The present invention relates to a device for the carrying out of chemical or biological reactions with a reaction vessel receiving element for receiving reaction vessels, wherein the reaction vessel receiving element-has several recesses arranged in a pattern to receive reaction vessels, a heating element for heating the reaction vessel receiving element, and a cooling device for cooling the reaction vessel receiving element.
Introduction
Testing of biological or chemical samples often requires a device for repeatedly subjecting multiple samples though a series of temperature cycles. Such devices are described as thermocyclers or thermocycling devices and are used to generate specific temperature cycles, i.e. to set predetermined temperatures in the reaction vessels and to maintain predetermined intervals of time.
A conventional device of this kind is known from U.S. Pat. No. 5,525,300. The disclosed device has four reaction vessel receiving elements, each with recesses arranged in a regular pattern. The pattern of the recesses corresponds to a known pattern of reaction vessels of standard microtiter plates, so that microtiter plates with their reaction vessels may be inserted in the recesses.
The heating and cooling devices of a reaction vessel receiving element are so designed that a stepped temperature gradient extending over the reaction vessel receiving element may be generated. This means that, during a temperature cycle, different temperatures may be obtained in the individual reaction vessels. This makes it possible to carry out certain experiments at different temperatures simultaneously.
This stepped temperature gradient is used to determine the optimal denaturing temperature, the optimal annealing temperature, and the optimal elongation temperature of a PCR reaction. To achieve this, the same reaction mixture is poured into the individual reaction vessels, and the temperature cycles necessary to perform the PCR reaction are executed. Such a temperature cycle comprises the heating of the reaction mixture to the denaturing temperature, which usually lies in the range 90°-95° C., cooling to the annealing temperature, which is usually in the range 40°-60° C. and heating to the elongation temperature, which is usually in the range 70°-75° C. If desired, the time of each cycle can also be varied. A cycle of this kind is repeated several times, leading to amplification of a predetermined DNA sequence.
Since a stepped temperature gradient can be set, different but predetermined temperatures are set in the individual reaction vessels. After completion of the cycles it is possible to determine, with the aid of the reaction products, those temperatures at which the PCR reaction will give the user the optimal result. Here the result may be optimised e.g. in respect of product volume or also product quality.
The annealing temperature, at which the primer is added, has a powerful influence on the result. However the elongation temperature too can have beneficial or adverse effects on the result. At a higher elongation temperature, the addition of the bases is accelerated, with the probability of errors increasing with higher temperature. In addition, the life of the polymerase is shorter at a higher elongation temperature.
A thermocycling device, by which the stepped temperature gradient may be set, makes it much easier to determine the desired temperatures, since a reaction mixture may simultaneously undergo cycles at different temperatures in a single thermocycling device.
Another important parameter for the success of a PCR reaction is the different residence volumes spread over different reaction vessels. Problems arise with conventional devices as these parameters can not be varied in one test series for an individual reaction vessel holder. To test different residence volumes, several test series are required and are performed either consecutively in one thermocycling device or simultaneously in several thermocycling devices.
For this purpose there are so-called multiblock thermocycling devices with several reaction vessel receiving elements, each provided with separate cooling, heating and control devices (see U.S. Pat. No. 5,525,300). The reaction mixture to be tested must be distributed over several microtiter plates, for testing independently of one another.
Problems arise in determining the optimal residence times, rates of temperature change, and residence volumes using conventional thermocycling devices because it is necessary to have either several thermocycling devices or a multiblock thermocycling device, or to carry out tests in several consecutive test series. The acquisition of several thermocycling devices or of a multiblock thermocycling device is costly and the carrying-out of several consecutive test series takes too long. In addition, handling is laborious when only part of the reaction vessels of several microtiter plates is filled, with each of the latter being tested and optimised in separate test series. This is especially disadvantageous in the case of devices which operate automatically and in which the reaction mixtures are subject to further operations, since several microtiter plates must then be handled separately. It is also extremely impractical when only part of the reaction vessels of the microtiter plates is filled, since the devices for further processing, such as e.g. sample combs for transferring the reaction products to an electrophoresis apparatus, are often laid out on the grid of the microtiter plates, which means that further processing is correspondingly limited if only part of the reaction vessels of the microtiter plate is used.
U.S. Pat. No. 5,819,842 discloses a device for the individual, controlled heating of several samples. This device has several flat heating elements arranged in a grid pattern on a work surface. Formed below the heating elements is a cooling device which extends over all the heating elements. In operation a specially designed sample plate is placed on the work surface. This sample plate has a grid plate, covered on the underside by a film. The samples are poured into the recesses of the grid plate. In this device the samples lie on the individual heating elements, separated from them only by the film. By this means, direct heat transfer is obtained. Problems arise with this device because specially designed microtiter plates must be used and commonly available ones cannot be used.
Moreover, with increasing automation in biotechnology, thermocyclers are increasingly being used in automated production lines and with robots as one of several work stations. Here it is customary for the samples to be passed in microtiter plates from one work station to the next. Problems arise with the themocycler disclosed by U.S. Pat. No. 5,819,842 as it would be necessary for the samples to be pipetted out of a microtiter plate into the specially designed sample plate before temperature adjustment, and from the sample plate into a microtiter plate after temperature adjustment. Here there is a risk of contamination of the samples. The use of this specially designed sample plate must therefore be regarded as extremely disadvantageous.
Thus, there is a need to overcome these and other problems of the prior art to provide a method and system for controlling the temperature of a sample block of a thermocycler.
According to various embodiments, the present teachings include a thermocycler for processing biological or chemical samples. The thermocycler can include a sample block configured to receive one microtiter plate and configured to define a plurality of zones and a thermoelectric cooling device (TEC) disposed in each of the plurality of zones, wherein the TEC provides course heating of the zone to near a control temperature. The thermocycler can further include a heating element disposed in each of the plurality of zones, wherein the heating element provides fine heating of the zone to about the control temperature.
According to various embodiments, the present teachings also include a system for processing biological or chemical samples. The system can include a sample block defining a plurality of zones and a detachable microtiter plate configured to detach into a plurality of segments, wherein the plurality of segments correspond to the plurality of zones. The system can further include a thermoelectric cooling device (TEC) disposed in each of the plurality of zones and a temperature sensor disposed in each of the plurality of zones. The system can also include a heating element disposed in each of the plurality of zones, wherein the TEC provides course heating of the zone and the heating element provides fine heating of the zone.
According to various embodiments, the present teachings further include a method for processing biological or chemical samples. The method can include denaturing samples in a first portion of a microtiter plate at a temperature Td1 by heating a first zone of a sample block, wherein a first thermo electric cooling device (TEC) provides coarse heating of the first zone to a temperature near Td1 and a first heating element provides fine heating of the first zone to about Td1. The method can also include denaturing samples in a second portion of the microliter plate at a temperature Td2 by heating a second zone of the sample block, wherein a second thermo electric cooling device (TEG) provides coarse heating of the second zone to a temperature near Td2 and a second heating element provides fine heating of the second zone to about Td2.
It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are not restrictive of the invention, as claimed.
The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate several embodiments of the invention and together with the description, serve to explain the principles of the invention.
FIGS. 6 to 9 depict schematic plan views of reaction vessel receiving elements with differing segmentation;
FIGS. 14B-C depict perspective views of sample block segments in accordance with the present teachings;
In the following description, reference is made to the accompanying drawings that form a part thereof, and in which are shown by way of illustration specific exemplary embodiments in which the invention may be practiced. These embodiments are described in sufficient detail to enable those skilled in the art to practice the invention and it is to be understood that other embodiments may be utilized and that changes may be made without departing from the scope of the invention. The following description is, therefore, not to be taken in a limited sense.
Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, the numerical values set forth in the specific examples are reported as precisely as possible. Any numerical value, however, inherently contains certain errors necessarily resulting from the standard deviation found in their respective testing measurements. Moreover, all ranges disclosed herein are to be understood to encompass any and all sub-ranges subsumed therein. For example, a range of “less than 10” can include any and all sub-ranges between (and including) the minimum value of zero and the maximum value of 10, that is, any and all sub-ranges having a minimum value of equal to or greater than zero and a maximum value of equal to or less than 10, e.g., 1 to 5.
As used herein, the terms “sample plate,” “microtitration plate,” “microtiter plate,” and “microplate” are interchangeable and refer to a multi-welled sample receptacle for testing of chemical and biological samples. Microplates can have wells that are conical, cylindrical, rectilinear, tapered, and/or flat-bottomed in shape, and can be constructed of a single material or multiple materials. The microplate can conform to SBS Standards or it can be non-standard. Microplates can be open-faced (e.g. closed with a sealing film or caps) or close-chambered (e.g. microcard as described in U.S. Pat. No. 6,825,047). Open-faced microplates can be filled, for example, with pipettes (hand-held, robotic, etc.) or through-hole distribution plates. Close-chambered microplates can be filled, for example, through channels or by closing to form the chamber.
FIGS. 1 to 21 depict exemplary embodiments of methods and systems that include a reaction vessel receiving element divided into several segments, with the individual segments thermally decoupled and each segment assigned a heating element which may be actuated independently.
By this means the individual segments of the device may be set to different temperatures independently of one another. This makes it possible not only to set different temperature levels in the segments, but also for them to be held for varying lengths of time or altered at different rates of change. The device according to the invention thus permits optimization of all physical parameters critical for a PCR process, while the optimization process may be carried out on a single reaction vessel receiving element in which a microtiter plate may be inserted.
With the device according to the invention it is therefore also possible to optimise the residence times and rates of temperature change without having to distribute the reaction mixture over different microtiter plates for this purpose. Moreover, it is also possible to optimize the mixture volume by varying the mixture volume over different reaction vessel segments.
The thermocycling device according to the invention is in particular suitable for optimizing the multiplex PCR process, in which several different primers are used.
The device has a housing 2 with a bottom 3 and side walls 4. Located just above and parallel to the bottom 3 is an intermediate wall 5, on which are formed several bases 5a. In the embodiment shown in
Mounted on each of the bases 5a is a heat exchanger 6, a Peltier element 7 and a segment 8 of a reaction vessel receiving element 9. The heat exchanger 6 is part of a cooling device and the Peltier element 7 is part of a combined heating and cooling device. The elements (heat exchanger, Peltier element, segment) mounted on the bases 5a are bonded by an adhesive resin with good heat conducting properties, so that good heat transfer is realized between these elements, and the elements are also firmly connected to a segment element 10. The device has altogether six such segment elements 10. Instead of adhesive resin, a heat conducting film or a heat conducting paste may also be provided.
Each of the segments 8 of the reaction vessel receiving element 9 has a base plate 11 on which tubular, thin-walled reaction vessel holders 12 are integrally formed. In the embodiment depicted in
By providing the distance d between adjacent segments, an air gap which thermally decouples the segments 8 and segment elements 10 respectively is formed.
The reaction vessel holders 12 of the device shown in
The Peltier elements 7 are each connected electrically to a first control unit 13. Each of the heat exchangers 6 is connected via a separate cooling circuit 14 to a second control unit 15. The cooling medium used is for example water, which is cooled in the cool temperature control unit before transfer to one of the heat exchangers 6.
The first control unit 13 and the second control unit 15 are connected to a central control unit 16 which controls the temperature cycles to be implemented in the device. Inserted in each cooling circuit 14 is a control valve 19, which is controlled by the central control unit 16 to open or close the respective cooling circuit 14.
Pivotably attached to the housing 2 is a cover 17 in which additional heating elements 18 in the form of Peltier elements, heating films or semiconductor heating elements may be located. The heating elements 18 form cover heating elements, each assigned to a segment 8 and separately connected to the first control unit 13, so that each heating element 18 may be individually actuated. In various embodiments, heating element 18 can be single or multiple heating elements that cover the all of the reaction vessel segments or overlap to cover several segments.
The mode of operation of the device according to the invention is explained in detail below.
There are three modes of operation.
In the first operating mode all segments are set to the same temperature, i.e., the same temperature cycles are run on all segments. This operating mode corresponds to the operation of a conventional thermocycling device.
In the second operating mode the segments are actuated with different temperatures, wherein the temperatures are so controlled that the temperature difference ΔT of adjacent segments 8 is less than a predetermined value K which amounts for example to 5°-15° C. The value to be chosen for K depends on the quality of the thermal decoupling. The better the thermal decoupling, the greater the value which can be chosen for K.
The temperature cycles input by the user may be distributed automatically by the central control unit 16 to the segments 8, so that the temperature differences between adjacent segments are kept as small as possible.
This second operating mode may be provided with a function by which the user inputs only a single temperature cycle or PCR cycle, and the central control unit 16 then varies this cycle automatically. The parameters to be varied, such as temperature, residence time, mixture volume, or rate of temperature change, may be chosen by the user separately or in combination. Variation of the parameters is effected either by linear or sigmoidal distribution.
In the third operating mode, only part of the segments is actuated. In plan view (
In this operating mode the actuated segments are not influenced by the other segments, and their temperature may be set completely independently of the other actuated segments. By this means it is possible to run quite different temperature cycles on the individual segments, with one of the segments for example heated up to the denaturing temperature and another held at the annealing temperature. Thus it is possible for the residence times, i.e. the intervals of time for which the denaturing temperature, the annealing temperature and the elongation temperature are held, also the rates of temperature change, to be set as desired, and run simultaneously on the individual segments. In this way it is possible to optimize not only the temperatures, but also the residence times, mixture volume, and the rates of temperature change.
In this operating mode it may be expedient to heat the non-actuated segments 8 a little, so that their temperature lies roughly in the range of the lowest temperature of the adjacent actuated segments. This avoids the non-actuated segments forming a heat sink for the actuated segments and affecting their temperature profile adversely.
A second embodiment of the device according to the invention is shown in
The second embodiment differs from the first embodiment by virtue of the fact that the side edges 20 of the segments 8 adjacent to the side walls 4 of the housing 2 engage in a slot 21 running round the inner face of the side walls 4, and are fixed therein for example by bonding. By this means the individual segment elements 10 are fixed in space, thereby ensuring that despite the form of the gaps between the segment elements 10, all reaction vessel holders 12 are arranged in the pattern of the reaction vessels of a microtiter plate. The side walls 4 of the housing 2 are made of a non heat conducting material. This embodiment may also be modified such that the slot 21 is introduced in a frame formed separately from the housing 2. The frame and the segments inserted in it form a part which may be handled separately during production and is bonded to the heating and cooling devices.
A third embodiment is shown schematically in
This type of position fixing is very advantageous since the boundary areas between the segments 8 and the ties 22 are very small, so that heat transfer via the ties 22 is correspondingly low. Moreover this arrangement is easy to realise even in the confined space conditions between adjacent segment elements.
Shown in schematic plan view in FIGS. 6 to 9 are reaction vessel receiving elements 9 which represent further modifications of the device according to the invention. In these reaction vessel receiving elements 9, the individual segments 8 are joined by webs 24 of a thermally insulating material joined to form a single unit. The ties 22 are arranged between the side edges 20 of the base plates 11, to which they are fixed for example by bonding.
The segmentation of the reaction vessel receiving element of
The reaction vessel receiving element 9 shown in
In the reaction vessel receiving element 9 shown in
For the relatively finely sub-divided reaction vessel receiving elements 9 it is expedient to integrate temperature sensors in the thermocycling device. These temperature sensors sense the temperatures of the individual segments, so that the temperature of the segments 8 is regulated in a closed control loop on the basis of the temperature values determined by the temperature sensors.
Infrared sensors may for example be used as temperature sensors, located e.g. in the cover. With this sensor arrangement it is possible to sense the temperature of the reaction mixture directly.
The segments 8 of the reaction vessel receiving element 9 are made from a metal with good heat conducting properties, e.g. aluminium. The materials described above as non-heat conducting materials or thermally insulating materials are either plastics or ceramics.
A further embodiment of the device according to the invention is shown in
The clamping frame 25 is grid-shaped and formed by longitudinal ties 26 and cross ties, wherein the ties 26, 27 span openings. Through these openings extend the reaction vessel holders 12 of the segments 8b. In the present embodiment, the ties 26, 27 are for instance in positive contact with the reaction vessel holders 12 and with the base plate 11 which protrudes from the reaction vessel holders. The 25 is provided with holes 28, through which pass bolts 29 for fixing the clamping frame to a thermocycling device 1.
Located below each of the segments 8b is a separately actuable Peltier element 7 and a cooling element 30 which extends over the area of all the segments 8b. Located in each case between the cooling element 30 and the Peltier element 7, and between the Peltier element 7 and the respective segment 8b is a heat conducting foil 31. The cooling element 30 is provided with holes through which extend the bolts 29, each fixed by a nut 32 to the side of the cooling element 30 facing away from the reaction vessel receiving element 9.
The clamping frame 25 is made from a non heat conducting material, in particular POM or polycarbonate. It therefore allows a fixing of the segments 8b of the reaction vessel receiving element 9 wherein the individual elements between the segments 8b and the cooling element 30 are under tension, thereby ensuring good heat transfer in the vertical direction between the individual elements. Since the clamping frame itself has poor heat conducting properties, the heat transfer between two adjacent segments 8b is kept low. For further reduction of heat transfer between two adjacent segments, the surfaces of the clamping frame 25 in contact with the segments 8b may be provided with narrow webs, so that in the areas adjoining the webs, air gaps are formed between the clamping frame 25 and the segments 8b.
In the embodiment shown in
Through integration of such a heat pipe in the segments 8b of the reaction vessel receiving element 9, a temperature equalisation is effected over the segment 8b. By this means it is ensured that the same temperature is present over the whole segment 8b.
A further embodiment of the thermocycling device 1 according to the invention is shown in
The segments 8c of this therm ocycling device 1, however, have no heat pipe. Instead of heat pipes, a temperature equalisation plate 34 is provided in the area beneath each of the segments 8c. These temperature equalisation plates 34 are flat elements with a surface corresponding to the basic surface of one of the segments 8c. These temperature equalisation plates 34 are hollow bodies with a small amount of fluid, and work on the same principle as the heat pipes. By this means it is once again ensured that there are no temperature variations within a segment 8c.
The temperature equalisation plate may however be made from materials with very good heat conducting properties, such as e.g. copper. Additional heating and/or cooling elements, e.g. heating foils, heating coils or Peltier elements, may be integrated in such a temperature equalisation plate. The heating and cooling elements support homogeneity and permit more rapid heating and/or cooling rates. A Peltier element, which generally does not have an even temperature distribution, is preferably combined with a flat heating element.
The reaction vessel receiving elements described above are comprised of a base plate with roughly tubular reaction vessel holders. Within the scope of the invention it is also possible to use a sample block, for example formed of metal, in which recesses to receive the reaction vessels of the microtiter plate are made.
Referring to
Heat pipe coolers have relatively high thermal conductivity (e.g., over one thousand times more conductive than copper) and a relatively flexible configuration so as to be capable of adapting to various physical environments. Due to such high thermal conductivity, heat pipe technology can reduce the delay between the heating/cooling source or a resistive heater and the sample block, as well as improve thermal uniformity throughout the sample block. In various exemplary embodiments, one or more heat pipes, for example, any number of pipes ranging from about 1 to about 10, may be used to transfer heat.
The use of heat pipes also may facilitate the proportional integral derivative (PID) control of the temperature and/or provide a higher precision temperature stability and uniformity. As discussed above, the ability to minimize temperature nonuniformities and maintain the sample block at a substantially uniform temperature may be desirable in many circumstances so as to be able to maintain the samples at a uniform reaction temperature.
As mentioned above, heat pipes for use in cooling in thermal cyclers utilize a phase change of a coolant from liquid to vapor inside the pipe. In various exemplary embodiments, the coolant may be water or a refrigerant. The pipes include a hot side (e.g., condenser end) and a cold side (e.g., evaporator end). The hot side may be in thermal communication with a heat sink to transfer heat from the heat pipe or the hot side may be cooled by directly circulating a cooling fluid (e.g., air, water, etc.) around the heat pipe hot side. Condensed liquid may circulate through the heat pipe from the hot side to the cold side. In various embodiments, internal surface portions of the heat pipe may be lined with a wicking material capable of capillarity such that the condensed liquid travels via the wicking material from the hot side to the cold side. Other mechanisms for circulating the condensed liquid also may be used, such as, for example, relying on gravity, pumps, or other mechanisms known to those skilled in the art. The physics and principles of operation of heat pipe technology are known to those skilled in the art and have been used for cooling in various computer systems, including, for example, notebook computers. Suitable heat pipe configurations include straight heat pipes, for example with vapor flowing in the center region in one direction and condensed liquid traveling around interior peripheral surface portions (e.g., via the wicking material) of the pipe in the opposite direction. In various alternative embodiments, heat pipes may be U-shaped or form a loop. Other curved heat pipe configurations also may be utilized.
Embodiments of heat pipe coolers include those marketed by Thermacore International (Lancaster, Pa.), which comprise a vacuum tight envelope, a wick structure and a working fluid. The heat pipe may be evacuated and back-filled with a small quantity of working fluid so as to saturate the wick. Inside the heat pipe, a vapor-liquid equilibrium is established. As heat enters the pipe at one end, the equilibrium is upset and generates vapor at a slightly higher pressure. This higher pressure vapor travels to the other condensing end where the slightly lower temperatures cause the vapor to condense and give up its latent heat of vaporization. Condensed fluid is then pumped back to the evaporator end by capillary forces developed in the wick structure. This continuous cycle transfers large quantities of heat with very low thermal gradients. For further information regarding Thermacore International's heat pipe technology, reference is made to http://www.thermacore.com/hpt.htm and http://www.electronics-cooling. com/Resources/EC Articles/SEP96/sep96 02.htm.
In various other embodiments, heat pipe coolers manufactured by Cooler Master Co., Ltd. of Taiwan, such as the Hyper 6 KHC-V81 model, and/or by Thermaltake Co., Ltd., such as the Big Typhoon model, may be used as the cooling member 592, 692, 792, 1092, or 1292. For further information on these heat pipe coolers, reference is made to http://www.coolermaster.com/index.php?LT=english&Language s=2&url place=product &p serial=KHC-V81 and http://www.thermaltake.com/coolers/4in1heatpipe/cl-p0114bigtyphoon/cl-p0114.htm, respectively.
Sample block 35 can be formed of any material that exhibits good thermal conductivity including, but not limited to, metals, such as, aluminum, silver, gold, and copper, carbon or other conductive polymers. Sample block 35 can be configured to receive one microtiter plate. For example, the top of sample block 35 can include a plurality of recesses arranged in an array that correspond to the wells in the microtiter plate. For example, common microtiter plates can include 96 depressions arranged as an 8×12 array, 384 depressions arranged as a 16×24 array, and 48 depressions arranged as a 8×6 array or 16×3 array. Alternatively, the sample block can be flat or without recesses to mate with flat-bottomed wells of a microplate or a flat portion of the chambers of a microcard.
Sample block 35 can be configured to define a plurality of zones.
According to various embodiments, the sample block can comprise a plurality of separate sample block segments, where each segment defines a zone.
In various other embodiments, as shown in
Each zone can further include a heating element 18. Heating element 18 can be can be, for example, resistive heaters known to one of ordinary skill in the art and shaped, for example, as foils or loops to distribute heat uniformly across a zone. In other embodiments, heating element 18 can be a resistive ink heater or an adhesive backed heater, such as, for example, a Kapton heater.
In various embodiments, each zone can also include a first metal plate. As shown in
Each zone further includes a TEC, such as, for example, a Peltier device. The plurality of TECs 7 can be configured to correspond to the plurality of zones. For example, the plurality of TECs 7 can correspond to the six zones defined by sample block 35. According to various embodiments, TECs 7 can provide course heating to near a control temperature and the heating elements 18 can provide fine heating to about the control temperature. The TEC can provide all heating and cooling. As used herein, the term “control temperature” refers to any desired temperature that can be set by a user, such as, for example, temperatures for denaturing, annealing, and elongation during PCR reactions. Each of the plurality of TECs can function independently without affecting other of the plurality of TECs. This can provide improved temperature control at each of the zones.
In various other embodiments, TECs 7 can be integrated into a single unit. As shown in
In various embodiments, the thermocycler can further include second metal plate 37 disposed between TECs 7 and heatsink 38. In various embodiments, the segmented block can be cooled by a single TEC device and heated by individualized resistive heaters for each segment. Alternatively, the segmented block can be cooled by individualized TEC devices for each segment and heated by a single resistive heater.
Thermocycler 1 can be operated in three modes as disclosed above. In a first mode, each zone is set to the same temperature. In a second mode, each of the zones is actuated with a different temperature. And, in a third mode only some of the zones are utilized. In an exemplary method of operation, themocycler 1 can process biological or chemical samples for PCR. Referring to
Zones 39-44 can then be cooled to an annealing temperature Ta. In an embodiment, each zone can be cooled to a different temperature, for example, where Ta1 is the annealing temperature in zone 39, Ta2 is the annealing temperature in zone 40, Ta3 is the annealing temperature in zone 41, Ta4 is the annealing temperature in zone 42, Ta5 is the annealing temperature in zone 43, and Ta6 is the annealing temperature in zone 44. The ramp rate to the annealing temperatures Ta1-a6 and the residence time at Te1-e6 can vary as desired.
During an elongating step, zones 39-44 can then be heated to an elongating temperature Te. In an embodiment, each zone can be heated to a different temperature, for example, where Te1 is the elongating temperature in zone 39, Te2 is the elongating temperature in zone 40, Te3 is the elongating temperature in zone 41, Te4 is the elongating temperature in zone 42, Te5 is the elongating temperature in zone 43, and Te6 is the elongating temperature in zone 44. The ramp rate to the elongating temperatures Ta1-a6 as and the residence time at Ta1-a6 can vary as desired. As shown in
The number of cycles, the mixture volumes the steps of denaturing, annealing, and elongating, can also vary for each zone. For example, the samples in zone 39 can undergo a first number of cycles, such as, for example, fifty, while the samples in zone 40 can undergo a second number of cycles, such as, for example, one hundred. One of skill in the art will understand that the exemplary method is described with reference to a sample block configured to define six zones and that more than six or less than six zones can be used. In various other embodiments, the reaction vessel mixture volume can be filled with different volume at each zone 39-44 and each reaction vessel segment can be set according to the filled mixture volume for optimizing the PCR performance.
According to various embodiments, sample block 35 can be configured to define a plurality of zones in which the zones have different shapes. Referring to the exploded perspective view of
In various embodiments, multiple power amplifiers can be used to provide current to the TECs to heat and/or cool the multiple zones of the sample block. Referring to
In operation, first switch 56 and second switch 57 can direct current flow from any power amplifier to any TEC. For example, first switch 56 and second switch 57 can direct current flow from first power amplifier 58 to first TEC 53 to heat and/or cool the first zone, and from second power amplifier 59 to second TEC 54 to heat and/or cool the second zone. Alternatively, first switch 56 and second switch 57 can direct current flow, for example, from first power amplifier 58 and from second power amplifier 59 to first TEG 53 to heat and/or cool the first zone. Similarly, first switch 56 and second switch 57 can direct current flow, for example, from first power amplifier 58 and from second power amplifier 59 to second TEC 54 to heat and/or cool the second zone. In this manner, the ramp rate to control the temperature in each of the plurality of zones can be increased or varied as desired. Although two switches and two power amplifiers are depicted, one of ordinary skill in the art will understand that more than two switches and power amplifiers can be used.
In various other embodiments, a system for processing biological or chemical samples can further include a thermocycler and a detachable microtiter plate configured to detach into a plurality of segments that correspond to the plurality of zones. The detached microtiter segments can correspond, for example, to the plurality of zones defined by sample plate 35.
In various embodiments, the microtitler plate can be modularto provide flexibility to the user.
According to various embodiments, sample blocks 35 and sample block segments 51 and 52, as shown in
Sample blocks and sample block segments can also be formed by metal injection molding (MIM). MIM can combine the design freedom of plastic injection molding with the performance of metal. MIM can be used with metals such as aluminum, copper, tungsten, and alloys thereof. In various embodiments, MIM can include feedstock mixing wherein very small powders are mixed with a thermoplastic polymer (known as a binder) to form a precise mixture of ingredients that is pelletized and directly fed into a plastic molding machine. This pelletized powder-polymer is known as feedstock. The metal powder and binders can be mixed and heated in a mixer and cooled to form granulated feedstock. MIM can further include injection molding, wherein the feedstock is heated to melt the plastic and then with pressure is forced into a mold to form the desired geometry. The molded part is known as the “green” part. MIM can further include de-binding, wherein the polymer or binder is removed thermally by heating the “green” part to about 400° C. (or about 752° F.). While retaining its shape and size, the de-bound or “brown” part is a powder skeleton that is very brittle and porous. De-binding can be performed in an oven where heat and air flow are fluxed in and exhaust products are fluxed out. The oven converts the “green” part to the “brown” part. MIM can further include sintering, wherein the “brown” part is heated to more than 1200° C. allowing densification and shrinking of the powder into a dense solid with the elimination of pores. Sintering can be performed in an over where heat, hydrogen gas, and argon gas are fluxed in. Usually the sintering density is similar to a casting at about 98% of theoretical. The end result is the molded thermal part, e.g, the sample block.
In various embodiments, MIM can provide sample blocks with sizes of about 100 millimeters by about 100 millimeters. A typical 9-well sample block has larger dimensions. However, several sample block segments can be constructed by MIM to provide thermal cycling for a 96-well or 384-well microplate as described in European Pat. No. 1,216,098.
Referring to
In various embodiments, the sample blocks and sample block segments described herein can be manufactured by MIM. The sample blocks and sample block segments formed by MIM can include copper, silver, aluminum, and/or gold. The sample blocks and sample block segments formed by MIM can provide substantial temperature uniformity throughout the array of biological samples contained in the array of sample wells coupled to the block for thermal cycling.
In various embodiments, methods for thermally cycling biological sample can be provided by the present teachings by providing the sample blocks and sample block segments produced by a MIM process such that heating and cooling of the sample blocks and sample block segments provides substantial temperature uniformity throughout the plurality of biological samples contained in the plurality of sample wells. The heating can be provided by heat from a resistive heater. In various embodiments, the cooling can be provided by pumping heat out with the thermoelectric module, which can be also be used for providing bias heat during heating cycles. In various embodiments, the cooling can be provided by spinning the block thereby convectively dissipating heat from the sample blocks and sample block segments to the environment during cooling cycles. For example, the sample blocks and/or sample block segments can be disk-like in shape and provide concentric rings of holes to receive the sample wells. The disk can spin along the central axis creating a convective current over the thermal block. Alternatively, the sample blocks and/or sample block segments of any shape can spin along an axis balanced by another sample block and/or sample block segment to provide a convective current similar to a centrifuge. In various embodiments, cooling can be achieved by providing forced gas, such as air or nitrogen, to contact the sample blocks and/or sample block segments. The forced gas can have ambient temperature or can be chilled to below ambient temperature.
In various embodiments, MIM can provide sample blocks and sample block segments that cannot be produced by machining the thermal block from a solid piece of metal because the MIM sample blocks and sample block segments have a thickness that cannot be uniformly machined such that every one of the plurality of sample wells is surrounded by portions of the sample block having similar thickness. For example, MIM can provide rounded surfaces for contacting the sample wells and rounded exterior surfaces with a flat bottom as in
The invention is described above with the aid of embodiments with 96 recesses for receiving a microtiter plate with 96 reaction vessels. The invention is not, however, limited to this number of recesses. Thus for example the reaction vessel receiving element may also have 384 recesses to receive a corresponding microtiter plate. With regard to features of the invention not explained in detail above, express reference is made to the claims and the drawing.
In the embodiments described above, a cooling device with a fluid cooling medium is used. Within the scope of the invention it is also possible to use a gaseous cooling medium, in particular air cooling, Instead of a fluid cooling medium.
Other embodiments of the invention will be apparent to those skilled in the art from consideration of the specification and practice of the invention disclosed herein. It is intended that the specification and examples be considered as exemplary only, with a true scope and spirit of the invention being indicated by the following claims.
This application is a continuation-in-part of application Ser. No. 10/089,136, filed Dec. 23, 2002, and a continuation-in-part of Ser. No. 11/383,140 filed on May 12, 2006, both of which are incorporated herein by reference in their entirety.
Number | Date | Country | |
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Parent | 10089136 | Dec 2002 | US |
Child | 11470463 | Sep 2006 | US |
Parent | 11383140 | May 2006 | US |
Child | 11470463 | Sep 2006 | US |