- About us
- Asset Management
- Home
- Interpersonal relation
- Points store
- Production and operation
- 01, Production systems and operations management
- 02, Operations Strategy
- 03, Tours of operations
- 04, Forecasting
- 05, Product Design and Operations
- 06, Capability Planning and Facility Location
- 07, Selecting the Process Structure and Technology
- 08, Process Design and Facility Layout
- 09, Waiting or Queueing System
- 10, Job design, Work methods, and Organization
- 11, The Quality management system
- Quality Management Doctor
- Aseptic production of milk and juice
- 00.Introduction
- 01.UHT processing
- 02.Aseptic packaging
- 03. Sterilising Effect
- 04. H2O2 as a sterilant
- 05. Packaging material
- 06. Application of microbiology to UHT processing and aseptic packaging
- 07. Installation
- 08. Cleaning and house keeping
- 09. Commissioning
- 10. Changes during milk processing
- 11. Product changes during storage
- 12. Quality control of aseptic product-Part1
- 12. Quality control of aseptic product-Part2
- Bacteria, virus an human life
- Food Safety and Microbial Quality
- Keeping Cows Cool and Comfortable to Improve milk production of cow
- Operation and quality management
- Aseptic production of milk and juice
- Quality Management Doctor
- OCE to measure the personnel performance？
- TPM world class management
- Team building
运营卓越Operational excellence
012.Indirect UHT
English
2. Indirect UHT Systems
A heat exchange surface separates the product from the heating or cooling media in indirect UHT systems. The heating medium may be either steam or superheated water (Figure 2). A time-temperature diagram for indirect systems is shown in
figure 3. Typically, the product enters the steriliser via a balance inlet tank and a centrifugal feeding pump at about 4°C. Subsequently, it is heated to 70 -75°C, at which temperature the product is homogenised. For milk homogenisation, pressures of 200 to 250 kg/cm2 (150 to 200 at the first stage, and about 50 kg/cm2 at the
second) are often used. The omogeniser is a positive piston pump which pushes the product through the remaining equipment directly to the aseptic filling machine or into an aseptic tank for subsequent filling. Sterilisation temperatures are usually between 135°C and 140°C. Holding times between 2 and 6 seconds at the sterilisation temperature are common. Though more expensive, downstream (aseptic) homogenisation results in better flavour characteristics for some products. In order to lower the oxygen content of the product, deaeration can be introduced prior to upstream homogenisation. Milk entering the steriliser is normally saturated with oxygen. Since indirect working sterilisers are closed systems, the incoming and outgoing oxygen content of the product is the same. Depending upon temperature, milk may contain 6 to 9 ppm of oxygen (ca 7ppm), (168). Passing a vacuum chamber (deaerator) at high temperature prior to homogenisation (~ 70°C), the oxygen
content can be reduced to about < 1 to 3 ppm (0.3 - 0.9 ppm), (168). The degree of deaeration depends upon the temperature and the underpressure applied in the process. During heat processing, deposits form on heat exchange surfaces, particularly in the temperature range > 80°C. In order to reduce this deposit formation and thus prolong the running time, a holding cell can be introduced: the product (milk) is held for a few minutes at a temperature of about 90°C (Figure 4). Indirect systems offer good possibilities for regenerative energy recovery: the incoming productis heated by the outgoing.
In the equipment shown in figure 5, a pressure drop takes place. As a consequence of this, the pressure of the incoming product is higher than the pressure of the commercially sterile outgoing product. Leakage in the regenerative section and the final cooler may lead to reinfection. This risk can be eliminated by introducing a “booster pump” after the final heating section (figure 6). Advantages of indirect UHT systems are:
a) technically, they are relativelysimple;
b) they are comparatively inexpensive in terms of investment cost;
c) they permit high values of regenerative energy recovery (for plate heat exchangers up to 93%);
d) they require limited service;
e) they have comparatively low running costs.
For both plate and tubular (single and multiple tube) systems for commercial production, the capacity range available is from 2,000 to 30,000 litres/hour or even more.