The invention relates to a device for heating and regulating an intermediate thermal conductor to allow the scientist to conduct physical adsorption experiments with an adsorption medium utilizing liquid Nitrogen as the primary coolant.
Characterization of surface area and porosity of materials is widely performed by Nitrogen adsorption at the temperature of the boiling point of liquid Nitrogen (77K) using different well established existing techniques (mainly gravimetric and volumetric methods).
However, a recent IUPAC study, published by De Gruyter, which is readily available for review with the use of any web search engine by searching the phrase “PAC-2014-1117”, states that the technique of using Nitrogen has some weaknesses for the micropore distribution determination of samples. These weaknesses can be overcome by using Argon instead of Nitrogen as an analysis gas. For such instances, the analysis must be performed at the temperature of the boiling point of Argon (87K).
Accordingly, to use Argon as the analysis gas, existing analyzers primarily use three different techniques for controlling samples at the Argon boiling point temperature (which is greater than the boiling point of liquid Nitrogen), each of which have some disadvantages. 1) Immersion in liquid Argon: availability of liquid Argon is not widespread as liquid Nitrogen is and the cost of liquid Argon is much higher than liquid Nitrogen; 2) controlling the temperature of the Argon with a cryostat: the amount of time a cryostat can maintain the target temperature is often not enough for completing an analysis and the cost of cryostats are high; and 3) controlling the temperature with a compression cryocooler: the cost of these systems are very high.
It is accordingly an object of the invention to provide a method and device for controlling temperature of an analysis gas, which overcomes the above-mentioned and other disadvantages of the heretofore-known devices and methods of this general type and which provides for an improvement over the prior art and solves both the problem of accurate temperature control while significantly reducing cost of using Argon (or any other costlier gases) as the analysis gas. The present invention controls sub-ambient temperatures to be used with volumetric sorption analyzers that makes use of liquid Nitrogen, similar cryogenic fluids (any fluid with a boiling point less than 123.15K) or sub-ambient fluids (liquids at temperatures less than 220K) as cooling fluid, allowing for flexibility in analysis duration and cost by controlling the temperature locally at a sample.
The present invention provides an apparatus that permits sorption analysis at temperatures greater than, or equal to, the temperature of a given cryogenic fluid. This is achieved by a thermostatic block made with a material having a high thermal conductivity (thermal conductivity greater than 35 W/m*K) surrounded by a thermal insulation material (preferably an insulation foam or a vacuum chamber or a combination of both with a thermal conductivity less than 1.1 W/ m*K) and with a heat sink made with a material having a high thermal conductivity (thermal conductivity greater than 35 W/m*K). The heat sink is, in turn, partially immersed in a cooling fluid (preferably liquid Nitrogen) and is surrounded by a thermal insulation material (preferably an insulation foam or a vacuum chamber or a combination of both with a thermal conductivity less than 1.1 W/ m*K) with the exception of a portion which is in direct contact with the cooling fluid. A heater is provided in the apparatus and is positioned between the thermostatic block and the portion of the heat sink in contact with the cooling fluid.
One part of a sample holder (where the sample to be analyzed) is placed inside the thermostatic block while the other part is connected to a volumetric analyzer.
The temperature of the thermostatic block is established by the equilibrium between the cooling capacity of the heat sink, the power introduced by the heater and the heat losses through the insulation. The cooling capacity of the heat sink changes very little with any fill level change (due to evaporation) of the cryogenic fluid since the major part of the heat transfer is performed by the part of the heat sink directly exposed to the cryogenic fluid, where the part of the heat sink directly exposed to the cryogenic fluid is well below the fill level of the vessel. The insulation material is impermeable to the cryogenic fluid. The insulation material and the dimensions thereof are selected so the total heat transfer through the surface of the material is smaller than the total heat transfer of the heat sink.
A temperature probe is installed in the thermostatic block and temperature readings from the temperature probe are processed by a temperature controller that regulates the heater output in order to achieve a pre-established target temperature in the thermostatic block (at the temperature probe).
The system of the present invention can maintain the target temperature in the thermostatic block for a long period of time (dependent on specific configuration) as shown in
With the foregoing and other objects in view there is provided, a cryogenic temperature controller assembly that includes a controller and a thermostatic block that has a chamber for receiving a sample holder therein. The thermostatic block has a heat sink with an exposed surface for exposure to a cryogenic fluid. A heater is disposed intermediate the exposed surface and the chamber. The heater is connected to the controller. A temperature probe is disposed in the thermostatic block. The probe is connected to the controller. The controller regulates the heater based on an actual temperature from the probe to maintain a predetermined set point temperature in the thermostatic block
In accordance with another feature of the invention, an insulation sleeve at least partially surrounds the thermostatic block.
In accordance with an added feature of the invention, the insulation sleeve includes a portion surrounding the heat sink.
In accordance with an additional feature of the invention, an insulation cap mates with the insulation sleeve and covers an end of the thermostatic block.
In accordance with yet an additional feature of the invention, the heat sink is a rod that is thermally conductively connected to the thermostatic block and extends therefrom.
In accordance with yet another added feature of the invention, the heater is disposed at a juncture between the rod and the thermostatic block.
In accordance with still another added feature of the invention, a threaded connection is between the thermostatic block and the rod.
In accordance with yet still another added feature of the invention, the threaded connection includes a female tap hole with a base, the heater is disposed in the tap hole at the base.
In accordance with yet still another further feature of the invention, a vessel has a basin for receiving the thermostatic block and the heat sink and the cryogenic fluid.
In accordance with still a further feature of the invention, the heat sink is a rod that is thermally conductively connected at a connection to the thermostatic block, the rod extends to a position next to a base of the basin to allow the exposed surface to maintain contact with the cryogenic fluid at a low level of fill of the basin.
In accordance with still another feature of the invention, the rod has a free end opposite of the connection, the free end having an end cap for preventing the rod from damaging the basin.
In accordance with yet an additional feature of the invention, a sample holder is at least partially disposed in the chamber.
In accordance with yet an added feature of the invention, an insulation sleeve at least partially surrounds the thermostatic block and a portion at least partially surrounds the heat sink.
In accordance with yet a further feature of the invention, an insulation cap covers an end of the thermostatic block.
In accordance with yet a further feature of the invention, the thermostatic block has two chambers for simultaneously carrying out two separate sample analyses.
With the objects of the invention in view, there is also provided a cryogenic temperature controller assembly that includes a thermostatic block with a chamber for receiving a sample holder therein. The thermostatic block has a heat sink with an exposed surface for exposure to a cryogenic fluid. A temperature probe is disposed in the thermostatic block. A heater is disposed and configured for maintaining a predetermined set point temperature in the thermostatic block by introducing thermal energy on the basis of actual temperatures observed by the temperature probe.
In accordance with still a further feature of the invention, an insulation sleeve partially surrounding said thermostatic block.
In accordance with still another feature of the invention, a controller connected to said heater and said temperature probe, said controller regulating said heater based on actual temperatures observed by said probe for maintaining the predetermined set point temperature in said thermostatic block.
With the foregoing and other objects in view there is also provided a method for maintaining a predetermined set point temperature during a testing period. The method provides a thermostatic block that has a heat sink with an exposed surface. The exposed surface of the heat sink is brought into contact with a cryogenic fluid during the testing period to cool the thermostatic block. The method regulates a heater disposed to maintain the predetermined set point temperature in the thermostatic block by introducing thermal energy into the thermostatic block on the basis of actual temperatures observed by the temperature probe to maintain the predetermined set point temperature in the thermostatic block during the testing period.
Although the invention is illustrated and described herein as embodied cryogenic temperature controller for volumetric sorption analyzers, it is nevertheless not intended to be limited to the details shown, since various modifications and structural changes may be made therein without departing from the spirit of the invention and within the scope and range of equivalents of the claims.
The construction and method of operation of the invention, however, together with additional objects and advantages thereof will be best understood from the following description of specific embodiments when read in connection with the accompanying drawings.
Referring now to the drawing figures in which like reference designators refer to like elements, there is shown in
A thermostatic block 5 includes a chamber 5c, which receives a sample holder 8 therein. The chamber 5c is dimensioned to correspond to the outside diameter of the sample holder 8, so that the sample holder 8 is in heat conducting contact with the wall defining the chamber 5c. The sample holder 8 holds the sample that is to be tested and an analysis gas such as argon. The sample holder 8 is connected to a volumetric sample/adsorption analyzer 13, shown in
The thermostatic block 5 has a heat sink portion 3 that is in thermal conducting contact therewith. In
The rod 3 is partially surrounded by the insulation material sleeve 6s that also surrounds a longitudinal extent of the thermostatic block 5. The rod 3 is free of insulation material at an exposed surface 3e that is in thermal contact with the cryogenic fluid 2 (opposite the thermostatic block 5 at a base of the basin 1b). The insulation material for the insulation sleeve 6s and the insulation cap 6c may be a dense, closed cell foam (preferably polyisocyanurate) barrier of 0.5-1.0 inch thickness. Furthermore, a cylindrical outer surface of the insulation material sleeve 6s may be provided with a sheath 6sh to protect the insulation material sleeve 6s from wear during handling of the assembly 20. The sheath 6sh can be made of steel. It is also possible for either or both of the insulation cap 6c and the insulation sleeve 6s to be encased in a liner and internally vacuumed by connection to a vacuum pumping system, which provides for a reduced thermal conductivity and thus a better insulation. Alternatively, the liner is vacuumed and sealed during manufacture of the particular insulation material component, to maintain the vacuum. The exposed surface 3e that is not covered by the insulation material sleeve 6s is opposite the location of the thermostatic block 5. The insulation material cap 6c and the insulation sleeve 6s are releasably connected to one another for removing the sample holder 8 and or for refilling cryogenic fluid 2 into the basin 1b. A distal end (end of the exposed surface) of the rod 3 may be provided with a soft material tip 11, such as plastic to prevent damage to the glass of the basin 1b, when inserting the device into the vacuum flask 1.
The apparatus 20 includes at least one heater 4 in a position that is intermediate the exposed surface 3e of the heat sink 3 and the chamber 5c. As an example, heater 4 may be installed in the heat sink 3 at a location not in direct contact with the cryogenic fluid 2 i.e. along a portion of the heat sink 3 underneath the insulation material sleeve 6s. Such position allows the heater 4 to control the energy removed from the thermostatic block 5 by the cryogenic fluid 2 via the heat sink 3. A particular suitable position for the heater 4, is recessed at a juncture between the thermal block 5 and the heat sink rod 3. In the
The thermostatic block 5 includes a temperature probe/thermal detection device 7, which is a PT100 (Platinum Resistance Temperature Detector) that is utilized in conjunction with a PID (proportional-integral-derivative) controller 12 or similar thermal control device (shown in
The temperature of the thermostatic block 5 is established by the equilibrium between the cooling capacity of the heat sink 3, the power introduced by the heater 4, and the heat losses through the insulation material 6. The cooling capacity of the heat sink 3 changes very little with the level change (due to evaporation) of the cryogenic fluid 2 since the major part of the heat transfer is carried out by the exposed surface 3e that is in contact with the cryogenic fluid 2. The insulation material 6 is not permeable to the cryogenic fluid 2. The insulation material 6 is dimensioned so the total heat transfer therethrough is less than the total heat transfer of the heat sink 3.
For more localized temperature control, it is possible to provide the thermostatic block 5 with multiple heat sinks 3, where each of the heat sinks 3 is provided with a respective heater and a respective thermal detection device 7. In this case, the controller 12 would control the respective heaters 4 individually based upon the corresponding temperatures.
When the assembly 20 is in operation, the exposed surface 3e is submerged within liquid Nitrogen, or a similar cryogenic fluid 2, within the basin 1b of the vacuum flask 1 such that the exposed surface 3e of the heat sink 3 is in direct contact with the cryogenic fluid 2. This is done to provide physical stability to the system while also providing an optimal duration contact between the exposed surface 3e of the heat sink 3 and the cryogenic fluid 2. The system described can maintain the target temperature in the thermostatic block for a long period (dependent on specific configuration) as shown in
The heat sink 3 is provided as a rod 3 that is disposed centrally between the two chambers 5c at the base of the thermostatic block 5 and is of thermally conductive material (greater than 35 W/m*K). The rod 3 extends into a basin 1b, as shown above with respect to
This application claims benefit of U.S. Provisional Patent Application No. 62/355,449 filed Jun. 28, 2016, titled Cryogenic Temperature Controller And Its Use In Volumetric Sorption Analyzers, the disclosure of which is incorporated herein by reference in its entirety.
Number | Name | Date | Kind |
---|---|---|---|
3176472 | Cox | Apr 1965 | A |
3236133 | De Pas | Feb 1966 | A |
3836779 | Bruno et al. | Sep 1974 | A |
4672202 | Crossley, Jr. | Jun 1987 | A |
4712607 | Lindemans | Dec 1987 | A |
4888956 | le Roux Murray | Dec 1989 | A |
4984628 | Uchida | Jan 1991 | A |
5181382 | Middlebrook | Jan 1993 | A |
5239482 | Ajot | Aug 1993 | A |
5305825 | Roehrich et al. | Apr 1994 | A |
5408864 | Wenman | Apr 1995 | A |
5598888 | Sullivan | Feb 1997 | A |
5613366 | Schoenman | Mar 1997 | A |
5646335 | Wenman | Jul 1997 | A |
5829256 | Rada | Nov 1998 | A |
6094923 | Rada | Aug 2000 | A |
6387704 | Thomas | May 2002 | B1 |
6413252 | Zavislan | Jul 2002 | B1 |
6595036 | Nakai | Jul 2003 | B1 |
7043968 | Hildebrandt | May 2006 | B1 |
7320224 | Ash | Jan 2008 | B2 |
8596340 | Horn, Jr. | Dec 2013 | B1 |
8826728 | Hildebrandt | Sep 2014 | B1 |
20060057555 | Damari | Mar 2006 | A1 |
20060236703 | Rada | Oct 2006 | A1 |
20070261429 | Teehan | Nov 2007 | A1 |
20110229928 | Dorward | Sep 2011 | A1 |
20120292528 | Oh | Nov 2012 | A1 |
20130125673 | Kanipayor | May 2013 | A1 |
20140335614 | Schryver | Nov 2014 | A1 |
20150346069 | Inoue | Dec 2015 | A1 |
20150355061 | Inoue | Dec 2015 | A1 |
20160223463 | Schmidt | Aug 2016 | A1 |
Number | Date | Country |
---|---|---|
WO-0045956 | Aug 2000 | WO |
Entry |
---|
Matthias Thommes, et al., Physisorption of Gases, With Special Reference to the Evaluation of Surface Area and Pore Size Distribution (IUPAC Technical Report), Pure Appl. Chem. 2015; 87(9-10): 1051-1069, De Gruyter, Research Triangle Park, North Carolina, USA. |
Number | Date | Country | |
---|---|---|---|
20170370817 A1 | Dec 2017 | US |
Number | Date | Country | |
---|---|---|---|
62355449 | Jun 2016 | US |