S-TF40A-D Tubular Heat Exchanger
S-TF40A-D Tubular Heat Exchanger Operation
The S-TF40A-D tubular heat exchanger is a heat exchanger consisting of three or four concentric tubes. The product flows through the central annular space while the service does it through the outer and inner channels.
S-TF40A-D Tubular Heat Exchanger Applications
Heating processes (pasteurization, sterilization, UHT, etc.) or cooling of products with high viscosity. The products may contain fibers or particles. This model is designed for products such as chocolates, butters, tomato paste, jams, pudding, custards, rice with milk, baby food and yogurt, among others.
S-TF40A-D Tubular Heat Exchanger Technical Data Sheet
Standard Design Conditions
Design Temperature: 180°C
Design Pressure: 10 barg
For higher design pressure or temperatures as well as hazardous fluids, the heat exchangers can be checked according to AD 2000 Merkblätt, ASME VIII Div.1, PD 5500, EN13445 or by Finite Elements Analysis and CE certificated by individual inspection modules.
Included: 3.1 Quality certificate and CE Marking according 2014/68/UE.
Shell side: 52mm – 204mm
Inner tubes: ≥ 16 mm
Lenght: 1-1,5-2-3-6 m
Other available sizes under request.
Shell and tubes:
Stainless Steel 304 or 316L
Other materials available on request (2205, 2507, 254 SMO among others)
Other connections available on request.
Product channel designed to promote CIP (Clean In Place)
Mineral wool coated in 304 stainless steel metal sheet.
Stainless Steel 304.
The type and shape of the frame will be selected to fit the needs of each project. If required, equipment may be sloping for better drainage.
In case the equipment contains several units in series, SACOME can provide the interconnections for the product channel and the service channel. This model is specially designed to get compact frames.
SACOME TYPE DEFINITION
Annular space and axial product inlet
Removable inner tube
Without / with expansion joint
Ø TUBE 3 (mm)
Ø TUBE 2 (mm)
Ø TUBE 1 (mm)
Ø TUBE 0 (mm)
Nominal lenght (mm)
Shell side material
Tube side material
Corrugation indicator (Hard/Soft/Plain)
Hairpin heat exchangers have a more efficient and economical design compared to a multiple pass heat exchanger when the process requires a temperature crossing between the cold and hot fluid.
All productive processes can be classified according to how the raw material input stage is carried out, and how the product is subsequently obtained. These processes are basically divided into continuous processes and batch processes, although we can find variations combining features from both processes.
The starting point in the design of any heat exchange system is the definition of how the thermal properties evolve throughout the process, whether heating or cooling.