Titanium Heat Exchange Titanium Heat Exchange Titanium Heat Exchange Titanium Heat Exchange Titanium Heat Exchange Titanium Heat Exchange
Titanium Heat Exchange Titanium Heat Exchange Titanium Heat Exchange Titanium Heat Exchange Titanium Heat Exchange Titanium Heat Exchange

Titanium Heat Exchange

18.00 - 60.00 USD ($)/Kilograms

Product Details:

  • Size 6000*600*2000mm
  • Usage titanium heat exchanger
  • Max Pressure 1000 m3/hr
  • Thickness 2mm Millimeter (mm)
  • Air Volume 1 m3/hr
  • Product Type titanium condenser
  • Width 600 Millimeter (mm)
  • Supply Ability : 20 Kilograms Per Month
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Price And Quantity

  • 1set Kilograms
  • 18.00 - 60.00 USD ($)/Kilograms

Product Specifications

  • titanium condenser
  • 1 m3/hr
  • 0.2mpa
  • 6000*600*2000mm
  • 41.6 sq m/s
  • 2mm Millimeter (mm)
  • tube Heat Exchanger
  • 1000 m3/hr
  • titanium heat exchanger
  • 511 Kilograms (kg)
  • 600*600*2000 Millimeter (mm)
  • silver
  • New
  • 600 Millimeter (mm)
  • 600 Millimeter (mm)
  • Low temperature
  • 600 Millimeter (mm)
  • 2000 Millimeter (mm)

Trade Information

  • shanghai guangzhou tianjing
  • Paypal, Western Union, Telegraphic Transfer (T/T), Letter of Credit at Sight (Sight L/C), Letter of Credit (L/C), Cash in Advance (CID), Cash Advance (CA), Cash on Delivery (COD), Cash Against Delivery (CAD)
  • 20 Kilograms Per Month
  • 2 Week
  • Contact us for information regarding our sample policy
  • Pack with wooden case
  • Middle East, Western Europe, Eastern Europe, South America, North America, Central America, Australia, Asia
  • All India
  • ISO9001:2015 BV SGS

Product Description

Titanium heat exchange advantages
  • The cooling water can be recycled without being contaminated by secondary steam;
  • Since the water is closed in the condenser without the impact of water, unlike the cooling water used by the water jet, the sound of water is exposed to the outside;
  • independent of the space height constraints, vertical installation or horizontal installation, unlike the atmospheric condenser is limited by the space height (atmospheric condenser installation height is above 10.5m).
  • the cooling effect is not worse than the direct condenser, and easy to control.

The impact factors of the heat exchange

The heat transfer area of the condenser must be sufficient, otherwise it is difficult for the secondary steam entering the condenser to be completely cooled to increase the evaporation temperature, thereby reducing the production capacity of the tubular condenser.
Here, in addition to the heat transfer coefficient of the condenser should be selected properly, some factors that directly affect the heat transfer effect when calculating the heat transfer area of  the condenser are not negligible.

3.1, the effect of the heat released by the condensate on the condenser effect

The condensed water in the shell side of the multi-effect evaporation equipment is generally discharged from the condenser together with the condensed water in the shell side of the condenser (this is not only simple in structure, but also mainly energy saving). Since the condensed water temperature in the shell side of the effect body is higher than the shell side temperature of the condenser, the degree of vacuum is high, and when the condensed water enters the shell side of the condenser, the condensed water releases a certain amount of heat due to self-evaporation. Therefore, this part of the heat should be included in the calculation when calculating the heat transfer area of ‹the condenser.

3.2. Effect of steam extracted from various non-condensable ports on the condenser

The multi-effect evaporation device generally has two upper and lower non-condensing air ports for each shell side to extract non-condensable gas in the shell side. The upper and lower condenser ports are directly connected to the inlet of the condenser. Each effect body takes steam from the shell side, and the material is taken away from the tube. It is often extracted from the non-condensable gas interface and a certain amount of heating steam is taken out. This is because the theoretical heating process is based on the heat balance. There is no remaining heat in the shell side. In fact, each effect can be seen as a condenser heating steam can not be absolutely no surplus, because heat loss should also be considered in the calculation process.

3.3, the influence of material preheater on the condenser

The temperature of the material before entering the evaporation equipment is relatively low, and it needs to be preheated step by step to reach the temperature above the boiling point or boiling point. For materials with lower temperature, it is generally divided into four levels for preheating. The preheating on top of the final effect separator provides a coiled material preheater for the first stage of preheating. The preheater preheats the material with secondary steam that is not produced. The other three stages of preheating were completed in three shells of the shell. Therefore, this part of the heat should be subtracted when calculating the heat transfer area of the condenser.


Baoji City Changsheng Titanium Co., Ltd.

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