Patent Application
20180111058
The present disclosure relates to an apparatus, and related methodology, for the regulation of carbon dioxide expansion in a carbon dioxide based chromatographic system. In particular, the present disclosure relates to minimizing or eliminating the deleterious effects of carbon dioxide expansion on the solvent, the analyte(s) of interest, the separation, the detection of the analyte(s) of interest, and other related aspects in a carbon dioxide based chromatographic system.
Carbon dioxide based chromatographic systems use carbon dioxide as a component of the mobile phase. An example of a carbon dioxide based chromatography system is a supercritical fluid chromatography system designed to use CO2 in the mobile phase flow stream. In some systems, the carbon dioxide based mobile phase is delivered from the pump, or pumps, and carried through the separation column as a liquid. After exiting the separation column, the mobile phase and the analyte(s) of interest are directed to a detector for analysis where the analyte(s) of interest is identified, quantified or both. Prior to entering or after exiting the detector the carbon dioxide may undergo a deliberate phase change, e.g., from liquid to gas. This phase change absorbs energy and can abruptly drop the temperature of the mobile phase, as well as the temperature experienced by any analyte(s) of interest. This phase change and temperature drop can have negative impacts on the system.
Currently, the temperature drop associated with the phase change is managed by the use of a back pressure regulator heater. The heater is typically located downstream of the separation column and upstream of the regulator. The heater is usually located in a position that heats the mobile phase after it has undergone the phase change. Standard practice is to set the back pressure regulator heater, or similar heating device, to a constant temperature that is sufficient to prevent the mobile phase, or any components thereof, from freezing as a result of the temperature drop. Standard practice, however, ignores the effect(s) of insufficient or excess heat being delivered to the system.
The present disclosure relates to the regulation of carbon dioxide expansion in a carbon dioxide based chromatographic system. In particular, the present disclosure relates to the regulation of the carbon dioxide expansion and dynamic control of the temperature of the mobile phase, as well as for any analyte(s) of interest.
In one embodiment, the present disclosure relates to a chromatographic expansion regulation system comprising a chromatographic column having an inlet and an outlet, a mobile phase including a compressed room temperature gas in substantially liquid form flowing through the column, a temperature sensor downstream of the outlet and located in an area where a substantial portion of the mobile phase expands from liquid form to gas form, wherein the sensor is capable of measuring the temperature of the expanded mobile phase, a heater in thermal communication with at least one of the column, the expansion area or the expanded mobile phase capable of adjusting the column temperature, expansion area temperature or expanded mobile phase temperature; and a temperature controller in signal communication with the sensor and the heater, wherein the controller is capable of receiving the temperature measurement from the sensor, comparing the temperature measurement with a desired temperature in the expansion area or expanded mobile phase, and sending a signal to the heater to adjust the column temperature, expansion area temperature or expanded mobile phase temperature to obtain the desired temperature.
In another embodiment, the present disclosure relates to a method of reducing or preventing crystallization or freezing of a mobile phase upon expansion. The method includes the steps of measuring an expansion area temperature of the mobile phase in an area where a substantial portion of the mobile phase expands from a liquid form to a gas form, comparing the expansion area temperature with a desired temperature in the expansion area or expanded mobile phase, and adjusting the temperature of the mobile phase before, during or after expansion to obtain the desired temperature.
In another embodiment, the present disclosure relates to a method of reducing or preventing degradation of an analyte contained in a mobile phase upon expansion. The method includes the steps of measuring an expansion area temperature of the mobile phase in an area where a substantial portion of the mobile phase expands from a liquid form to a gas form, comparing the expansion area temperature with a desired temperature in the expansion area or expanded mobile phase, and adjusting the temperature of the mobile phase before, during or after expansion to obtain the desired temperature.
In another embodiment, the present disclosure relates to a method of reducing or preventing precipitation of an analyte in a mobile phase upon expansion. The method includes the steps of measuring an expansion area temperature of the mobile phase in an area where a substantial portion of the mobile phase expands from a liquid form to a gas form, comparing the expansion area temperature with a desired temperature in the expansion area or expanded mobile phase, and adjusting the temperature of the mobile phase before, during or after expansion to obtain the desired temperature.
The embodiments of the present disclosure are applicable to preparative, analytical and micro-analytical chromatographic systems and can include one or more of the following features. These systems can employ a mobile phase comprising only a compressed room temperature gas in liquid form (e.g., carbon dioxide) or can include modifiers, such as methanol. Because of the dynamic control associated with the present disclosure, embodiments of the present disclosure are also applicable to separations having mobile phase conditions or separation conditions that change (e.g., mobile phase gradient, column temperature gradient, column pressure gradient, etc.) during the separation. The carbon dioxide based chromatographic systems can also include a dedicated gas/liquid separator (GLS) to assist with the mobile phase expansion, the extraction of the liquid component of the mixture, or both. The temperature sensor can also be incorporated in the body of the GLS or in direct fluid communication therewith. The embodiments of the present disclosure are capable to controlling the temperature of the expansion area to specific ranges, such as 0° C. and 5° C. Further, some embodiments feature continuous or substantially continuous monitoring and adjusting of the temperature. Some embodiments feature feedback/overshoot control, such that temperature can be regulated and controlled dynamically throughout a separation, including a separation with gradient operating conditions.
Current systems use dynamic temperature control with no feedback across the phase change, e.g., no monitoring or adjusting of the temperature based on conditions or events related to phase change. Advantages of the present disclosure include dynamic control of the temperature in the mobile phase expansion area. The negative impacts on the system, such as crystallization, freezing, degradation, or precipitation of the mobile phase or analyte(s) of interest can be avoided. In particular, the present disclosure can minimize the effects of overheating the solvent which can degrade samples or analyte(s) of interest, can maintain a desired outlet temperature to prevent sample fallout from low solubility of an analyte(s) of interest or can maintain a desired outlet temperature to prevent crystallization or freezing of the solvent, or any portion thereof.
The foregoing and other features and advantages provided by the present disclosure will be more fully understood from the following description of exemplary embodiments when read together with the accompanying drawings.
The present disclosure relates to the regulation of carbon dioxide expansion in a carbon dioxide based chromatographic system. In particular, the present disclosure relates to minimizing or eliminating the deleterious effects of carbon dioxide expansion on the solvent, the analyte(s) of interest, the separation, the detection of the analyte(s) of interest, and other related aspects in a carbon dioxide based chromatographic system.
In one embodiment, the present disclosure relates to a chromatographic expansion regulation system comprising a chromatographic column having an inlet and an outlet, a mobile phase including a compressed room temperature gas in substantially liquid form (e.g., at least about 85% in liquid form, at least about 90% in liquid form) flowing through the column, a temperature sensor downstream of the outlet and located in an area where a substantial portion of the mobile phase expands from liquid form to gas form, wherein the sensor is capable of measuring the temperature in the expansion area, a heater in thermal communication with at least one of the column or the expansion area capable of adjusting the column temperature or expansion area temperature; and a temperature controller in signal communication with the sensor and the heater, wherein the controller is capable of receiving the temperature measurement from the sensor, comparing the temperature measurement with a desired temperature in the expansion area, and sending a signal to the heater to adjust the column temperature or expansion area temperature to obtain the desired temperature in the expansion area. The mobile phase can also be supercritical. For example, the mobile phase can be supercritical in the column where the conditions are above the critical temperature.
The chromatographic regulation system can be applied to any chromatographic system that uses a solvent and/or analyte of interest which undergoes a phase change. The phase change can be an expansion from liquid or supercritical to gas form. Upon expansion, a temperature drop occurs wherein the system of the present disclosure dynamically controls this temperature change through regulation. The phase change can also be a compression from gas to liquid or supercritical form. Upon compression, a temperature rise occurs wherein the system of the present disclosure dynamically controls this temperature change. For embodiments involving compression regulation systems, the temperature controlling device can be a chiller (e.g., column chiller). Embodiments herein dynamically control temperature after or during a phase change event. As a result of the devices, systems and methods described herein, temperature change of the solvent and/or analyte of interest is monitored and dynamically controlled to minimize adverse effects of expansion/compression of the mobile phase.
The embodiments of the present disclosure are applicable to preparative, analytical and micro-analytical chromatographic systems. The chromatographic column can be any column for use in any of these systems having an inlet and an outlet. In some embodiments, mobile phase gradient conditions are used.
The solvent, or mobile phase, can include any compressed room temperature gas that can be used in liquid or supercritical form during at least a portion of a chromatographic separation (e.g., carbon dioxide). The mobile phase can consist solely of the compressed room temperature gas or can have co-solvents or modifiers. The mobile phase can also have two or more compressible room temperature gases and/or one or more modifiers. In some embodiments, the mobile phase is 100% carbon dioxide. In other embodiments, the mobile phase is carbon dioxide with one or more modifiers, such as methanol.
Without wishing to be bound to theory, it is believed that the addition of co-solvents to the mobile phase reduces phase change and other set point temperatures. For example, when controlling post phase change conditions, the addition of a co-solvent reduces the temperature setpoint. Expansion of the mobile phase to a gas requires a known amount of energy. As thermal energy is typically the only available source, the expansion drops the temperature of the gas/fluid. The added thermal mass of the co-solvent(s) hold additional thermal energy that is then absorbed by the expanding carbon dioxide. The energy required is typically determined by the difference in enthalpy of the carbon dioxide at the heated condition before expansion and the desired condition after expansion. The co-solvent is not part of the expansion cooling load, but it can store thermal energy to transfer to the carbon dioxide during expansion. This extra energy from the co-solvent can change or reduce the liquid temperature.
The temperature sensor can be located downstream of the column outlet and in, near or adjacent to the area where a substantial portion of the expansion from liquid to gas occurs. The temperature sensor can include any traditional temperature sensor used in chromatographic systems to measure the temperature of a mobile phase in either liquid, gas, or mixed form. The sensor can be capable of measuring the temperature in, near or adjacent to the expansion area. For example, the temperature sensor can be a thermocouple, a thermistor or a resistance temperature detector (RTD). During operation of a carbon dioxide based chromatographic system the mobile phase can experience unintended phase change (e.g., liquid to gas). These unintended phase change occurrences are typically short in duration and not widespread throughout the system, and do not typically involve a substantial portion of the mobile phase.
The temperature sensor can be placed in an area at or just downstream of where the mobile phase (e.g., carbon dioxide) phase change occurs. The placement of the sensor can also be affected by the flow rate. The slower the flow rate, the closer the sensor can be placed to the phase change location. The present disclosure can be used with chromatographic systems that also use a gas/liquid separator (GLS). A GLS is a device designed to effectively and efficiently control the expansion of the solvent or mobile phase, and separate the gas portion from the liquid portion with minimal effects on the separated analyte(s) of interest. In one embodiment, the expansion area (110) is inside the GLS. In another embodiment, the temperature sensor (115) can be incorporated into, or placed at or inside, the GLS.
The heater can include any mobile phase heater, column heater or similar type heater used in chromatographic systems. For example, the heater can be a cartridge, a flexible circuit or a coil. The heater can be in thermal communication with at least one of the column, the expansion area, or both, such that the heater can effectively transfer heat energy to these devices or areas and can adjust the temperature in the column, expansion area or both. In one embodiment, the heater is located near the column outlet. In another embodiment, the heater is located adjacent to and upstream of the expansion area. The efficiency of heating is increased by heating the liquid phase. However, in some embodiments, the heater is located in or near the expansion area. Heat can be added in an amount sufficient to only heat to maintain the desired temperature after the phase change, and avoid heating the liquid phase.
In some embodiments, the heater can be a controlled heating device having an additional sensor within the heater. The second control point can add stability and provide control of the maximum temperature in the heating system.
The temperature controller can include any controller system used in chromatographic systems. The controller can be in signal communication with the sensor, the heater or both. For example, the controller can be a P controller, a PI controller, a PID controller, a Fuzzy Logic controller, or combinations thereof. The controller can also be capable of receiving the temperature measurement from the sensor, comparing the temperature measurement with a desired temperature in the expansion area, and sending a signal to the heater to adjust the column temperature or expansion area temperature to obtain the desired temperature in the expansion area.
The controller can also have a set of instructions utilized by the controller, wherein the controller is capable of receiving the temperature value from the sensor, comparing it against a desired temperature or temperature range, and adjusting at least one system component or parameter (e.g., the upstream heater) to achieve the desired temperature or temperature range in either solvent or mobile phase flowing into the expansion area, or the temperature or temperature range in the expansion area. The controller can also have a set of instructions utilized by the controller to handle temperature overshoot. Further the controller can control ramp rate of the heater to minimize the deleterious effects of the phase change event(s) on the separation and/or analysis.
The temperature measurement recorded by the sensor and received by the controller can vary over the course of the separation, assuming only static control, or no control, of such temperature. For example, in a gradient mobile phase separation in which the concentration of modifier varies over the course of the separation the temperature in the expansion area may vary over time. Similarly, in a temperature gradient separation in which the temperature of the column is varied during the separation, the temperature in the expansion area may vary over time. To avoid the deleterious effect of such temperature variations, an ideal or desired temperature in the expansion area can be pre-determined based on the system parameters (e.g., mobile phase composition, analyte(s) of interest, etc.). For example, a separation system including an analyte of interest that is subject to degradation upon freezing or upon exposure to excess heat can have a desired temperature, or temperature range, that avoids such freezing or such exposure. In one embodiment, the desired temperature is 0° C., 1° C., 2° C., 3° C., 4° C., 5° C., 6° C., 7° C., 8° C., 9° C., 10° C., 11° C., 12° C., 13° C., 14° C., 15° C., 16° C., 17° C., 18° C., 19° C. and 20° C. These temperatures can also define ranges, such as between about 0° C. and 5° C., or between about 5° C. and 20° C. The desired temperature or temperature range can be dependent on the system. Temperature affects such conditions as solvent condensing and separation in a GLS. High temperatures can degrade samples whereas low temperatures can cause freezing and external condensation. The desired temperature or temperature ranges can be one that eliminates or minimizes a combination of these affects.
Upon receiving the measured temperature in the expansion area, the controller can compare the temperature against the desired temperature as pre-determined to avoid or minimize any negative effects on the system, and send a signal to the heater to adjust the heat energy delivered to the mobile phase to adjust the measured temperature in the expansion area. In one embodiment, the system could be driven with a cascade control loop where the post phase change temperature feeds back to a controller that changes the heater set point temperature. The system can be designed to use the minimum heat required to maintain the desired temperature after the phase change. One intent, applicable to some embodiments, is to use as little heat as possible upstream to prevent freezing/sputtering, etc. during the phase change.
Adjustments to the solvent or mobile phase temperature can be made by the heater including cycling on and off (% duty cycle) the heating mechanism of the heater. The temperature can also be adjusted by adding a chiller or by the addition of make-up solvent or mobile phase. Make-up solvent or mobile phase can be added to the system to adjust the temperature hotter or colder. For example, make-up solvent or mobile phase can be added at or near the heater upstream of the expansion area to reduce the temperature and reduce the maximum temperature seen by the sample.
In another embodiment, the present disclosure relates to a chromatographic expansion regulation system having dual stage heating. The dual stage heating can be either before and after, before and during, or during and after the phase change. In other embodiments, the system can have multiple stage heating before, during or after the phase change. Dual and multiple stage heating provides additional controls and methods to reduce the minimum and maximum temperatures of the system. Variable heating (e.g., timing and intensity) with the multiple heaters can be designed to reduce the impact and change in temperature. Each heater can be in thermal communication with the column, the expansion area or the expanded mobile phase. Each heater can be capable of adjusting the column temperature, expansion area temperature or expanded mobile phase, as appropriate. Each heater can be in signal communication with the controller to adjust the column temperature, expansion area temperature or expanded mobile phase to obtain a desired temperature or temperature profile.
The present disclosure also relates to a method of reducing or preventing crystallization or freezing of a mobile phase upon expansion, the method comprising the steps of measuring an expansion area temperature or an expanded mobile phase temperature of the mobile phase in an area where a substantial portion of the mobile phase expands from a liquid or supercritical form to a gas form, comparing the expansion area temperature or expanded mobile phase temperature with a desired temperature, and adjusting the temperature of the mobile phase before or during expansion to obtain the desired temperature. In one embodiment, the desired temperature is a temperature, or temperature range, that reduces or prevents at least one of crystallization or freezing of the mobile phase in the expansion area. The desired temperature is at least about 0.5° C., 1° C., 1.5° C., 2° C., 2.5° C., 3° C., 3.5° C., 4° C., 4.5° C., 5° C., 5.5° C., 6° C., 6.5° C., 7° C., 7.5° C., 8° C., 8.5° C., 9° C., 9.5° C., 10° C., 11° C., 12° C., 13° C., 14° C., 15° C., 16° C., 17° C., 18° C., 19° C. and 20° C. above the crystallization or freezing temperature of the mobile phase, a component therefor. These temperatures can also define ranges, such as between about 0.5° C. and 20° C., or between about 1° C. and 15° C. The deleterious effects that can be addressed include no or reduced flow, damage to on-line equipment, sample damage, external condensation, prevention of sample propagation, etc.
The present disclosure also relates to a method of reducing or preventing degradation of an analyte contained in a mobile phase upon expansion. The method includes the steps of measuring an expansion area temperature or an expanded mobile phase temperature of the mobile phase in an area where a substantial portion of the mobile phase expands from a liquid or supercritical form to a gas form, comparing the expansion area temperature or expanded mobile phase temperature with a desired temperature, and adjusting the temperature of the mobile phase before or during expansion to obtain the desired temperature. The desired temperature is at least about 0.5° C., 1° C., 1.5° C., 2° C., 2.5° C., 3° C., 3.5° C., 4° C., 4.5° C., 5° C., 5.5° C., 6° C., 6.5° C., 7° C., 7.5° C., 8° C., 8.5° C., 9° C., 9.5° C., 10° C., 11° C., 12° C., 13° C., 14° C., 15° C., 16° C., 17° C., 18° C., 19° C. and 20° C. below the degradation temperature of at least one analyte of interest. These temperatures can also define ranges, such as between about 0.5° C. and 20° C., or between about 1° C. and 15° C. In one embodiment, the desired temperature, or temperature range, is a temperature that reduces or prevents degradation of an analyte contained in the mobile phase.
The present disclosure also relates to a method of reducing or preventing precipitation of an analyte in a mobile phase upon expansion. The method includes the steps of measuring an expansion area temperature or an expanded mobile phase temperature of the mobile phase in an area where a substantial portion of the mobile phase expands from a liquid or supercritical form to a gas form, comparing the expansion area temperature or expanded mobile phase temperature with a desired temperature, and adjusting the temperature of the mobile phase before or during expansion to obtain the desired temperature. The desired temperature is at least about 0.5° C., 1° C., 1.5° C., 2° C., 2.5° C., 3° C., 3.5° C., 4° C., 4.5° C., 5° C., 5.5° C., 6° C., 6.5° C., 7° C., 7.5° C., 8° C., 8.5° C., 9° C., 9.5° C., 10° C., 11° C., 12° C., 13° C., 14° C., 15° C., 16° C., 17° C., 18° C., 19° C. and 20° C. above the temperature at which at least one analyte of interest precipitates out of the mobile phase during or related to the expansion. These temperatures can also define ranges, such as between about 0.5° C. and 20° C., or between about 1° C. and 15° C. In another embodiment, the desired temperature is a temperature, or temperature range, that reduces or prevents precipitation of an analyte contained in the mobile phase.
The disclosures of all cited references including publications, patents, and patent applications are expressly incorporated herein by reference in their entirety. Further, when an amount, concentration, or other value or parameter is given as either a range, preferred range, or a list of upper preferable values and lower preferable values, this is to be understood as specifically disclosing all ranges formed from any pair of any upper range limit or preferred value and any lower range limit or preferred value, regardless of whether ranges are separately disclosed. Where a range of numerical values is recited herein, unless otherwise stated, the range is intended to include the endpoints thereof, and all integers and fractions within the range. It is not intended that the scope of the invention be limited to the specific values recited when defining a range.
This application claims priority to U.S. Provisional Patent Application Ser. No. 62/412,448 entitled “Expansion Regulation in Carbon Dioxide Based Chromatographic Systems,” filed on Oct. 25, 2016, the content of which is hereby incorporated by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 62412448 | Oct 2016 | US |
