Cooler for insulating material
By using a plate-type and shell-and-tube-type heat exchange system and an open channel design, the problems of high energy consumption and low heat utilization rate of spray dryers are solved, achieving efficient heat recovery and improved material yield, thereby increasing production efficiency.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- ZIBO QILU HIGH VOLTAGE INSULATION MATERIALS CO LTD
- Filing Date
- 2025-04-16
- Publication Date
- 2026-04-24
AI Technical Summary
In the existing insulation material production process, spray dryers have high energy consumption and low heat utilization rate. Heat is discharged with the exhaust gas, requiring additional equipment to improve efficiency, and the material yield is low.
The heat exchange system adopts a simulated plate and shell-and-tube heat exchanger system, with an open channel and condensate separation structure to achieve efficient separation and recovery of hot air and condensate. The simulated plate heat exchanger system is used to improve heat exchange efficiency, and tube-side components are installed in the condensate for further heat recovery.
It improves heat utilization, reduces energy consumption, increases material yield, avoids the need for subsequent liquid separation buffer tanks, and improves production efficiency.
Smart Images

Figure CN224163053U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to a cooler for insulating materials, belonging to the field of cooling equipment. Background Technology
[0002] Spray dryers are used in the production of insulating materials. These dryers are energy-intensive, requiring high-temperature hot air to rapidly evaporate moisture. Some heat is discharged with the exhaust gas, resulting in a thermal efficiency typically of only 30% to 50%, necessitating additional equipment to improve efficiency. Furthermore, the yield of spray dryers is only around 80%, meaning some material is carried out with the exhaust gas, requiring equipment for material recovery or treatment. Summary of the Invention
[0003] Based on the problems described in the background, the problem that this utility model aims to solve is:
[0004] How to improve the utilization rate of heat in hot and humid air and subsequent condensate.
[0005] To achieve the above objectives, this utility model provides the following technical solution:
[0006] A cooler for insulating materials includes a cooler shell, an air heat exchange section, and a condensate heat exchange section. The air heat exchange section is located at the upper interior of the cooler shell, and the condensate heat exchange section is located at the lower interior of the cooler shell. The air heat exchange section adopts a plate-like heat exchange system and is divided into a high-temperature side and a low-temperature side. The bottom of the high-temperature side has an open channel that communicates with the interior space of the cooler shell. The high-temperature side inlet and the low-temperature side outlet are located at the upper part of the air heat exchange section, and the low-temperature side inlet is located at the lower part of the air heat exchange section. Hot air enters the high-temperature side through the high-temperature side inlet and then leaves the air heat exchange section through the open channels of each high-temperature side, and is discharged through the air outlet at the top of the cooler shell. The condensate heat exchange section adopts a shell-and-tube heat exchange system and has tube-side components immersed in condensate. The bottom of the cooler shell has a condensate outlet, and both ends of the tube-side components have tube-side outlets and tube-side inlets that penetrate the cooler shell. The tube-side outlet is connected to the low-temperature side inlet.
[0007] Hot air enters each high-temperature side through the high-temperature inlet. After exchanging heat with the adjacent low-temperature side, the hot air, mixed with water vapor, cools down to generate low-temperature air and condensate. The air and condensate are discharged together into the cooler shell through an open channel. Unlike ordinary condensate and air separation, the air and condensate move in the same direction within the high-temperature side. Air and gravity cause the condensate droplets to accelerate downwards and converge. When the air flows upwards to the air outlet, the condensate already has a certain initial velocity, easily overcoming the upward force of the air and converging at the bottom of the cooler shell. At the same time, the tube-side components are completely immersed in the condensate, with a condensate outlet at the bottom to directly supply the cooled condensate to the water-requiring process before drying, and can also recover a small amount of material from the condensate.
[0008] Preferably, the inner walls on both sides of the high-temperature side are provided with guide plates running from top to bottom. The guide plates help to collect condensate faster and better, resulting in larger condensate droplets that are more difficult for air to carry out of the cooler.
[0009] Preferably, the tube assembly has a support plate in the middle.
[0010] Preferably, a support base is connected to the lower part of the cooler housing.
[0011] Preferably, a level gauge is provided at the bottom of the cooler housing.
[0012] The beneficial effects of this utility model are:
[0013] This invention efficiently recovers unused heat from spray dryers; it employs a plate-type heat exchange system with an open channel design, ensuring high heat exchange efficiency while improving the separation of air and condensate. No subsequent liquid separation buffer tank is required. Attached Figure Description
[0014] Figure 1 This is a front cross-sectional view of the present invention.
[0015] Figure 2 This is a schematic diagram of the rear cross-section of the present invention.
[0016] In the diagram: 1 is the cooler shell; 2 is the air heat exchange section; 3 is the tube-side assembly; 4 is the support base; 5 is the level gauge; 21 is the high-temperature side; 22 is the low-temperature side; 23 is the high-temperature side inlet; 24 is the open channel; 25 is the low-temperature side inlet; 26 is the low-temperature side outlet; 27 is the air outlet; 28 is the guide plate; 31 is the tube-side outlet; 32 is the support plate; 33 is the condensate outlet. Detailed Implementation
[0017] Example 1: A cooler for insulating materials includes a cooler shell 1, an air heat exchange section 2, and a condensate heat exchange section. The air heat exchange section 2 is located at the upper interior of the cooler shell 1, and the condensate heat exchange section is located at the lower interior of the cooler shell 1. The air heat exchange section 2 adopts a plate-type heat exchange system and is divided into a high-temperature side 21 and a low-temperature side 22. The bottom of the high-temperature side 21 has an open channel 24 that communicates with the internal space of the cooling shell 1. The high-temperature side inlet 23 and the low-temperature side outlet 26 are located at the upper part of the air heat exchange section 2, and the low-temperature side inlet 25 is located at the lower interior of the air heat exchange section 2. The lower part of the hot section 2; hot air enters the high-temperature side 21 through the high-temperature side inlet 23, and then leaves the air heat exchange section 2 through the open channels 24 of each high-temperature side 21, and finally exits through the air outlet 27 at the top of the cooler shell 1. The condensate heat exchange section adopts a shell-and-tube heat exchange system. The condensate heat exchange section is equipped with tube-side components 3, which are immersed in condensate. The bottom of the cooler shell 1 is provided with a condensate outlet 33. The tube-side components 3 are provided with tube-side outlets 31 and tube-side inlets that penetrate the cooler shell 1 at both ends. The tube-side outlets 31 are connected to the low-temperature side inlet 25.
[0018] The inner walls on both sides of the high-temperature side 21 are provided with guide plates 28 running from top to bottom.
[0019] The tube assembly 3 has a support plate 32 in the middle.
[0020] A support base 4 is connected to the lower part of the cooler housing 1.
[0021] A level gauge 5 is provided at the bottom of the cooler housing 1.
[0022] Hot air enters the air heat exchange section through the high-temperature side inlet 23, exchanges heat with the low-temperature side 22, and then enters the cooler through the open channel 24. At this time, the cooled air separates from the condensate, the condensate falls to the bottom of the cooler, and the air is discharged through the exhaust outlet 27. Coolant enters the tube-side assembly 3 through the tube-side inlet, exchanges heat with the condensate, and then enters the low-temperature side 22 through the low-temperature side inlet 25. After heat exchange, it is discharged through the low-temperature side outlet 26.
Claims
1. A cooler for insulating material, characterized in that The system includes a cooler shell (1), an air heat exchange section (2), and a condensate heat exchange section. The air heat exchange section (2) is located at the upper part of the cooler shell (1), and the condensate heat exchange section is located at the lower part of the cooler shell (1). The air heat exchange section (2) adopts a plate-type heat exchange system, which is divided into a high-temperature side (21) and a low-temperature side (22). The bottom of the high-temperature side (21) is provided with an open channel (24), which is connected to the internal space of the cooler shell (1). The high-temperature side inlet (23) and the low-temperature outlet (26) are located at the upper part of the air heat exchange section (2), and the low-temperature side inlet (25) is located at the lower part of the air heat exchange section (2). The air enters the high-temperature side (21) through the high-temperature side inlet (23), then leaves the air heat exchange section (2) through the open channels (24) of each high-temperature side (21), and finally exits through the air outlet (27) at the top of the cooler shell (1). The condensate heat exchange section adopts a shell-and-tube heat exchange system. The condensate heat exchange section is equipped with a tube-side assembly (3). The tube-side assembly (3) is immersed in condensate. The cooler shell (1) is equipped with a condensate outlet (33) at the bottom. The tube-side assembly (3) is equipped with a tube-side outlet (31) and a tube-side inlet at both ends that penetrate the cooler shell (1). The tube-side outlet (31) is connected to the low-temperature side inlet (25).
2. The cooler for insulation material according to claim 1, wherein The inner walls on both sides of the high-temperature side (21) are provided with guide plates (28) running from top to bottom.
3. The cooler for insulation material according to claim 1, wherein The tube assembly (3) has a support plate (32) in the middle.
4. The cooler for insulation material according to claim 1, wherein A support base (4) is connected to the lower part of the cooler housing (1).
5. The cooler for insulation material according to claim 1, wherein A level gauge (5) is provided at the bottom of the cooler housing (1).