CN206818021U - Horizontal discontinuous stagnation serpentine tube membrane wall powder material efficient heat exchange device - Google Patents

Abstract

The utility model discloses a kind of laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger, including：Body of heater and the multiple vertical coiled pipe membrane wall structures being packed in the body of heater, the size of multiple coiled pipe membrane wall structures is identical, and each coiled pipe membrane wall structure includes：A piece pipeline and multiple fins being vertically arranged, the pipeline be bent to form it is snakelike, it is described it is snakelike be made up of multiple curved pipes in the spaced horizontal tube of vertical direction and connection adjacent level pipe, be fixed with a fin per between 2 adjacent horizontal tubes.Its falling speed is constantly by interruption stagnation in the utility model material dropping process, falling speed is greatly lowered, material-heat-exchanging efficiency increases substantially in unit length flow, simultaneously, because coiled pipe membrane wall structure adds extended surface, rate of metal improves, and manufacturing cost is greatly lowered.

Description

Horizontal discontinuous stagnation serpentine tube membrane wall powder material efficient heat exchange device

technical field

The utility model belongs to the technical field of waste heat utilization of powdery particles, in particular relates to a horizontal intermittent stagnation serpentine tube-film wall powder high-efficiency heat exchange device.

Background technique

The existing direct heat exchange device between powder and solid wall adopts the form of multi-layer water jacket. Cooling water is passed into the inside of the water jacket, and the water jacket is placed vertically. Down flow, the water jacket is formed by two-layer plates through spot welding, and it is called a water jacketed plate heat exchanger in the industry. At present, the water jacketed plate heat exchanger has the following technical defects:

1) The cooling water is completely penetrated in the water jacket, which cannot form a counterflow with the material, and cannot realize the cascade extraction of waste heat, which seriously restricts the utilization efficiency of waste heat.

2) The water jacket is spot-welded with two layers of plates. The resistance of the material circulation channel between the two layers of water jacket is too small, the material is close to free fall, the flow rate is too fast, the heat transfer efficiency of the material per unit length of the process is too low, and the metal waste is serious.

3) The material is close to free fall, the flow rate is too fast, the wear of the particles on the solid surface is serious, and the life of the heat exchanger is short.

The existing direct heat exchange device between powder and solid wall also has a structure in which horizontally staggered tube bundles are used, and the powder moves down and laterally scours the tube bundles outside the tubes by its own weight (staggered buried tube heat exchanger). The technical defect is that the material is easy to bridge, which affects the forward movement of the material in the heat exchanger.

Aiming at the problems existing in the existing water-jacketed plate heat exchangers and staggered buried tube heat exchangers, a utility model is a horizontal discontinuous stagnation serpentine tube-film wall powder material high-efficiency heat exchange device.

Contents of the invention

Aiming at the deficiencies of the prior art, the purpose of the utility model is to provide a horizontal discontinuous stagnation serpentine tube-membrane wall powder high-efficiency heat exchange device.

The purpose of this utility model is achieved through the following technical solutions.

A horizontal discontinuous stagnation serpentine tube membrane wall powder high-efficiency heat exchange device, comprising: a furnace body and a plurality of vertical serpentine tube membrane wall structures fixed in the furnace body, the furnace body A feed inlet is formed at the upper end for feeding solid particles into the furnace body, and a discharge port is formed at the lower end of the furnace body;

A plurality of serpentine tube-membrane wall structures have the same size, each of the serpentine tube-membrane wall structures includes: a pipe and a plurality of vertically arranged fins, the pipe is bent to form a serpentine shape, the The serpentine shape is composed of a plurality of horizontal tubes arranged at intervals in the vertical direction and arc-shaped tubes connected to adjacent horizontal tubes. A fin is fixed between every two adjacent horizontal tubes, wherein the fins are up and down. The edges at both ends are seamlessly connected with the outer wall of the horizontal pipe;

A plurality of the serpentine tube-membrane wall structures are parallel to each other, and horizontal tubes of adjacent serpentine tube-membrane wall structures are interlaced; the water inlet of the pipeline is located below the water outlet.

In the above technical solution, a discharge valve is installed on the discharge port.

In the above technical solution, the distance between adjacent horizontal tubes of each serpentine tube-membrane wall structure is the same.

In the above technical solution, the position of the horizontal tube corresponds to the middle position of a fin of the serpentine tube-membrane wall structure adjacent to the horizontal tube.

In the above technical solution, it also includes: a general water inlet pipe, which extends into the furnace body and communicates with a plurality of water inlets of the serpentine tube-membrane wall structure respectively.

In the above technical solution, it also includes: a main water outlet pipe, which extends into the furnace body and communicates with a plurality of water outlets of the serpentine tube-membrane wall structure respectively.

In the above technical solution, the plurality of water inlets of the serpentine tube-membrane wall structure protrude out of the furnace body and communicate with the water inlet source.

In the above technical solution, the plurality of water outlets of the serpentine tube-membrane wall structure extend out of the furnace body and communicate with the drainage device.

Compared with the prior art, the beneficial effects of the utility model are:

1) Materials (solid particles) and cooling water can form a countercurrent structure, which greatly improves the cascade quality of waste heat extraction and waste heat utilization efficiency.

2) During the falling process of the material, its falling speed is continuously stagnated intermittently, the falling speed is greatly reduced, and the heat exchange efficiency of the material per unit length of the process is greatly improved. The utilization rate is improved, and the manufacturing cost is greatly reduced.

3) During the falling process of the material, its falling speed is continuously stagnated intermittently, the falling speed is greatly reduced, the wear of the tube wall is greatly improved, and the life of the heat exchange device is greatly improved.

4) During the falling process of the material, its falling speed is continuously stopped intermittently. Due to the continuous strong disturbance in the flow process, the mixing speed of hot and cold particles inside the powdery material is fast and the uniformity is high, which greatly improves the powder (solid particle) The heat transfer coefficient with the tube wall.

Description of drawings

Fig. 1 is the cross-sectional view (horizontal transverse direction) of the utility model's horizontal discontinuous stagnation serpentine tube film type wall powder material high-efficiency heat exchange device;

Fig. 2 is the schematic diagram of the serpentine tubular membrane type wall structure of the present utility model;

Fig. 3 is a cross-sectional view (horizontally and vertically) of the utility model's horizontal intermittent stagnation serpentine tube-film wall powder high-efficiency heat exchange device.

Among them, 1 is a solid particle, 2 is a furnace body, 3 is a serpentine tube membrane wall structure, 3-1 is a pipeline, 3-1-1 is a horizontal tube, 3-1-2 is an arc tube, 3-2 4 is a discharge valve, 5 is a feed inlet, 6 is a water outlet, 7 is a water inlet, and 8 is a flow track of solid particles.

detailed description

The following is a further description of the horizontal intermittent stagnation serpentine tube-film wall powder material high-efficiency heat exchange device of the present invention in conjunction with the accompanying drawings.

As shown in Figures 1 to 3, it includes: a furnace body 2 and a plurality of vertical serpentine tube membrane wall structures 3 fixed in the furnace body 2, and a feed inlet 5 is formed on the upper end of the furnace body 2 for Put solid particles 1 into the furnace body 2, and a discharge port is formed at the lower end of the furnace body 2; a discharge valve 4 is installed on the discharge port.

Each serpentine tube-membrane wall structure 3 includes: a pipe 3-1 and a plurality of vertically arranged fins 3-2, the pipe 3-1 is bent to form a serpentine shape, and the serpentine shape is composed of a plurality of fins 3-2 in the vertical direction. Composed of horizontal tubes 3-1-1 arranged at intervals and arc-shaped tubes 3-1-2 connected to adjacent horizontal tubes 3-1-1, fixed between every two adjacent horizontal tubes 3-1-1 There is a fin 3-2, wherein, the upper and lower edges of the fin 3-2 are seamlessly connected with the outer wall of the horizontal tube 3-1-1.

The distance between the adjacent horizontal tubes 3-1-1 of each pipeline is the same, and the dimensions of the plurality of serpentine tube-membrane wall structures 3 are the same and parallel to each other. The horizontal tubes 3-1-1 of the adjacent serpentine tube-membrane wall structures 3 are interlaced, and the position of the horizontal tubes 3-1-1 is the same as that of the adjacent serpentine tube-membrane wall structures 3 of the horizontal tubes 3-1-1. The middle position of a fin 3-2 is corresponding.

The water inlet 7 of the pipeline 3-1 is located below the water outlet 6.

The water flow mode of the water inlet 7 and the water outlet 6 can be one of the following two situations:

1. Including: a main water inlet pipe and a main water outlet pipe, the main water inlet pipe extends into the furnace body 2 and communicates with the water inlets 7 of multiple (all) serpentine tube membrane wall structures 3 respectively. The total water outlet pipe extends into the furnace body 2 and communicates with the water outlets 6 of a plurality of serpentine tube membrane wall structures 3 (not shown in the figure).

2. The water inlets 7 of multiple (all) serpentine tube-membrane wall structures 3 protrude out of the furnace body 2 and communicate with the water inlet source (not shown in the figure). The water outlets 6 of the plurality of serpentine tube membrane wall structures 3 extend out of the furnace body 2 and communicate with the drainage device (not shown in the figure), as shown in FIG. 3 .

Technical scheme of the utility model:

1) Change the vertically placed water jacket to a vertically placed serpentine tube-membrane wall structure 3, the horizontal tube 3-1-1 part of the serpentine tube-membrane wall structure 3 is set parallel to the horizontal plane, and the working medium is placed in the tube 3 -1 flows from bottom to top, and the powder flows from top to bottom between the two serpentine tube membrane wall structures 3 by its own weight, and a countercurrent flow is formed between the hot and cold substances. If the temperature of the powder is high enough, the heat exchange device When arranged in sections, the working fluid can be heated into medium-temperature and medium-pressure steam, which greatly improves the efficiency of waste heat utilization.

2) The horizontal tubes 3-1-1 of two adjacent serpentine tube membrane wall structures 3 are staggered in the height direction, and the powder flow channel forms an S-shaped channel, and the powder flows in the S-shaped channel every time during the falling process When turning, its falling speed is stagnated to 0, that is, its falling speed is continuously stagnated intermittently during the material falling process, the falling speed is greatly reduced, and the heat transfer efficiency of the material per unit length process and the wear of the pipe wall are greatly improved.

Structural features of the utility model:

The horizontal discontinuous stagnant snake-shaped tube-film wall powder material high-efficiency heat exchange device is composed of multiple sets of vertically arranged snake-shaped tube-film wall structures 3, the cooling water flows from bottom to top in the pipe 3-1, and the solid particles 1 are formed by The feed inlet 5 enters the furnace body, and the horizontal tubes of two adjacent serpentine tube membrane wall structures 3 are staggered to form an S-shaped channel for powdery materials. The powdery material moves downward continuously in the S-shaped channel. During the downward movement, the solid particles meet the horizontal tube and the velocity is stagnated to 0, and then bypass the horizontal tube and start to move downward at an accelerated rate. When encountering the adjacent serpentine tube film The velocity behind the horizontal tube of the type wall structure 3 is once again stagnated to 0, so it moves down in the process of being continuously stagnated until the heat exchange ends, leaving the furnace body, and the solid particle flow track 8 is shown in Figure 2, the furnace body The flow of medium solid particles (powder materials) is controlled by the discharge valve 4. The furnace body is filled with insulation material and has the function of heat insulation and sealing.

The utility model has been described as an example above. It should be noted that, without departing from the core of the utility model, any simple deformation, modification or other equivalent replacements that can be made by those skilled in the art without costing creative labor all fall into the Into the scope of protection of the utility model.

Claims (8)

1. A kind of 1. laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger, it is characterised in that including：Body of heater (2) and The multiple vertical coiled pipe membrane wall structures (3) being packed in the body of heater (2), the upper end of the body of heater (2) is formed with entering Material mouth (5), for the input solid particle (1) into the body of heater (2), in the lower end of the body of heater (2) formed with discharging opening；

   The size of multiple coiled pipe membrane wall structures (3) is identical, and each coiled pipe membrane wall structure (3) includes：A piece pipe Road (3-1) and multiple fins (3-2) being vertically arranged, the pipeline (3-1) be bent to form it is snakelike, it is described it is snakelike by multiple perpendicular Nogata forms to the curved pipe (3-1-2) of spaced horizontal tube (3-1-1) and connection adjacent level pipe (3-1-1), A fin (3-2) is fixed between per 2 adjacent horizontal tubes (3-1-1), wherein, the side of fin (3-2) upper and lower ends It is to be seamlessly connected between the outer wall of edge and horizontal tube (3-1-1)；

   Multiple coiled pipe membrane wall structures (3) are parallel to each other, and the horizontal tube (3- of adjacent coiled pipe membrane wall structure (3) It is 1-1) interlaced；The water inlet (7) of the pipeline (3-1) is located at the lower section of delivery port (6).
2. 2. laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger according to claim 1, it is characterised in that One discharge valve (4) is installed on the discharging opening.
3. 3. laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger according to claim 2, it is characterised in that The distance between the adjacent level pipe (3-1-1) of each coiled pipe membrane wall structure (3) is identical.
4. 4. laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger according to claim 3, it is characterised in that The position of the horizontal tube (3-1-1) and a fin (3-2) for the adjacent coiled pipe membrane wall structure (3) of the horizontal tube (3-1-1) Centre position it is corresponding.
5. 5. laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger according to claim 4, it is characterised in that Also include：One water inlet manifold road, the water inlet manifold road stretch into the body of heater (2) and respectively with multiple coiled pipe membrane types Water inlet (7) connection of wall construction (3).
6. 6. laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger according to claim 5, it is characterised in that Also include：One total outlet pipe road, the total outlet pipe road stretch into the body of heater (2) and respectively with multiple coiled pipe membrane types The connection of the delivery port (6) of wall construction (3).
7. 7. laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger according to claim 4, it is characterised in that The water inlet (7) of multiple coiled pipe membrane wall structures (3) extend out to the body of heater (2) outside and connected with feed source.
8. 8. laterally intermittent stagnation coiled pipe membrane wall powder high-efficiency heat exchanger according to claim 7, it is characterised in that The delivery port (6) of multiple coiled pipe membrane wall structures (3) extend out to the body of heater (2) outside and communicated with drainage arrangement.