Water reducing agent sulfonation device

By setting up a preheating tank and a sulfonation tank in the water reducing agent sulfonation device, and using the exhaust pipe to use high-temperature exhaust gas to preheat raw materials, the problem of resource waste in the prior art is solved and the energy-saving effect is achieved.

CN222624516UActive Publication Date: 2025-03-18武汉伯宇建材有限公司
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Patent Information

Application Number
CN202421365793.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-06-14
Publication Date
2025-03-18
Estimated Expiration
2034-06-14

AI Technical Summary

Technical Problem

In the prior art, the high-temperature exhaust gas generated during the sulfonation reaction cannot be fully utilized, resulting in waste of resources.

Method used

A water reducing agent sulfonation device is designed. By setting up a preheating tank and a sulfonation tank, and setting a preheating jacket on the outer wall of the preheating tank, an exhaust pipe is set above one side of the sulfonation tank, and the high-temperature exhaust gas in the sulfonation tank is introduced into the preheating tube in the preheating jacket, and the raw materials in the preheating tank are preheated using the preheating tube.

Benefits of technology

The high-temperature exhaust gas generated during the sulfonation reaction is fully utilized, the operating power of the heater is reduced, and the energy-saving effect is achieved.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a water reducing agent sulfonation device, which relates to the technical field of water reducing agent preparation devices and comprises a preheating tank and a sulfonation tank, the bottom of the preheating tank is communicated with the inside of the sulfonation tank through a transfer pipe, a preheating jacket is arranged on the outer wall of the preheating tank, a preheating pipe is arranged in the preheating jacket, and a conduction oil jacket is mounted on the outer wall of the sulfonation tank. A heating jacket is arranged on the outer wall of the heat-conducting oil jacket, an exhaust pipe is arranged above one side of the sulfonation tank, and the upper end of the exhaust pipe is connected with the inlet end of a preheating pipe; according to the sulfonation device, the preheating tank and the sulfonation tank are arranged, the preheating jacket is arranged on the outer wall of the preheating tank, high-temperature waste gas in the sulfonation tank is introduced into the preheating pipe in the preheating jacket through the exhaust pipe, and raw materials to be sulfonated in the preheating tank are preheated by utilizing the preheating pipe; and the preheated raw materials enter the sulfonation tank for sulfonation reaction, so that the high-temperature waste gas generated in the sulfonation reaction process is fully utilized.
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Description

Technical Field

[0001] The utility model relates to the technical field of water reducing agent preparation devices, in particular to a water reducing agent sulfonation device. Background Art

[0002] Water reducer is a concrete admixture that can reduce the amount of mixing water while maintaining the slump of concrete. Most of them are anionic surfactants, such as lignin sulfonate, naphthalene sulfonate formaldehyde polymer, etc. After being added to the concrete mixture, it has a dispersing effect on cement particles, which can improve its workability, reduce unit water consumption, improve the fluidity of the concrete mixture or reduce unit cement consumption, thus saving cement.

[0003] Naphthalene water reducer is the mainstream water reducer product on the market. The production of naphthalene water reducer needs to go through the process steps of melting naphthalene, sulfonation, hydrolysis, condensation, neutralization, filtration and drying to obtain the product. During sulfonation, the materials are mixed together and stirred to make them fully mixed and reacted. The sulfonation process needs to be carried out under high temperature conditions. High-temperature waste gas will be generated during the sulfonation reaction. In the prior art, the waste gas is discharged from the outside of the sulfonation device and purified by purification equipment before being discharged. The heat contained in the waste gas is not fully utilized in the reaction process of the sulfonation device, resulting in a waste of resources. Therefore, the utility model proposes a water reducer sulfonation device to solve the shortcomings of the prior art. Utility Model Content

[0004] In view of the above problems, the purpose of the utility model is to provide a water reducer sulfonation device, by arranging a preheating tank and a sulfonation tank, and arranging a preheating jacket on the outer wall of the preheating tank, and arranging an exhaust pipe above one side of the sulfonation tank, by introducing the high-temperature exhaust gas in the sulfonation tank into the preheating pipe in the preheating jacket through the exhaust pipe, and using the preheating pipe to preheat the raw materials waiting for sulfonation in the preheating tank, and the preheated raw materials then enter the sulfonation tank for sulfonation reaction, so as to realize the full utilization of the high-temperature exhaust gas generated in the sulfonation reaction process in this cycle.

[0005] In order to achieve the above purpose, the utility model provides the following technical solutions:

[0006] A water reducing agent sulfonation device comprises a preheating tank and a sulfonation tank, wherein the top of the sulfonation tank is provided with a preheating tank through a bracket, the bottom of the preheating tank is connected to the inside of the sulfonation tank through a transfer pipe, a preheating jacket is provided on the outer wall of the preheating tank, a preheating pipe is provided inside the preheating jacket, a heat-conducting oil jacket is installed on the outer wall of the sulfonation tank, a heating jacket is provided on the outer wall of the heat-conducting oil jacket, a heater for heating the heat-conducting oil in the heat-conducting oil jacket is provided inside the heating jacket, an exhaust pipe is provided above one side of the sulfonation tank, the upper end of the exhaust pipe is connected to the inlet end of the preheating pipe, an exhaust pump is provided on one side of the sulfonation tank, the outlet end of the preheating pipe is connected to the input port of the exhaust pump through a connecting pipe, and the output port of the exhaust pump is connected to an external purification device;

[0007] A first stirring mechanism is provided in the preheating tank, and a second stirring mechanism is provided in the sulfonation tank. The first stirring mechanism is driven by a first stirring motor, and the second stirring mechanism is driven by a second stirring motor.

[0008] A further improvement is that a feed pipe is provided on one side of the top of the preheating tank, a discharge pipe is provided on the bottom of the sulfonation tank, a first valve is provided on the transfer pipe, and a second valve is provided on the discharge pipe.

[0009] A further improvement is that a rotating ring is provided inside the heating jacket for rotation, the heater is installed on the rotating ring, the lower end of the rotating ring passes through the bottom of the heating jacket and a gear ring is provided on the outer wall, a support plate is provided below the side wall of the sulfonation tank, a rotating motor is provided on the support plate, and a gear meshing with the gear ring is provided at the output end of the rotating motor.

[0010] A further improvement is that the preheating tube is laid in an S shape inside the preheating jacket, and the preheating tube is in contact with the outer wall of the preheating tank.

[0011] A further improvement is that the first stirring mechanism includes a first stirring rod and a first stirring blade, the first stirring rod is rotatably arranged inside the preheating tank, the first stirring blade is installed on the outer wall of the first stirring rod, and the first stirring blades are arranged in groups of two symmetrically.

[0012] A further improvement is that the second stirring mechanism includes a second stirring rod, a second stirring blade and an auxiliary blade, a second stirring rod is rotatably provided inside the sulfonation tank, a second stirring blade is installed on the outer wall of the second stirring rod, a plurality of second stirring blades are symmetrically arranged in groups of two, and an auxiliary blade is provided on the top of the second stirring blade.

[0013] The beneficial effects of the utility model are as follows: the utility model provides a preheating tank and a sulfonation tank, and provides a preheating jacket on the outer wall of the preheating tank, and provides an exhaust pipe above one side of the sulfonation tank, and introduces the high-temperature exhaust gas in the sulfonation tank into the preheating pipe in the preheating jacket through the exhaust pipe, and uses the preheating pipe to preheat the raw materials waiting for sulfonation in the preheating tank, and the preheated raw materials enter the sulfonation tank for sulfonation reaction, so that the high-temperature exhaust gas generated in the sulfonation reaction process is fully utilized in this cycle, and the sulfonation reaction of the preheated raw materials can reduce the operating power of the heater to achieve energy saving. BRIEF DESCRIPTION OF THE DRAWINGS

[0014] Figure 1 It is a three-dimensional schematic diagram of the structure of the utility model;

[0015] Figure 2 This is a schematic diagram of the main view of the installation structure of the preheating tube inside the preheating jacket of the utility model;

[0016] Figure 3 It is a top view schematic diagram of the installation structure of the preheating tube inside the preheating jacket of the utility model;

[0017] Figure 4 This is a top view schematic diagram of the installation structure of the heater of the utility model;

[0018] Figure 5 This is a three-dimensional schematic diagram of the structure of the first stirring mechanism of the utility model;

[0019] Figure 6 It is a three-dimensional schematic diagram of the second stirring mechanism structure of the utility model.

[0020] Wherein: 1. preheating tank; 2. sulfonation tank; 3. bracket; 4. transfer pipe; 5. preheating jacket; 6. preheating pipe; 601, inlet end; 602, outlet end; 7. heat transfer oil jacket; 8. heating jacket; 9. heater; 10. exhaust pipe; 11. vacuum pump; 12. first stirring mechanism; 1201, first stirring rod; 1202, first stirring blade; 13. second stirring mechanism; 1301, second stirring rod; 1302, second stirring blade; 1303, auxiliary blade; 14. first stirring motor; 15. second stirring motor; 16. feed pipe; 17. discharge pipe; 18. first valve; 19. second valve; 20. slewing ring; 21. gear ring; 22. rotating motor; 23. gear. DETAILED DESCRIPTION

[0021] In order to deepen the understanding of the present invention, the present invention will be further described in detail below in conjunction with an embodiment. The embodiment is only used to explain the present invention and does not constitute a limitation on the protection scope of the present invention.

[0022] according to Figure 1-6As shown, this embodiment proposes a water reducing agent sulfonation device, including a preheating tank 1 and a sulfonation tank 2, the top of the sulfonation tank 2 is provided with a preheating tank 1 through a bracket 3, the bottom of the preheating tank 1 is connected to the inside of the sulfonation tank 2 through a transfer pipe 4, the outer wall of the preheating tank 1 is provided with a preheating jacket 5, the inside of the preheating jacket 5 is provided with a preheating pipe 6, the outer wall of the sulfonation tank 2 is installed with a heat transfer oil jacket 7, the outer wall of the heat transfer oil jacket 7 is provided with a heating jacket 8, the heating jacket 8 is provided with a heater 9 for heating the heat transfer oil in the heat transfer oil jacket 7, the sulfonation tank 2 is provided with a preheating jacket 5, and the heat transfer oil jacket 7 is provided with a preheating pipe 6. An exhaust pipe 10 is provided on the upper side, and the upper end of the exhaust pipe 10 is connected to the inlet end 601 of the preheating pipe 6. An exhaust pump 11 is provided on one side of the sulfonation tank 2. The outlet end 602 of the preheating pipe 6 is connected to the input port of the exhaust pump 11 through a connecting pipe, and the output port of the exhaust pump 11 is connected to an external purification device; a first stirring mechanism 12 is provided in the preheating tank 1, and a second stirring mechanism 13 is provided in the sulfonation tank 2. The first stirring mechanism 12 is driven by a first stirring motor 14, and the second stirring mechanism 13 is driven by a second stirring motor 15. When the water reducing agent sulfonation device of the utility model is used, the raw materials are put into the preheating tank 1. At this time, the high-temperature exhaust gas generated by the primary sulfonation reaction in the upper sulfonation tank 2 is transported to the preheating pipe 6 of the preheating jacket 5 to realize preheating of the raw materials entering the preheating tank 1, and the raw materials can be mixed by the first stirring mechanism 12 in the preheating tank 1. After the preheating is completed, the materials are discharged into the sulfonation tank 2 through the transfer pipe 4. At this time, the second stirring motor 15 mixes the materials entering the sulfonation tank 2. The high-temperature conditions required in the sulfonation reaction process are improved by the cooperation of the heat-conducting oil jacket 7 and the heating jacket 8. The heater 9 in the heating jacket 8 heats the heat-conducting oil in the heat-conducting oil jacket 7. The materials in the sulfonation tank 2 contact the inner wall and are heated by the heat-conducting oil.

[0023] A feed pipe 16 is provided on one side of the top of the preheating tank 1, a discharge pipe 17 is provided on the bottom of the sulfonation tank 2, a first valve 18 is provided on the transfer pipe 4, and a second valve 19 is provided on the discharge pipe 17. When the raw materials in the preheating tank 1 enter the sulfonation tank 2, the first valve can be opened; the second valve 19 can be opened to discharge the product after the sulfonation reaction from the sulfonation tank 2 through the discharge pipe 17.

[0024] A slewing ring 20 is rotatably provided inside the heating jacket 8, and the heater 9 is installed on the slewing ring 20. The lower end of the slewing ring 20 passes through the bottom of the heating jacket 8 and a gear ring 21 is provided on the outer wall. A support plate is provided below the side wall of the sulfonation tank 2, and a rotating motor 22 is provided on the support plate. A gear 23 meshing with the gear ring 21 is provided at the output end of the rotating motor 22. The utility model installs the heater 9 on the slewing ring 20 rotatably provided inside the heating jacket 8. When the rotating motor 22 is started, the gear 23 can be driven to drive the slewing ring 20 equipped with the gear ring 21 to rotate, thereby driving the heater 9 to heat the heat transfer oil in the heat transfer oil jacket in multiple directions, which can effectively improve the heating efficiency, reduce the number of heaters 9 installed, and save costs.

[0025] The preheating pipe 6 is laid in an S shape inside the preheating jacket 5, and the preheating pipe 6 contacts the outer wall of the preheating tank 1. The preheating pipe 6 laid in an S shape inside the preheating jacket 5 can fully contact the outer wall of the preheating tank 1 to preheat it.

[0026] The first stirring mechanism 12 includes a first stirring rod 1201 and a first stirring blade 1202. The first stirring rod 1201 is rotatably arranged inside the preheating tank 1. The first stirring blade 1202 is mounted on the outer wall of the first stirring rod 1201. The first stirring blades 1202 are arranged in pairs. The first stirring motor 14 is started to drive the first stirring rod 1201 to rotate, thereby driving the first stirring blades 1202 to rotate synchronously for stirring and mixing.

[0027] The second stirring mechanism 13 includes a second stirring rod 1301, a second stirring blade 1302 and an auxiliary blade 1303. The second stirring rod 1301 is rotatably arranged inside the sulfonation tank 2. The second stirring blade 1302 is mounted on the outer wall of the second stirring rod 1301. The second stirring blades 1302 are arranged in groups of two, and an auxiliary blade 1303 is arranged on the top of the second stirring blade 1302. The second stirring motor 15 is started to drive the second stirring rod 1301 to rotate, thereby driving the second stirring blade 1302 to rotate synchronously for stirring and mixing. During the process, the auxiliary blade 1303 can promote the stirring effect and make the mixing more uniform.

[0028] The utility model provides a preheating tank 1 and a sulfonation tank 2, and provides a preheating jacket 5 on the outer wall of the preheating tank 1, and provides an exhaust pipe 10 above one side of the sulfonation tank 2. The high-temperature exhaust gas in the sulfonation tank 2 is introduced into the preheating pipe 6 in the preheating jacket 5 through the exhaust pipe 10, and the preheating pipe 6 is used to preheat the raw materials waiting for sulfonation in the preheating tank 1. The preheated raw materials then enter the sulfonation tank 2 for sulfonation reaction, so that the high-temperature exhaust gas generated in the sulfonation reaction process is fully utilized in this cycle. The sulfonation reaction of the preheated raw materials can reduce the operating power of the heater 9 to achieve energy saving.

[0029] The above shows and describes the basic principles, main features and advantages of the utility model. Those skilled in the art should understand that the utility model is not limited by the above embodiments. The above embodiments and descriptions are only for explaining the principles of the utility model. Without departing from the spirit and scope of the utility model, the utility model may have various changes and improvements, which fall within the scope of the utility model to be protected. The scope of protection claimed by the utility model is defined by the attached claims and their equivalents.

Claims

1. A water reducing agent sulfonation device, characterized in that: The invention comprises a preheating tank (1) and a sulfonation tank (2), wherein the top of the sulfonation tank (2) is provided with the preheating tank (1) through a bracket (3), the bottom of the preheating tank (1) is connected to the interior of the sulfonation tank (2) through a transfer pipe (4), a preheating jacket (5) is provided on the outer wall of the preheating tank (1), a preheating pipe (6) is provided inside the preheating jacket (5), a heat transfer oil jacket (7) is installed on the outer wall of the sulfonation tank (2), a heating jacket (8) is provided on the outer wall of the heat transfer oil jacket (7), and the heating jacket (8) is provided on the outer wall of the heating oil jacket (7). A heater (9) for heating the heat-conducting oil in the heat-conducting oil jacket (7) is provided in the sleeve (8); an exhaust pipe (10) is provided above one side of the sulfonation tank (2); the upper end of the exhaust pipe (10) is connected to the inlet end (601) of the preheating pipe (6); an air extraction pump (11) is provided on one side of the sulfonation tank (2); the outlet end (602) of the preheating pipe (6) is connected to the input port of the air extraction pump (11) through a connecting pipe; and the output port of the air extraction pump (11) is connected to an external purification device; The preheating tank (1) is provided with a first stirring mechanism (12), and the sulfonation tank (2) is provided with a second stirring mechanism (13). The first stirring mechanism (12) is driven by a first stirring motor (14), and the second stirring mechanism (13) is driven by a second stirring motor (15).

2. A water reducing agent sulfonation device according to claim 1, characterized in that: A feed pipe (16) is provided on one side of the top of the preheating tank (1), a discharge pipe (17) is provided on the bottom of the sulfonation tank (2), a first valve (18) is provided on the transfer pipe (4), and a second valve (19) is provided on the discharge pipe (17).

3. A water reducing agent sulfonation device according to claim 1, characterized in that: A rotating ring (20) is rotatably provided inside the heating jacket (8), the heater (9) is mounted on the rotating ring (20), the lower end of the rotating ring (20) passes through the bottom of the heating jacket (8) and a gear ring (21) is provided on the outer wall, a support plate is provided below the side wall of the sulfonation tank (2), a rotating motor (22) is provided on the support plate, and a gear (23) meshing with the gear ring (21) is provided at the output end of the rotating motor (22).

4. A water reducing agent sulfonation device according to claim 1, characterized in that: The preheating pipe (6) is laid in an S shape inside the preheating jacket (5), and the preheating pipe (6) is in contact with the outer wall of the preheating tank (1).

5. A water reducing agent sulfonation device according to claim 1, characterized in that: The first stirring mechanism (12) comprises a first stirring rod (1201) and a first stirring blade (1202); the first stirring rod (1201) is rotatably provided inside the preheating tank (1); the first stirring blade (1202) is mounted on the outer wall of the first stirring rod (1201); and the first stirring blades (1202) are provided in a plurality of groups symmetrically in pairs.

6. A water reducing agent sulfonation device according to claim 1, characterized in that: The second stirring mechanism (13) comprises a second stirring rod (1301), a second stirring blade (1302) and an auxiliary blade (1303). The second stirring rod (1301) is rotatably provided inside the sulfonation tank (2). The second stirring blade (1302) is mounted on the outer wall of the second stirring rod (1301). The second stirring blades (1302) are provided in a plurality of groups symmetrically in pairs. An auxiliary blade (1303) is provided on the top of the second stirring blade (1302).