PTT304 Fermentation Technology. Sterilization and Equipment

Transcription

1 PTT304 Fermentation Technology Sterilization and Equipment

2 Sterilization Reading assignments: Chapter 10 Shuler & Kargi

3 Sterilization Fermentation process involves cultivation of a single microorganisms, e.g. monoseptic process is employed A reactor is built to promote growth, but inputs as well as outputs from the reactor must be devoid of any organism To obtain the required conditions for this process, bioreactor must be free of all other microbes prior to inoculate with a specific strain It applies to the nutrient solution installed in the bioreactor

4 Aseptic Operation Pipe Lines and Valves The pipelines transporting materials required for aseptic use should be sterilized with steam (usually at 120 o C for 20 to 30 minutes). Pipelines should free from steam condensate after sterilization. Building materials: stainless steel (with few exceptions). Valves have to be installed, diaphragm types are preferred as they committed less contamination risk. For considerations of costs, the conventional stop, angle, and globe valves are frequently used in the fermentation industry.

5 Aseptic Inoculation and Sampling the connections required for the aseptic transfer of a spore suspension to a seed tank

6 Aseptic Inoculation and Sampling The spore suspension vessel and its piping is first sterilized and then spores induced into the vessel. A sterile air is used to blow the spore suspension from the vessel to the seed tank. It is frequently necessary to sample the broth during fermentation; sampling point, should be steam sterilized. The end of the sampling pipe is immersed, for example, in 40 % formaldehyde solution. When a sample is required, the vessel containing the germicide is removed and steam is blown through sampling pipes long enough to sterilize the section. Steam is allowed to bleed for sometime then the valve is opened to allow some broth bleed for cooling and dissipate the wasted remains in the pipes, a sample is taken, valves closed

7 Sampling Point

8 Sterilization Sterility: Absence of any detectable viable organism Disinfection vs sterilization Sterilization, the destruction of the microorganism is carried out by means of chemical/thermal process or radiation (UV) Death: Failure of a cell, spore or virus to replicate or germinate when placed in a favorable environment

9 Sterilization Sterilized either in empty condition, or when filled with nutrient solution Sterilization is carried out in accordance with the basic principles of heat sterilization Reactor is heated up with the saturated vapour (between 121 C to 141 C) through heat transfer system (double jacket or other internal exchangers/direct steam injection and maintained at appropriate temperature for specific period of time, whereby internal pressure in reactor is at specific level).

10 Sterilization Reactor is cooled down by regulated introduction of sterile air, after completion of thermal ret. Time. Heat sterilization - ensure that all parts of reactor contact with medium are maintained at desired temp., for sufficient length of time. This applies particularly to ports, ducts, seals, etc which often present danger contamination.

11 Steam pressure table

12 Kinetics of death Probability of extinction of a population P 0 t N 1 p t 0 No of individuals at time t=0 Probability that an individual is still viable at time t p t e k D t First order death model, dependent on organism and environment D decimal reduction time k D e D D 0.10 k D time for which p t 0. 10

13 Kinetics of death Plot of ln N(t)/N0 vs time is called survival curve The curve is implicitly deterministic; which deterministic and probabilistic approaches give the same result as long as N(t)>>1 (10-100) Most real population are not homogenous, which oftenly a subgroup is more resistant to sterilization agent Microbes which grow in clumps has the tendency of resistance to death

14 Kinetics Survival Curves Death rate of spores of B. stearothermophillus in distilled water Death rate of E. Coli in buffer

15 Survival Curve for an Heterogeneous Population Survival curve (D) for a system with 3 distinct subpopulation (A,B,C). Population A is normally dominant, but it is the one most sensitive to the sterilizing agent, while C is far more resistant

16 Sterilization of liquids Liquids can be sterilized by chemical, thermal and radioactive agents Thermal much preferred for economics, large-scale UV radiation effective on surfaces but cannot penetrate fluids easily whereas x-rays can but costly and dangerous Chemical agent can be used as long as it leave no toxic residue to desired culture such as ethylene oxide (gas), 70% EtOH-H 2 O with HCl (ph 2), fomaldehyde and sodium hypochlorite

17 Most Common Method of Sterilization For large scale production, thermal sterilization is the most used method p t e k D t E0 RT Activation energy: kcal/g-mol. For spores of Bacillus stearothermophilus, it is 70 kcal/g-mol and for E. coli it is 127kcal/g-mol, E. coli much more sensitive, spores control. Activation energy values for vitamins and growth factors in the media is in the order of 2-20 kcal/g-mol, which means that can kill the organisms, but maintain integrity of media. k D e d

18 Difficulty of sterilization increases with scale Probability of unsuccessful sterilization 1 P0 t 1 1 e N 0 Consider two fermenters supplied with the same media: one 1 liter and the second is 10,000 liter. Assume that k d t= 15 and initial concentration of spores is 10 4 spores/l k D t

19 Difficulty of sterilization increases with scale For 1 liter bioreactor: 1 P t 1 1 e For 10,000 liter bioreactor: 1 P t 1 1 e 15 1 Need much longer exposure time for larger reactor, if the same temperature was used 4 10,

20 Sterilization Chart 1 P0 t 1 1 e k D t N 0

21 Batch Vs Continous Sterilization Steam sterilization in batch processes. Time it takes to warm up fluid to 121ºC and to bring it down to 37ºC much longer than required exposure time For spores, kd varies dramatically with temperature, falling by a factor of 10, when temperature changes from 121ºC to 110ºC. No additional killing by heating and cooling, but additional degradation of media The elevated temperatures during heat-up and cool-down can damage vitamins and proteins, can lead to carmelization reactions for sugar and can alter medium quality

22 Batch Vs Continous Sterilization Continuous sterilization, namely high temperature, short time, achieve adequate levels of kill and preserve media. Potential problems with foaming and dilution of media by steam. Plug flow system is essential.

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25 Filter sterilization It can be used when the medium contains heat-sensitive material Example the sterilization of medium to support the growth of animal cell Filter sterilization (pores less than 0.2 micron) is used for media that contains thermo labile components But it is not as reliable as steam sterilization, any defect in membrane can lead to failure, viruses and mycoplasma can pass the filter It can also sterilize process air

26 Sterilization of gases Volume of air required in industrial scale fermentation is huge, typically between 0,1 and 1 volumes of gas per volume of liquid per minute. Adiabatic compression of air is typically used (to about 220ºC and 30 seconds for spore inactivation). Surface filtration (sieving) is used in between compressor and fermentation vessel, to prevent contamination.

27 Sterilization of gases Air employed as carrier of O2 in aerobic processes and any other gases which may be fed into reactor must be sterile. Air sterilization is generally carried out by filtration If spent air from fermenter contains potentially pathological m/o, air must also be sterilized. Atmosphere contains a diversity of different particles countryside, populated areas, industrialization, weather, etc. Industrial regions and cities, particle densities (size ~ 0.5mm) at least 107 to 108/m3 are to be expected.

28 Sterilization of gases Small proportion of these aerosol particles germs (bacteria, spores, yeasts, moulds, viruses; approx. 50 mould spores and 40% G-ve bact.) The germ content in air stands at /m3 in rural areas, and 500 to 103/m3 in cities. Expected mean level of 104 germs/m3 for filter design. Human beings also provide a source of emission for particles, assumed that one germ capable of reproduction is contained in 1000 emitted particles.

29 Problem 10.6 A continuous culture system is being constructed. The fermentation tank is to be 50,000 liter in size and the residence time is to be 2 h. A continuous sterilizer is to be used. The unsterilized medium contains 10 4 spores/l. The value for kd has been determined to be 1 min -1 at 121 C and 61 min -1 at 140 C. For each temperature, determine the required residence time in the holding section so as to ensure that 99% of the time four weeks of continuous operation can be obtained without contamination.

30 Problem An autoclave malfunctions, and the temperature reaches only C. The sterilization time at maximum temperature was 20 min. The jar contains 10 liter of complex medium that has 10 5 spores/l. At 121 C, k d = 1.0 min -1 and E 0d = 90 kcal/g-mol. What is the probability that the medium was sterile?

31 Control Systems The basic principle of control involves a sensory sys-tem linked to a control system and feedback loop. Sensors are used to measure and record the events within the bioreactor. In conjunction with process control, they maintain the difference between the measured and desired values at a minimum level. Overall control can be manual or automated; newer systems have integral and derivative control systems. Data recorded from the sensors and control decisions are downloaded to a computer where appropriate calculations can be per-formed to determine production of biomass and product, overall oxygen and carbon dioxide transfer rates, nutrient utilisation, power usage, etc.

32 Control Systems All of this information may be used to construct a mathematical computer model of the process. If a deviation is discovered, appropriate alarm and correctional systems are activated, giving greater control of the fermentation. Any control system needs to be calibrated when first installed and then regularly checked to conform to good manufacturing practices (GMP).

33 Scheme for controlling fermenter temperature

34 Simple manual control loop for temperature control

35 Control Systems The process parameters may be controlled using control loops. A control loop consists of four basic components: 1. A measuring element. 2. A controller. 3. A final control element. 4. The process to be controlled.

36 Control Systems A Feedback Control Loop In the simplest type of control loop (feedback control): The measuring element senses a process property (flow, pressure, temperature, etc) then generates corresponding output signal. The controller compares the measurement signal with the set point and produces an output signal to counteract any differences between the two.

37 Control Systems The final control element receives the control signal and adjusts the process by changing a valve opening or pump speed and causing the controlled process property to return to the set point.

38 Manual Control A Simple example of control is manual control of a steam valve to regulate the temperature of water flowing through a pipe. Labor, cost and should be kept minimum and use automated control as much as possible. Simple manual control loop for temperature control

39 Automatic Control When an automatic control loop is used, certain modifications are necessary. The measuring element must generate an output signal which can be monitored by an instrument. E.g. the thermometer is replaced by a thermocouple, which is connected to a controller which in turn will produce a signal to operate the steam valve. Simple automatic control loop for temperature control

40 Computer Applications in Fermentation Technology Three distinct areas of computer function were recognized: 1. Logging of process data. Data logging is per-formed by the data acquisition system which has both hardware and software components. There is an interface between the sensors and the computer. The software should include the computer program for sequential scanning of the sensor signals and the procedure of data storage. 2. Data analysis (Reduction of logged data). Data reduction is performed by the data-analysis sys-tem, which is a computer program based on a series of selected mathematical equations. This analyzed information may then be put on a print out, fed into a data bank or utilized for process control.

41 Computer Applications in Fermentation Technology 3. Process control. Process control is also performed using a computer program. Signals from the computer are fed to pumps, valves or switches via the interface. In addition the computer program may contain instructions to display devices or teletypes, to indicate alarms, etc. There are two distinct fundamental approaches to computer control of fermenters. 1) Fermenter is under the direct control of the computer software. This is termed Direct Digital Control (DDC). 2) The use of independent controllers to manage all control functions of a fermenter and the computer communicates with the controller only to exchange information. This is termed Supervisory Set-Point Control (SSC).

42 Process Control Three levels process control that might be incorporated into a system were recognized. Each higher level involves more complex programs and needs a greater overall understanding of the process. The first level of control, involves sequencing operations, such as manipulating valves or starting or stopping pumps, instrument recalibration, on-line maintenance and fail-safe shut-down procedures. In most of these operations the time base is at least in the order of minutes, so that high-speed manipulations are not vital. Two applications in fermentation processes are sterilization cycles and medium batching.

43 Process Control The second level of control involves process control of temperature, ph, foam control, etc. where the sensors are directly interfaced to a computer, Direct Digital Control (DDC). When this is done separate controller units are not needed. The computer program determines the set point values and the control algorithms, such as PID, are part of the computer software package. Computer failure can cause major problems unless there is some manual back-up facility.

44 Process Control Layout of computer- controlled fermenter with only one control loop

45 Process Control The alternative approach is to use a computer in a pure supervisory role, All control functions are per-formed by an electronic controller using a system illustrated in the figure:

46 Process Control In such a system the linked computer only logs data from sensors and sends signals to alter set points when instructed by a computer program or manually. This system is known as Supervisory Set-Point Control (SSC) or Digital Set-Point Control (DSC). When SSC is used the modes of control are limited to proportional, integral and derivative because the direct control of the fermenter is by an electronic controller. In the event of computer failure the process controller can be operated independently.

47 Process Control The third (advanced) level of control is concerned with process optimization. This will involve understanding a process, being able to monitor what is happening and being able to control it to achieve and maintain optimum conditions. Firstly there is a need for suitable on-line sensors to monitor the process continuously. A number are now available for dissolved oxygen, dissolved carbon dioxide, ph, temperature, biomass (the bug meter, NADH fluorescence, near infra-red spectroscopy) and some metabolite (mass spectroscopy and near infra-red spectroscopy).

48 Process Control Secondly, it is important to develop a mathematical model that adequately describes the dynamic behavior of a process. This approach with appropriate on-line sensors and suitable model programs has been used to optimize bakers yeast production, an industrial antibiotic process and lactic acid production.