The invention is from the field of monitoring biological processes. Specifically, the invention is from the field of in-situ, real-time, noninvasive gas monitoring of fermentation processes.
In fermentation processes specific microorganism species are deliberately introduced into a fermentation container containing a material serving as growth medium in a metabolic process that consumes carbon source and other nutrients. The fermentation container is kept at suitable conditions (e.g. pH, agitation, temperature, etc.) and suitable growth medium encouraging growth of microorganisms and/or production of desired product by microorganisms using different processes.
For example, fermentation processes are used in the biotech industry for generating various biological cells such as: microbial cells (such as E. coli); fungi cells, yeast cells, and biological substances such as enzymes (catalase, amylase, protease, etc.); primary metabolites (ethanol, citric acid, glutamic acid, etc.); recombinant proteins and secondary metabolites (antibiotic, recombinant products: insulin, hepatitis B vaccine, interferon, etc.). In the food and beverage industries during conversion of carbohydrates into alcoholic beverages cells produce CO2 via metabolic cycles while cells grow and proliferate.
Current methods applied today (using techniques such as Optical Density, Live Counts, or glucose concentration/consumption) for tracking cells or microorganism growth and determining the optimal growth conditions need invasive sampling and therefore are prone to errors. Other online methods, such as pH or dO2 measurements are not considered to be accurate to correlate with biomass. A requirement of industry is an online, high resolution measurement system that enables, monitoring, controlling and optimizing in real-time, fermentation-based production processes in all scale fermenters. Among the processes that this solutions applies to (but not exclusively) are the production of small molecules, bio-similars, APIs, recombinant proteins, and vaccines.
High accuracy CO2 measurements are important in terms of predicting process stage and trend. CO2 value is a significant parameter in the growth, secondary metabolites biosynthesis and maintenance. During fermentation processes better CO2 monitoring and precise detection capabilities are essential for analyzing the culture nonlinear dynamics and multistage nature that can be reflected with high correlation by CO2 measurements.
Typically, a gas inlet is coupled to a fermentation container to supply suitable conditions for the microorganisms' metabolism and a gas outlet is also coupled to the fermentation container to remove waste gases, throughout an exhaust pipe.
In many cases, monitoring of fermentation processes is done by a combination of on-line and occasional offline sampling. The material in the fermenter/bioreactor is sampled and analyzed, in order to determine parameters reflecting the concentration of the microorganisms/cells and/or the yield/titer of the product in the process, thereafter, utilizing that data to control the fermentation process.
Conventional techniques for monitoring of some of the fermentation parameters are not performed continuously and may not be carried out with high accuracy in real-time. Typically, these measurements involve sporadic sampling of the fermenter/bioreactor and analysis methods that require the know-how and accuracy of a technician. Amongst these techniques are optical/critical density measurement, viable counts, and metabolites consumption in the growth media by measuring yield/titer of the product. Using these methods, the optimal time points for process harvest are often undetected. Other continuously methods such as pH, dO2 etc. are crucial for process control but cannot reflect biomass.
Co-pending patent application US 2017/0267964 to the applicant of the present application contains a description of a system and method that provides accurate real time and continuous/planned monitoring of fermentation processes by sampling the gas emission in a continuous/programmed manner. According to the rate and composition of the metabolic gas emitted from the fermenter/bioreactor. The collected data is based inter alia on the rate of metabolic gas production by microorganisms/cells contained therein or a change in such rate of production. From this data is determine the amount of the microorganisms/cells, biomass, or the rate of change in their growth rate.
The method described in US 2017/0267964 is based on measuring the absorption of illuminating light (typically in the infrared spectrum) transmitted through a gaseous atmosphere in fluid communication with the fermentation material, i.e. in the dead space above the fermentation material. Living microorganisms produce metabolic gases such as carbon dioxide (CO2) during respiration. By means of infrared absorption, the concentration of metabolic gases given off by the fermentation process can be measured inside the dead space.
Further provided in the system 10 is a control system 30 (e.g. controller), which is connectable to the optical system, i.e. to the light source 12 and to the detection module 15. The controller 30 is configured and operable for operating the light source 12 to emit light in the selected at least first and second wavelengths, and for receiving and analyzing measured/detected data/signals from the detection module and generating data indicative of a concentration of the metabolic gas in the region of interest.
In some embodiments, the light source 12 and the detector 14 are arranged in spaced-apart relationship defining the region of interest between them for spectroscopic measurements. To this end, light source 12 and the detector 14 are arranged such that a suitable container 24 of a fermenting material 26 and/or more specifically a dead space 28 associated with and being in fluid communication with such container 24 can be placed. The dead space 28 is where metabolic gases should be detected by optical/spectroscopic measurements performed by the system 10 of the present invention. As indicated above, the dead space 28 of the container is actually any space being in fluid communication with the atmosphere in the container above fermenting material 26. This may include any one of the following: the portion 28 of the container 24 above the fermenting material as illustrated for example in
The analysis of the measured data is generally based on the principles of spectroscopy. The first and second wavelengths are particularly selected to enable accurate and high-sensitivity measurements of the concentrations of metabolic gas, with absorption specific only to the desired gas molecule being measured with no cross-interference by any other molecule in the measurement volume. The first wavelength is selected to be highly affected by absorbance by the at least one metabolic gas in the region of interest, i.e. to overlap with the spectral absorption line. The second wavelength is on the other hand selected to be less affected by absorbance of the metabolic gas, but nevertheless it is selected to be spectrally close to the first wavelength, such that it provides reference data indicative of absorbance of the first wavelength by other materials in the region of interest.
In US 2017/0267964 there is described in detail the method of obtaining the data and analyzing it and also the required properties of the various components of the system. However, the system is limited to making measurements inside the fermentation container. US 2017/0267964 supplies no description of a specific practical system that could be connected to a fermentation container in order to make in-line measurements at a location remote from the container in which the fermentation process is taking place in a laboratory or an industrial environment.
It is therefore a purpose of the present invention to provide an apparatus configured to perform in-situ, real-time, noninvasive monitoring of fermentation processes at a location remote from the fermenter/bioreactor in a laboratory or an industrial environment.
It is another purpose of the invention to provide an apparatus configured to perform online, high resolution measurements that enable monitoring, controlling, and optimizing in real-time fermentation-based production processes in all scale or type of fermenters.
Further purposes and advantages of this invention will appear as the description proceeds.
An apparatus configured to perform in-situ, real-time, noninvasive monitoring of fermentation processes at a location remote from the fermenter/bioreactor is described. The apparatus comprises:
In embodiments of the apparatus the LSDM comprises:
In embodiments of the apparatus the light source is a broadly tunable light source having a tunable range of at least 2 cm−1 and emissions in the spectral range of the metabolic gas being observed.
In embodiments of the apparatus the metabolic gas is CO2 and the spectral range is 2100-2400 cm−1.
In embodiments of the apparatus the light source is a tunable Quantum Cascade Laser.
In embodiments of the apparatus the ETA is connected to the exhaust tube or a bypass to the exhaust tube by two pieces of flexible tubing, wherein a first piece of flexible tubing leads metabolic gas from the fermenter/bioreactor into the ETA and a second piece of flexible tubing leads metabolic gas out of the ETA.
In embodiments of the apparatus the ETA comprises:
In these embodiments of the apparatus the ETA can be disconnected from the LSDM and can be discarded after a fermentation process.
In embodiments of the apparatus the ETA comprises:
In these embodiments of the apparatus two opposing sides of the housing of the ETA comprise holes that are hermetically connected to the respective ends of a gap in the exhaust tube of the fermenter/bioreactor, the size of the housing depends on the diameter of the exhaust tube to which the ETA is connected, and the interface has the same dimensions for all sizes of housing.
In embodiments of the apparatus comprising a multi-pass system the multi-pass system is configured such that the number of passes of the light beam is dependent on the size of the housing to achieve the same optical path for housings of all sizes.
In embodiments of the apparatus the control and display module comprises:
All the above and other characteristics and advantages of the invention will be further understood through the following illustrative and non-limitative description of embodiments thereof, with reference to the appended drawings.
Herein is described an apparatus configured to perform in-situ, real-time, noninvasive monitoring of fermentation processes at a location remote from the fermenter/bioreactor in a laboratory or an industrial environment.
The apparatus enables monitoring and detection of CO2 in fermentation-based processes with high precision, continuously and in real time from the exhaust pipe or exhaust bypass of any size fermenter/bioreactor or pipe diameter.
The apparatus is comprised of a very sensitive, non-invasive meter device, called herein a light source and detection module (LSDM) that is removably attached to an exhaust tube adapter (ETA) or to a disposable bypass from fermenter exhaust pipe and a control and display module.
The ETA, assembled in-line with the fermentation vessel exhaust pipe, comes in different embodiments that enable the LSDM to provide continuous metabolic gas detection for highly accurate monitoring of the process in any size fermenter/bioreactor with same optical path.
The LSDM records and analyzes metabolic gas concentrations, CO2 produced during the respiration, and growth of living cells. Continuous, automatic measurements via an IR optical system allows the in-situ detection of metabolic gases without interrupting the process for invasive sampling.
The third module of the system is control and display module 52, which is in communication with the LSDM 48 via a wired or wireless communication channel symbolically shown by cable 50. The functions of the components of control and display module 52 can be provided by any combination of components or devices that include a processor, communication functions, and a graphic user interface. One example of a control and display module 52 that is suitable for use with the system is a personal computer that comprises dedicated software configured to operate and receive data from the LSDM 48, to analyze the data, and output information relating to the status of the fermentation process.
Mounts 58 are provided to support LSDM 48 and ETA 44. Grill 60 on the side of the casing of LSDM 48 is provided to allow heat generated by the light source and electronic components within the casing to be expelled to the surroundings.
Windows 76a and 76b are facing windows 70 in the wall of LSDM 48 when ETA 44 and LSDM 48 are bolted together as shown in
In order to keep air paths to a minimum length to minimize absorption by CO2 and other atmospheric gases, cylindrical spacers made of an infrared transmitting material, e.g. sapphire, are placed along the optic axis between the optical components to physically reduce the air path.
The method of determining the progress of a fermentation process is based on monitoring the concentration of a metabolic gas in the ETA, typically CO2, by optical/spectroscopic measurements. The method, which is described in detail in U.S. Pat. No. 9,441,260 (including the equations used by the software in the processor to calculate the concentration of the metabolic gas of interest), comprises measuring at least a first and a second predetermined wavelength of substantially narrow spectrum corresponding to respectively an absorption peak of at least one metabolic gas and a spectral region outside the absorption peak of the at least one metabolic gas, and measuring transmission of the first and second wavelengths through the ETA. The spectral separation between the first and second wavelengths of the light source is selected to be small such that the first and second wavelengths are characterized by same or similar transmission through materials in the optical path. This allows the transmission measurements at the second wavelength to be used to correct the measurements at the first wavelength for absorption by the windows and mirrors in the ETA, components of the volatile gas emitted in the fermentation process other than the specific metabolic gas whose concentration is being measured, and air paths, which are kept to a minimum.
In order to obtain the two wavelengths required for determining the concentration of the metabolic gas, the light source must be a broadly tunable light source having a tunable range of at least 2 cm−1 and emissions in the spectral range of the metabolic gas being observed, for example in the 2100-2400 cm−1 range (about 4.3 microns) which corresponds to a spectral regime of high absorbance by CO2. An embodiment of a light source that meets these requirements and is used in the system of this invention is a tunable Quantum Cascade Laser (QCL) 62. QCL 62 is used as the light source, since, in addition to being tunable over a wide wavelength range, a QCL also provides sufficiently narrow spectral width, i.e. sufficiently monochromatic light emission. Another possible light source that can be used is a broadband source equipped with suitable narrow-band spectral filters in the mid-IR regime.
In a typical embodiment of the system for measuring the concentration of CO2, the system utilizes a tunable QCL 62, IR detector 64, a CaF2 plano-convex lens 74, front surface coated mirrors 68,82, and sapphire windows 70 and 76a,b,c. The QCL operates, for example, in the pulse mode with repetition frequency of 5 kHz and pulse width 500 nsec. It is easily within the ability of persons skilled in the art to replace certain of these components and materials mutatis mutandis with similar components and materials that are suitable for detecting metabolic gases other than CO2 and/or in other spectral regions.
Embodiments of the LSDM 48 include an electronic signal processor/lock-in amplifier (whose components are shown but not labelled in the figures) that receives signals from the IR detector 64 and a control and display module 52. Use of the lock-in amplifier enables even further improvement of the signal to noise ratio (SNR) provided by the system thus further improving the sensitivity and accuracy of the measurements relating to the concentration(s) of metabolic gases and consequently to control of the fermentation process. To this end, in such embodiments the control system 52 is adapted for operating the tunable broadband IR light source 62 for applying time modulation to intensity of light emitted in one or more (e.g. in each) of at least two (first and second) wavelengths, and also operating the lock-in amplifier to determine/measure the detected intensity/intensities of the emitted light with high accuracy based on that modulation. Accordingly, transmittance of the region of interest to the first and second wavelengths (i. e. to all wavelengths used in the measurement) can be determined with high accuracy based on the intensity modulation, while noise is mostly discarded as it is generally not modulated in the same way. It should be noted that the configuration and operation of various types of lock-in amplifier are generally known in the art of signal processing and are therefore not specifically described herein. A person versed in this art would readily appreciate the various possible configurations of such lock-in amplifier with appropriate modulation to the emitted illumination to be used in the system of the invention.
The control and display module 52 is configured for operating the broadly tunable IR light source for modulating light intensity of the at least first and second wavelengths, and operating the lock-in amplifier or an Excitation/Oscillation clock to determine the transmission of the region of interest to the at least first and second wavelengths with high signal to noise ratio based on the modulation. The control and display module 52 also comprises software containing equations and algorithms for transforming the raw data from the detector into concentration of the metabolic gas of interest, data bases to store historical data, and input, output and display means, e.g. a keyboard, computer monitor, printer, and touch screen GUI.
The embodiment of the ETA described herein above is designed for use with fermentation vessels having different diameter exhaust tubes. When used, for example, with a pathogenic culture, this embodiment of ETA can be disconnected from the LSDM and discarded after each fermentation process saving a time-consuming cleaning and sterilization process. The LSDM is never in contact with the gases exiting the fermentation vessel and therefore requires no cleaning and can be connected to another ETA to monitor another process taking place in the same or a different fermentation vessel.
This embodiment of ETA is installed into a gap in the exhaust tube 42 that carries the metabolic gas away from fermentation vessel 40. Two opposite sides of the housing 90 contain holes that allow the interior of ETA 44′ to be filled with metabolic gas that exits the fermentation vessel through exhaust tube 42. The housing 90 of ETA 44′ is hermetically connected to the respective ends of exhaust tube 42 either by welding as shown in
In order to connect to exhaust tubes 42 having larger diameters, the dimensions of housing 90 of ETA 44′ had to be increased/were increased. The dimensions of interface 88 are the same for all housing 90 sizes in order to be able to use the same LSDM 48 with fermentation vessels having exhaust tube with a large range of diameters.
As the dimensions of the housing 90 increase the number of passes of the laser light beam through the gas in the housing can be decreased. In many cases this can be accomplished without any changes to the optical system but in some cases, in order to keep the same optical path between where the beam enters and exits housing 90 of ETA 44′, the angle at which the beam enters must be slightly (typically by 1-3 degrees) altered by rotating the folding mirrors 68 in LSDM 48.
Although embodiments of the invention have been described by way of illustration, it will be understood that the invention may be carried out with many variations, modifications, and adaptations, without exceeding the scope of the claims.
Number | Date | Country | Kind |
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260523 | Jul 2018 | IL | national |
This application is a continuation of International Patent Application No. PCT/IL2019/050750 filed on Jul. 7, 2019, now pending, which claims the benefit of Israel Application No. 260523 filed on Jul. 10, 2018. The contents of the above-referenced applications are hereby incorporated by reference.
Filing Document | Filing Date | Country | Kind |
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PCT/IL2019/050750 | 7/7/2019 | WO | 00 |