Condenser of mass vapor of vacuum apparatuses A and B, C products

Condenser of massague vapor of vacuum apparatuses A and B, C of products 

 

Designed for condensing massague vapor of vacuum apparatuses and secondary vapor of the last stage of evaporation of the evaporation station, creating the necessary vacuum to ensure the specified temperature regime of boiling of sugar production products. Also used in distillation and other food industry installations.

 

Design features

Advanced jet-cascade water distribution system.

Low sensitivity to possible scale deposits on the surfaces of the water distribution system.

Simplicity of design, designed for operation with deep vacuum.

Low hydraulic resistance.

Possibility of operation in a wide range of steam flow rates.

Easy installation (does not require fasteners).

Possibility of additional equipment with a remote separator for separating water from non-condensable gases.

Steam condensation in three stages: Stage I (jet) – for heating water to feed the diffusion apparatus, stage II (cascade-jet) – main condensation, III stage (cascade-jet) – condensation of the steam residues not condensed at the II stage, and cooling of uncondensed gases.

The massecuite steam condenser of vacuum apparatuses B and C of products (similar in principle of operation to that described above) differs in overall dimensions and the absence of a stage intended for heating water to feed the diffusion apparatus.

 

Quality

Optimization of the massecuite boiling process and heating steam consumption for this purpose due to the possibility of creating a vacuum set by the technological mode.

Wide range of steam and water consumption.

 

Economy

Minimal difference between the temperature of heated (waste) water and steam supplied to condensation, accordingly, the minimum possible water consumption.

Minimal water pumping costs.

Reduction of the load on vacuum air pumps due to cooling of non-condensable gases to the optimum temperature.

Maximum possible heating of water for supplying diffusion devices.

Possibility of operation using only recycled water in the absence of the need to use technical water to supply diffusion devices.

Reduction of fuel consumption for technological needs due to optimization of the massecuite boiling process.

Increased efficiency of condenser operation if a diffusion juice heater on massecuite steam is used in the vacuum condensation installation scheme.

 

Reliability

Stable operation throughout the entire production season, even with scale deposits on surfaces condenser.

Vacuum stability with variable operating modes of the enterprise and unstable quality of processed raw materials.

 

Automation

Maximum simplification of the automatic control system of the condenser.

Full automation of the operating mode (does not require operator intervention).

Maximum simplification of the maintenance process for removing scale at the end of the production period, provided that it is present, which is determined by the quality of the water used for condensation.

 

 

Characteristics

 

Steam consumption, t/h

45

Hydraulic resistance, Pa

≤ 50

Vacuum in condenser, kg/cm2

0.85

Weight, kg

1 200

Inner diameter, mm

3,400

Dimensions – length, mm

3,841

Dimensions – width, mm

3,690

Dimensions – height, mm

6 768