U.S. patent application number 12/381953 was filed with the patent office on 2012-03-29 for reaction apparatus.
Invention is credited to David Edge, Nelson Nazareth, David Ward.
Application Number | 20120077183 12/381953 |
Document ID | / |
Family ID | 38670142 |
Filed Date | 2012-03-29 |
United States Patent
Application |
20120077183 |
Kind Code |
A9 |
Ward; David ; et
al. |
March 29, 2012 |
Reaction apparatus
Abstract
An apparatus 20 for biological or chemical reactions, in
particular PCR, includes a heat removal module 22 adapted to
receive snugly a reaction vessel 24 in such a manner as to create
good thermal conductivity contact between the module and the
vessel. The heat removal module 22 is formed of a thermally
conductive material having therein a channel 64 adapted for the
flow of a coolant liquid. The heat removal module 22 is constructed
with an array of receiving stations 62 for the reception of a
corresponding array of reaction vessels 24.
Inventors: |
Ward; David; (Guisborough,
GB) ; Edge; David; (Warlingham, GB) ;
Nazareth; Nelson; (Upper Dean, GB) |
Prior
Publication: |
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Document Identifier |
Publication Date |
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US 20090263782 A1 |
October 22, 2009 |
|
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Family ID: |
38670142 |
Appl. No.: |
12/381953 |
Filed: |
March 18, 2009 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
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PCT/GB07/03564 |
Sep 18, 2007 |
|
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12381953 |
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Current U.S.
Class: |
435/3 ;
435/287.2; 435/303.1; 435/91.2 |
Current CPC
Class: |
G01N 2021/6441 20130101;
B01L 2300/0654 20130101; B01L 2300/1822 20130101; G01N 25/486
20130101; B01L 2300/185 20130101; B01L 2300/12 20130101; B01L
2300/1827 20130101; B01L 2300/0829 20130101; G01N 2021/0325
20130101; G01N 21/253 20130101; G01N 21/0332 20130101; B01L 7/52
20130101; B01L 3/50851 20130101 |
Class at
Publication: |
435/3 ;
435/303.1; 435/287.2; 435/91.2 |
International
Class: |
C12Q 3/00 20060101
C12Q003/00; C12P 19/34 20060101 C12P019/34; C12M 1/00 20060101
C12M001/00 |
Foreign Application Data
Date |
Code |
Application Number |
Sep 19, 2006 |
GB |
GB 0619128.2 |
May 29, 2007 |
GB |
GB 0718250.4 |
Claims
1. An apparatus for biological or chemical reactions, which
comprises: a heat removal module adapted to receive a reaction
vessel in such a manner as to create thermal conductivity contact
between the heat removal module and the reaction vessel; the heat
removal module being formed of a thermally conductive material; and
a channel formed in the heat removal module and adapted for the
flow of a coolant liquid.
2. The apparatus as set forth in claim 1, wherein the coolant
liquid is water.
3. The apparatus as set forth in claim 2, wherein the water is
deionized water with an antioxidant addition.
4. The apparatus as set forth in claim 1, which further comprises:
The heat removal module formed with a receiving station for receipt
therein of the reaction vessel.
5. The apparatus as set forth in claim 1, which further comprises:
the heat removal module formed with a plurality of receiving
stations in a prescribed array for receipt therein of a plurality
of reaction vessels.
6. The apparatus as set forth in claim 1, which further comprises:
an entry port formed at a first location of the heat removal
module; an exit port formed at a second location of the heat
removal module spaced from the first location; and the channel
extending between the entry port and the exit port in a serpentine
path.
7. The apparatus as set forth in claim 1, which further comprises:
the heat removal module formed as a unitary structure of the
thermally conductive material.
8. The apparatus as set forth in claim 1, which further comprises:
the heat removal module formed with a plurality of receiving
stations for receipt therein of reaction vessels; and the channel
being formed in a labyrinth configuration with each of a plurality
of spaced portions thereof being located adjacent at least a
portion of a respective one of the plurality of receiving stations
such that the coolant liquid flows adjacent the at least a portion
of each of the plurality of receiving stations, and any reaction
vessel which may be located in the respective one of the plurality
of receiving stations.
9. The apparatus as set forth in claim 8, which further comprises:
the labyrinth configuration of the channel being arranged so that
the coolant liquid flows adjacent at least two spaced portions of
at least one receiving station of the plurality of receiving
stations, and two spaced portions of any reaction vessel which may
be located in the at least one receiving station.
10. The apparatus as set forth in claim 7, which further comprises:
the unitary structure of the heat removal module formed as a single
block of the thermally conductive material.
11. The apparatus as set forth in claim 1, which further comprises:
the heat removal module being formed as a unitary structure
comprising: a first mating plate formed of a thermal conductive
material and having a first interfacing surface; a second mating
plate formed of a thermal conductive material and having a second
interfacing surface; and the first interfacing surface being in
facing engagement with the second interfacing surface; and the
channel being formed in a labyrinth configuration in at least one
of the first mating plate and the second mating plate.
12. The apparatus as set forth in claim 11, which further
comprises: a first portion of the channel formed in the first
interfacing surface; a second portion of the channel formed in the
second interfacing surface; and the first portion of the channel
and the second portion of the channel being located in the first
mating plate and the second mating plate, respectively, such that
the channel is formed when the first interfacing surface is in
facing engagement with the second interfacing surface.
13. The apparatus as set forth in claim 11, which further
comprises: a sealant located between the first interfacing surface
and the second interfacing surface.
14. The apparatus as set forth in claim 8, which further comprises:
a plurality of flow passages formed through the heat removal module
to facilitate the forming of the channel.
15. The apparatus as set forth in claim 14, which further
comprises: each flow passage of the plurality of flow passages
having at least one port located in an outer surface of the heat
removal module; and a stopper located in the at least one port to
preclude the flow passage from communication with the environment
externally of the at least one port.
16. The apparatus as set forth in claim 14, which further
comprises: each flow passage of the plurality of flow passages
formed through the heat removal module from a first side surface
thereof to a second side surface thereof opposite the first side
surface; each flow passage of the plurality of flow passages having
a first port coincidental with the first side surface of the heat
removal module, and a second port coincidental with the second side
surface of the heat removal module; and each flow passage of the
heat removal module having a stopper located in the first port and
a stopper located in the second port to preclude the flow passage
from communication with the environment externally of the heat
removal module.
17. The apparatus as set forth in claim 8, which further comprises:
the heat removal module being formed as a single block.
18. The apparatus as set forth in claim 8, which further comprises:
the heat removal module being formed by: a first mating plate; and
a second mating plate in interfacing engagement with the first
mating plate.
19. The apparatus as set forth in claim 1, which further comprises:
a first flow passage formed in the heat removal module and being
located in a prescribed plane; a second flow passage formed in the
heat removal module and being located in the prescribed plane; the
first flow passage arranged to intersect with the second flow
passage to normally provide communication therebetween; and a flow
stopper located in the first flow passage to separate the first
flow passage into a communicating portion thereof, which is in
communication with the second flow passage, and a non-communicating
portion, which is precluded from communication with the second flow
passage.
20. The apparatus as set forth in claim 19, which further
comprises: the second flow passage and the communicating portion of
the first flow passage forming a portion of the channel, whereby
the coolant liquid flows only in the second flow passage and in the
communicating portion of the first flow passage.
21. The apparatus as set forth in claim 19, which further
comprises: a stopper passage formed in the heat removal module
having an inboard end angularly intersecting the first flow
passage; and the flow stopper located within the stopper passage
with an inboard end of the flow stopper extending into and blocking
the first flow passage to separate the first flow passage into the
communicating portion and the non-communicating portion.
22. The apparatus as set forth in claim 1, which further comprises:
a first plurality of normally non-communicating flow passages
formed in the heat removal module and being located in a prescribed
plane; a second plurality of normally non-communicating flow
passages formed in the heat removal module and being located in the
prescribed plane; each flow passage of the first plurality of flow
passages arranged to intersect with each flow passage of the second
plurality of flow passages to normally provide communication
amongst the first and second plurality of flow passages; a
plurality of flow stoppers located spacially in each flow passage
of the first plurality of flow passages to separate each flow
passage of the first plurality of flow passages into a plurality of
spaced communicating portions interspersed by a plurality of spaced
non-communicating portions, and the spaced communicating portions
of the first plurality of flow passages being in communication with
the second plurality of flow passages to form the channel in a
labyrinth configuration.
23. The apparatus as set forth in claim 22, which further
comprises: the labyrinth configuration of the channel being formed
in a serpentine path.
24. The apparatus as set forth in claim 1, wherein the heat removal
module further comprises: a receiving station formed by a receptor
passage which extends between and through a first major surface of
the heat removal module and a second major surface of the heat
removal module; and the receptor passage is formed with a wall.
25. The apparatus as set forth in claim 24, which further
comprises: the wall being formed in a configuration which generally
matches a configuration of an external surface of at least a
portion of the reaction vessel to be received within the receptor
passage.
26. The apparatus as set forth in claim 24, which further
comprises: the wall of the receptor passage being electrically
insulated to preclude electrical contact with any portion of the
reaction vessel to be located within the receptor passage.
27. The apparatus as set forth in claim 1, wherein the heat removal
module is composed of a material selected from the group consisting
of any one or more of copper, aluminum alloy, silver, gold, boron
nitride, diamond and graphite.
28. The apparatus as set forth in claim 1, wherein the heat removal
module forms at least a portion of an electrically-conducting path
for facilitating the heating of any reaction vessel received in the
heat removal module.
29. The apparatus as set forth in claim 1, which further comprises:
an external surface of the heat removal module being coated with a
layer of an electrically insulative material.
30. The apparatus as set forth in claim 1, which further comprises:
an external surface of the heat removal module being anodized.
31. The apparatus as set forth in claim 1, which further comprises:
the heat removal module being structured for use with a reaction
vessel having: a reaction portion formed with a length of 8 mm and
a mean bore of 2.5 mm; a contact portion having an outside diameter
of approximately 4 mm and a length of 3 mm; and a funnel portion
having a mean outside diameter of 6 mm and a length of 7 mm.
32. The apparatus as set forth in claim 1, which further comprises:
the heat removal module being structured for use with a reaction
vessel formed at least partially with a casing of an electrically
conductive material with an electrically insulative liner.
33. The apparatus as set forth in claim 1, which further comprises:
the heat removal module being structured for use with a reaction
vessel having a wall thickness of generally 0.3 mm.
34. The apparatus as set forth in claim 1, which further comprises:
the heat removal module being structured for use with a reaction
vessel having a base which has a toroid formed thereon to
accommodate a temperature sensor.
35. The apparatus as set forth in claim 1, which further comprises:
the heat removal module being structured for use with a reaction
vessel having a funnel shape, a contact portion, and a lid for
sealing the reaction vessel when in use, the lid having a window at
a base thereof above a reaction chamber of the vessel to permit
optical interrogation of a reaction process occurring within the
reaction vessel.
36. The apparatus as set forth in claim 1, which further comprises:
the heat removal module being composed of an electrically
conductive material; the heat removal module being formed with at
least one receiving station for receiving therein the reaction
vessel formed with a first electrical contact surface for
electrical engagement with the heat removal module and a second
electrical contact surface spaced from the first electrical contact
surface, whereby, when the reaction vessel is located within the
receiving station, and an electrical power source is connectable
between the heat removal module and the second electrical contact
surface of the reaction vessel, electrical current will flow in the
reaction vessel.
37. The apparatus as set forth in claim 36, which further
comprises: the receiving station includes a receptor passage formed
through the heat removal module and having a wall extending between
an entry port at a first end of the receptor passage and an exit
port at a second end of the receptor passage spaced from the entry
port; the heat removal module, including the wall of the receptor
passage, being anodized, except for an electrically exposed area
adjacent the entry port which, when the reaction vessel is located
within the receptor passage, is in electrical engagement with the
first electrical contact surface of the reaction vessel.
38. The apparatus as set forth in claim 36, which further
comprises: an electrical contact element positionable for
electrical engagement with the second contact surface of the
reaction vessel, when the vessel is located in the receiving
station, and connectable to the electrical power source.
39. The apparatus as set forth in claim 1, which further comprises:
an optical monitoring means for monitoring the progress of a
reaction within the reaction vessel.
40. The apparatus as set forth in claim 39, wherein the optical
monitoring means comprises: a laser source; means for directing a
laser beam into the reaction vessel, and a multi-anode
photomultiplier tube for detecting emitted light resulting from a
reaction occurring within the reaction vessel.
41. The apparatus as set forth in claim 39, wherein the optical
monitoring means comprises: a printed circuit board positioned
adjacent the reaction vessel; the printed circuit board including
an array of light emitting diodes selected so as to be within an
excitation spectrum of the reactive content of the reaction vessel
which are under interrogation and arranged to direct light into the
reaction vessel; the printed circuit board having a small opening
located to allow passage of the light emission spectra of the
reactive content of the reaction vessel; a detector located to
detect the emission spectra; and a filter for blocking the path of
the excitation spectra to the detector.
42. The apparatus as set forth in claim 41, wherein the filter
comprises: an optical filter placed across the small opening.
43. The apparatus as set forth in claim 41, wherein the light
emitting diodes are arranged to emit light at a wavelength of 470
nm or above.
44. The apparatus as set forth in claim 39, which further
comprises: a detector selected from the group consisting of a photo
multiplier tube, an avalance photodiode, a charge coupled device, a
light-dependent resistor, and a photovoltaic cell; and a Fresnel
lens arranged to direct emitted light from the reaction in the
reaction vessel onto an XY scanning mirror set and thereby into the
detector.
45. The apparatus as set forth in claim 1, wherein the heat removal
module further comprises: a receiving station in the heat removal
module for receiving the reaction vessel; means for monitoring the
reaction in the reaction vessel; and a vessel temperature sensor
located at the receiving station.
46. The apparatus as set forth in claim 1, which further comprises:
the heat removal module composed of an electrically conductive
material; and the heat removal module having an electrical terminal
to facilitate connection of the heat removal module to an
electrical power source.
47. The apparatus as set forth in claim 1, which further comprises:
the heat removal module formed with a recess in one surface thereof
from which a portion of the reaction vessel extends; and a printed
circuit board attachable to the heat removal module and having an
electrical contact extending therefrom which is mountable in the
recess when the printed circuit board is attached to the heat
removal and electrically engagable with the portion of the reaction
vessel to facilitate connection of the reaction vessel to an
electrical power source.
48. The apparatus as set forth in claim 45, which further
comprises: the vessel temperature sensor is selected from the group
consisting of an infra-red detector, a thermistor, and a thermopile
sensor.
49. The apparatus as set forth in claim 1, which further comprises:
means for heating the coolant liquid to a desired temperature.
50. The apparatus as set forth in claim 45, which further
comprises: a heat guide arranged to guide heat radiated from a
surface of the reaction vessel onto the vessel temperature
sensor.
51. An apparatus for biological or chemical reactions, which
comprises: a heat removal module being formed of an electrically
conductive material; a vessel-receiving passage formed in the heat
removal module, having a first portion thereof spaced from a second
portion thereof by a prescribed distance, for receiving therein a
reaction vessel having a prescribed length and an electrically
conductive outer section; an exposed contact surface of the heat
removal module located adjacent the first portion of the
vessel-receiving passage for engagement with a first portion of the
electrically conductive outer section of the reaction vessel; and
the prescribed distance of the vessel-receiving passage being less
than the prescribed length of the reaction vessel such that a
second portion of the electrically conductive outer section of the
reaction vessel extends outward from the second portion of the
vessel-receiving passage; whereby, upon connection of an electrical
power source to the heat removal module and the second portion of
the electrically conductive outer section of the reaction vessel,
electrical current will flow through the electrically conductive
outer section of the reaction vessel.
52. A heat removal module for use in conducting biological or
chemical reactions, which comprises: structure formed in the heat
removal module for receiving a reaction vessel in such a manner as
to create thermal conductivity contact between the heat removal
module and the reaction vessel; the heat removal module being
formed of a thermally conductive material, and a channel formed in
the heat removal module for facilitating the flow of a coolant
liquid therethrough.
53. A method of conducting a biological or chemical reaction
process, which comprises the steps of: forming a heat removal
module of a thermally conductive material and with a receiving
station and a channel; placing a reactive sample into a reaction
vessel; placing the reaction vessel into the receiving station to
create thermal conductivity contact between the heat removal module
and the reaction vessel; flowing a coolant liquid through the
channel; heating the coolant liquid to a temperature in a specified
thermocycling program; and conducting the specified thermocycling
program on the reactive sample.
54. The method as set forth in claim 53, wherein the reaction
vessel is a microtiter vessel.
55. The method as set forth in claim 53, which further comprises
the step of: forming a plurality of receiving stations in the heat
removal module for receiving a plurality of reaction vessels.
56. The method as set forth in claim 53, which further comprises
the step of: forming a plurality of receiving stations in the heat
removal module for 96n reaction vessels, where n is an integer.
57. The method as set forth in claim 53, which further comprises
the step of: monitoring the temperature of the of the reaction
vessel with a temperature sensor.
58. The method as set forth in claim 57, which further comprises
the step of: connecting the temperature sensor in an electric
circuit arranged for heating the reaction vessel.
59. The method as set forth in claim 55, which further comprises
the steps of: providing a temperature sensor for each of the
plurality of receiving stations, and connecting each temperature
sensor in an electrical circuit for providing individual and
discrete heating for each of the plurality of reaction vessels.
60. The method as set forth in claim 57, wherein the temperature
sensor is selected from the group consisting of an infra-red
detector, a thermistor, and a thermopile sensor.
61. The method as set forth in claim 53, which further comprises
the step of: optically monitoring a reaction occurring within the
reaction vessel.
Description
[0001] This application claims the benefit of International
Application No. PCT/GB2007/003564, filed on Sep. 18, 2007, which,
in turn, claims the benefit of UK applications GB 0619128.2, filed
on Sep. 19, 2006, and GB 0718250.4, filed on May 29, 2007, all
three of which are incorporated herein by reference thereto.
FIELD OF THE INVENTION
[0002] This invention relates to apparatus for biological or
chemical reactions where thermal cycling is employed in the
reaction. It is particularly concerned with reactions such as
polymerase chain reactions (PCR).
[0003] The PCR process is described in detail in U.S. Pat. Nos.
4,683,195, which issued on Jul. 28, 1987, and 4,683,202, which
issued on Jul. 28, 1987.
BACKGROUND OF THE INVENTION
[0004] Typically a large number of reduced volume reactions are
carried out simultaneously in one apparatus, with a plurality of
reaction vessels being received in a reaction apparatus at one
time. Often the reaction vessels are in the form of a tray, known
as a microtiter plate, made up of an array of vessels. In one
standard microtiter plate, 96 vessels are formed in one array. In
order to control and monitor the reactions, the apparatus includes
means to monitor the temperature and to control the heating power
applied to the reaction vessel contents.
[0005] Often, in reactions involving multiple thermal cycles, the
cooling part of the cycle is effected using a cooling block and/or
a fan blowing cooled air over the vessel or vessels. Often the
cooling is continuously present and the heating part of the cycle
is carried out against a background of the cooling. Thus, for
example, in conventional block thermal cyclers, heating is effected
using a direct heater, for example thermal mats, and cooling by
either forced air or actively by thermo electric heat pumps. In
other thermal cycling apparatus, heating and cooling are effected
by shuttling between blown hot air and blown cold air.
[0006] There are situations, for example, when it is required to
identify what may be a dangerous pathogen, in which it is highly
desirable to minimize the time taken by such a reaction. Apparatus
for minimizing the time required in the heating part of the cycle
is described in UK Patent Nos. GB 2404883B, published on Feb. 27,
2006, and GB 2424380B, published on Jun. 27, 2007, both of which
are incorporated herein by reference thereto. In this apparatus, an
electrically conductive polymer is employed as, or as part of, the
material of the reaction vessel. Cooling is effected using forced
cooled or ambient air.
[0007] Normally, the maximum cooling rate achievable using forced
air is 8.degree. C. per second. A higher cooling rate than this
would be very useful. The present invention provides means whereby
cooling in biological or chemical reactions requiring thermal
cycling is significantly accelerated.
SUMMARY OF THE INVENTION
[0008] According to the present invention, an apparatus for
biological and chemical reactions includes a heat removal module
adapted to receive snugly a reaction vessel in such a manner as to
create good thermal conductivity contact between the module and the
vessel, the module being formed of a thermally conductive material
having therein a channel adapted for the flow of a coolant
liquid.
[0009] The coolant liquid may be water, preferably deionized water
with an antioxidant addition. A typical example of such a coolant
liquid is FluidXP+, which is supplied by Integrity PC Systems &
Technologies, Inc. of Riverdale, Calif. USA.
[0010] Typically, thermo-cycling reaction apparatus is arranged to
receive in stations a standard array of 96, or an integer multiple
thereof, microtiter reaction vessels in a rectangular array,
usually comprising 12 by 8 such stations.
[0011] According to a feature of the present invention the heat
removal module may comprise a single block of thermally conductive
material arranged to provide an array of receiving stations for
microtiter reaction vessels and the channel is in labyrinthine form
whereby the coolant liquid flows adjacent each receiving station
and each reaction vessel.
[0012] It has been found that with a heat removal module according
to the present invention a mean vessel cooling rate of 18.degree.
C. per second can be achieved, with a peak of 24.degree. C. per
second.
[0013] In one embodiment, the heat removal module is formed of two
mating plates and the channel is formed in one plate or in mating
surfaces of both plates, for example, by milling or routing. When
fitting the two plates together, a suitable sealant may be used
between two interfacing surfaces of the plates to ensure no escape
of the coolant liquid. The sealant may also be required to insulate
one plate from the other electrically.
[0014] In another preferred embodiment, the heat removal module is
formed of a single block and the channel is formed by drilling
through the block, and then blocking any unwanted exits or routes
using stoppers such as grub or set screws.
[0015] The material of the block is composed of any one, or
combination, of copper, aluminum alloy, silver, or gold, boron
nitride, diamond and graphite among the possibilities.
[0016] In a preferred context, where the vessel incorporates
heating means, for example, it includes an electrically conductive
polymer (ECP), the module may be arranged to provide a path in the
electrical circuitry. In such a case it may be advantageous for the
module to be coated, where necessary, with an electrical insulation
material. For example, it may be anodized.
[0017] Where the heating of each vessel is to be individually
controlled then, given the space constraints of a microtiter array,
the heat removal module may be adapted to receive contact elements
for the supply of electric current while acting as the return
contact element, or vice versa. The contact elements may be formed
of beryllium, copper, or a woven polyester coated or plated with
copper and/or nickel. Since the heat removal module may be located
on a printed circuit board (PCB), which includes electrical contact
elements, a jig may be constructed to ensure that the electrical
contact elements will attach to the PCB so as to fit
non-interferingly in recesses formed in the module.
[0018] Where the heating is not obtained by using the vessel, or
part thereof, as the heating element, the heat removal module may
be adapted to receive the heating element(s). A heating element
such as a Peltier cell may be employed in this situation.
[0019] Fortunately it is usually the case that the lower
temperature required in biological or chemical reactions involving
thermo-cycling is higher than ambient. Often it is anyway necessary
that the lower temperature is as precisely controlled as the upper
temperature. Accordingly, apparatus for effecting such reactions,
and incorporating a heat removal module according to the invention,
may also have a heater for heating the coolant liquid to the
desired temperature. This has the added advantage of preventing
condensation from forming on the exterior of the heat removal
module.
[0020] The standard pitch of microtiter reaction vessels in a 12 by
8 array is 9 mm. The bore of the channel may be of the order of 3
mm.
[0021] A reaction vessel, particularly suitable for use in a heat
removal module according to the invention, is described in the
above-noted UK Patent GB 2404883B and comprises a working or
reaction portion 8 mm long with a mean bore of 2.5 mm, a contact
portion of approximately 4 mm outside diameter and 3 mm length and
a funnel-like portion of 6 mm mean outside diameter and 7 mm
length. The vessel is formed of electrically conductive material
with an electrically insulated plastics liner. The electrically
conductive material may comprise a carbon based filler such as
Buckminster fullerine tubes or balls, carbon flake or powder within
a polypropylene matrix. Typically, the carbon content is up to 70%
by weight, with 10% being carbon black and the rest graphite. The
total wall thickness of the vessel is of the order of 0.3 mm. The
base of the vessel has a toroid formed thereon to accommodate a
temperature sensing device, which may be of the thermal contacting
type, for example a thermistor, or the remote sensing type, for
example a thermopyle type. A lid fits into an open end of the
funnel-like portion and the contact portion of the vessel and seals
the vessel when in use. The lid has a window at the base thereof
immediately above the working portion of the vessel, and
facilitates optical interrogation of the reaction process.
[0022] The module may however be constructed for use with a vessel
of a different form, including a BioChip.
[0023] According to a second aspect of the invention, a reaction
apparatus, in which one or more reaction vessels are received and
the reactions therewithin monitored, includes one or more vessel
receiving stations each for receiving a reaction vessel and, for
each receiving station, a method of thermometry of the reaction
vessel. This may comprise contact thermometry or infra-red
detection.
[0024] In the case of infra-red detection, each receiving station
may have a thermopile sensor. If necessary, there may also be a
heat guide arranged to collect heat radiated from the surface of
the vessel and to guide it onto the sensor. This can avoid having
to ensure that the sensor is exactly aligned normal to the surface
of an adjacent station and vessel. Typically, the heat guide is
formed of aluminum, copper, or another material with low emissivity
and high reflectivity arranged to reflect the heat radiated from
the vessel onto the thermopile.
[0025] Preferably such thermopile sensors are mounted upon a PCB
including bores through which the reaction vessels pass. The PCB
and the heat guide may be formed with small openings, including
bores larger than the local diameter of the vessel, to allow the
passage of a cooling gas such as air.
[0026] This provides an extremely robust, reproducible and
non-invasive means of measuring and/or controlling the temperature
of individual reaction vessels independently of the other reaction
vessels within the reaction vessel matrix. Typically the distance
of the thermopile sensor to the vessel is between 0.5 mm and 30 mm.
In the context of microtiter vessels having a maximum diameter of 1
cm, this distance is under 1 cm. Where the location of such a
sensor is impossible due to space restrictions, a thermal guide
such as a glass fiber strand/optical fiber may be used as a
waveguide to transport the infra-red energy to a remote sensor.
[0027] Advantageously, the outer layer of the vessel is highly
thermally emissive to provide a vessel having as close as possible
to black body external surface properties. This is particularly
suited to systems where non-contact temperature measurement is
required. Where highly thermally emissive materials cannot be used,
the difference between perfect and actual emissivity may be used to
derive the correct temperature of the vessel and the contents
thereof.
[0028] Where thermally emissive materials are not available, or
non-contact thermometry is not suitable, contact thermometry may be
used to derive the temperature of the vessel. Such a contact
temperature sensor is preferably sited other than at actively
heated or cooled portions of the vessel. A thermally conductive
material duct may, if desired, be employed between the vessel and
the sensor.
[0029] It is usually the case that the vessel is sealed with the
lid, or a cap, for the duration of a reaction and such a lid may be
translucent or even transparent for at least a part thereof to form
a window adjacent the reaction sample, whereby the progress of the
reaction can be monitored. According to features of the invention,
such a lid may be provided and may be arranged so that the window
is heated to slightly above sample temperature and leaves only a
minimal, if any, air gap above the sample. This feature, and/or
heating the window, serves to prevent condensation on the window,
enable rapid temperature rise in the sample, and prevent
concentration of the sample by evaporation. Advantageously, the lid
has a low thermal mass to allow it to be heated and cooled as
quickly as possible.
[0030] In an alternative construction, such lids or caps are made
of a thermally conductive material and heated individually to a
thermal profile in a manner to encourage the condensation in the
vessel to evaporate during an optical detection process, and cooled
when optical detection is not required to encourage the condensate
to collect on the lid and drip into the vessel. Alternatively, the
lid may be held at a constant temperature to minimize evaporation
that might cause concentration of the reaction within the
vessel.
[0031] Preferably the vessel is arranged to contain the entire
sample in a minimally tapered cylinder at a lower section of the
vessel, with the taper angle being chosen for the optical
application and ease of molding if the vessel is produced by a
molding method. Typically, the taper angle is of the order of
1-6.degree. and the thickness of the outer layer is between 0.01
and 1 mm. The taper has the advantage of permitting air above the
sample to escape when the lid is being located on the vessel.
[0032] In order for the maximum heat transfer to be able to take
place as effectively as possible, the tube shape of the vessel
should have as large a surface area to volume ratio as possible.
The ideal shape would be to have the fluid held between two plates
of ECP that would be heated and cooled. However, this design does
not lend itself to molding with ECP, and neither does it lend
itself to being locatable in a 96 well microtiter plate (MTP)
format in a 9 mm square vessel array context. However, it may be
suitable with a non-microtiter vessel context, for example a
BioChip.
[0033] Inside this footprint, the ideal vessel reaction chamber has
substantially capillary dimensions and a high aspect ratio. As thin
a wall thickness as is possible for ready and reproducible
moldability and safe handling has advantages then in terms of heat
transfer and material costs. Consequently, the wall thickness may
be between 0.1 mm and 2 mm.
[0034] The ability to transfer heat into and out of the reaction
vessel is directly proportional to the wall thickness of the
reaction vessel in contact with the heating or cooling medium.
Doubling the wall thickness will double the thermal gradient
required to transfer the same amount of energy into the reaction
vessel. The higher the ratio of surface area to volume ratio the
better the results. Preferably, the ratio of surface area to volume
is above 3 and preferably above 6.
[0035] Preferably, the reaction vessel is constructed for use in
apparatus with the base of the vessel and an upper edge portion of
the outer heating layer thereof providing electrical contact
areas.
[0036] According to yet another feature of the invention, an
optical monitoring system for a reaction apparatus may be provided,
where the reaction apparatus defines a plurality of receiving
stations, each such station receiving a reaction vessel in which a
reaction may take place.
[0037] The optical monitoring system may comprise at least one
radiation source. Also provided is a scanning apparatus for
directing radiation to vessels in the receiving stations, and for
directing radiation emitted by the reaction vessel contents into
photometric apparatus. The photometric apparatus directs received
radiation to a diffraction grating or equivalent technology, and
thence to a photomultiplier tube assembly, preferably operating in
a photon counting mode.
[0038] The photomultiplier tube assembly may comprise a series of
single channel multi-anode photomultiplier tubes, but preferably
the assembly comprises a multi-channel multi-anode photomultiplier
tube (MAPMT).
[0039] Radiation emitted by the vessel contents is dispersed over
the pixels of the MAPMT by use of a diffraction grating such that
the range of wavelengths of radiation impinging upon a photocathode
of the MAPMT correlates with the position of the photocathode in
the MAPMT.
[0040] In one embodiment, the MAPMT is a 32 pixel linear array over
which radiation from around 510-720 nm is dispersed. Thus, the
optical monitoring system provides for the use of a broad range of
fluorophores emitting radiation at wavelengths between about 510 nm
and about 720 nm without the need to change filter sets as required
in other instrumentation.
[0041] The use of the MAPMT, and operating it in photon counting
mode, provides for sensitive detection of radiation, thereby
facilitating the measurements of low levels of incident
fluorescence associated with high sampling frequencies.
Measurements using a MAPMT, operating in photon counting mode, are
less affected by changes in the electromagnetic environment, than
if the MAPMT is operated in analog mode.
[0042] The optical monitoring means is preferably an integral part
of the reaction apparatus.
[0043] Preferably, the light source is a single light source,
typically a laser, and the laser is a diode pumped solid-state
laser (DPSSL) in contrast to the gas lasers used in conventional
reaction apparatus and optical monitoring systems.
[0044] Preferably means are provided for monitoring the reactions
within a plurality of vessels, by directing radiation from a single
excitation source to the vessels, and collecting the resultant
radiation from the vessels to be measured by a single photometric
system. Such a means may comprise one or more rotatable mirrors,
where the configuration of mirrors can be controlled to direct
light to and from any specific vessel. An array of two mirrors is
preferred. The size and bulk of the mirror is arranged to be such
as to achieve efficient radiation collection with minimum scanning
frequency.
[0045] The use of a single excitation source and a single
photometric system in the same way for all vessels under
observation reduces the possibility of variability being introduced
into measurements due to the differences between multiple detectors
or sources of excitation. In addition, it facilitates the
cost-effective use of high quality components in excitation and
detection sub systems. This is particularly suited for use with
high quality photomultiplier systems
[0046] The acquisition of a full spectrum from each vessel at each
sampling point facilitates the concurrent use of multiple different
fluorophores in the array of reaction vessels in the apparatus
(including use of multiple different fluorophores within a single
vessel) as required by some fluorometric applications. Such a
spectrum may also be acquired in a single operation reading all
channels of the MAPMT concurrently, in contrast to systems where
readings at different wavelengths must be acquired consecutively,
for example by use of a filter wheel or other means. This technique
affords higher sampling rates, and removes effects related to
variation in signal between the acquisitions of different
wavelengths.
[0047] A Fresnel lens may be used in the path of the laser, and is
light, cost-effective and very compact compared to a standard lens
of the same diameter and optical properties. The Fresnel lens
ensures that the radiation from the excitation source is always
directed substantially vertically when it enters each vessel. The
rotating mirrors cause the beam to be reflected at an angle, such
that it hits the Fresnel lens at a point above the vessel to be
illuminated, the Fresnel lens refracts the beam from this point to
enter the vessel vertically. The resultant emitted radiation from
the vessel is refracted from vertical travel to the correct angle
to return to the rotating mirrors and hence to the photometric
system.
[0048] A plurality of light sources may be used as the excitation
source to illuminate the sample with a variation of radiation
spectra. The excitation sources may be a plurality of individually
attenuated lasers, a plurality of Light Emitting Diodes, a Light
Emitting Diode (LED) capable of generating a variety of spectra
(RGB LED's) or multiple incandescent or fluorescent lamps.
[0049] Software and/or physical filters may be used to remove
incident light from the detected sample spectra and also to remove
emissions resultant from excitation from one source from those
resultant from another source, and in this way allow non
source-specific emissions to be subtracted and experimentally link
fluorophores in the reaction to specific light sources as discussed
above. This allows the apparatus to excite at a number of
individual wavelengths simultaneously while removing the necessity
to change filters using a filter wheel. Where single excitation
sources are used, a physical filter may be used to remove the
excitation spectra from the detected sample spectra. Filter Wheels
are generally regarded as slow devices capable of performing
several color changes per second. The use of the software filtering
allows up to 1500 samples per second to be filtered. Regarding
detection, CCD, a photomultiplier tube or an avalanche photo diode
array are among the possibilities.
[0050] An alternative optical monitoring system comprises a PCB
located above the reaction vessels, with the PCB holding an array
of LEDs selected so as to be within the excitation spectrum of the
vessel contents under interrogation and arranged for the direction
of light into the vessel. The PCB also has a plurality of small
openings arranged to permit the passage of a light emission spectra
from the content of each vessel. The system also includes detector
apparatus arranged to detect the emission spectra and filter means
to block the path of excitation spectra to the detector.
[0051] Preferably the LEDs are arranged to emit light at the blue
end of the optical spectrum, typically at a wavelength of 470 nm or
above. One suitable detector apparatus may comprise a Fresnel lens
arranged to direct the light onto an XY scanning mirror set and
thereby into a detector such as a PMT, APD (avalanche photo-diode),
CCD (charge couple device), LDR (light dependent resistor) or a
photovoltaic cell. The PMT may be single cell or, if the emission
beam is split into a spectrum, an array thereof. The filter means
may include an optical filter placed, for example, across the small
opening, or software associated with the detector. With the lid
usually covering the vessel, the optical monitor system is arranged
for light path association therewith.
BRIEF DESCRIPTION OF THE DRAWINGS
[0052] Embodiments of the invention will now be described, by way
of example only, with reference to the accompanying drawings, in
which:
[0053] FIG. 1 is a perspective view, with a part cut away, showing
a heat removal module having receiving stations for supporting a
plurality of reaction vessels, in accordance with certain
principles of the invention;
[0054] FIG. 2 is a plan view of a bottom of the heat removal module
of FIG. 1, in accordance with certain principles of the
invention;
[0055] FIG. 3 is a side view of the heat removal module of FIG. 1,
with dotted lines showing the location of the receiving stations
and a portion of a labyrinth channel, in accordance with certain
principles of the invention;
[0056] FIG. 4 is a sectional side view of the heat removal module
of FIG. 1 showing the receiving stations and a portion of the
labyrinth channel, in accordance with certain principles of the
invention;
[0057] FIG. 5 is a partial sectional view showing a single
receiving station of the heat removal module of FIG. 1, with a
single reaction vessel within the receiving station, in accordance
with certain principles of the invention;
[0058] FIG. 6 is a partial sectional view showing the heat removal
module of FIG. 1 with a stopper located to facilitate formation of
the labyrinth channel, in accordance with certain principles of the
invention;
[0059] FIG. 7 is a diagram of a first optical interrogation system,
in accordance with certain principles of the invention; and
[0060] FIG. 8 is a diagram of a second optical interrogation
system, in accordance with certain principles of the invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0061] Referring to FIGS. 1, 2, 3 and 4, in accordance with certain
principles of the invention, an apparatus 20, for biological and
chemical reactions, includes a heat removal module 22 (hereinafter
"the module") formed from a heat conductive material. In addition,
the material which forms the module 22 is electrically conductive,
and may be selected from any one material, or combinations thereof,
consisting of copper, aluminum alloy, silver, gold, boron nitride,
diamond and graphite. Aluminum alloy is the preferred material.
[0062] As shown in FIGS. 1 and 5, the module 22 is structured to
support a reaction vessel 24 (hereinafter "the vessel") of the type
commonly used in biological and chemical reaction testing of
various reagents. The vessel 24 is formed with an electrically
non-conductive inner casing 26, or electrically insulative liner,
and includes an upper larger section 28 having an upper funnel
opening 29 of the vessel, through which reagents are introduced
into the vessel. The inner casing 26 of the vessel 24 further
includes a transition section 27, an intermediate mid-size section
30, a transition section 31, and a lower smaller section 32, which
forms a reaction portion, such as a reaction chamber 34, or cavity,
with each section having a slightly tapered wall to form the inner
casing in a stepped, funnel-like shape with a closed bottom at a
base 36 of the vessel to form a floor of the reaction chamber 34.
The reaction portion or chamber 34 is formed with a length of eight
millimeters and a mean bore of two and one-half millimeters. The
upper section 28, the intermediate section 30, and the lower
section 32 of the inner casing 26 are formed with successively
smaller diameters, with the upper opening 29 forming the only
opening into the vessel 24. Further, the vessel 24 includes an
electrically conductive outer casing 38, which includes an upper
larger section 40 formed with a contact ledge 41 at an upper
portion of the larger section. The outer casing further includes a
lower smaller section 42, with a transition section 43 between the
upper larger section and the lower smaller section, and a base 44,
which conform to, and are integrally joined with, outer surfaces of
the intermediate section 30, the transition section 31, the lower
section 32, and the base 36, respectively, of the funnel-like shape
of the inner casing 26. The base 36 of the inner casing and the
base 44 of the outer casing 38 combine to form a closed base 46 of
the vessel 24. The outer casing 38 of the vessel 24 has an outside
diameter of approximately four millimeters and a length of three
millimeters. The upper section 28 of the vessel 24, formed by the
inner casing 26, is a funnel portion of the vessel and has a mean
outside diameter of six millimeters and a length of seven
millimeters. The vessel 24 has a wall thickness of generally three
tenths of a millimeter.
[0063] The inner casing 26 and the outer casing 38 of the vessel 24
are formed by a two-shot molding process, in which the two layers
are formed of different polymers. The inner casing 26 is composed
of electrically non-conductive polypropylene, which provides an
optimal surface for contact with the reagents in the reaction
chamber 34 as anticipated in many biological reactions, and also
provides good thermal coupling between the outer casing 38 and the
reagents located within the reaction chamber. The outer casing 38
is an electrically conductive polypropylene (ECP), and contains
carbon fiber and carbon black, which heats when a voltage
differential is applied thereacross, resulting in current flow
therethrough, whereby an even and predictable heating of the
reaction chamber 34 occurs. The carbon fibers are milled carbon
fibers so that the fibers are of optimal length for the
manufacturing process of the vessel 24. Also, the outer casing 38
varies in thickness so that the heat applied to the contents is
even.
[0064] In preparation for use of the vessel 24, a sample of a
reagent is deposited into the vessel 24 through the upper opening
29, and settles onto the floor of the base 36. A lid 48, having a
tapered nose 50, is inserted into the opening 29 of the vessel 24,
and is tapered to conform to a tapered inner surface of the
intermediate section 30 of the inner casing 26. A base 52 of the
lid 48 eventually rests on a mating tapered transition surface 54,
at a juncture between the intermediate section 30 and the lower
section 32. Further, an outward rib 56 formed on an external
surface of the lid 48, near the top thereof, is snapped below an
inward ledge 58 formed at the top of the inner casing 26. With this
arrangement, the engagement of the rib 56 below the ledge 58 urges
the base 52 of the lid 48 firmly into engagement with the
transition surface 54 to lock the lid in place as shown in FIG. 5,
and to effectively seal the opening of the reaction chamber 34. The
base 52 of the lid 48 is formed with a sealed translucent or
transparent window 60, which allows optical interrogation of the
reaction of the heated reagent sample within the reaction chamber
34.
[0065] As illustrated in FIGS. 1 through 5, the module 22 is formed
with at least one receiving station 62 (hereinafter "the station")
to receive snugly the reaction vessel 24 in such a manner that good
thermal conductivity contact is created between the module and the
vessel. As shown in FIG. 2, the module 22 is also formed internally
with a channel 64, which extends between an entry port 66 and an
exit port 68 formed in the module. The channel 64 extends through
the module 22 in a labyrinth configuration, and in a serpentine
fashion, as described below. A coolant liquid is fed into the entry
port 66, flows through the channel 64 adjacent the station 62 and
any vessel 24 located in the station, and exits through the exit
port 68. As the coolant liquid flows through the channel 64, the
liquid passes adjacent the station 62 and the vessel 24 therein,
and cools and maintains the vessel at a desired temperature. The
coolant liquid may be water, and is preferably deionizsed water,
with an antioxidant added thereto, of the type referred to
commercially as FluidXP+, which is available from Integrity PC
Systems & Technologies, Inc. of Riverdale, Calif., USA.
[0066] In the preferred embodiment, the module 22 is formed as a
unitary structure, in the form of a single block 70 (FIG. 1). As
represented partially by dashed lines in FIGS. 1 and 4, the module
22 could be formed as a unitary structure, including a first mating
plate 70a, having a first interfacing surface 72, which is in
facing engagement with a second mating surface 74 of a second
mating plate 70b, without departing from the spirit and scope of
the invention.
[0067] Referring to FIG. 1, the block 70 of the module 22 is formed
with a first side surface 76, and a second side surface 78 spaced
from, and parallel with, the first side surface. The module 22 is
further formed with a third side surface 80, and a fourth side
surface 82 spaced from, and parallel with, the third side surface,
with the surfaces 80 and 82 being perpendicular with the surfaces
76 and 78 to form the block 70 in a rectangular configuration. The
block 70 is also formed with a top surface 84 and a bottom surface
86. A plurality of the receiving stations 62 are formed through the
block 70, from the top surface 84 to the bottom surface 86. As
shown in FIG. 1, typically, the plurality of receiving stations 62
are arranged in a twelve by eight matrix of ninety six receiving
stations, referred to as a standard microtiter array, with the
vessels 24 placed therein being referred to as microtiter vessels.
The ninety-six vessels 24, arranged in the twelve by eight array
are located at nine millimeter centers. The module 22 can be formed
with a single receiving station 62, or with any number of receiving
stations, including a number of stations based on integer multiples
of ninety six, without departing from the spirit and scope of the
invention.
[0068] Referring to FIG. 4, each receiving station 62 is formed
with a receptor passage 88, which extends through the module 22,
from the top surface 84 to the bottom surface 86. Each passage 88
includes a top contact recess 90 formed in the top surface 84 at an
entry port of the passage, an upper section 92, a lower section 94,
and a bottom recess 96. The upper section 92 is formed with a
larger tapering diameter than a tapering diameter of the lower
section 94 at an exit port of the passage. A transition surface 98
is formed at a juncture between the upper section 92 and the lower
section 94, with the upper section and the lower section being
tapered to conform to the tapers of the upper section 40 and lower
section 42, respectively, of the outer casing 38 of the vessel 24.
The receptor passage 88 of each receiving station 62 is formed with
a wall 89, or wall surface, which extends between the top contact
recess 90 and the bottom recess 96. The flow passages 100a and
100b, and thereby the channel 64, are formed by a three millimeters
bore size.
[0069] As shown in FIGS. 1, 2, 3 and 4, in the forming of the
channel 64, a plurality of parallel, spaced flow passages 100a are
formed, by drilling or other methods, through the module 22, in a
common plane, from the first side surface 76 to the second side
surface 78, with each of the flow passages having ports in the
first side surface and the second side surface. As shown in FIG. 2,
two parallel, spaced flow passages 100b are formed, by drilling or
other methods, through the module 22, in the common plane, from the
third side surface 80 to the fourth side surface 82, with the flow
passages 100a intersecting each of the flow passages 100b, in the
common plane, to normally provide communication amongst the flow
passages 100a and 100b. With respect to the flow passages 100b, the
third side surface 80 and the fourth side surface 82 may be
referred to as the first and second side surfaces, respectively, of
those flow passages. A stopper 102, in the form of a set or grub
screw, is inserted into, and secured within, each port of the flow
passages 100a and 100b, which essentially seals the flow passages
from communication with the exterior environment of the module 22,
except through the entry port 66 and the exit port 68.
[0070] It is noted that, if the unitary structure of the module 22
is in the form of the above-described first mating plate 70a and
the second mating plate 70b, portions of the flow passages 100a and
100b can be formed in the first interfacing surface 72 and the
remaining portions formed in the second interfacing surface 74.
when the two mating plates 70a and 70b are assembled together, the
respective portions of the flow passages 100a and 100b will mate to
form the complete flow passages.
[0071] Referring to FIGS. 2, 3 and 6, a plurality of selectively
placed holes 104 are formed, by drilling or other methods, into the
module 22, from the floor of the bottom recess 96, and into the
flow passages 100b. A flow stopper 106, in the form of a set or
grub screw, is secured within each of the holes 104, and extends
into the respective passages 100b to preclude the flow of the
coolant liquid through the respective blocked portions of the flow
passages 100b. With this arrangement, the flow passages 100b are
separated into alternating communicating portions 108, which
communicate with the flow passages 100a, and alternating
non-communicating portions 110, which are not in flow
communications with the flow passages 100a. Portions of the flow
passages 100a and 100b now provide a flow path in the labyrinth
configuration to form the channel 64, and to force the coolant
liquid to flow in the serpentine path.
[0072] Referring to FIG. 2, for purposes of describing the
serpentine path, the flow passages 100a will be referred to as
being arranged in a vertical orientation in the figure, and the
flow passages 100b will be referred to as being arranged in a
horizontal orientation in the figure. In actual use of the module
22, the common plane of the flow passages 100a and 100b is
typically in a horizontal orientation, but could be in other
orientations without departing from the spirit and scope of the
invention. Also, in the description below, it is to be understood
that the stoppers 102 preclude the outflow of the coolant liquid
from any of the ports of the flow passages 100a and 100b.
[0073] The coolant liquid flows into the entry port 66, and
horizontally into one of the communicating portions 108 of a lower
one of the flow passage 100b. As the coolant liquid approaches the
first intersection of the flow passages 100a and 100b, the liquid
encounters the flow stopper 106 located in one of the
non-communicating portions of the flow passage 100b, and is urged
vertically upward into the flow passage 100a. As the coolant liquid
reaches the vertically upper end of the flow passage 100a, the
liquid is urged, and flows horizontally, into an upper one of the
communicating portions of the flow passages 100b. As the liquid
approaches the next intersection of the flow passages 100a and
100b, the liquid encounters the flow stopper located in one of the
non-communicating portions of the flow passage 100b, and is urged
vertically downward into the flow passage 100a. This pattern of
vertically upward and vertically downward travel of the liquid is
continued, in the serpentine path until the liquid reaches the exit
port 68, and exits the module 22. With respect to the channel 64,
the coolant liquid flows vertically upward through a vertical leg
64a of the channel, and vertically downward through a second
vertical leg 64b. This flow pattern is continued until the liquid
flows vertically upward through the last vertical leg 64k of the
channel 64.
[0074] As further shown in FIG. 2, the coolant fluid exits the
module 22 through the exit port 68, and flows into a return conduit
112, and eventually into a reservoir 114. A pump 116, within the
reservoir pumps the coolant liquid from the reservoir 114 into an
input conduit 118, where the liquid passes through a heater 120 to
selectively preheat the liquid. The coolant liquid is then fed into
the entry port 66 of the module 22, and continues through the
serpentine path of the channel 64 as described above. With the
labyrinth configuration, the coolant fluid is directed adjacent at
least on side of each receiving station 62, and adjacent two sides
of most of the receiving stations.
[0075] As noted above, the module 22 is formed of an electrically
conductive material. The exposed surfaces of the module 22,
including the walls 89 of the receiving station 62 and the bottom
recesses 96, and excluding the top contact recesses 90, are coated
with an electrically non-conducting or insulative material, as
represented partially by a coating layer 122, shown in FIG. 1. The
insulating of the exposed surfaces of the module 22, except for the
top contact recesses 90, can be accomplished by anodizing such
surfaces. The top contact recesses remain uncoated to provide
electrical contact surfaces as described below.
[0076] Referring again to FIG. 5, an electrical system 124, for
heating the reaction vessel 24, and controlling the temperature
thereof during the reaction process, includes an electrical power
source 126, a heat controller 128, a switch 130, a PCB 132 and a
contact 134 mounted on the PCB. To provide an electrical path for
current flow to heat the reaction chamber 34, the electrical system
124 further includes the conductive outer casing 38 of the vessel
24, and the electrically conductive material of the module 22,
which includes the top contact recess 90. Also, one side of the
electrical power source 126 is connectable, through the switch 130,
to a contact formed on the electrically conductive module 22. The
other side of the electrical power source 126 is connected, through
the heat controller 128 to a conductive terminal on the PCB 132,
with the terminal being electrically connected to the contact 134
through a conductive path on the PCB.
[0077] The heat controller 128 is responsive to an output from a
heat sensor 136, which is positioned adjacent the reaction chamber
34 to constantly monitor the temperature in the chamber. If an
infrared sensor is used as a heat sensor, a heat guide 138 may be
employed to collect radiated from the surface of the vessel 24, and
guide the radiated heat to the infrared sensor. A toroid 140 may be
located about the base 46 of the vessel 24 to accommodate a
temperature sensing device, which could be a thermal contacting
type, for example a thermistor, or a remote sensor, for example a
thermocouple type.
[0078] With respect to the following description of the use of the
apparatus 20, the description will be with respect to a single
vessel 24 and a single receiving station 62 within the module 22,
it being understood that the same procedure will be followed with
respect to use of two or more of the vessels in two or more
respective receiving stations.
[0079] When the apparatus 20 is to be used for the reaction
process, the electrical system 124 is established as described
above. A sample of the reagent is deposited in the vessel 24, and
the reagent settles on the floor of the reaction chamber 34. The
vessel 24, with the deposited reagent, is then placed into the
receptor passage 88 of the receiving station 62 of the module 22.
It is noted that the reagent could be placed in the vessel 24 after
placement of the vessel in the receiving station 62, without
departing from the spirit and scope of the invention. As the vessel
24 is placed into the receptor passage 88, the contact ledge 41 of
the conductive outer casing 38 of the vessel is moved into firm
electrical contact with the uncovered top contact recess 90 of the
module 22. At the same time, the base 46 of the vessel 24 extends
into the insulated bottom recess 96 of the receiving station 62 in
the manner illustrated in FIG. 5. Relative movement is effected
between the module 22 and the PCB 132 to move the PCB-mounted
contact 134 into electrical contact engagement with the exposed
base 46 of the vessel 24, The lid 48 is then placed into the
funnel-shaped opening of the inner casing 26 of the vessel 24 to
seal the reaction chamber 34 in the manner described above, with
the lid window 60 in place for optical interrogation of the reagent
sample during the reaction process. It is noted that the lid window
60 is located well within an intermediate portion of the outer
casing 38 to heat the window. This arrangement reduces the
possibility of condensation forming on the window 60, and thereby
allows for accurate and reproducible optical monitoring of the
reactions occurring in the reaction chamber 34 of the vessel.
[0080] Typically, in biological or chemical reactions involving
thermo cycling, it is necessary to precisely control the
temperature range between lower and upper temperature levels, where
the lower temperature is higher than the ambient. Accordingly, the
apparatus 20 for effecting the reaction of the reagent within the
reaction chamber 34 utilizes the module 22 in accordance with
certain principles of the invention by providing the heater 120 for
preheating the coolant liquid to the desired temperature. This
arrangement has an added advantage of preventing condensation from
forming on the exterior of the module 22. In this context,
pre-heated coolant liquid is pumped through the channel 64, in
preparation for the initiation of a heating cycle to apply heat to
the reaction chamber 34.
[0081] Thereafter, the switch 130 is closed to complete the
electrical circuit, whereby current flows through the outer casing
38, between the contact ledge 41 and the base 46 thereof, and the
reaction chamber 34 is heated to initiate the reaction process.
During the reaction process, the heat sensor 136 feeds temperature
data to the heat controller 128, which responds to the data to
increase, decrease, or hold steady, the level of current flowing in
the outer casing 38 of the vessel 24, in accordance with preset
standards.
[0082] As illustrated in FIG. 7, an optical monitoring system 142,
hereinafter referred to as "the optical system," is provided as a
part of the apparatus 20, wherein a representation of a plurality
of receiving stations is shown, with each station receiving a
reaction vessel 144 in which a reaction may take place. The system
comprises at least one light source 146, a scanning apparatus 148
for directing the light to the reaction vessels 144 in the
receiving stations and for receiving radiation emitted by the
reaction vessels and directing the radiation via a diffraction
grating 150 to a multi-anode photomultiplier tube assembly 152
operating in a photon counting mode. A foraminous mirror 154
contains a small opening at forty-five degrees to the plane of the
mirror, permitting laser light to pass through it to the vessels
144. The majority of diverging emitted light from the vessels 144
is reflected to the diffraction grating 150, since at this point
the emitted light beam is of much greater diameter than the small
opening.
[0083] The multi-anode photomultiplier tube assembly 152 includes a
multi-anode photomultiplier tube (MAPMT) with a 32 pixel array over
which radiation from around 510 to 720 nm is dispersed. Radiation
emitted by the reaction vessel 24 contents is dispersed over the
pixels of the MAPMT by the diffraction grating 150 such that the
wavelength range of the radiation impinging on a photocathode of
the MAPMT correlates with the position of the photocathode in the
MAPMT.
[0084] The light source 146 is a diode pumped solid state laser
(DPSS Laser) which is smaller and lighter than conventional gas
lasers typically used in optical monitoring systems.
[0085] The scanning apparatus 148 includes one or more planar
rotatable mirrors, for clarity only one such mirror is illustrated.
These are motor driven and controlled by means which are omitted
from the drawings for clarity. The system of mirrors can be
configured to direct the light from the laser to any receiving
station. Radiation emitted is returned to the foraminous mirror 154
which reflects the majority of the emitted radiation through a lens
156 which focuses the radiation upon the diffraction grating 150. A
Fresnel lens 158 is interposed between the rotatable mirrors, e.g.
mirror 148, and the receiving stations to ensure verticality of the
light entering each reaction vessel 144.
[0086] Referring to FIG. 8, an optical arrangement 160, which is an
alternate embodiment of the optical system 142, includes a PCB 162,
located above a pair of spaced lids 164, positioned over respective
reaction vessels 166. An array of LEDs 168 are mounted on the PCB
162, and are selected to emit light at 470 nm and arranged for the
light thereof to be directed through a window 170, or translucent
portion, of each of the lids 164. An optical filter 172 is located
above a plurality of small openings 174 formed through the PCB 162,
whereby only emission spectra and not excitation spectra is allowed
to pass. A Fresnel lens 174 directs the light emerging from the
vessels onto a detector 176 in the form of a photomultiplier
tube.
[0087] In general, the above-identified embodiments are not to be
construed as limiting the breadth of the present invention.
Modifications, and other alternative constructions, will be
apparent which are within the spirit and scope of the invention as
defined in the appended claims.
* * * * *