Pipeline heat tracing and water draining device for water reducing agent macromonomer production

In the production of large water reducing agent monomers, the heat-tracing pipe is separately connected to the vertical free float trap, and the collection tank and straight section pipe are set up, the problem of pressure imbalance in the traditional steam drain plate is solved, the heat-tracing effect is improved, the steam consumption is reduced, and the equipment failure rate is reduced.

CN222687937UActive Publication Date: 2025-03-28FUJIAN ZHONGSHAN CHEM CO LTD
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Patent Information

Application Number
CN202421413910.8
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-06-20
Publication Date
2025-03-28
Estimated Expiration
2034-06-20

AI Technical Summary

Technical Problem

When producing large monomers of water reducer, traditional group steam hydrophobic trays have imbalance in the pressure of steam condensation water, resulting in hedging of the pressure of the heat-tracing pipeline, poor hydrophobic effect, increased steam consumption, and may cause problems such as water accumulation and water hammers, causing equipment damage.

Method used

A pipeline heat tracing and hydrophobic device is designed. By connecting each heat tracing pipe separately, a vertical free float ball trap is changed to a separate steam drainage to avoid the pressure hedging of the steam condensate water, and a low drain pipe and straight section pipe are installed in the collection tank to collect condensate and observe the hydrophobic situation.

Benefits of technology

It improves the heating effect of the pipeline, reduces steam loss, prevents water hammer phenomenon, reduces equipment failure rate, and allows the hydrophobic conditions of each heat-tracing pipeline to be visually observed, and troubleshooting is promptly detected and handled.

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Abstract

The utility model discloses a pipeline heat tracing and water draining device for water reducing agent macromonomer production, which comprises a rack, a water draining tank arranged above the rack, a collecting tank arranged on the rack and below the water draining tank, a plurality of heat tracing pipelines arranged on the water draining tank, a water draining valve assembled on each heat tracing pipeline, and a water draining pipe arranged on the water draining tank. And one end, far away from the heat tracing pipeline, of the drain valve extends into the collecting tank. After the technical scheme is adopted, according to the pipeline heat tracing and water draining device for producing the water reducing agent macromonomer, each heat tracing pipeline is independently connected with one vertical free floating ball type water draining valve, namely group steam water draining is changed into independent steam water draining, so that the pipeline heat tracing effect can be improved, and the steam loss can be reduced; the water hammer phenomenon is prevented, and the equipment failure rate is reduced; and the drainage condition of each heat tracing pipeline can be visually observed, and the fault condition can be timely checked and processed.
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Description

Technical Field

[0001] The utility model relates to the technical field of chemical production, in particular to a pipeline heat tracing and drainage device for the production of large monomers of water reducing agents. Background Art

[0002] In the existing production of water-reducing agent monomers, in order to prevent the water-reducing agent monomer materials from solidifying, it is necessary to use steam drain pans to heat the water-reducing agent monomer materials. However, the existing steam drain pans are traditional group steam drain pans. Due to the unbalanced pressure of steam condensate in traditional group steam drain pans, the pressure of each heating pipeline will be hedged. On the one hand, it will lead to poor drainage effect and increased steam consumption; on the other hand, problems such as water accumulation and water hammer will occur inside the equipment, causing equipment damage. Utility Model Content

[0003] In view of the above problems, the utility model provides a pipeline heat tracing and draining device for the production of large monomers of water reducing agent.

[0004] In order to solve the above technical problems, the technical solution adopted by the utility model is: a pipeline heating and draining device for the production of large monomers of water reducing agent, including a frame, a drain box arranged above the frame, the frame is provided with a collecting tank below the drain box, a plurality of heating pipes are arranged on the drain box, each of the heating pipes is equipped with a drain valve, and the drain valve extends into the collecting tank at one end away from the heating pipe.

[0005] Preferably, a low row pipe is provided at the bottom of the collecting tank.

[0006] Preferably, a straight pipe is further provided in the drain tank, one end of the straight pipe is connected to a portion of the heating pipe extending into the drain tank, and the other end of the straight pipe extends into the collecting tank.

[0007] Preferably, a plurality of fixed limiting rods are provided on the inner top of the collecting tank.

[0008] Preferably, a hand valve is provided on the drain tank, and the other end of the hand valve is connected to a part of the heating pipe located in the drain tank.

[0009] Preferably, the top of the drain tank is provided with a top inlet for a plurality of the heating pipes to enter.

[0010] Preferably, the steam trap is a vertical free float steam trap.

[0011] From the above description of the structure of the utility model, it can be seen that compared with the prior art, the utility model has the following advantages:

[0012] The utility model provides a pipeline heating and draining device for the production of large-sized water-reducing agent monomers. By connecting each heating pipeline to a vertical free-floating ball-type drain valve individually, that is, changing the group steam draining to the individual steam draining, the pipeline heating effect can be improved, the steam loss can be reduced, the water hammer phenomenon can be prevented, and the equipment failure rate can be reduced. Moreover, the drainage conditions of each heating pipeline can be visually observed, and the failure conditions can be timely checked and handled. BRIEF DESCRIPTION OF THE DRAWINGS

[0013] The drawings constituting a part of this application are used to provide a further understanding of the present invention. The illustrative embodiments of the present invention and their descriptions are used to explain the present invention and do not constitute an improper limitation on the present invention. In the drawings:

[0014] Figure 1 It is a schematic diagram of a pipeline heat tracing and draining device for the production of large monomers of water reducing agent according to the utility model;

[0015] Figure 2 It is a schematic diagram of the connection between the straight section pipeline and the heating pipeline of the pipeline heating and draining device for the production of large monomers of water reducing agent according to the utility model;

[0016] Figure 3 The utility model is a schematic diagram of a collection tank of a pipeline heat-tracing and draining device for producing large monomers of a water-reducing agent. DETAILED DESCRIPTION

[0017] It should be noted that, in the absence of conflict, the embodiments of the present invention and the features in the embodiments can be combined with each other.

[0018] In the description of the present utility model, it should be understood that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside" and the like indicate positions or positional relationships based on the positions or positional relationships shown in the accompanying drawings, and are only for the convenience of describing the present utility model and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as a limitation on the present utility model. In addition, the terms "first", "second", etc. are only used for descriptive purposes, and cannot be understood as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Therefore, features defined as "first", "second", etc. may explicitly or implicitly include one or more of the features. In the description of the present utility model, unless otherwise specified, "multiple" means two or more.

[0019] In the description of the present invention, it should be noted that, unless otherwise clearly specified and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection, or it can be an indirect connection through an intermediate medium, or it can be the internal communication of two components. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood by specific circumstances.

[0020] The present invention will be described in detail below with reference to the accompanying drawings and in combination with embodiments.

[0021] Example

[0022] like Figure 1 , Figure 2 and Figure 3 As shown, a pipeline heat tracing and draining device for the production of large monomers of water reducing agent comprises a frame 1, a drain box 2 arranged above the frame 1, a collecting tank 3 arranged below the drain box 2 on the frame 1, a plurality of heat tracing pipes 4 arranged on the drain box 2, each heat tracing pipe 4 is equipped with a drain valve 41, the drain valve 41 is a vertical free float type drain valve, one end of the drain valve 41 away from the heat tracing pipe 4 extends into the collecting tank 3, and a top inlet 21 for the plurality of heat tracing pipes 4 to enter is arranged on the top of the drain box 2. With this structure, by connecting each heat tracing pipe 4 to a vertical free float type drain valve 41 individually, that is, changing the group steam draining to the individual steam draining, the pipeline heat tracing effect can be improved, the steam loss can be reduced; the water hammer phenomenon can be prevented, and the equipment failure rate can be reduced; and the draining condition of each heat tracing pipe 4 can be visually observed, and the failure condition can be timely checked and handled.

[0023] like Figure 1 and Figure 3 As shown, a low drain pipe 5 is provided at the bottom of the collecting tank 3. With this structure, the low drain pipe 5 can be used for drainage.

[0024] like Figure 1 and Figure 2 As shown, a straight pipe 6 is also provided in the drain tank 2, one end of the straight pipe 6 is connected to the part of the heating pipe 4 extending into the drain tank 2, and the other end of the straight pipe 6 extends into the collecting tank 3. This structure can be used to collect condensed water and observe the draining condition of the drain valve 41.

[0025] like Figure 1 and Figure 3 As shown, a plurality of fixed limiting rods 7 are arranged on the inner top of the collecting tank 3. With this structure, it is convenient to fix the limiting rods 7.

[0026] like Figure 1As shown, a hand valve 8 is provided on the steam trap 2, and the other end of the hand valve 8 is connected to a portion of the heat tracing pipe 4 located in the steam trap 2. With this structure, the hand valve 8 can be closed when the steam trap 41 fails, and the steam trap 41 can be isolated and replaced.

[0027] During specific use, each heating pipe 4 is individually connected to a vertical free-float steam trap 41 (model: CS41H-16C; diameter: 15mm; selected discharge capacity: 300KG / H; working pressure before the valve: 3barg), so that each heating pipe 4 can be drained separately without mutual offset; a collecting tank 3 is added under the rack 1 to collect condensed water; the straight section pipe 6 is set to collect condensed water and observe the drainage condition of the steam trap 41; a low discharge pipe 5 (diameter: 25mm) is added to the bottom of the collecting tank 3 for drainage.

[0028] The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. Any modifications, equivalent substitutions and improvements made within the spirit and principles of the present invention should be included in the protection scope of the present invention.

Claims

1. A pipeline heat tracing and draining device for the production of large monomers of water reducing agent, comprising a frame and a drain box arranged above the frame, characterized in that: The frame is provided with a collecting tank below the drain box, and a plurality of heating pipes are provided on the drain box. Each of the heating pipes is equipped with a drain valve, and one end of the drain valve away from the heating pipe extends into the collecting tank.

2. The pipeline heat tracing and draining device for the production of large monomers of water reducing agent according to claim 1, characterized in that: A low-drain pipe is arranged at the bottom of the collecting tank.

3. The pipeline heat tracing and draining device for the production of large monomers of water reducing agent according to claim 1, characterized in that: A straight pipe is also provided in the drain tank, one end of which is connected to a portion of the heating pipe extending into the drain tank, and the other end of which extends into the collecting tank.

4. The pipeline heat tracing and draining device for the production of large monomers of water reducing agent according to claim 1, characterized in that: A plurality of fixed limiting rods are arranged on the inner top of the collecting tank.

5. The pipeline heat tracing and draining device for the production of large monomers of water reducing agent according to claim 1, characterized in that: The drain tank is provided with a hand valve, and the other end of the hand valve is connected to a part of the heating pipeline located in the drain tank.

6. The pipeline heat tracing and draining device for the production of water reducing agent macro-monomers according to claim 1, characterized in that: The top of the drain box is provided with a top inlet for a plurality of the heating pipes to enter.

7. The pipeline heat tracing and draining device for the production of large monomers of water reducing agent according to claim 1, characterized in that: The steam trap is a vertical free float steam trap.