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S35 Donghwa Staineless Steel 304 316 Heat Exchanger Gasket Glue Type

Jiangyin M&C Heat Parts Co.,Ltd

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S35 Donghwa Staineless Steel 304 316 Heat Exchanger Gasket Glue Type

Country/Region china
City & Province wuxi jiangsu
Categories Gaskets
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Product Details

Marine industry M/E JACKET F.W COOLER GLUE TYPE STAINELESS STEEL 316L 0.5mm Plate Heat Exchanger Sondex/Donghwa S35

 

MC Plate Heat Exchanger Main Components

 

 

1. Head for connections and clamping the plate pack

2. Follower for clamping the plate pack

3. End support for supporting the top and bottom bars

4. Top bar for carrying and guiding the follower and plate pack

5. Bottom bar for guiding the follower and plate pack

6. Tie bars for clamping the plate pack between head and follower

7. Flow plate (Figure 1)

8. Flow gasket (Figure 1)

9. Nut for tie bar

10. Adjustable or fixed legs

11. Connector grid for additional fluid connector bosses

12. Connector bosses

 

H17 Gasket Parameter

 

 

Rubber TypeNBREPDMVITON/FKMHNBR
Application Temperature-20°C- +130°C-50°C-+150°C-30°C-+251°C-15°C- +160°C
Fluid Media

Water

Sea water

Mineral oil

Salt brine

Hot water

Steam

Acid

Alkali

High temperature resistance

Strong oxidants

Oil

Acid and alkali

High temperature mineral oil and water
FeatureEasier to replace than the traditional gasket, high pressure, high temperature, longer life, should not be leaked

 

Material of GasketOperating Temperature(℃)Suited Liquid kinds
NBR-15 to +135Water,sea water etc
EPDM-25 to +180Hot water,steam etc
FPM/VITON-55 to +230Acid,Caustic,Fluid
HNBR0 to +160Concentrated acid etc
 

 

 

Gasket failures are generally a result of:
• old age
• excessive exposure to ozone
• high operating temperature – above the temp. limit of the material
• exposure to pressure surges
• chemical attack
• physical damage, resulting from incorrect assembly work, or damage
• resulting from a misaligned plate (check the hanging system at the top of the plate for
distortion).
 
Plate Heat Exchanger Reasons of Performance Degradation

 

Decrease in performance is generally a result of:
• plate surfaces require cleaning or de-scaling
• pumps or associated controls have failed
• plate channels blocked
• liquid flows not as per design specification
• associated chiller / cooling tower / boiler under sized or dirty
• cooling water temperature to the exchanger is higher than the design
• heating media temperature to the exchanger is lower than the design
• steam flow not sufficient – control valve malfunction
• steam trap broken or jammed – unit becomes filled with condensate
• plate package has been assembled incorrectly
• unit is running in co-current flow, instead of counter current – check with contract
drawing and alter pipe work if necessary. Check direction of pump flows.
• air lock has developed in the plate package or pipe work
 

Goods Pictures

 

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