SUS304 Stainless Steel Plate Heat Exchanger For Pulp And Paper Industry
B60B Series Gasket Plate Heat Exchanger SUS304 Material For Pulp and Paper Industry
The history of gasketed plate heat exchangers (GPHEs) dates back to the early 20th century. The development of plate heat exThe history of gasketed plate heat exchangers (GPHEs) dates back to the early 20th century. The development of plate heat exchangers can be attributed to Dr. Richard Seligman, a German engineer who filed a patent for a plate heat exchanger design in 1923. His invention laid the foundation for the modern GPHEs we use today.
In the 1930s, the Swedish company Alfa Laval pioneered the commercialization of plate heat exchangers. They introduced the first gasketed plate heat exchanger in 1931, known as the "Plate-and-Gasket" heat exchanger. This design utilized plates with gaskets in between to create separate flow channels for the fluids being exchanged. Alfa Laval's innovation revolutionized the heat transfer industry by offering a compact and efficient alternative to traditional shell-and-tube heat exchangers.
Over the years, the design and technology of GPHEs have evolved and improved. In the 1960s, the introduction of laser welding technology enabled the production of more durable and reliable plate heat exchangers. Laser welding eliminated the need for gaskets in certain applications, leading to the development of fully welded plate heat exchangers.
GPHEs gained popularity in various industries due to their compact size, high heat transfer efficiency, and ease of maintenance. They found extensive use in HVAC systems, industrial processes, refrigeration, food and beverage processing, and many other applications where efficient heat transfer was essential.
Advancements in plate design, materials, and sealing technologies have further enhanced the performance and reliability of GPHEs. Today, GPHEs are available in a wide range of sizes, configurations, and materials to meet specific application requirements.
The continuous innovation and refinement of gasketed plate heat exchangers have made them a preferred choice for many heat transfer applications. Their history is marked by the contributions of engineers, inventors, and manufacturers who have worked to improve the efficiency and functionality of these heat exchangers over the years.
| TYPE | A(mm) | B(mm | C(mm | D(mm) | E(mm) | Height ( mm ) ( from middle of bottom to ground )(mm) |
MAX,LC (mm) |
Connector Path (mm) | Max Flow (m3/h) | Design Pressure (Mpa) | Max Pieces |
| B30B | N(2.5+X) | 180 | 60 | 480 | 357 | 62 | 500 | 32 | 18 | 1.0 | 95 |
| B60B | N2.0+X | 320 | 140 | 920 | 640 | 140 | 1200 | 50 | 36 | 1.6 | 250 |
| B60H | N(3.0+X) | 320 | 140 | 920 | 640 | 140 | 1200 | 50 | 36 | 1.6 | 203 |
| B100B | N(2.55+X) | 470 | 225 | 1069 | 719 | 183 | 1600 | 100 | 140 | 1.0/1.6/2.5 | 278 |
| B100H | N(3.95+X) | 470 | 225 | 1069 | 719 | 200 | 1600 | 100 | 140 | 1.0/1.6/2.5 | 180 |
| B150B | N(2.5+X) | 610 | 298 | 1815 | 1294 | 275 | 3000 | 150 | 360 | 1.0/1.6/2.5 | 600 |
| B150H | N(3.95+X) | 610 | 298 | 1815 | 1294 | 275 | 3000 | 150 | 360 | 1.0/1.6/2.5 | 600 |
| B200H | N(4+X) | 780 | 353 | 2260 | 1478 | 380 | 3000 | 200 | 600 | 1.0/1.6 | 480 |
| B250B | N(2.5+X) | 920 | 439 | 2895 | 1939 | 435 | 3000 | 250 | 750 | 1.0/1.6/2.5 | 500 |
| B350B | N(3.3+X) | 1150 | 596 | 2882 | 1842 | 470 | 4800 | 350 | 997 | 1.0/1.6 | 700 |
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