, characterized in that: It also includes a rotary drive mechanism for adjusting the rotation of the rotating sleeve (4), the rotary drive mechanism including a gear ring (14) fixedly installed at the bottom of the rotating sleeve (4) via a rotating frame (13), a support ring frame (10) fixedly installed at the bottom of the vertical reactor body, a gear (11) rotatably connected to the support ring frame (10) and meshing with the gear ring (14), and a drive motor (12) fixedly installed on the support ring frame (10), the output end of the output shaft gear (11) of the drive motor (12) being fixedly connected.
3. The hydrolysis reactor for OB acid production and processing with easy material discharge as described in claim 2, characterized in that: The gears (11) are configured in three groups, and the output shaft of the drive motor (12) is fixedly connected to any one of the gears (11).
4. The hydrolysis reactor for OB acid production and processing with easy material discharge as described in claim 3, characterized in that: The vertical reactor body includes a reactor body (1), with a reactor cover (2) and a reactor bottom (3) fixedly installed at the top and bottom of the reactor body (1), respectively. The bottom discharge valve (5) is fixedly connected to the bottom of the reactor bottom (3), and the support ring frame (10) is fixedly connected to the bottom of the reactor bottom (3). Multiple side discharge ports (8) are opened on the reactor body (1), and the rotating sleeve (4) is in a sealed rotating sliding fit with the reactor body (1).
5. The hydrolysis reactor for OB acid production and processing with easy material discharge as described in claim 4, characterized in that: The rotating frame (13) and the support ring frame (10) are in a rotating sliding fit.
6. The hydrolysis reactor for OB acid production and processing according to claim 5, characterized in that: The multiple side discharge ports (8) are arranged in a staggered manner in a circumferential direction.