In the design process, the outer diameter (Do) of the floating head tube sheet must be considered. This diameter should be smaller than the inner diameter (Di) of the shell. A recommended gap (b1) between the floating head tube sheet and the inner wall of the shell is generally 3-5mm. This allows the tube bundle to be pulled out of the shell after removing the hook ring, facilitating inspection and cleaning. Assembly of the floating head cover can only take place after the tube bundle is inserted, so the necessary space for the floating head cover during assembly should be considered in the design.

 

The hook ring plays a crucial role in ensuring the sealing of the floating head end and preventing leakage between media. With advancements in the design and manufacturing technology of floating head heat exchangers and the accumulation of long-term usage experience, the structure of the hook ring has been continuously improved and perfected.

 

The hook ring is generally of an open structure, requiring reliable sealing, simple and compact structure, and ease of manufacturing and disassembly.

 

Floating head heat exchangers, with their high reliability and wide adaptability, have accumulated rich experience during long-term use, continuously promoting their own development. Thus, they continue to dominate among various types of heat exchangers.

 

 

Floating Head Heat Exchanger Pros:

1. The tube bundle can be pulled out for easy cleaning of tube and shell sides.

2. Not restricted by temperature differences between media.

3. Can operate at high temperatures and pressures, generally up to 450 degrees Celsius and 6.4 MPa.

4. Suitable for applications where scaling is severe.

5. Applicable in situations where the tube side is prone to corrosion.

 

Floating Head Heat Exchanger Cons:

1. Small floating heads are prone to internal leakage.

2. High metal material consumption, with a cost 20% higher.

3. Complex structure.

 

 

The manufacturing process of heat exchange equipment involves the selection and testing of materials, chemical composition testing, and mechanical performance testing. After ensuring the steel plates chemical composition and mechanical properties meet the requirements, the

 

 plate undergoes straightening using methods such as manual straightening, mechanical straightening, and flame straightening.

Material preparation – Marking – Cutting – Edge processing (inspection for flaws) – Forming – Pairing – Welding – Weld quality inspection – Assembly welding – Pressure testing

 

 

Chemical equipment undergoes material inspections not only before manufacturing but also at various stages during the manufacturing process.

 

 

One end of the tube sheet in a floating head heat exchanger is fixed between the shell and the tube box, while the other end of the tube sheet can move freely within the shell. This characteristic is visible in the field. The thermal expansion between the shell and the tube bundle is free, and the tube bundle can be pulled out for easy cleaning between tubes and inside tubes. The disadvantage is that the structure is complex, and the cost is higher (20% higher than fixed tube sheet heat exchangers). Leakage at the floating head during operation is not easy to detect. The floating head heat exchanger is suitable for conditions where there is a significant temperature difference between the shell and tube bundle or where the shell-side medium is prone to scaling.

 

 

In the production process, due to the flushing of the tube sheet in the floating head heat exchanger by water, cavitation, and corrosion of trace chemical media, leaks often occur at the weld seams of the tube sheet. This leads to the mixing of water and chemical materials, making it difficult to control the production process temperature and resulting in the production of other products, significantly affecting product quality and reducing product grades. After leaks occur at the tube sheet weld seams of the condenser, enterprises usually use traditional welding methods for repair. Internal stresses are easily generated in the tube sheet, and they are difficult to eliminate, causing leaks in other heat exchangers. Enterprises use pressing, inspecting equipment repair conditions, repeatedly welding, experimenting, and it takes several days for 2 to 4 people to complete the repair. After a few months of use, corrosion occurs again at the tube sheet weld seams, leading to wasted manpower, materials, and finances, increasing production costs. By using high molecular composite materials for corrosion resistance and erosion resistance, and by protecting new heat exchangers in advance, not only are welding and sanding issues effectively addressed, but chemical corrosion of heat exchanger metal surfaces and weld points is also avoided during subsequent periodic maintenance. Even if leaks occur after use, they can be repaired in a timely manner using technology, avoiding long-term welding repairs that affect production. It is this fine management that greatly reduces the probability of heat exchanger leaks, not only reducing equipment procurement costs but also ensuring product quality, production time, and increasing product competitiveness.