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This four-stage, high-efficiency evaporator system maximizes energy savings while purifying tons of product per hour with perfect precision.

Efficient Evaporator

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Equipment

Evaporators are heat exchange equipment used to concentrate liquid mixtures by removing volatile components (usually water) from them. These devices are widely used in many industries such as food, chemical, pharmaceutical, and biotechnology. Their fundamental principles are based on heat transfer and evaporation. The purpose of an evaporator is to reduce the volume of a liquid in an energy-efficient manner and obtain a more concentrated product.
 

The evaporation process typically occurs in three main stages. In the first stage, the feed liquid is generally preheated to the target temperature using a preheater. In the second stage, the heated liquid enters the evaporator body and comes into contact with the heating surface. This surface is heated by saturated steam or another heat source. As a result, the water or volatile components within the liquid begin to evaporate. In the third stage, the evaporated vapor is usually condensed and removed from the system using a condenser, while the concentrated product is discharged from the bottom of the system.
 

Evaporators can be designed in various types according to their structure and intended use. In single-effect systems, there is only one evaporation stage. These systems are preferred in small-scale operations due to their simple design and low initial investment cost. However, energy efficiency is low in these systems, as approximately 1 kg of steam is required to evaporate 1 kg of water.

Multi-effect evaporators operate based on the principle of energy recovery. The vapor generated in the first stage is used as the heat source for the second stage. In this way, multiple evaporation processes can be performed with the same amount of energy. Three-effect, four-effect, and even seven-effect evaporator systems are available. These systems significantly reduce energy consumption, although the initial investment cost and control systems are more complex.
 

In addition, forced circulation evaporators are used for the evaporation of high-viscosity or crystallizing products. In these systems, a powerful circulation pump forces the liquid at high speed over the heating surface to prevent product buildup in the pipes.

Since the liquid is heated to its boiling point during the evaporation process, energy consumption is high. Therefore, technologies such as Thermal Vapor Recompression (TVR) or Mechanical Vapor Recompression (MVR) are used to improve steam economy. These systems recycle the generated vapor back into the system to enhance energy efficiency.
 

From a control perspective, modern evaporator systems typically operate with PLC-supported automation. Parameters such as temperature, pressure, concentration, and level are continuously monitored and optimized. In addition, Clean-in-Place (CIP) systems are integrated to maintain product quality and ensure continuous operation.
 

In conclusion, the correct design of an evaporator system is crucial and must be determined based on the characteristics of the product, desired output concentration, energy efficiency, and investment budget. Factors such as the feed concentration, target concentration, process temperature, and viscosity directly influence the type and configuration of the system.

We can provide you with technical and project consultancy services in this field.

Product
Capacity (m³/h)
Input Brix (%)
Output Brix (%)
Steam Consumption (kg/h)
Pump Power (kW)
Viscosity
Ethanol (Ethyl Alcohol)
3
8–12
92–96
1340
9
Low
Ethanol (Ethyl Alcohol)
5
8–12
92–96
1700
11
Low
Ethanol (Ethyl Alcohol)
10
8–12
92–96
2600
15
Low
Ethanol (Ethyl Alcohol)
15
8–12
92–96
3500
19
Low
Ethanol (Ethyl Alcohol)
20
8–12
92–96
4400
23
Low
Ethanol (Ethyl Alcohol)
30
8–12
92–96
6200
31
Low
Ethanol (Ethyl Alcohol)
50
8–12
92–96
9800
47
Low
Corn Starch
3
15–20
95–98
1500
11
Medium
Corn Starch
5
15–20
95–98
1900
13
Medium
Corn Starch
10
15–20
95–98
2900
18
Medium
Corn Starch
15
15–20
95–98
3900
23
Medium
Corn Starch
20
15–20
95–98
4900
28
Medium
Corn Starch
30
15–20
95–98
6900
38
Medium
Corn Starch
50
15–20
95–98
10900
58
Medium
Citric Acid
3
10–15
92–96
1340
9
Medium
Citric Acid
5
10–15
92–96
1700
11
Medium
Citric Acid
10
10–15
92–96
2600
15
Medium
Citric Acid
15
10–15
92–96
3500
19
Medium
Citric Acid
20
10–15
92–96
4400
23
Medium
Citric Acid
30
10–15
92–96
6200
31
Medium
Citric Acid
50
10–15
92–96
9800
47
Medium
Xanthan Gum
3
2–4
97–99
1660
13
Very High
Xanthan Gum
5
2–4
97–99
2100
16
Very High
Xanthan Gum
10
2–4
97–99
3200
22
Very High
Xanthan Gum
15
2–4
97–99
4300
28
Very High
Xanthan Gum
20
2–4
97–99
5400
34
Very High
Xanthan Gum
30
2–4
97–99
7600
46
Very High
Xanthan Gum
50
2–4
97–99
12000
70
Very High
Wheat Starch
3
10–18
95–98
1500
11
Medium
Wheat Starch
5
10–18
95–98
1900
13
Medium
Wheat Starch
10
10–18
95–98
2900
18
Medium
Wheat Starch
15
10–18
95–98
3900
23
Medium
Wheat Starch
20
10–18
95–98
4900
28
Medium
Wheat Starch
30
10–18
95–98
6900
38
Medium
Wheat Starch
50
10–18
95–98
10900
58
Medium
Lysine
3
12–18
95–98
1500
11
Medium
Lysine
5
12–18
95–98
1900
13
Medium
Lysine
10
12–18
95–98
2900
18
Medium
Lysine
15
12–18
95–98
3900
23
Medium
Lysine
20
12–18
95–98
4900
28
Medium
Lysine
30
12–18
95–98
6900
38
Medium
Lysine
50
12–18
95–98
10900
58
Medium
Sorbitol
3
20–25
95–98
1500
11
Medium
Sorbitol
5
20–25
95–98
1900
13
Medium
Sorbitol
10
20–25
95–98
2900
18
Medium
Sorbitol
15
20–25
95–98
3900
23
Medium
Sorbitol
20
20–25
95–98
4900
28
Medium
Sorbitol
30
20–25
95–98
6900
38
Medium
Sorbitol
50
20–25
95–98
10900
58
Medium
Maltodextrin
3
30–40
97–99
1660
13
High
Maltodextrin
5
30–40
97–99
2100
16
High
Maltodextrin
10
30–40
97–99
3200
22
High
Maltodextrin
15
30–40
97–99
4300
28
High
Maltodextrin
20
30–40
97–99
5400
34
High
Maltodextrin
30
30–40
97–99
7600
46
High
Maltodextrin
50
30–40
97–99
12000
70
High
Modified Starch
3
30–35
97–99
1660
13
High
Modified Starch
5
30–35
97–99
2100
16
High
Modified Starch
10
30–35
97–99
3200
22
High
Modified Starch
15
30–35
97–99
4300
28
High
Modified Starch
20
30–35
97–99
5400
34
High
Modified Starch
30
30–35
97–99
7600
46
High
Modified Starch
50
30–35
97–99
12000
70
High
Maltose / Dextrose Syrup
3
25–35
95–98
1500
11
Medium-High
Maltose / Dextrose Syrup
5
25–35
95–98
1900
13
Medium-High
Maltose / Dextrose Syrup
10
25–35
95–98
2900
18
Medium-High
Maltose / Dextrose Syrup
15
25–35
95–98
3900
23
Medium-High
Maltose / Dextrose Syrup
20
25–35
95–98
4900
28
Medium-High
Maltose / Dextrose Syrup
30
25–35
95–98
6900
38
Medium-High
Maltose / Dextrose Syrup
50
25–35
95–98
10900
58
Medium-High
Lactic Acid
3
8–12
92–96
1340
9
Low
Lactic Acid
5
8–12
92–96
1700
11
Low
Lactic Acid
10
8–12
92–96
2600
15
Low
Lactic Acid
15
8–12
92–96
3500
19
Low
Lactic Acid
20
8–12
92–96
4400
23
Low
Lactic Acid
30
8–12
92–96
6200
31
Low
Lactic Acid
50
8–12
92–96
9800
47
Low
Monosodium Glutamate
3
10–14
95–98
1500
11
Medium
Monosodium Glutamate
5
10–14
95–98
1900
13
Medium
Monosodium Glutamate
10
10–14
95–98
2900
18
Medium
Monosodium Glutamate
15
10–14
95–98
3900
23
Medium
Monosodium Glutamate
20
10–14
95–98
4900
28
Medium
Monosodium Glutamate
30
10–14
95–98
6900
38
Medium
Monosodium Glutamate
50
10–14
95–98
10900
58
Medium

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