CA1319539C - Method and apparatus for collecting samples for analysis of chemical composition - Google Patents
Method and apparatus for collecting samples for analysis of chemical compositionInfo
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- CA1319539C CA1319539C CA 602535 CA602535A CA1319539C CA 1319539 C CA1319539 C CA 1319539C CA 602535 CA602535 CA 602535 CA 602535 A CA602535 A CA 602535A CA 1319539 C CA1319539 C CA 1319539C
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N1/00—Sampling; Preparing specimens for investigation
- G01N1/02—Devices for withdrawing samples
- G01N1/10—Devices for withdrawing samples in the liquid or fluent state
- G01N1/18—Devices for withdrawing samples in the liquid or fluent state with provision for splitting samples into portions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/281—Sorbents specially adapted for preparative, analytical or investigative chromatography
- B01J20/291—Gel sorbents
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N1/00—Sampling; Preparing specimens for investigation
- G01N1/28—Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
- G01N1/40—Concentrating samples
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/84—Preparation of the fraction to be distributed
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N35/00—Automatic analysis not limited to methods or materials provided for in any single one of groups G01N1/00 - G01N33/00; Handling materials therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/54—Sorbents specially adapted for analytical or investigative chromatography
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N1/00—Sampling; Preparing specimens for investigation
- G01N1/28—Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
- G01N1/40—Concentrating samples
- G01N1/4022—Concentrating samples by thermal techniques; Phase changes
- G01N2001/4027—Concentrating samples by thermal techniques; Phase changes evaporation leaving a concentrated sample
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N2030/022—Column chromatography characterised by the kind of separation mechanism
- G01N2030/027—Liquid chromatography
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/26—Conditioning of the fluid carrier; Flow patterns
- G01N30/28—Control of physical parameters of the fluid carrier
- G01N30/30—Control of physical parameters of the fluid carrier of temperature
- G01N2030/3084—Control of physical parameters of the fluid carrier of temperature ovens
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/62—Detectors specially adapted therefor
- G01N30/74—Optical detectors
- G01N2030/743—FTIR
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/84—Preparation of the fraction to be distributed
- G01N2030/8411—Intermediate storage of effluent, including condensation on surface
- G01N2030/8417—Intermediate storage of effluent, including condensation on surface the store moving as a whole, e.g. moving wire
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/88—Integrated analysis systems specially adapted therefor, not covered by a single one of the groups G01N30/04 - G01N30/86
- G01N2030/8804—Integrated analysis systems specially adapted therefor, not covered by a single one of the groups G01N30/04 - G01N30/86 automated systems
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/0005—Field flow fractionation
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/26—Conditioning of the fluid carrier; Flow patterns
- G01N30/38—Flow patterns
- G01N30/44—Flow patterns using recycling of the fraction to be distributed
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/80—Fraction collectors
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- Chemical & Material Sciences (AREA)
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- General Health & Medical Sciences (AREA)
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Abstract
ABSTRACT
An automated, on-line solvent elimination interface system is described for use in characterizing the Composition Distribution (CD) of unknown materials emerging from a fractionating unit or a process stream. Fractionated samples to be analyzed, such as a polymer, in highly diluted form in one or more solvents, are provided by a fractionation unit such as a gel permeation chromatograph (GPC), a high pressure liquid chromatograph (HPLC), or a field flow fractionator (FFF). A
number of discharges of each particular fraction are supplied to individual collection units within the interface system under controlled conditions of flow rate, temperature and pressure (vacuum) such that the solvents are flash-evaporated at the collection unit. A sufficient solid residue is built up on the collection unit for analysis by, for example, a Fourier transform infrared (FTIR) analyzer.
An automated, on-line solvent elimination interface system is described for use in characterizing the Composition Distribution (CD) of unknown materials emerging from a fractionating unit or a process stream. Fractionated samples to be analyzed, such as a polymer, in highly diluted form in one or more solvents, are provided by a fractionation unit such as a gel permeation chromatograph (GPC), a high pressure liquid chromatograph (HPLC), or a field flow fractionator (FFF). A
number of discharges of each particular fraction are supplied to individual collection units within the interface system under controlled conditions of flow rate, temperature and pressure (vacuum) such that the solvents are flash-evaporated at the collection unit. A sufficient solid residue is built up on the collection unit for analysis by, for example, a Fourier transform infrared (FTIR) analyzer.
Description
~3 ~ ~3~
METHOD AND APPARATUS FOR COLLECTING
SAMPLES FOR ANALYSIS OF CHEMICAL COMPOSITION
BACKGROUND OF THE INVENTION
On-line analysis of the chemical composition o a solute in a carrier medium (e.g., a solvent) combination has been accompiished using various known techniques, such as a gel permeation chromatograph ~GPC) coupled to an ultraviolet (W) spectrometer. Generally, the success of such a technique depends on how well the solutes can be differentiated from the carrier medium. This differentiation has been relatively easy in most cases, but there are cases in which the carrier medium seriously interferes with the on-line analysis of the solute, rendering a particular analysis technique less useful tha~
desired.
For example, in flow-thru high pxessure liquid chromatographic (HPLC) systems coupled to a Fourier transform infrared (FTIR) spectrometer, the chrvmatographis solvent often interferes with the detection of the solute. Th~refore, various flow-thru cells (e.g., see C.C~ Johnson and L.T.
Taylor, Anal. che~., 56, 2642-2647 (1984)) as well as interfaces to eliminate the solvent prior to analysis (e.g., see C.M. Conroy, P.R. Griffiths, and R. Jinno, Anal. ChemO, 57, 822-825 (1985)) have been designed. Eliminating low-boiling point 501vent5 such as hexane is easy to accomplish, but not so with water or higher-boiling organic solvents. With high boiling point solvents such as trichlorobenzene (TCB), which is a common solvent in the analysis of polymers by gel permeation chromatography tGPC), the situation is one of the worst.
Consequently, on-line polymer composition analysis in a TCB
solvent system by GPC/FTIR has so far remained in the realm of concept only. Similarly, FTIR as a powerful and versatile analytical tool for HPLC, GPC and process analyzers has been limited in its application because o~ the solvent or process interference problems.
~3~3~
Ideally, to eliminate the solvent-solute interference problems, whether in a GPC experiment or in continuous process control, one would like to eliminate the solvent altogether.
If a technique can eliminate TCB, then it readily may be used to eliminate substantially any other chromatographic or process solvent.
Overcoming the above mentioned problem in high-temperature (HT) GPC would benefit studies aimed at determining composition distributions (CD) in polymers ~e.g.,L. Wild, T.R.
Ryle, D.C. Knobeloch, and I.R. Peat, J._ Polymer Science:
Polymer Physics Edition, 20 441-455 (1982~). CD is the change in comonomer composition of polymer chains as a function of their molecular weight (MW). Most CD studies of crystalline or amorphous polymers have depended on large-scale fractionation or cross-fractionation, often followed by a slow solvent-stripping step to prepare the fractions for subse~uent analytical measurements. Only in favorable cases, such as in semicrystalline polymers, where a relationship may be established between comonomer content and melting temperature has the need for an on-line composition detector not been essential. In contrast, amorphous polymers cannot benefit from such empirical relationships. Consequ~ntly, most separations have depended on solvent/non-solvent fractionations (e.g., H.
Sato et al, Macromolecules, 19, 2613 (1986)). These operations are very tedious and time-intensive, and although the individual steps can be automated to reduce manpower requirements (D.L. Newhouse, R.G. Wheeler, and R.H. Waltz, U.S.
Patent 4,604,363 (1586)), the time-intensive nature of the analysis still remains a big hurdle to be overcome. Recent advances in HT-GPC- W have been used for composition analysis (e.g., S~ Mori and T. Suzuki, J. of Liquid Chrom., 4(10), 1685 (1981)), but the limitations impo~ed on the choice o~ solvent and the rPquirement that the polymer or solute must have a W -active group restrict the applicability of this technique.
Although FTIR is a less sensitive tool than W, it is by far the more powerful structural tool because of its superior selectivity in terms of chemical species differentiation.
3 ~ 3 ~
Another area where FTIR would be of tremendous importance is in the area o~ on-line analysis of liquid proc~ss streams, regardless if the strsam is heterogeneous in nature or if the solutes are UV~inactive. The essential question is how to eliminate the solvent on-line for subsequent, automated on-line or off-line analytical measurements such as by FTIR.
SUMMARY OF THE INVENTION
In accordance with the present invention, methods and apparatus are provided which are particularly suitabl-e for determining the compositional distribution (CD~ of unknown materials such as polymers using a fractionation unit which employs a high boiling point solvent (such as TCB). To that end, an interface system is provided between such fractionation unit (typically a GPC unit) and an analyzer unit such as a Fourier transform infrared (FTIR) analyzer. The interface system comprises a vacuum oven, the temperature and pressure of which is adjusted depending on the boiling point/vapor pressure characteristics of the solvent or solvent mixture that is to be eliminated. The oven may be configured in various ways. One is to equip it with a carousel-type programmable fraction collector having a discrete number of plates or hollowed dishes formed of potassium bromide (KBx~.
Another is to us~ a continuous collector which may be used, for instance, as an on-line plant stream (liquid phase) analyzer.
In that case, the device would be separated into two differentially pumped chambers; one for collection of solvent-free samples and the other for on-line analysis (e.g. by FTIR
or near-infrared fiber optic systems). Either way, the effluent from a fractionator unit is supplied as droplets and, as each droplet falls on the fraction collector, the solvent is flashed off immediately, leaving behind a residue. The process may be repeated as many times as desired before moving to the next collector position. Either during or after the collection step, the compositions of the fractions are determined automatically using a chosen microanalytical technique.
13~9~3~
For safety reasons, it is preferable that the interface system have no exposed heating elements. Pressure and temperature are regulated so that when a solution droplet comes in contact with the collecting medium on a fraction collector (e.g., infrared window-dish), the solvent flash evaporates, leaving behind a rPsidue. In the case of hi~h-boiling point solvents such as trichlorobenzene, an additional stream of preheated nitrogen or other inert gas blowing over the collection site hPlps smooth the flash evaporation and eliminates potential splashing problems during the collection step.
Splashing could occur, for example, if the oven temperature is too high or too low for a given pressure. The droplet size may also play a role, depending on the physical properties of the droplet such as surface tension. Splashing may be minimized using different tip geometries to control droplet size, adjusting the flow and/or temperature of the inert gas blown onto the collection site, and/or adjusting the gap between the effluent tip and the collecting plate. Under such conditions, the gap could be so small that the effluent flows onto the collecting plate without forming droplets but the solvent is, nevertheless, flash-evaporated.
A preferable approach to suppress splashing and othsr problems, however, is to atomize the effluent such as by using an ultrasonic atomizer, pre~erably of the non-pneumatic and non-electrostatic type (for safety). If such a nozzle is used, then the inert gas flow pattern in the vacuum oven preferably is designed so that the atomi~ed particles are channeled only toward the collecting plate.
In any case, so long as the droplets are confined to falling on the collecting plate, smaller droplets are preferred to enhance evaporation.
The improved system of this invention can be used with either homogeneous or heterogeneous solutions to study compositional variations in a complex chemical system as it emerges from the interfaced unit.
~ 3 ~
Although the exampl~s which will be described hereinafter are based on fractionations using size exclusion chromatography, the interface unit can be adapted, with proper modifications and valvings, to other fractionations based on crystallinity differences (temperature elution fractionation), field flow fractionations (FFF), adsorption chromatography, or other arrangements which may involve homogeneous or heterogeneous polymer solutions or other mixtures.
DESCRIPTION-OF THE DRAWINGS
Figure 1 is a schematic diagram, not drawn to scale, including a fractionator and an interface system constructed in accordance with the invention; and Figure 2 is a Fourier Transform Infrared (FTIR) spectrum of an ethylene-propylene rubber residue collected utilizing an apparatus of the type shown in Figure 1;
Figure 3 illustrates a CD ~rofile ~upper trace) and gel permeation chromatogram (lower trace) for one type of ethylene-propylene rubber (EPR) which was analy~ed employlng this invention;
Figure 4 illustrates a CD profile (upper trace) and gel permeation chromatogram (lower trace) for a second EPR
sample collected by the method of this invention;
Figure S illustrates in a cross-sectional view, an oven and associated apparatus constructed in accordance with this invention.
DETAILED DESCRIPTION OF.THE INVENTTON
A schemati~ diagram, not drawn to scale, including a fractionator, and an interface system according to the present invention, i5 shown in Figure 1. The interface is relatively enlarged to show its details.
Referring to Figure 1, a fractionator lO such as a gel permeation chromatograph of a conventional and commercially available type such as a Waters Type 150-C GPC, is shown.
Fractions of a sample of a material to be analyzed are provided in the form of a solute carried by a liquid solvent such as trichlorobenzene (TCB) via an outlet line 11~ The outlet line 11 is connected to a sample inlet port 12 of a vacuum oven 13.
~3~3~
An effluent sample supplying means 14, for example, stainless steel tubing of 0.009 inches inner diameter, extends from sample inlet port 12 to a point within oven 13 adjacent a sample collection s station 15. Suitable valving (not shown) may be provided between outlet line 11 and sample inlet port 12 as needed to insure that liquid samples are provided at an appropriate rate at the collection station 15. It is preferable that small droplets be 10 supplied to enhance the desired step of flash evaporation. Typically, oven 13 may have a capacity of 0.2 cubic feet and preferably is capable of being heated to a controlled temperature of the order of 200C. Vacuum ovens which are available commercially (such as NAPCO ~ Model 5831) may be modified so as to be suited for such use, provided there are no heating elements exposed on the inside of oven 13 or the oven may be constructed specifically for the present purposes. A hole 20 having a vacuum seal 16 is provided in the center of the ceiling 17 of the oven 13 through which a shaft 18 is inserted. The shaft 18 is attached to a fraction collector 19 inside the oven 13. The fraction collector 19 is a disk of, for example, 25 aluminum of 14.5 centimeters diameter. As will appear below, such a configuration is particularly suitable where subsequent FTIR analysis is to be performed. Holes are provided along the circum-ference of the disk to hold, for example, sixteen 30 KBr (potassium bromide) plates, cups or vials 20.
The shaft 18 is attached to a stepper motor unit 21 which is mounted externally on top of the oven 13.
A power and logic signal cable 22 is connected from the stepper motor 21 to a command or control system 35 23 including, for example, a Compaq ~ Computer.
The position of the fraction collector 19 is sensed - 6a - ~ ~ 9 ~3~
using a position sensor 24 (such as a fixed photocell and a slotted wheel connected to shaft 18). The position of the fraction collector 19 is controlled making use of the sensor 24, stepper s motor 21, and the command system 23 (software commands) in a conventional closed loop position control arrangement.
Another hole is provided in the side wall 25 of the oven 13 to introduce a nitrogen line 26 10 which is connected to - 6a -an external nitrogen supply 36. The nitrogen line 26 is associated with a heater 27 so that nitrogen provided via line 26 can maintain the desired temperature at the surface of th~
KBr cups 20, a~ required. Line 26 may be coaxial with tubing 14, (surrounding tubing 14) or may be separate from tubing 14.
In the latter case, line 26 preferably is also made flexible or movable to adjust the position of a blowing point 30.
A heater 28 is provided outside of oven 13 and a temperature sensing apparatus 29 (such as a thermocouple) is provided within oven 13 in the vicinity of collection station 15. The héater 28, temperature sensor 29 and command system 23 are coupled in a closed loop temperature control system. While the heaters 27 and 28 are shown as separate devices, in practice they may be parts of a single heater. A single heater arrangement may be advantageous in that the temperature of oven 13 and that of the blown nitrogen then may readily be maintained substantially equal. For safety reasons, it is preferable that the temperature of the hot nitrogen should not exceed that of oven 13.
Oven 13 is provided with a vacuum line 31 which extends inside of oven 13, a pressure (vacuum~ sensing apparatus 32 connected to oven 13, and a vacuum pump 33 arranged to maintain the pressure within oven 13 at a predetermined level.
A dual cold trap 34 is associated with vacuum line 31 for collection of solvent evaporated within oven 13 as will be explained below~
The pressure sensing apparatus 32 is coupled to command system 23 to assist in maintaining the pressure (vacuum) within oven 13 in a predetermined range. The control arrangement preferably is configured so that if pressure and/or temperature exceed predetermined safety limits, warning signals are generated, power to the oven 13 is shut off and the chromatographic effluent is diverted away from the oYen 13.
The geometry of the XBr collecting crystal 20 was found to be an important parameter. Flat KBr plates were found to be a less suitable collection media when the effluent is ~3~5~
introduced as droplets. In that case, droplets of solution tend to flow to the edges of the plate 20 before the solvent evaporates. Consequently the collected sample (e.g.l a polymer) deposits along the edges of plate 20 and it is difficult to get a good spectrum from such a sample.
Therefore, the use of KBr cups 20 is o~ten preferred. The latter act as a small ~vial~ and position the solute at the center of the cup 20.
If, on the other hand, flat KBr plates are to be used, then the GPC effluent should be applied to the plate 20 as a fine mist, using such devices as a non-electrostatic, ultrasonic atomizing nozzle (e.g. a Sono-Tek ultrasonic nozzle). The fine particle sizes of the atomized spray help the flash-evaporation, depositing a thin layer of fractionated materia} on the collection plate 20.
Depending on the particular circumstances, besides KBr cups, other collection media are possible. One possibility is the use of metal or glass cups containing suitable powders for diffuse reflectance measurements using normal accessories or microsampling devices. Another is to use a metal strip (with low infrared absorption characteristics) on which the material is deposited for subsequent surface analysis (e.g., using surface analysis techniques or microsampling accessories). A third possibility is to use tiny metal dishes for collecting fractions to be analyzed using a mass spectrometric technique, for example.
The apparatus according to this invention can be ~iniaturized, converted to a continuous on-line process analyzer using the dual chamber configuration described above, or used as an interface device for other types of analytical techniques. In particular, a grid type design, typical of some fxaction collection devices, is an alternative. If the interface is to be used for on-line process analysis, then the details of the oven and that of the collecting medium are likely to be changed.
During a run, the varuum oven 13 is maintained at a high enough temperature and vacuum to allow the solvents to ~1 3 ~
flash evaporate as they come in contact with the KBr dish 20.
The effluent to be sampled (e.g. GPC effluent) is directed into the oven 13 through the stainless steel tubing 14 inserted through the vacuum-tight opening on the sidewall of the oven 13. Although this tubing 14 may be externally valved for proper flow-rate control, it was not needed for the experiments described herein.
The effluent enters the oven 13, and falls on the KBr cups 20 drop-by-drop at a flow rate of, for example, 0.5 milliliters per minute. In order to assure that each droplet immediately loses its solvent, the temperature and pressure of the oven 13 should be adjusted, depending on the boiling point/vapor pressure characteristics of the solvent to be eliminated. For example, if TCB is the solvent, the temperature-pressure relationship given below should be consulted.
Table: Vapor pressure of TCB
Vapor pressure 760 400 100 40 10 5 (mn~Ig) Temp-erature 213.0 187.7 140.0 114.8 87.7 67.3 38.4 C) This relationship establishes a minimum temperature needed for evaporation o a single drop, but actual temperatures in oven 13 should be maintained above the theoretical value by, for example, at least 4QC to insure efficient evaporation of many drops falling on the same cup 20.
This additional temperature increment is required since the heat of vaporization will drop the temperature of the cup 20 below the boiling point of the solvent (under the given conditions). To insure the cup 20 is hot enough throughout the collection stage, the temperature of oven 13 should therefore be maintained higher than the theoretical boiling point of the solvent, and/or one must provide an additional source of heat directly to the cup surface.
With TCB as the chromatographic solvent, a stream of hot nitrogen blowing over the collecting cup 20 was found to be ~ 3 ~
beneficial, and at the same time effectively eliminated splashing problems. The heated nitrogen was introduced via the flexible metal tubing 26. The temperature of the nitrogen is controlled by means of a thermocouple (not shown) placed after the heating cartridge 27. The tip of the nitrogen line 26 may be equipped with a baf~le to control the size of the heated area. Alternatively, a perforated toroidal (ring-shaped) nozzle may be employed to provide a unifo~m cylindrical jet of inert gas at the sample collection station 15.
As droplets fall on a cup 20 at collection station 15, and the solvent immediately flash~s off, the cup 20 will contain the fractionated residue. The flashed-off solvent is continuously carried away from the vacuum oven via vacuum line 31 into cold trap 34 where the solvent is condensed. Cold trap 24 is emptied on a regular basis. A~ter a fraction is collected, the carousel 19 moves to the next position, and so on. It was found that sample quantities as small as one microgram were sufficient for subsequent FTIR analysi~. The residence time at each position is either preset or triggered, depending on the experimental setup and the distribution pattern of the chromatographic information ~ie. continuous or discrete signals)~ If an ult~asonic atomizer is used, especially of the non-electrostatic type, then the nozzle-to-plate distance is adjusted, depending on the desired pattern of the sprayed material. The nozzle geometry and the ultrasonic frequency can also be adjusted to control the spray pattern or the spot size. To assure that the atomized mist emerging from the nozzle is channeled entirely toward the collecting plate 20, the vacuum port 31 preferably is positioned beneath the carousel 19, and pr~ferably ben~ath plate 20 at collection station 15. If the latter option i5 chosen, then additional openings on the carousel 19, in the vicinity of plate 20, will assure a uniform flow of heated nitro~en around the plate 20.
In addition, a cylindrical jet of hot nitrogen in the direction of the plake 20, and of a chosen diameter, will further channel or direct the atomized particles emerging from the nozzla toward plate 20 only.
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Af~er the collection is ovPr, the temperature of the oven 13 is brought down and the vacuum broken. The carousel 19 i5 now ready for composition analysis using selected microanalytical techniques. Since FTIR was contemplated in this case, the carousel 19 is detached from shaft 18, removed from the oven 13 and placed into the auto sampler assembly of the FTIR spectrometer (into which it is designed to fit) to automatically record the spectra of the collected samples.
An interface system of the type shown in Figure 1 was connected to a GPC (Waters, Inc., Type 150-C~ and the effect of the vacuum on the flow rate and the system pressure was examined. It was found that the flow rate in the GPC is not at all affected by the pressure drop in the vacuum oven 13 at 1 mm Hg as compared to 760 mm Hg.
Experimental details.
In the experiment, first, a 0.6 weight percent solution of EPR was prepared in TCB and 100 microliters of this solution was injected into the GPC coupled to the interface system of the type shown in Figur~ 1. The column temperature was maintained at 120C, flow rate at 0.5 ml/min. The pressure of the oven 13 was maintained at 40 mm Hg, while its temperature was about 150~C, with a gentle flow of N2 through the system. The operation of ~he interace system was observed. The effluent was continuously flash evaporated in the interface oven 13 and a thin film of the EPR residue was formed on a gBr cup 20 (13x2 mm). The FTIR spectrum of the sample was recorded and is shown in Figure 2. Similar experiment~ were performed successfully with ethylene-vinyl acetats ~EVA) copolymers.
In the FTIR spectrum shown in Figure 2, not only a C-H stretching region at about 2800-3000 cm~1 but also a bending region at about 1400 cm~l can clearly be observed.
Based on experiments similar to those described above, the detectability limit of the method was investigated. It was found that one microgram of sample is sufficient to permit quanitatlve analysis. With typical concentrations of the low ~ 3 ~
and high ends of the GPC effluent of the order of 10-6 grams per milliliter, if ten fractions are collected for each sample, the collection period will be about two minutes per fraction and the deposition amounts of sample at the extremes will be about one microgram (minimum). A residue of, for example 6.6 micrograms would display an excellent signal-to-noise ratio.
In two separate experiments, seven fractions were collected from each of two rubbers. The ov~n temperature was maintained ~t 130'C, oven pressure was in the vicinity of 5-10 mm Hg, and the nitrogen flow rate was about o.3 cc/minute.
The mov~ments of carousel 19 were timed based on an analysis of the elution time profile from a previous chromatogram of the same material utilizing a conventional differential refractometer (DRI). Durin~ the actual fraction collection, the DRI detector was bypas~ed.
To adjust the temperature and the pressure of the oven 13 to assure smooth flash-evaporation and eliminate splashing problems, an external source of heated nitrogen 36 was introduced into the system and directed at the sample-collection site 15. Although this additional flow calls for a slight sacrifice in the vacuum of the oven 13, the loss is small, since it could bring the vacuum from 1 mm to 5 mm Hg or hi~her. From standard temperature-pressure tables, it appears that 1-5 mm Hg vacuum at 50-70~C would be a minimum vacuum to accomplish the task. Actual oven temperatures should be maintained 30-50C higher than the theoretical evaporation point to account for any heat of vaporization at the collector position 15. The flashed-off solvents were collected in the dual cold trap 34.
The amount of polymer deposited in each dish 20 will depend on the particular fractionation and polymer system studied. For instance, if ethylene-propylene co-polym0rs are fractionated on a GPC column at a temperature of 130-150C, using trichlorobe~zene as a solvent, the average weight of the deposit will be in the 1-50 microgram range. Under these conditions, good quantitative FTIR spectra are obtained.
13 ~ 5~
The two EPR samples were fractionated using the apparatus of Figure 1. The spectra Qf the collected fractions were obtained by placing the carousel 19 into the autosampler of an FTIR spectrometer. From the spectra, the percent ethylene of each fraction was calculated. The retention time vs. percent ethylene profile is shown in the upper trace of Figure 3 for the first sample. The vertical lines on the GPC
curve show the timing of the fraction collection. The ease of obtaining such CD information is unprecedented. The higher molecular weight samples are retrieved earlier (lower trace-left hand end) while the higher molecular weight samples are retrieved later.
The Ethylene CD for the second sample is shown in the upper trace in Figure 4. In this case the percent ethylene decreases with decreasing k~. The presence of a low-ethylene content, low-MW fraction is evident from Figure 4 (right hand end). Although these profiles were obtained from a single GPC
fractionation, the extension to more complex cxoss-fractionations or solvent/non-solvent fractionations will readily be apparent to those engaged in this art.
A more accurate representation of an oven 13 and associated components as explained above is shown in cross section in Figure 5 wherein the same r~Prence characters are used as in Figure 1 for corresponding parts.
The concept of flash evaporating such high boiling solvents as TCB has been successfully demonstrated by means of the illustrated apparatus. It could be used for further investigation of structure-property relationships.
While the apparatu~ described above may be implemented utilizing various arrangements of commercially available hardware elements or may be custom designed according to a particular application, one set of readily usable controller components which was obtained from Cybernetic Microsystems of San Gregoria, California comprises their ModPl CY525 Motor Controller, CY750 I/0 Controller, CY232 Serial Controller, CY300 LCD/Keyboard Controller, CY250 System Controller and CYB-002 Csntrol Board.
In general, the sensing and control elements themselves may be constructed in a conventional manner (See, for example, the description of similar components in U.S.
Patent No. 4,604,363 referred to abovP).
The novel aspects of the foregoing method and apparat~s are set forth in the following claims.
1~
METHOD AND APPARATUS FOR COLLECTING
SAMPLES FOR ANALYSIS OF CHEMICAL COMPOSITION
BACKGROUND OF THE INVENTION
On-line analysis of the chemical composition o a solute in a carrier medium (e.g., a solvent) combination has been accompiished using various known techniques, such as a gel permeation chromatograph ~GPC) coupled to an ultraviolet (W) spectrometer. Generally, the success of such a technique depends on how well the solutes can be differentiated from the carrier medium. This differentiation has been relatively easy in most cases, but there are cases in which the carrier medium seriously interferes with the on-line analysis of the solute, rendering a particular analysis technique less useful tha~
desired.
For example, in flow-thru high pxessure liquid chromatographic (HPLC) systems coupled to a Fourier transform infrared (FTIR) spectrometer, the chrvmatographis solvent often interferes with the detection of the solute. Th~refore, various flow-thru cells (e.g., see C.C~ Johnson and L.T.
Taylor, Anal. che~., 56, 2642-2647 (1984)) as well as interfaces to eliminate the solvent prior to analysis (e.g., see C.M. Conroy, P.R. Griffiths, and R. Jinno, Anal. ChemO, 57, 822-825 (1985)) have been designed. Eliminating low-boiling point 501vent5 such as hexane is easy to accomplish, but not so with water or higher-boiling organic solvents. With high boiling point solvents such as trichlorobenzene (TCB), which is a common solvent in the analysis of polymers by gel permeation chromatography tGPC), the situation is one of the worst.
Consequently, on-line polymer composition analysis in a TCB
solvent system by GPC/FTIR has so far remained in the realm of concept only. Similarly, FTIR as a powerful and versatile analytical tool for HPLC, GPC and process analyzers has been limited in its application because o~ the solvent or process interference problems.
~3~3~
Ideally, to eliminate the solvent-solute interference problems, whether in a GPC experiment or in continuous process control, one would like to eliminate the solvent altogether.
If a technique can eliminate TCB, then it readily may be used to eliminate substantially any other chromatographic or process solvent.
Overcoming the above mentioned problem in high-temperature (HT) GPC would benefit studies aimed at determining composition distributions (CD) in polymers ~e.g.,L. Wild, T.R.
Ryle, D.C. Knobeloch, and I.R. Peat, J._ Polymer Science:
Polymer Physics Edition, 20 441-455 (1982~). CD is the change in comonomer composition of polymer chains as a function of their molecular weight (MW). Most CD studies of crystalline or amorphous polymers have depended on large-scale fractionation or cross-fractionation, often followed by a slow solvent-stripping step to prepare the fractions for subse~uent analytical measurements. Only in favorable cases, such as in semicrystalline polymers, where a relationship may be established between comonomer content and melting temperature has the need for an on-line composition detector not been essential. In contrast, amorphous polymers cannot benefit from such empirical relationships. Consequ~ntly, most separations have depended on solvent/non-solvent fractionations (e.g., H.
Sato et al, Macromolecules, 19, 2613 (1986)). These operations are very tedious and time-intensive, and although the individual steps can be automated to reduce manpower requirements (D.L. Newhouse, R.G. Wheeler, and R.H. Waltz, U.S.
Patent 4,604,363 (1586)), the time-intensive nature of the analysis still remains a big hurdle to be overcome. Recent advances in HT-GPC- W have been used for composition analysis (e.g., S~ Mori and T. Suzuki, J. of Liquid Chrom., 4(10), 1685 (1981)), but the limitations impo~ed on the choice o~ solvent and the rPquirement that the polymer or solute must have a W -active group restrict the applicability of this technique.
Although FTIR is a less sensitive tool than W, it is by far the more powerful structural tool because of its superior selectivity in terms of chemical species differentiation.
3 ~ 3 ~
Another area where FTIR would be of tremendous importance is in the area o~ on-line analysis of liquid proc~ss streams, regardless if the strsam is heterogeneous in nature or if the solutes are UV~inactive. The essential question is how to eliminate the solvent on-line for subsequent, automated on-line or off-line analytical measurements such as by FTIR.
SUMMARY OF THE INVENTION
In accordance with the present invention, methods and apparatus are provided which are particularly suitabl-e for determining the compositional distribution (CD~ of unknown materials such as polymers using a fractionation unit which employs a high boiling point solvent (such as TCB). To that end, an interface system is provided between such fractionation unit (typically a GPC unit) and an analyzer unit such as a Fourier transform infrared (FTIR) analyzer. The interface system comprises a vacuum oven, the temperature and pressure of which is adjusted depending on the boiling point/vapor pressure characteristics of the solvent or solvent mixture that is to be eliminated. The oven may be configured in various ways. One is to equip it with a carousel-type programmable fraction collector having a discrete number of plates or hollowed dishes formed of potassium bromide (KBx~.
Another is to us~ a continuous collector which may be used, for instance, as an on-line plant stream (liquid phase) analyzer.
In that case, the device would be separated into two differentially pumped chambers; one for collection of solvent-free samples and the other for on-line analysis (e.g. by FTIR
or near-infrared fiber optic systems). Either way, the effluent from a fractionator unit is supplied as droplets and, as each droplet falls on the fraction collector, the solvent is flashed off immediately, leaving behind a residue. The process may be repeated as many times as desired before moving to the next collector position. Either during or after the collection step, the compositions of the fractions are determined automatically using a chosen microanalytical technique.
13~9~3~
For safety reasons, it is preferable that the interface system have no exposed heating elements. Pressure and temperature are regulated so that when a solution droplet comes in contact with the collecting medium on a fraction collector (e.g., infrared window-dish), the solvent flash evaporates, leaving behind a rPsidue. In the case of hi~h-boiling point solvents such as trichlorobenzene, an additional stream of preheated nitrogen or other inert gas blowing over the collection site hPlps smooth the flash evaporation and eliminates potential splashing problems during the collection step.
Splashing could occur, for example, if the oven temperature is too high or too low for a given pressure. The droplet size may also play a role, depending on the physical properties of the droplet such as surface tension. Splashing may be minimized using different tip geometries to control droplet size, adjusting the flow and/or temperature of the inert gas blown onto the collection site, and/or adjusting the gap between the effluent tip and the collecting plate. Under such conditions, the gap could be so small that the effluent flows onto the collecting plate without forming droplets but the solvent is, nevertheless, flash-evaporated.
A preferable approach to suppress splashing and othsr problems, however, is to atomize the effluent such as by using an ultrasonic atomizer, pre~erably of the non-pneumatic and non-electrostatic type (for safety). If such a nozzle is used, then the inert gas flow pattern in the vacuum oven preferably is designed so that the atomi~ed particles are channeled only toward the collecting plate.
In any case, so long as the droplets are confined to falling on the collecting plate, smaller droplets are preferred to enhance evaporation.
The improved system of this invention can be used with either homogeneous or heterogeneous solutions to study compositional variations in a complex chemical system as it emerges from the interfaced unit.
~ 3 ~
Although the exampl~s which will be described hereinafter are based on fractionations using size exclusion chromatography, the interface unit can be adapted, with proper modifications and valvings, to other fractionations based on crystallinity differences (temperature elution fractionation), field flow fractionations (FFF), adsorption chromatography, or other arrangements which may involve homogeneous or heterogeneous polymer solutions or other mixtures.
DESCRIPTION-OF THE DRAWINGS
Figure 1 is a schematic diagram, not drawn to scale, including a fractionator and an interface system constructed in accordance with the invention; and Figure 2 is a Fourier Transform Infrared (FTIR) spectrum of an ethylene-propylene rubber residue collected utilizing an apparatus of the type shown in Figure 1;
Figure 3 illustrates a CD ~rofile ~upper trace) and gel permeation chromatogram (lower trace) for one type of ethylene-propylene rubber (EPR) which was analy~ed employlng this invention;
Figure 4 illustrates a CD profile (upper trace) and gel permeation chromatogram (lower trace) for a second EPR
sample collected by the method of this invention;
Figure S illustrates in a cross-sectional view, an oven and associated apparatus constructed in accordance with this invention.
DETAILED DESCRIPTION OF.THE INVENTTON
A schemati~ diagram, not drawn to scale, including a fractionator, and an interface system according to the present invention, i5 shown in Figure 1. The interface is relatively enlarged to show its details.
Referring to Figure 1, a fractionator lO such as a gel permeation chromatograph of a conventional and commercially available type such as a Waters Type 150-C GPC, is shown.
Fractions of a sample of a material to be analyzed are provided in the form of a solute carried by a liquid solvent such as trichlorobenzene (TCB) via an outlet line 11~ The outlet line 11 is connected to a sample inlet port 12 of a vacuum oven 13.
~3~3~
An effluent sample supplying means 14, for example, stainless steel tubing of 0.009 inches inner diameter, extends from sample inlet port 12 to a point within oven 13 adjacent a sample collection s station 15. Suitable valving (not shown) may be provided between outlet line 11 and sample inlet port 12 as needed to insure that liquid samples are provided at an appropriate rate at the collection station 15. It is preferable that small droplets be 10 supplied to enhance the desired step of flash evaporation. Typically, oven 13 may have a capacity of 0.2 cubic feet and preferably is capable of being heated to a controlled temperature of the order of 200C. Vacuum ovens which are available commercially (such as NAPCO ~ Model 5831) may be modified so as to be suited for such use, provided there are no heating elements exposed on the inside of oven 13 or the oven may be constructed specifically for the present purposes. A hole 20 having a vacuum seal 16 is provided in the center of the ceiling 17 of the oven 13 through which a shaft 18 is inserted. The shaft 18 is attached to a fraction collector 19 inside the oven 13. The fraction collector 19 is a disk of, for example, 25 aluminum of 14.5 centimeters diameter. As will appear below, such a configuration is particularly suitable where subsequent FTIR analysis is to be performed. Holes are provided along the circum-ference of the disk to hold, for example, sixteen 30 KBr (potassium bromide) plates, cups or vials 20.
The shaft 18 is attached to a stepper motor unit 21 which is mounted externally on top of the oven 13.
A power and logic signal cable 22 is connected from the stepper motor 21 to a command or control system 35 23 including, for example, a Compaq ~ Computer.
The position of the fraction collector 19 is sensed - 6a - ~ ~ 9 ~3~
using a position sensor 24 (such as a fixed photocell and a slotted wheel connected to shaft 18). The position of the fraction collector 19 is controlled making use of the sensor 24, stepper s motor 21, and the command system 23 (software commands) in a conventional closed loop position control arrangement.
Another hole is provided in the side wall 25 of the oven 13 to introduce a nitrogen line 26 10 which is connected to - 6a -an external nitrogen supply 36. The nitrogen line 26 is associated with a heater 27 so that nitrogen provided via line 26 can maintain the desired temperature at the surface of th~
KBr cups 20, a~ required. Line 26 may be coaxial with tubing 14, (surrounding tubing 14) or may be separate from tubing 14.
In the latter case, line 26 preferably is also made flexible or movable to adjust the position of a blowing point 30.
A heater 28 is provided outside of oven 13 and a temperature sensing apparatus 29 (such as a thermocouple) is provided within oven 13 in the vicinity of collection station 15. The héater 28, temperature sensor 29 and command system 23 are coupled in a closed loop temperature control system. While the heaters 27 and 28 are shown as separate devices, in practice they may be parts of a single heater. A single heater arrangement may be advantageous in that the temperature of oven 13 and that of the blown nitrogen then may readily be maintained substantially equal. For safety reasons, it is preferable that the temperature of the hot nitrogen should not exceed that of oven 13.
Oven 13 is provided with a vacuum line 31 which extends inside of oven 13, a pressure (vacuum~ sensing apparatus 32 connected to oven 13, and a vacuum pump 33 arranged to maintain the pressure within oven 13 at a predetermined level.
A dual cold trap 34 is associated with vacuum line 31 for collection of solvent evaporated within oven 13 as will be explained below~
The pressure sensing apparatus 32 is coupled to command system 23 to assist in maintaining the pressure (vacuum) within oven 13 in a predetermined range. The control arrangement preferably is configured so that if pressure and/or temperature exceed predetermined safety limits, warning signals are generated, power to the oven 13 is shut off and the chromatographic effluent is diverted away from the oYen 13.
The geometry of the XBr collecting crystal 20 was found to be an important parameter. Flat KBr plates were found to be a less suitable collection media when the effluent is ~3~5~
introduced as droplets. In that case, droplets of solution tend to flow to the edges of the plate 20 before the solvent evaporates. Consequently the collected sample (e.g.l a polymer) deposits along the edges of plate 20 and it is difficult to get a good spectrum from such a sample.
Therefore, the use of KBr cups 20 is o~ten preferred. The latter act as a small ~vial~ and position the solute at the center of the cup 20.
If, on the other hand, flat KBr plates are to be used, then the GPC effluent should be applied to the plate 20 as a fine mist, using such devices as a non-electrostatic, ultrasonic atomizing nozzle (e.g. a Sono-Tek ultrasonic nozzle). The fine particle sizes of the atomized spray help the flash-evaporation, depositing a thin layer of fractionated materia} on the collection plate 20.
Depending on the particular circumstances, besides KBr cups, other collection media are possible. One possibility is the use of metal or glass cups containing suitable powders for diffuse reflectance measurements using normal accessories or microsampling devices. Another is to use a metal strip (with low infrared absorption characteristics) on which the material is deposited for subsequent surface analysis (e.g., using surface analysis techniques or microsampling accessories). A third possibility is to use tiny metal dishes for collecting fractions to be analyzed using a mass spectrometric technique, for example.
The apparatus according to this invention can be ~iniaturized, converted to a continuous on-line process analyzer using the dual chamber configuration described above, or used as an interface device for other types of analytical techniques. In particular, a grid type design, typical of some fxaction collection devices, is an alternative. If the interface is to be used for on-line process analysis, then the details of the oven and that of the collecting medium are likely to be changed.
During a run, the varuum oven 13 is maintained at a high enough temperature and vacuum to allow the solvents to ~1 3 ~
flash evaporate as they come in contact with the KBr dish 20.
The effluent to be sampled (e.g. GPC effluent) is directed into the oven 13 through the stainless steel tubing 14 inserted through the vacuum-tight opening on the sidewall of the oven 13. Although this tubing 14 may be externally valved for proper flow-rate control, it was not needed for the experiments described herein.
The effluent enters the oven 13, and falls on the KBr cups 20 drop-by-drop at a flow rate of, for example, 0.5 milliliters per minute. In order to assure that each droplet immediately loses its solvent, the temperature and pressure of the oven 13 should be adjusted, depending on the boiling point/vapor pressure characteristics of the solvent to be eliminated. For example, if TCB is the solvent, the temperature-pressure relationship given below should be consulted.
Table: Vapor pressure of TCB
Vapor pressure 760 400 100 40 10 5 (mn~Ig) Temp-erature 213.0 187.7 140.0 114.8 87.7 67.3 38.4 C) This relationship establishes a minimum temperature needed for evaporation o a single drop, but actual temperatures in oven 13 should be maintained above the theoretical value by, for example, at least 4QC to insure efficient evaporation of many drops falling on the same cup 20.
This additional temperature increment is required since the heat of vaporization will drop the temperature of the cup 20 below the boiling point of the solvent (under the given conditions). To insure the cup 20 is hot enough throughout the collection stage, the temperature of oven 13 should therefore be maintained higher than the theoretical boiling point of the solvent, and/or one must provide an additional source of heat directly to the cup surface.
With TCB as the chromatographic solvent, a stream of hot nitrogen blowing over the collecting cup 20 was found to be ~ 3 ~
beneficial, and at the same time effectively eliminated splashing problems. The heated nitrogen was introduced via the flexible metal tubing 26. The temperature of the nitrogen is controlled by means of a thermocouple (not shown) placed after the heating cartridge 27. The tip of the nitrogen line 26 may be equipped with a baf~le to control the size of the heated area. Alternatively, a perforated toroidal (ring-shaped) nozzle may be employed to provide a unifo~m cylindrical jet of inert gas at the sample collection station 15.
As droplets fall on a cup 20 at collection station 15, and the solvent immediately flash~s off, the cup 20 will contain the fractionated residue. The flashed-off solvent is continuously carried away from the vacuum oven via vacuum line 31 into cold trap 34 where the solvent is condensed. Cold trap 24 is emptied on a regular basis. A~ter a fraction is collected, the carousel 19 moves to the next position, and so on. It was found that sample quantities as small as one microgram were sufficient for subsequent FTIR analysi~. The residence time at each position is either preset or triggered, depending on the experimental setup and the distribution pattern of the chromatographic information ~ie. continuous or discrete signals)~ If an ult~asonic atomizer is used, especially of the non-electrostatic type, then the nozzle-to-plate distance is adjusted, depending on the desired pattern of the sprayed material. The nozzle geometry and the ultrasonic frequency can also be adjusted to control the spray pattern or the spot size. To assure that the atomized mist emerging from the nozzle is channeled entirely toward the collecting plate 20, the vacuum port 31 preferably is positioned beneath the carousel 19, and pr~ferably ben~ath plate 20 at collection station 15. If the latter option i5 chosen, then additional openings on the carousel 19, in the vicinity of plate 20, will assure a uniform flow of heated nitro~en around the plate 20.
In addition, a cylindrical jet of hot nitrogen in the direction of the plake 20, and of a chosen diameter, will further channel or direct the atomized particles emerging from the nozzla toward plate 20 only.
~ 3 ~
Af~er the collection is ovPr, the temperature of the oven 13 is brought down and the vacuum broken. The carousel 19 i5 now ready for composition analysis using selected microanalytical techniques. Since FTIR was contemplated in this case, the carousel 19 is detached from shaft 18, removed from the oven 13 and placed into the auto sampler assembly of the FTIR spectrometer (into which it is designed to fit) to automatically record the spectra of the collected samples.
An interface system of the type shown in Figure 1 was connected to a GPC (Waters, Inc., Type 150-C~ and the effect of the vacuum on the flow rate and the system pressure was examined. It was found that the flow rate in the GPC is not at all affected by the pressure drop in the vacuum oven 13 at 1 mm Hg as compared to 760 mm Hg.
Experimental details.
In the experiment, first, a 0.6 weight percent solution of EPR was prepared in TCB and 100 microliters of this solution was injected into the GPC coupled to the interface system of the type shown in Figur~ 1. The column temperature was maintained at 120C, flow rate at 0.5 ml/min. The pressure of the oven 13 was maintained at 40 mm Hg, while its temperature was about 150~C, with a gentle flow of N2 through the system. The operation of ~he interace system was observed. The effluent was continuously flash evaporated in the interface oven 13 and a thin film of the EPR residue was formed on a gBr cup 20 (13x2 mm). The FTIR spectrum of the sample was recorded and is shown in Figure 2. Similar experiment~ were performed successfully with ethylene-vinyl acetats ~EVA) copolymers.
In the FTIR spectrum shown in Figure 2, not only a C-H stretching region at about 2800-3000 cm~1 but also a bending region at about 1400 cm~l can clearly be observed.
Based on experiments similar to those described above, the detectability limit of the method was investigated. It was found that one microgram of sample is sufficient to permit quanitatlve analysis. With typical concentrations of the low ~ 3 ~
and high ends of the GPC effluent of the order of 10-6 grams per milliliter, if ten fractions are collected for each sample, the collection period will be about two minutes per fraction and the deposition amounts of sample at the extremes will be about one microgram (minimum). A residue of, for example 6.6 micrograms would display an excellent signal-to-noise ratio.
In two separate experiments, seven fractions were collected from each of two rubbers. The ov~n temperature was maintained ~t 130'C, oven pressure was in the vicinity of 5-10 mm Hg, and the nitrogen flow rate was about o.3 cc/minute.
The mov~ments of carousel 19 were timed based on an analysis of the elution time profile from a previous chromatogram of the same material utilizing a conventional differential refractometer (DRI). Durin~ the actual fraction collection, the DRI detector was bypas~ed.
To adjust the temperature and the pressure of the oven 13 to assure smooth flash-evaporation and eliminate splashing problems, an external source of heated nitrogen 36 was introduced into the system and directed at the sample-collection site 15. Although this additional flow calls for a slight sacrifice in the vacuum of the oven 13, the loss is small, since it could bring the vacuum from 1 mm to 5 mm Hg or hi~her. From standard temperature-pressure tables, it appears that 1-5 mm Hg vacuum at 50-70~C would be a minimum vacuum to accomplish the task. Actual oven temperatures should be maintained 30-50C higher than the theoretical evaporation point to account for any heat of vaporization at the collector position 15. The flashed-off solvents were collected in the dual cold trap 34.
The amount of polymer deposited in each dish 20 will depend on the particular fractionation and polymer system studied. For instance, if ethylene-propylene co-polym0rs are fractionated on a GPC column at a temperature of 130-150C, using trichlorobe~zene as a solvent, the average weight of the deposit will be in the 1-50 microgram range. Under these conditions, good quantitative FTIR spectra are obtained.
13 ~ 5~
The two EPR samples were fractionated using the apparatus of Figure 1. The spectra Qf the collected fractions were obtained by placing the carousel 19 into the autosampler of an FTIR spectrometer. From the spectra, the percent ethylene of each fraction was calculated. The retention time vs. percent ethylene profile is shown in the upper trace of Figure 3 for the first sample. The vertical lines on the GPC
curve show the timing of the fraction collection. The ease of obtaining such CD information is unprecedented. The higher molecular weight samples are retrieved earlier (lower trace-left hand end) while the higher molecular weight samples are retrieved later.
The Ethylene CD for the second sample is shown in the upper trace in Figure 4. In this case the percent ethylene decreases with decreasing k~. The presence of a low-ethylene content, low-MW fraction is evident from Figure 4 (right hand end). Although these profiles were obtained from a single GPC
fractionation, the extension to more complex cxoss-fractionations or solvent/non-solvent fractionations will readily be apparent to those engaged in this art.
A more accurate representation of an oven 13 and associated components as explained above is shown in cross section in Figure 5 wherein the same r~Prence characters are used as in Figure 1 for corresponding parts.
The concept of flash evaporating such high boiling solvents as TCB has been successfully demonstrated by means of the illustrated apparatus. It could be used for further investigation of structure-property relationships.
While the apparatu~ described above may be implemented utilizing various arrangements of commercially available hardware elements or may be custom designed according to a particular application, one set of readily usable controller components which was obtained from Cybernetic Microsystems of San Gregoria, California comprises their ModPl CY525 Motor Controller, CY750 I/0 Controller, CY232 Serial Controller, CY300 LCD/Keyboard Controller, CY250 System Controller and CYB-002 Csntrol Board.
In general, the sensing and control elements themselves may be constructed in a conventional manner (See, for example, the description of similar components in U.S.
Patent No. 4,604,363 referred to abovP).
The novel aspects of the foregoing method and apparat~s are set forth in the following claims.
1~
Claims (24)
1. A method of collecting samples of materials for analysis wherein the samples to be analyzed are carried in a liquid solvent comprising:
supplying an output stream from a fractionation system to an input port of a vacuum sealed oven;
controlling the temperature and the pressure within the oven to levels selected with respect to temperature/vapor pressure characteristics of said solvent so as to provide an excess in temperature above the solvent boiling point at the operating pressure level of the oven;
delivering droplets of said output stream from said input port to a collection station within said oven;
sequentially positioning sample collectors at said collection station, each for a predetermined time interval, to permit said droplets of said output stream to impinge thereon;
maintaining the temperature and pressure in the immediate vicinity of said sample collector on which said droplets are impinging at levels so as to flash evaporate said solvent upon contact with said collector while depositing solid samples at said sample collector; and maintaining each said sample collector at said collection station for a time interval to collect a sample sufficient for analysis.
supplying an output stream from a fractionation system to an input port of a vacuum sealed oven;
controlling the temperature and the pressure within the oven to levels selected with respect to temperature/vapor pressure characteristics of said solvent so as to provide an excess in temperature above the solvent boiling point at the operating pressure level of the oven;
delivering droplets of said output stream from said input port to a collection station within said oven;
sequentially positioning sample collectors at said collection station, each for a predetermined time interval, to permit said droplets of said output stream to impinge thereon;
maintaining the temperature and pressure in the immediate vicinity of said sample collector on which said droplets are impinging at levels so as to flash evaporate said solvent upon contact with said collector while depositing solid samples at said sample collector; and maintaining each said sample collector at said collection station for a time interval to collect a sample sufficient for analysis.
2. A method of collecting samples for analysis according to claim 1 wherein said output stream comprises chemical fractions supplied from a fractionating system; and said operating pressure level within said oven is established by evacuating said oven to a relatively low pressure level below atmospheric pressure and thereafter substantially maintaining said pressure level throughout the collection operation.
3. A method of collecting samples for analysis according to claim 2 wherein:
said step of controlling the temperature within said oven comprises sensing the temperature within said oven and supplying heat to the interior of said oven by means of a heater so as to maintain the temperature of said collection station a predetermined increment above the solvent boiling point at the operating pressure level of said oven.
said step of controlling the temperature within said oven comprises sensing the temperature within said oven and supplying heat to the interior of said oven by means of a heater so as to maintain the temperature of said collection station a predetermined increment above the solvent boiling point at the operating pressure level of said oven.
4. A method of collecting samples for analysis according to claim 3 wherein said predetermined increment is greater than twenty degrees Celsius.
5. A method of collecting samples according to claim 2 wherein said droplets are delivered to said collection station at a volumetric rate and droplet size sufficiently low to permit flash evaporation of said solvent at said collection station.
6. A method of collecting samples according to claim 5 wherein said droplets are sprayed onto said sample collector.
7. A method of collecting samples according to claim 3 wherein said droplets are delivered to said collection station at a volumetric rate and droplet size sufficiently low to permit flash evaporation of said solvent at said collection station.
8. A method of collecting samples according to claim 1 wherein said sample collectors are hollowed-center dishes and said droplets are delivered to a central depressed portion of said dishes at said collection station at a rate sufficiently low to prevent splashing.
9. A method of collecting samples according to claim 1 wherein said step of controlling temperature and pressure further comprises supplying a flow of heated inert gas to said collection station so as to maintain the temperature of said sample collectors above the boiling point of said solvent during flash evaporation of said solvent.
10. A method of collecting samples according to claim 9 wherein said gas is nitrogen and the temperature of said nitrogen is elevated above the solvent boiling point.
11. A method of collecting samples according to claim 10 wherein said temperature of said nitrogen is in the range of 20°C to 50°C above the solvent boiling point.
12. A method of collecting samples according to claim 11 wherein the temperature of said nitrogen is maintained substantially equal to the temperature within said oven.
13. Apparatus for collecting samples of materials for analysis wherein the samples to be analyzed are carried in a liquid solvent comprising:
a vacuum sealed oven;
means for supplying an output stream from a system undergoing analysis to an input port of said vacuum sealed oven;
means for controlling the temperature and the pressure within said oven to levels selected with respect to temperature/vapor pressure characteristics of said solvent so as to provide an excess in temperature above the solvent boiling point at the operating pressure level;
a plurality of sample collectors within said oven;
mean for sequentially positioning said sample collectors at a collection station adjacent said input port within said oven, each for a predetermined time interval, to permit said output stream to impinge thereon; and means for maintaining the temperature and pressure in the immediate vicinity of said sample collector on which said output stream is impinging at levels so as to flash evaporate said solvent upon contact with said collector while depositing solid samples at said sample collector.
a vacuum sealed oven;
means for supplying an output stream from a system undergoing analysis to an input port of said vacuum sealed oven;
means for controlling the temperature and the pressure within said oven to levels selected with respect to temperature/vapor pressure characteristics of said solvent so as to provide an excess in temperature above the solvent boiling point at the operating pressure level;
a plurality of sample collectors within said oven;
mean for sequentially positioning said sample collectors at a collection station adjacent said input port within said oven, each for a predetermined time interval, to permit said output stream to impinge thereon; and means for maintaining the temperature and pressure in the immediate vicinity of said sample collector on which said output stream is impinging at levels so as to flash evaporate said solvent upon contact with said collector while depositing solid samples at said sample collector.
14. Apparatus for collecting samples for analysis according to claim 13 wherein said output stream comprises chemical fractions supplied from a fractionating system; and said means for controlling pressure within said oven comprises a vacuum pump for evacuating said oven to a relatively low pressure level below atmospheric pressure and thereafter substantially maintaining said pressure level throughout the collection operation.
15. Apparatus for collecting samples for analysis according to claim 14 wherein:
said means for controlling the temperature within said oven comprises means for sensing the temperature within said oven and a heater for maintaining the temperature of said collection station a predetermined increment above the solvent boiling point at the operating pressure level of said oven.
said means for controlling the temperature within said oven comprises means for sensing the temperature within said oven and a heater for maintaining the temperature of said collection station a predetermined increment above the solvent boiling point at the operating pressure level of said oven.
16. Apparatus for collecting samples for analysis according to claim 15 wherein said predetermined increment is greater than twenty degrees Celsius.
17. Apparatus for collecting samples according to claim 14 wherein said means for supplying an output stream comprises a relatively small outlet such that droplets are delivered to said collection station at a volumetric rate and droplet size sufficiently low to permit flash evaporation of said solvent at said collection station.
18. Apparatus for collecting samples according to claim 17 wherein said means for supplying an output stream comprises an ultrasonic spray nozzle.
19. Apparatus for collecting samples according to claim 15 wherein said means for supplying an output stream comprises a relatively small outlet such that droplets are delivered to said collection station at a volumetric rate and droplet size sufficiently low to permit flash evaporation of said solvent at said collection station.
20. Apparatus for collecting samples according to claim 13 wherein said sample collectors are hollowed-center dishes and said droplets are delivered to a central depressed portion of said dishes at said collection station at a rate sufficiently low to prevent splashing.
21. Apparatus for collecting samples according to claim 13 wherein said means for controlling temperature and pressure further comprises means for supplying localized heat at said collection station to maintain the temperature of said sample collector at said collection station above the boiling point of said solvent during flash evaporation of said solvent.
22. Apparatus for collecting samples according to claim 13 wherein said means for controlling temperature and pressure further comprises means for supplying a flow of heated inert gas to said collection station so as to maintain the temperature of said sample collectors above the boiling point of said solvent during flash evaporation of said solvent.
23. Apparatus for collecting samples according to claim 22 wherein said gas is nitrogen and the temperature of said nitrogen is elevated above the solvent boiling point.
24. Apparatus for collecting samples according to claim 23 wherein said means for supplying a flow of heated inert gas comprises a toroidally shaped nozzle having a plurality of holes spaced about its circumference so as to direct a cylindrical column of said gas towards said collection station.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US20777088A | 1988-06-16 | 1988-06-16 | |
US207,770 | 1988-06-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1319539C true CA1319539C (en) | 1993-06-29 |
Family
ID=22771939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA 602535 Expired - Fee Related CA1319539C (en) | 1988-06-16 | 1989-06-12 | Method and apparatus for collecting samples for analysis of chemical composition |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU3851389A (en) |
CA (1) | CA1319539C (en) |
WO (1) | WO1989012828A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9389162B2 (en) | 2014-04-10 | 2016-07-12 | City University Of Hong Kong | Detection of analyte using coffee-ring effect |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2267478A (en) * | 1992-05-29 | 1993-12-08 | Apv Corp Ltd | Apparatus for sampling fluids |
KR101113341B1 (en) | 2002-10-15 | 2012-09-27 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | Multiple catalyst system for olefin polymerization and polymers produced therefrom |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4367391A (en) * | 1980-08-14 | 1983-01-04 | Toshihiko Furukawa | Method for pattern controlled electrode movement for E.D.M. |
US4552723A (en) * | 1983-08-01 | 1985-11-12 | International Business Machines Corporation | LC/FTIR System with thermospray solvent separation |
US4604363A (en) * | 1984-10-18 | 1986-08-05 | Analytical Bio-Chemistry Laboratories Inc. | Automatic evaporator system |
US4659014A (en) * | 1985-09-05 | 1987-04-21 | Delavan Corporation | Ultrasonic spray nozzle and method |
EP0268434B1 (en) * | 1986-11-15 | 1991-04-03 | The British Petroleum Company p.l.c. | Transport detector system |
-
1989
- 1989-06-12 CA CA 602535 patent/CA1319539C/en not_active Expired - Fee Related
- 1989-06-13 WO PCT/US1989/002580 patent/WO1989012828A1/en unknown
- 1989-06-13 AU AU38513/89A patent/AU3851389A/en not_active Abandoned
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9389162B2 (en) | 2014-04-10 | 2016-07-12 | City University Of Hong Kong | Detection of analyte using coffee-ring effect |
Also Published As
Publication number | Publication date |
---|---|
AU3851389A (en) | 1990-01-12 |
WO1989012828A1 (en) | 1989-12-28 |
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