1. Classification by Flow Arrangement
Type | Flow Structure | Features | Typical Applications |
---|
Type I | Single-channel on both sides | Continuous flow path, low resistance, high heat transfer efficiency | Liquid-to-liquid, oil heating, water heating |
Type II | Single-channel + Multi-channel | One side is single-channel, the other side is divided into multiple channels; ideal for condensation | Steam condensation, gas-liquid heat exchange |
Type III | Multi-channel on both sides | Both sides are multi-channel; suitable for large flow, low pressure drop | Large water cooling systems, low-pressure applications |
2. Classification by Structure and Pressure Rating
Model | Structure | Typical Pressure Ratings | Features |
---|
B-type (Welded) | Fully welded, non-removable | 0.6 MPa / 1.6 MPa | Compact, sealed, ideal for clean fluids, low maintenance |
T-type (Detachable) | With removable end cover | 0.6 MPa / 1.6 MPa | Easy to open and clean, suitable for fouling or impure fluids |
Common Combined Models:
I 6B Type: Type I flow pattern, 0.6 MPa, fully welded
I 16B Type: Type I flow pattern, 1.6 MPa, fully welded
I 6T Type: Type I flow pattern, 0.6 MPa, detachable
I 16T Type: Type I flow pattern, 1.6 MPa, detachable
3. Key Technical Parameters Explained
1. Nominal Heat Exchange Area
This is the effective surface area available for heat transfer between fluids, typically measured in square meters (㎡).
Larger surface areas allow for greater heat transfer capacity.
2. Channel Spacing
Refers to the gap between two adjacent spiral plates, measured in millimeters (mm).
Small spacing (e.g., 5mm): Ideal for clean liquids, higher heat transfer rates
Larger spacing (e.g., 10–20mm): Suitable for gas or fluid with suspended solids; reduces clogging
3. Flow Velocity
The actual velocity of fluid within the channel, measured in meters per second (m/s).
Typical design range is 0.5–2.5 m/s:
4. Flow Rate at 1 m/s
Indicates the processing capacity (in m³/h) when the fluid flows at 1 meter per second.
It’s a standardized reference value for evaluating capacity across different models.
4. Parameter Table
公称换热 面积 | 通道间距 | 计算换热面积 | 流速1m/ces时 处理量 | 接管公称直径 | 重量(kg) |
|
Nominal Heat Exchange Area | Channel Spacing | Calculated Heat Exchange Area | Processing Capacity at 1 m/s Flow Velocity | Nominal Pipe Diameter | Weight (kg) |
|
m² | mm | m² | m³/h | mm | I 6B Type | I 16B Type |
1 | 6 | 1 | 3.89 | 40 | 44 | 50 |
2 | 6 | 2.1 | 78 | 85 |
4 | 6 | 4.4 | 8.2 | 50 | 131 | 135 |
10 | 4.5 | 17.3 | 80 | 129 | 133 |
10 | 4.8 | 13.7 | 70 | 161 | 205 |
8 | 6 | 7.3 | 8.21 | 50 | 212 | 215 |
10 | 7.85 | 17.3 | 80 | 235 | 273 |
10 | 7.3 | 20.9 | 237 | 275 |
10 | 6 | 11.1 | 8.21 | 50 | 295 | 355 |
10 | 11.5 | 17.3 | 80 | 315 | 405 |
10 | 11.2 | 20.9 | 305 | 395 |
15 | 6 | 16.9 | 12.54 | 70 | 415 | 490 |
10 | 14.72 | 17.3 | 80 | 405 | 575 |
10 | 15 | 28.1 | 400 | 570 |
14 | 15.6 | 39.3 | 100 | 505 | 680 |
20 | 6 | 21.7 | 8.21 | 50 | 540 | 710 |
10 | 21 | 20.9 | 80 | 555 | 735 |
14 | 20.9 | 39.3 | 100 | 660 | 830 |
25 | 10 | 26.6 | 29.9 | 80 | 610 | 950 |
14 | 26.9 | 39.2 | 100 | 720 | 1060 |
30 | 10 | 28.2 | 28.1 | 750 | 1180 |
14 | 32.2 | 39.2 | 980 | 1370 |
40 | 10 | 45.4 | 35.3 | 1130 | 1515 |
14 | 40.2 | 19.4 | 125 | 1200 | 1630 |
50 | 10 | 53.9 | 35.3 | 100 | 1360 | 1755 |
60 | 10 | 61.05 | 1920 | 2112 |
14 | 60.08 | 49.4 | 125 | 2000 | 2200 |
80 | 10 | 81.83 | 35.3 | 100 | 2560 | 2816 |
14 | 80.9 | 49.4 | 125 | 2667 | 1934 |
100 | 10 | 101.9 | 35.3 | 100 | 3200 | 3520 |
14 | 100.06 | 49.4 | 125 | 3333 | 3666 |
120 | 10 | 115.5 | 35.3 | 100 | 3870 | 4257 |
14 | 119 | 49.4 | 125 | 4020 | 4422 |
130 | 14 | 128.8 | 4241 | 4665 |
18 | 129.09 | 63.5 | 150 | 4462 | 4908 |
150 | 14 | 148.1 | 49.4 | 125 | 4702 | 5172 |
18 | 148.2 | 63.5 | 150 | 4962 | 5458 |
5. Model Selection Recommendations
Operating Condition | Recommended Model |
---|
Clean media, continuous operation | B-type (welded) |
Fouling or dirty fluids | T-type (detachable) |
High heat exchange efficiency, low pressure drop | Type I |
Condensation or gas-liquid heat transfer | Type II |
Large flow rate, low pressure systems | Type III |
Proper model selection ensures efficient heat transfer, reduces maintenance, and extends equipment lifespan.
Conclusion
Spiral Plate Heat Exchangers offer multiple configurations to meet diverse industrial needs. Understanding the differences between Type I, II, III, as well as structural models like B-type and T-type, along with interpreting parameters such as channel spacing, flow velocity, and processing capacity, is key to effective application and selection.
Need a custom solution or detailed specification sheet? Contact our engineering team for a tailored recommendation based on your operating conditions.