Production plant for the production of a 6C-polycarboxylic acid water reducer

Abstract

Production plant for producing a 6C-polycarboxylic acid water reducer, comprising a vessel body, a vessel lid and a stirring device, characterized in that the production plant comprises a first feeding device and the second feeding device arranged under the boiler lid, wherein the first feeding device comprises at least one first feed pipe and a plurality of first material distribution pipes each provided with a plurality of material distribution holes, the plurality of first material distribution pipes being arranged side by side in the transverse direction and connected to the first feed pipe; wherein the second feed device comprises at least one second feed pipe and a plurality of second material distribution pipes, each of which is also provided with a plurality of material distribution holes, the plurality of second material distribution pipes being arranged side by side in the transverse direction and connected to the second feed pipe; wherein the plurality of first material distribution pipes and the plurality of second material distribution pipes are arranged alternately.

Description

TECHNICAL FIELD

[0001] The utility model relates to the technical field of mechanical production equipment, specifically a production equipment for the manufacture of a polycarboxylic acid water reducer. STATE OF THE ART

[0002] A water reducer is a concrete additive that can reduce the amount of mixing water without significantly changing the slump of the concrete.

[0003] The reaction mechanism of the polycarboxylic acid water reducer is that alkenyl polyethers such as HPEG, TPEG, GPEG, VPEG, and unsaturated monomers such as acrylic acid, maleic acid, and acrylates undergo radical copolymerization under the initiation of the redox system, resulting in a chain reaction to form the polycarboxylic acid water reducer. The reaction temperature, the dropping process, and the mass transfer efficiency of the reaction vessel are the main factors affecting the quality of polycarboxylic acid water reducer products.

[0004] In recent years, polycarboxylic acid water reducer synthesized from 6C monomer (GPEG, VPEG) has emerged among many polycarboxylic acid water reducers due to its ambient and low-temperature production process, excellent product performance, and high cost-performance ratio. However, there are many discrepancies between the conventional polycarboxylic acid water reducer production equipment and the production of 6C water reducers. First, the conventional polycarboxylic acid water reducer production equipment mostly uses paddle or anchor impellers. Due to the structural design, a dead angle for stirring is created.After the A / B materials are drained, they remain in the upper layer of the reaction liquid, which poses a risk of explosion, often resulting in gel formation on the reaction vessel body. Second, the existing production equipment for polycarboxylic acid water reducers mostly uses jacket heating and agitation to increase the solubility of the polyether monomers.Due to the strong activity of the 6C monomer, the synthesis temperature of the water reducer is mostly controlled at room temperature and low temperature, and the heat transfer efficiency of the conventional jacket temperature control is generally not suitable for the preparation of 6C polycarboxylic acid water reducer; moreover, the A / B material dropping device mostly uses a single tube for dropwise addition, which is not conducive to the diffusion of the A / B material in the reaction liquid and negatively affects the quality of the water reducer.

[0005] To solve the above-mentioned technical problems, the industry has conducted research on improving stirring performance, improving heat exchange efficiency, and accelerating material mixing. The Chinese Utility Model Application Announcement No. CN 220803225 U describes a production equipment for a glass-lined reaction vessel, comprising a vessel body, the top of which is provided with an inlet port and a drip feed port, and the bottom of which is provided with a discharge port; the outer surface of the vessel body is covered with a jacket; a hose and a drip ring pipe are also provided in the vessel body; the lower end of the hose passes through the drip feed port into the interior of the vessel body and is connected to the drip ring pipe via a drip flange, and the drip ring pipe is each provided with a drip hole.The hose is attached to the drip feed port through the central flange, and the upper end of the hose is connected to the drip material line; the boiler body is provided with a cartridge body with open upper and lower ends, which is firmly mounted in the boiler body; inside the cartridge body there is a rotating shaft on which a lifting screw is mounted;One end of the rotary shaft passes through the top of the kettle body and is connected to the output port of the electric motor, and the other end is equipped with a U-shaped stirring blade located between the outer wall of the cartridge body and the inner wall of the kettle body. The reaction kettle forms flow channels with different flow directions inside, achieving efficient and uniform mixing of materials without dead corners, thereby improving the heat transfer and heat exchange efficiency and the efficiency of the synthesis reaction. The utility model improves the stirring performance to a certain extent, but for a large-volume reaction kettle, the upper layer of the reaction liquid is still in a certain stirring dead angle, and jacket temperature control and ring tube draining only improve the reaction to a certain extent. CONTENT OF THE PRESENT UTILITY MODEL

[0006] The utility model aims to remedy the deficiencies of the prior art and to provide a production plant for the production of a 6C-polycarboxylic acid water reducer, which serves to avoid the formation of stirring dead angles in a stirred tank and to distribute the material evenly and densely.

[0007] To achieve the above-mentioned object, a production plant for producing a 6C-polycarboxylic acid water reducer is developed, which comprises a kettle body, a kettle lid, and a stirring device, and further comprises a first feeding device and a second feeding device arranged under the kettle lid, wherein the first feeding device comprises at least one first feeding pipe and a plurality of first material distribution pipes each provided with a plurality of material distribution holes, wherein the plurality of first material distribution pipes are arranged side by side in the transverse direction and connected to the first feeding pipe;wherein the second feed device comprises at least one second feed pipe and a plurality of second material distribution pipes, each of which is also provided with a plurality of material distribution holes, wherein the plurality of second material distribution pipes are arranged transversely adjacent to one another and connected to the second feed pipe; wherein the plurality of first material distribution pipes and the plurality of second material distribution pipes are arranged alternately.

[0008] Preferably, the first supply device of the present utility model also comprises a mounting frame, wherein the first supply pipe is connected to the liquid supply opening on the kettle lid and is arranged at the lower end of the kettle lid, wherein one end of the mounting frame is connected to the kettle lid and the other end of the mounting frame is connected to the first material distribution pipe, wherein an end of the first material distribution pipe facing the kettle body is connected to the lower end of the first supply pipe, wherein a plurality of material distribution holes for material distribution are provided at regular intervals on the underside of the first material distribution pipe;wherein the second supply device also comprises a fixing frame, wherein the second supply pipe is connected to the liquid supply opening on the kettle lid and is arranged at the lower end of the kettle lid, wherein one end of the fixing frame is connected to the kettle lid and the other end of the fixing frame is connected to the second material distribution pipe, wherein an end of the second material distribution pipe facing the kettle body is connected to the lower end of the second supply pipe, wherein a plurality of material distribution holes for material distribution are provided at regular intervals on the underside of the second material distribution pipe; wherein the first material distribution pipe and the second material distribution pipe are provided with a gap near the center position of the kettle body;

[0009] Preferably, the present utility model further comprises a heat exchange device, wherein the heat exchange device comprises a spherical tube coil arranged on the inner wall of the boiler body, wherein the spherical tube coil is arranged spirally, wherein a tube coil inlet is arranged at the lower part of the boiler body and connected to the tube coil, wherein a tube coil outlet is arranged at the upper part of the boiler body and connected to the tube coil.

[0010] Preferably, the present utility model also comprises a stirring device, wherein the stirring device comprises a guide cartridge and a stirrer, wherein the guide cartridge is fastened in the kettle body via a supporting bracket and the stirrer comprises a stirring shaft, wherein the stirring shaft is arranged and movably connected at the central axis position of the kettle lid, wherein the stirring shaft is fixedly provided from top to bottom in succession with a drain pressure disc, a first drive vane, a second drive vane, a folded vane disc, a third drive vane, a fourth drive vane and a composite vane, wherein the top of the stirring shaft is fixedly connected to an electric motor.

[0011] Preferably, the outside of the boiler body of the present utility model is wrapped with heat-insulating cotton, the inlet and outlet of the heat exchange device are connected to an integrated high and low temperature machine, a lifting-type discharge valve is arranged at the bottom of the boiler body, and a temperature sensor is arranged inside the boiler body.

[0012] Preferably, the spherical tube winding of the present utility model consists of a plurality of interconnected thin-walled spherical shells, wherein the plurality of thin-walled spherical shells are arranged tangentially to one another and are connected to one another in a sealed manner to form a fluid channel in the tube winding.

[0013] Preferably, the guide cartridge of the stirring device of the present utility model is a circular cylindrical tubular construction, wherein a gap is provided in the center of the guide cartridge through which the folded blade plate can be passed.

[0014] Preferably, the discharge pressure disc of the present utility model comprises an inner ring, an outer ring, and a curved blade, wherein a gap is formed between the inner ring and the outer ring of the discharge pressure disc, wherein the curved blades are arranged vertically in the gap and are firmly connected to the inner ring and the outer ring of the discharge pressure disc; wherein the folded blade disc comprises an inner ring, an outer ring, and a blade, wherein the outer diameter of the outer ring of the folded blade disc is smaller than the inner diameter of the tube winding, wherein the inner ring of the folded blade disc is arranged in the gap of the guide cartridge, wherein the width of the inner ring of the folded blade disc is greater than the thickness of the guide cartridge, wherein the inner ring and the outer ring of the folded blade disc are firmly connected to one another by the blades,wherein the blades are arranged transversely in the vessel body and vertically connected to the agitator shaft, wherein the inner parts of the blades of the folded blade disc, which lie within the inner ring of the folded blade disc, are inclined at an obtuse angle, and the parts of the blades of the folded blade disc, which lie in the gap between the outer ring and the inner ring of the folded blade disc, are inclined at an acute angle; wherein the plurality of drive blades are connected to the agitator shaft at an upward incline and arranged offset on the agitator shaft.

[0015] Preferably, the composite blade of the present utility model comprises an inner ring and an outer ring arranged transversely on the lower part of the boiler body, the outer ring being higher than the inner ring to form a staggered structure, the outer ring of the composite blade being fixedly connected to the agitator shaft via a plurality of transversely arranged folded blade plates, the inner ring of the composite blade being fixedly connected to the agitator shaft via a plurality of transversely arranged folded blade plates, the folded blade plates on the inner ring and outer ring of the composite blade being connected to one another in the vertical direction by a plurality of supporting rods, a plurality of inclined scrapers being arranged along the circumference of the outer sides of the inner ring and outer ring of the composite blade,wherein the folded blade plates on the outer ring of the composite blade are arranged on the lower part of the guide cartridge in the boiler body and there is a gap between them and the lower part of the guide cartridge.

[0016] Compared to the state of the art, the utility model has the following advantages: 1. The various structural units of the stirring device cooperate, and the inside and outside of the guide cartridge and the upper and lower layers of the reaction liquid are stirred without dead angles to make the liquid flow in multiple directions, which greatly improves the stirring and dispersing effect and improves the mass transfer efficiency; 2. The heat exchange device uses spherical tube winding, which greatly increases the heat exchange area and improves the heat exchange efficiency, and combined with the stirring system, the monomer can be quickly dissolved at 10-15 °C, thereby reducing energy consumption in the manufacturing process and effectively controlling production costs; 3. The flat dripping through the distribution device can avoid safety and quality problems caused by excessively vigorous reactions due to local high concentrations, and meanwhile, the excellent mass transfer efficiency of the stirring system in cooperation with the distribution device can shorten the reaction time and improve the production efficiency of the water reducer. SHORT DESCRIPTION OF THE DRAWING Fig. 1 is a sectional view of the utility model; Fig. 2 is a plan view of the spherical tube coil of the present utility model; Fig. 3 is a front view of the spherical tube coil of the present utility model; Fig. 4 is a plan view of the distribution device of the present utility model; Fig. 5 is a bottom view of the distribution device of the present utility model; Fig. 6 is a plan view of the drain pressure disc of the present utility model; Fig. 7 is a front view of the drain pressure plate of the present utility model; Fig. 8 is a plan view of the folded blade disc of the present utility model; Fig. 9 is a plan view of the composite blade of the present utility model; Fig. 10 is a bottom view of the composite blade of the present utility model; Fig. 11 is a front view of the composite blade of the present utility model. List of reference symbols

[0017] In the drawings: 1. Solids feed opening, 2. First fluid supply opening, 2.1. Second fluid supply opening, 3. Guide cartridge, 4. Spherical tube winding, 4.1. Supporting bolt, 5. Supporting bracket, 6. Inlet of the spherical tube winding, 7. Lifting type drain valve, 8. Outlet of the spherical tube winding, 9. Electric motor, 10. Stirring shaft, 11. Distribution device, 11.1. Feed pipe, 11.2. Material distribution pipe, 11.3. Flange, 11.4. Mounting frame, 11.5. Material distribution hole, 12. Drain pressure disc, 12.1. Inner ring of the drain pressure disc, 12.2. Outer ring of the drain pressure disc, 12.3. Supporting rod of the drain pressure disc, 12.4. Curved blade, 13. Drive blade, 14. Folded blade disc, 14.1. Obtuse-angled blade, 14.2. Acute-angled blade, 14.3. Supporting rod of the folded blade disc, 14.4. Inner ring of the folded blade disc, 14.5. Outer ring of the folded blade disc, 15. Composite bucket, 15.1. Composite bucket inner ring, 15.2. Composite bucket outer ring, 15.3. Composite bucket upper supporting rod; 15.4. Composite bucket upper positively folded blade, 15.5. Composite bucket upper reversely folded blade, 15.6. Composite bucket lower supporting rod; 15.7. Composite bucket lower reversely folded blade, 15.8. Inclined scraper, 15.9. Vertical supporting rod, 15.10. Vertical folded plate. DETAILED DESCRIPTION

[0018] In order to clarify the purpose, technical solutions, and advantages of the embodiments of the present utility model, the technical solutions in the embodiments of the present utility model are described clearly and completely in conjunction below. Obviously, the described embodiments are some of the embodiments of the present utility model, not all of them. All other embodiments that a person skilled in the art can derive from the embodiments in the present utility model without creative effort are within the scope of the present utility model.

[0019] With reference to Fig. 1 to Fig. 11 shows a production plant for the production of a 6C-polycarboxylic acid water reducer.

[0020] The production system includes a heat exchange device consisting of a spherical tube coil 4, a spherical tube coil inlet 6, and a spherical tube coil outlet 8. The spherical structural design of the spherical tube coil 4 increases the heat exchange area and significantly improves heat exchange efficiency. The spherical tube coil 4 consists of several conductively connected hollow spherical shells, and the spherical tube coil 4 is spirally arranged on the inner side wall of the boiler body and firmly connected to the boiler body via several support bolts 4.1. The boiler body is provided with a spherical tube coil inlet 6 and a spherical tube coil outlet 8, the inlet and outlet being connected to the spherical tube coil 4 and the integrated high-and-low-temperature machine, respectively.

[0021] The production facility also includes a distribution device 11, which serves to drip the A / B materials of the 6C polycarboxylic acid water reducer over a large area to fully distribute them, thus preventing explosion and aggregation that would impair product quality. The distribution device 11 specifically includes two groups of symmetrically arranged feed pipes 11.1, material distribution pipes 11.2, and fixing frames 11.4. The fixing frames 11.4 play a supporting role, and the two ends of the fixing frames are respectively fixedly connected to the kettle lid and the material distribution pipes 11.2. The end of the material distribution pipe 11.2 facing the kettle body is conductively connected to the lower end of the feed pipe 11.1, and the other end of the feed pipe 11.1 is connected to the first liquid supply port 2 of the kettle lid via a flange. The two groups of material distribution pipes 11.2 of the distribution device 11 consist of several thin tubes, wherein the thin tubes are arranged parallel and crosswise and at the lower ends of the thin tubes several material distribution holes 11.5 are arranged at equal intervals.

[0022] An agitator shaft 10 is arranged on the central axis of the kettle body, the upper side of which protrudes from the kettle lid. An electric motor 9 is also arranged on the upper side of the agitator shaft 10. For the parts of the agitator shaft in the kettle body, the agitator shaft 10 is provided with a plurality of drive blades 13, which are arranged asymmetrically and staggered in layers. The drive blade is designed to be inclined upwards to effect deflection in a specific direction.

[0023] At the upper end of the agitator shaft 10 in the kettle body, a discharge pressure disc 12 is arranged. Under the action of the curved blade 12.4, the discharge pressure disc 12 ensures that the upper liquid in the kettle flows radially to avoid the dead corner caused by the upper kettle wall during stirring. The discharge pressure disc 12 comprises an inner ring 12.1 and an outer ring 12.2. The inner ring 12.1 is transversely connected to the agitator shaft 10 via a supporting rod 12.3. The diameter of the outer ring 12.2 is larger than the diameter of the inner ring 12.1, and a gap exists between the two. The plurality of curved blades 12.4 are arranged vertically in the circumferential direction in the gap and firmly connect the inner ring 12.1 and the outer ring 12.2. The curved blade 12.4 is a long blade in the shape of a curved surface, arranged in a lateral position with a curved edge and in a vertical position with a straight edge of the curved blade 12,4. The curved blades 12.4 are arranged on top of the discharge pressure disc 12 to form a flow guide with a specific direction.

[0024] At the lower end of the discharge pressure disc 12 of the agitator shaft 10 in the vessel body, a folded blade disc 14 is also provided, wherein the folded blade disc 14 comprises an inner ring 14.4 and an outer ring 14.5, wherein the inner ring and the outer ring are connected to the agitator shaft 10 via a supporting rod 14.1, wherein several blade plates are also arranged on the supporting rod 14.1, and acute-angled blades 14.2 are arranged on the supporting rod 14.1 on the inner ring of the inner ring 14.4, wherein obtuse-angled blades 14.1 are arranged on the supporting rod 14.1 between the inner ring 14.4 and the outer ring 14.5, wherein the obtuse angle and the acute angle are expressed in the same reference system, and there is a mathematical correspondence between the degrees of inclination of the two blades and the degree of inclination of the obtuse-angled blade 14.1. is 90° to 180° and the inclination of the acute-angled blade 14.2 is 0° to 90°.

[0025] At the lower end of the folded blade disc 14 of the agitator shaft 10 in the boiler body, a composite blade 15 is also provided, wherein the composite blade 15 has an outer ring 15.2 arranged on the upper layer and an inner ring 15.1 arranged on the lower layer, wherein the outer ring 15.2 is connected to the agitator shaft 10 via an upper supporting rod 15.3 and the inner ring 15.1 is connected to the agitator shaft 10 via a lower supporting rod 15.6.

[0026] The upper supporting rod 15.3 of the outer ring 15.2 is constructed similarly to the discharge pressure plate 12. A reverse-folded blade 15.5 is arranged on the upper supporting rod 15.3 of the inner ring, and a positive-folded blade 15.4 is arranged on the upper supporting rod 15.3 of the outer ring. A lower reverse-folded blade 15.7 is arranged on the lower supporting rod 15.6 of the inner ring 15.1.

[0027] A vertical folded plate 15.10 is also connected between the upper supporting rod 15.3 and the lower supporting rod 15.6. The outer sides of the outer ring 15.2 and the inner ring 15.1 are also connected to an inclined scraper 15.8. The inclined scraper 15.8 is in positive engagement with the bottom of the boiler body, and the lower end of the inclined scraper 15.8 extends to the lifting type 7 discharge valve at the lower end of the boiler body.

[0028] The inclined scraper 15.8 of the composite blade 15 cooperates with the folded plate to make the polyether solid flow and avoid bottom deposition, and the drain pressure disc 12, the folded blade disc 14, the multiple positive-folded and reverse-folded blades of the composite blade 15 cooperate with the multiple drive blades 13 and the guide cartridge 3, so that the liquid flows upward inside the cartridge and downward outside the cartridge, which greatly improves the mass transfer efficiency and has a positive effect on improving the dissolution efficiency, preventing local explosions, and accelerating heat exchange.

[0029] A guide cartridge 3 is also provided in the kettle body. The guide cartridge 3 comprises an upper part and a lower part, the inner diameter of the cartridge body of the guide cartridge 3 being larger than the rotational circumference of the plurality of drive blades 13, and the guide cartridge 3 is firmly connected to the inner wall of the kettle body via a plurality of supporting brackets 5. A gap exists between the upper and lower parts of the guide cartridge 3, the gap being able to accommodate the discharge pressure disc 12, which can rotate freely in the space formed by the gap. The guide cartridge 3 serves to generate a guide flow in a specific direction so that the materials are thoroughly mixed.

[0030] In the specific manufacturing process of the 6C-polycarboxylic acid water reducer, first, according to the proposed operation procedures and process maps, a nominal amount of water is added into the reaction vessel through the second liquid supply port 2.1, then the electric motor 9 is started and the stirring device is turned on, meanwhile, 6C-polyether is added through the solid supply port 1 for pre-stirring (6C-polyether is configured with an aqueous solution with a concentration below 55% and can be quickly dissolved by sufficient stirring under the synergistic action of the stirring device), the temperature in the vessel is read, and the integrated high and low temperature machine is started, so that the spherical tube coil 4 connected to the integrated high and low temperature machine starts to work and regulate the temperature.Initially, the temperature in the kettle is controlled at 10-15°C by the spherical tube coil 4. After the feeding is completed, the initiator is added through the second liquid feed port 2.1 and stirred for 5 minutes. Then, the integrated high and low temperature machine is shut down, the feed valve of the first liquid feed port 2 is opened, and materials A and B are dripped through the distributor 11. As the reaction progresses, the temperature gradually rises. When the dripping of materials A and B is completed, the temperature rises to approximately 20-25°C. Stirring and reaction are continued for another 30 minutes while maintaining heat, and then the lift-type discharge valve 7 at the bottom of the kettle is opened to discharge the material.

[0031] The above represents only specific embodiments of the present utility model, but the scope of protection of the present utility model is not limited thereto. Any person familiar with the technical field may, within the technical scope disclosed by the utility model, make equivalent substitutions or modifications according to the technical solution and novel concept of the utility model, which should be included within the scope of protection of the utility model. QUOTES CONTAINED IN THE DESCRIPTION

[0000] This list of documents submitted by the applicant was generated automatically and is included solely for the convenience of the reader. This list is not part of the German patent or utility model application. The DPMA assumes no liability for any errors or omissions. Cited patent literature

[0000] CN 220803225 U

[0005]

Claims

[1] Production plant for producing a 6C-polycarboxylic acid water reducer, comprising a vessel body, a vessel lid and a stirring device, characterized by , that the production plant comprises a first feeding device and the second feeding device arranged under the boiler lid, wherein the first feeding device comprises at least one first feed pipe and a plurality of first material distribution pipes each provided with a plurality of material distribution holes, the plurality of first material distribution pipes being arranged side by side in the transverse direction and connected to the first feed pipe; wherein the second feed device comprises at least one second feed pipe and a plurality of second material distribution pipes, each of which is also provided with a plurality of material distribution holes, the plurality of second material distribution pipes being arranged side by side in the transverse direction and connected to the second feed pipe; wherein the plurality of first material distribution pipes and the plurality of second material distribution pipes are arranged alternately. [2] Production plant for producing a 6C-polycarboxylic acid water reducer according to claim 1, characterized by , that the first feeding device also comprises a fixing frame, wherein the first feeding pipe is connected to the liquid feeding opening on the kettle lid and is arranged at the lower end of the kettle lid, wherein one end of the fixing frame is connected to the kettle lid and the other end of the fixing frame is connected to the first material distribution pipe, wherein an end of the first material distribution pipe facing the kettle body is connected to the lower end of the first feeding pipe, wherein a plurality of material distribution holes for material distribution are provided at regular intervals on the underside of the first material distribution pipe; wherein the second feed device also comprises a fixing frame, wherein the second feed pipe is connected to the liquid feed opening on the kettle lid and is arranged at the lower end of the kettle lid, wherein one end of the fixing frame is connected to the kettle lid and the other end of the fixing frame is connected to the second material distribution pipe, wherein an end of the second material distribution pipe facing the kettle body is connected to the lower end of the second feed pipe, wherein a plurality of material distribution holes for material distribution are provided at regular intervals on the underside of the second material distribution pipe; wherein the first material distribution pipe and the second material distribution pipe are provided with a gap near the center position of the boiler body. [3] Production plant for producing a 6C-polycarboxylic acid water reducer according to claim 1, characterized bythat the production plant further comprises a heat exchange device, wherein the heat exchange device comprises a spherical tube coil arranged on the inner wall of the boiler body, wherein the spherical tube coil is arranged spirally, wherein a tube coil inlet is arranged at the lower part of the boiler body and connected to the tube coil, wherein a tube coil outlet is arranged at the upper part of the boiler body and connected to the tube coil. [4] Production plant for producing a 6C-polycarboxylic acid water reducer according to claim 1, characterized bythat the production plant also comprises a stirring device, wherein the stirring device comprises a guide cartridge and a stirrer, wherein the guide cartridge is fastened in the kettle body via a supporting bracket and the agitator comprises an agitator shaft, wherein the agitator shaft is arranged at the central axis position of the kettle lid and movably connected, wherein the agitator shaft is fixedly provided from top to bottom in succession with a drain pressure disc, a first drive vane, a second drive vane, a folded vane disc, a third drive vane, a fourth drive vane and a compound vane, wherein the top of the agitator shaft is fixedly connected to an electric motor. [5] Production plant for producing a 6C-polycarboxylic acid water reducer according to claim 1, characterized bythat the outside of the boiler body is wrapped with heat-insulating cotton, the inlet and outlet of the heat exchange device are connected to an integrated high and low temperature machine, a lifting-type drain valve is arranged at the bottom of the boiler body, and a temperature sensor is arranged inside the boiler body. [6] Production plant for producing a 6C-polycarboxylic acid water reducer according to claims 1 and 2, characterized by that the spherical tube winding consists of a plurality of interconnected thin-walled spherical shells, wherein the plurality of thin-walled spherical shells are arranged tangentially to one another and are connected to one another in a sealed manner in order to form a fluid channel in the tube winding. [7] Production plant for producing a 6C-polycarboxylic acid water reducer according to claim 1, characterized bythat the guide cartridge of the stirring device is a circular cylindrical tubular construction, with a gap provided in the center of the guide cartridge through which the folded blade plate can be passed. [8] Production plant for producing a 6C-polycarboxylic acid water reducer according to claim 1, characterized by , that the discharge pressure disc comprises an inner ring, an outer ring and curved blades, wherein a gap is formed between the inner ring and the outer ring of the discharge pressure disc, wherein the curved blades are arranged vertically in the gap and fixedly connected to the inner ring and the outer ring of the discharge pressure disc; wherein the folded blade disc comprises an inner ring, an outer ring, and a blade, wherein the outer diameter of the outer ring of the folded blade disc is smaller than the inner diameter of the tube winding, wherein the inner ring of the folded blade disc is arranged in the gap of the guide cartridge, wherein the width of the inner ring of the folded blade disc is greater than the thickness of the guide cartridge, wherein the inner ring and the outer ring of the folded blade disc are firmly connected to one another by the blades, wherein the blades are arranged transversely in the vessel body and vertically connected to the agitator shaft, wherein the inner parts of the blade of the folded blade disc that lie within the inner ring of the folded blade disc are inclined at an obtuse angle, wherein the parts of the blade of the folded blade disc that lie in the gap between the outer ring and the inner ring of the folded blade disc,are inclined at an acute angle;, wherein the plurality of drive blades are connected to the agitator shaft in an upwardly inclined manner and are arranged offset on the agitator shaft. [9] Production plant for producing a 6C-polycarboxylic acid water reducer according to claim 1, characterized byin that the composite blade comprises an inner ring and an outer ring which are arranged transversely on the lower part of the boiler body, the outer ring being higher than the inner ring to form a staggered structure, the outer ring of the composite blade being fixedly connected to the agitator shaft via a plurality of transversely arranged folded blade plates, the inner ring of the composite blade being fixedly connected to the agitator shaft via a plurality of transversely arranged folded blade plates, the folded blade plates on the inner ring and outer ring of the composite blade being connected to one another in the vertical direction by a plurality of supporting rods, a plurality of inclined scrapers being arranged along the circumference of the outer sides of the inner ring and outer ring of the composite blade, the folded blade plates on the outer ring of the composite blade being arranged on the lower part of the guide cartridge in the boiler body and a gap being present between them and the lower part of the guide cartridge.

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