JP6004486B2 - Nucleic acid amplification method using microfluidic device - Google Patents
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Description
本発明は、蛇行流路内の核酸を超高速に増幅するための方法に関する。より具体的には、本発明は、連続流マイクロ流体システムを用いて、温度及び残留時間を正確にコントロールするための送液条件と流路デザインを提供し、超高速なポリメラーゼ連鎖反応(PCR)を実行する方法に関する。 The present invention relates to a method for amplifying nucleic acid in a meandering flow path at an ultra-high speed. More specifically, the present invention provides a flow condition and a channel design for accurately controlling temperature and residual time using a continuous flow microfluidic system, and an ultrafast polymerase chain reaction (PCR). On how to perform.
半導体微細加工技術などを用いて作製されたマイクロ流路チップで、微量のDNAサンプルから目的とする遺伝子配列領域を高速・簡便に増幅させるポリメラーゼ連鎖反応(Polymerase chain Reaction, PCR)が注目されている。 Polymer chain reaction (PCR), which uses a microchannel chip fabricated using semiconductor microfabrication technology, to amplify the target gene sequence region from a small amount of DNA sample at high speed and easily, has attracted attention. .
従来技術として、例えば、蛇行マイクロ流路を備えた核酸増幅装置であって、熱変性温度帯(94℃程度)、アニーリング温度帯(60℃程度)、伸長温度帯(72℃程度)を有し、かつ、PCR試料液が気体に挟まれた試料プラグの形状でポンプにより蛇行流路内に送液される核酸増幅装置(特許文献1,2)や、PCR試料液の還流を最適化する事によって高速な遺伝子増幅を達成した方法(特許文献3)が公開されている。 As a conventional technique, for example, a nucleic acid amplification device having a meandering microchannel, which has a heat denaturation temperature zone (about 94 ° C.), an annealing temperature zone (about 60 ° C.), and an extension temperature zone (about 72 ° C.) In addition, a nucleic acid amplification device (Patent Documents 1 and 2) in which a PCR sample solution is fed into a meandering channel by a pump in the shape of a sample plug sandwiched between gases, and the reflux of the PCR sample solution is optimized. A method (Patent Document 3) that achieves high-speed gene amplification is disclosed.
特許文献1,2では、平板型マイクロ流体装置内を流れているPCR試料プラグ液の前後の気体との界面に生じる蒸気圧差を利用することで、高速な温度制御を達成しているが、
(i)入口からの気体吐出によって試料プラグ液を送液させる場合、連続蛇行状のマイクロ流路は高い内圧上昇が発生するため、蛇行状流路の入口付近、中央付近、出口付近は流速が著しく異なる。そのため、蒸気圧差による流体制御を効果的に作用させるには、煩雑な流体制御法が必要になること。
(ii)出口からの気体吸引によって試料プラグ液を送液させる場合、マイクロ流路内の高い蒸気圧は、出口からの吸引による減圧によって解放されるため、マイクロ流路内の蒸気圧差は薄れること。
(iii)蒸気圧差の効果は、装置に接しているヒーターブロックのPID制御のバラつきと、装置とヒーター接触面の熱伝導の不均一さによる影響を大きく受けること。
(iv)1サイクル分或はそれ以上隔てられた状態で、セグメントフロー方式により複数の試料プラグ液を送液する場合、蒸気圧差が発生しているマイクロ流路内を、其々の試料プラグ液の流体制御を実現しながら送液し続けることは、技術的に極めて困難であること、の問題があった。
In Patent Documents 1 and 2, high-speed temperature control is achieved by utilizing the vapor pressure difference generated at the interface with the gas before and after the PCR sample plug solution flowing in the flat microfluidic device.
(i) When the sample plug liquid is fed by gas discharge from the inlet, the continuous serpentine micro-channel causes a high internal pressure rise, so the flow velocity is near the inlet, near the center, and near the outlet of the serpentine channel. Remarkably different. Therefore, a complicated fluid control method is required to effectively perform fluid control based on the difference in vapor pressure.
(ii) When the sample plug liquid is sent by gas suction from the outlet, the high vapor pressure in the microchannel is released by pressure reduction due to suction from the outlet, so the vapor pressure difference in the microchannel is reduced. .
(iii) The effect of the vapor pressure difference is greatly affected by variations in PID control of the heater block in contact with the device and non-uniform heat conduction between the device and the heater contact surface.
(iv) When a plurality of sample plug liquids are sent by the segment flow method in a state separated by one cycle or more, each sample plug liquid is passed through the micro flow path where the vapor pressure difference is generated. However, it is technically difficult to continue liquid feeding while realizing the fluid control.
特許文献3では、試料液自身の還流を活用することで、正確な温度制御と迅速な昇降操作を可能にしているが、煩雑な制御系が必要であることと、他の生化学反応部との接続を考えた場合、構造上自由度が低く扱い難いという問題がある。 In Patent Document 3, by utilizing the reflux of the sample solution itself, accurate temperature control and quick raising / lowering operation are possible. However, a complicated control system is necessary, and other biochemical reaction units are used. However, there is a problem that the degree of freedom is structurally difficult to handle.
これまでの技術では、現場で処理可能な、迅速かつ簡便なPCRを行うことが不可能であり、超高速に増幅を行える方法が望まれていた。 With the conventional technology, it is impossible to perform rapid and simple PCR that can be processed in the field, and a method capable of performing ultra-high-speed amplification has been desired.
本発明は、流路内の核酸を超高速に増幅するための方法を提供することを目的とする。 An object of this invention is to provide the method for amplifying the nucleic acid in a flow path at ultra high speed.
そこで上記課題を解決するために、本発明者は、流体の粘性を活用できるように流路の構造を工夫して、PCRの伸長部で十分な反応時間が確保され、冷却部の反応液の通過を短時間で行い、簡便な制御で満足のいく核酸伸長反応が行えるようにした。 Therefore, in order to solve the above problems, the present inventor devised the structure of the flow path so that the viscosity of the fluid can be utilized, a sufficient reaction time is ensured in the PCR extension part, and the reaction liquid in the cooling part is Passing was performed in a short time so that a satisfactory nucleic acid elongation reaction could be performed with simple control.
本発明は、以下の核酸増幅方法及び核酸増幅装置を提供するものである。
項1. PCR反応を行うことができる蛇行流路、前記蛇行流路の片側のループ部に対応する熱変性温度帯と反対側のループ部に対応するアニーリング温度帯、アニーリング温度帯と熱変性温度帯との間の伸長温度帯、さらに前記熱変性温度帯、伸長温度帯及びアニーリング温度帯を形成できるヒーターを備えた核酸増幅装置であって、前記蛇行流路は伸長部、熱変性部、冷却部及びアニーリング部から構成され、流路断面積は、伸長部<冷却部<熱変性部≦アニーリング部であり、熱変性部は熱変性温度帯に配置され、伸長部と冷却部は伸長温度帯に配置され、アニーリング部はアニーリング温度帯に配置されている核酸増幅装置。
項2. 熱変性温度帯に配置された熱変性部の伸長部側の端部が、伸長部と同じ流路断面積を有する、項1に記載の核酸増幅装置。
項3. 蛇行流路の入口にPCR反応液の吐出用ポンプを接続し、蛇行流路の出口にPCR反応液の吸引用ポンプを接続してなる、請求項1又は2に記載の核酸増幅装置。
項4. ヒーターがステンレス製の平板状ヒーターであり、蛇行流路を有する平板状PCR用マイクロ流体基板を平板状ヒーターとマグネットにより挟持し、ヒーターと基板の安定な接触を磁力により確保する、項1〜3のいずれかに記載の核酸増幅装置。
項5. 項1〜4のいずれかに記載の核酸増幅装置の蛇行流路にPCR試料液を供給してPCR反応を行う核酸増幅方法において、PCR試料液は気体に挟まれた試料プラグの形状でポンプにより蛇行流路内に送液され、気体によりPCRの1サイクル分或いはそれ以上隔てられた状態で前記蛇行流路内に供給されることを特徴とする、核酸増幅方法。
項6. 複数の試料プラグは、伸長部、熱変性部、冷却部及びアニーリング部からなる群から選ばれる同じ流路に位置するように蛇行流路内に送液される、項5に記載の核酸増幅方法。
The present invention provides the following nucleic acid amplification method and nucleic acid amplification apparatus.
Item 1. A meandering channel capable of performing a PCR reaction, an annealing temperature zone corresponding to a loop portion on the opposite side to a loop portion on one side of the meandering channel, an annealing temperature zone and a heat denaturing temperature zone A nucleic acid amplification apparatus comprising a heater capable of forming an extension temperature zone, and further a heat denaturation temperature zone, an extension temperature zone, and an annealing temperature zone, wherein the meandering channel has an extension portion, a heat denaturation portion, a cooling portion, and an annealing The cross-sectional area of the flow path is extended portion <cooling portion <heat-denatured portion ≦ annealing portion, heat-denatured portion is placed in the heat-denatured temperature zone, and stretched portion and cooled portion are placed in the stretched temperature zone. The nucleic acid amplification device in which the annealing part is disposed in the annealing temperature zone.
Item 2. Item 2. The nucleic acid amplification device according to Item 1, wherein an end of the heat denaturing part disposed in the heat denaturing temperature zone on the side of the extending part has the same flow path cross-sectional area as that of the extending part.
Item 3. The nucleic acid amplification device according to claim 1 or 2, wherein a PCR reaction solution discharge pump is connected to the meandering channel inlet, and a PCR reaction solution suction pump is connected to the meandering channel outlet.
Item 4. Items 1 to 3, wherein the heater is a flat plate heater made of stainless steel, and a flat plate microfluidic substrate having meandering channels is sandwiched between the flat plate heater and a magnet, and a stable contact between the heater and the substrate is ensured by magnetic force. The nucleic acid amplification device according to any one of the above.
Item 5. Item 5. The nucleic acid amplification method for performing PCR reaction by supplying a PCR sample solution to the meandering flow path of the nucleic acid amplification device according to any one of Items 1 to 4, wherein the PCR sample solution is in the form of a sample plug sandwiched between gases by a pump. A method for amplifying a nucleic acid, wherein the method is fed into a meandering channel and supplied into the meandering channel in a state separated by one cycle of PCR or more by a gas.
Item 6. Item 6. The nucleic acid amplification method according to Item 5, wherein the plurality of sample plugs are fed into the meandering channel so as to be located in the same channel selected from the group consisting of an extension unit, a heat denaturing unit, a cooling unit, and an annealing unit. .
遺伝子検査のように、医療現場において微量に採取した生体試料から、高感度に遺伝子の有無を検査可能なシステムの実現が求められる。本発明では、遺伝子増幅技術であるPCRにおいて、空気に挟まれた試料プラグの形態(形状)を利用し、かつ、蛇行流路の断面積を伸長部<冷却部<熱変性部≦アニーリング部とすることで、これまでの平板型マイクロ流体装置を用いた連続流PCRにおいて課題であった高速と高効率の両立を、試料プラグの前後の空気との界面に生じた試料液自身の蒸気圧と流体の粘度を活用することで実現することができる。これにより、新たに特別な外部装置を必要とせず、マイクロ流体装置の長所を最大限に生かした連続流PCRシステムの微量化ならびに高速化に資する特徴を備える。 Realization of a system capable of testing the presence or absence of a gene with high sensitivity from a biological sample collected in a small amount at a medical site, such as genetic testing, is required. In the present invention, in PCR, which is a gene amplification technique, the form (shape) of a sample plug sandwiched between air is used, and the cross-sectional area of the meandering channel is defined as an extension portion <cooling portion <thermal denaturation portion ≦ annealing portion. Thus, the high-speed and high-efficiency compatibility that has been a problem in the continuous flow PCR using the flat plate-type microfluidic device up to now can be achieved with the vapor pressure of the sample liquid itself generated at the interface with the air before and after the sample plug. This can be realized by utilizing the viscosity of the fluid. As a result, there is a feature that contributes to the miniaturization and speeding up of the continuous flow PCR system that makes the best use of the advantages of the microfluidic device without requiring a special external device.
本発明は、複数の温度帯を蛇行しながら繰り返し通過する微小流路内において極めて高速にポリメラーゼ連鎖反応(PCR)により核酸を増幅するための方法及び装置に関する。より具体的には、本発明は、連続流PCRのための平板型マイクロ流体システムにおいて、蛇行流路を用いて、気体に挟まれ試料プラグとして流れるPCR試料液に対して、熱変性部、伸長部、冷却部、アニーリング部の各反応部における温度と滞留時間を正確に制御するための流路デザインと、送液条件を適切に設定し、流路内の核酸を超高速に増幅するための装置及び方法に関する。 The present invention relates to a method and apparatus for amplifying a nucleic acid by polymerase chain reaction (PCR) at a very high speed in a microchannel that repeatedly passes through a plurality of temperature zones while meandering. More specifically, the present invention relates to a plate-type microfluidic system for continuous flow PCR, using a meandering flow path, a heat denaturing portion and an extension for a PCR sample solution sandwiched between gases and flowing as a sample plug. The flow path design for accurately controlling the temperature and residence time in each reaction section of the cooling section, cooling section, and annealing section, and the liquid feed conditions are set appropriately to amplify the nucleic acid in the flow path at ultra-high speed The present invention relates to an apparatus and a method.
特に断りのない限り、本明細書で使用されるすべての技術および科学用語は、本発明が関係している技術分野の当業者に通常理解される意味と同じ意味を有する。次に実施の形態を挙げて本発明を具体的に説明するが、本発明はこれらの実施の形態のみに限定されるものではなく、本明細書で説明されているものと類似のまたは同等の多数の方法および材料についてどれも本発明を実施する際に使用することができる。好ましい材料および方法について以下に説明する。 Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention is related. Next, the present invention will be specifically described with reference to embodiments, but the present invention is not limited to these embodiments, and is similar or equivalent to that described in this specification. Any of a number of methods and materials can be used in practicing the present invention. Preferred materials and methods are described below.
本明細書において、複数の温度帯とは、熱変性温度帯、アニーリング温度帯、伸長温度帯の3つの温度帯が挙げられる。これらの3つの温度帯は加熱装置(ヒーター)或いは冷却装置などにより明確に区別されていてもよく、隣接する温度帯(熱変性温度帯と伸長温度帯、或いは、伸長温度帯とアニーリング温度帯)の境界は明確でなくてもよい。図面で示される具体的な実施形態では、熱変性温度帯は95℃、伸長温度帯は72℃、アニーリング温度帯は30℃に設定されているが、核酸増幅反応(PCR)が進行する限り多少温度を上下させることができる。伸長温度帯とアニーリング温度帯は、見かけ上一体的になった1つの温度帯に見える場合もあるが、本明細書ではこのような場合であっても、より温度の高い部分を伸長温度帯と表現し、より温度の低い部分をアニーリング温度帯と表現する。 In the present specification, examples of the plurality of temperature zones include three temperature zones: a heat denaturing temperature zone, an annealing temperature zone, and an extension temperature zone. These three temperature zones may be clearly distinguished by a heating device (heater) or a cooling device, etc., and adjacent temperature zones (thermal denaturation temperature zone and extension temperature zone, or extension temperature zone and annealing temperature zone). The boundary may not be clear. In the specific embodiment shown in the drawings, the heat denaturation temperature zone is set to 95 ° C., the extension temperature zone is set to 72 ° C., and the annealing temperature zone is set to 30 ° C. However, as long as the nucleic acid amplification reaction (PCR) proceeds, The temperature can be raised or lowered. Although the extension temperature zone and the annealing temperature zone may seem to be one temperature zone that is apparently integrated, in this specification, even in such a case, the higher temperature part is referred to as the extension temperature zone. The lower temperature part is expressed as an annealing temperature zone.
本発明の蛇行流路は、PCR用マイクロ流体基板に形成される。この基板は平板状であるのが好ましい。本発明の核酸増幅基板は、PCR用マイクロ流体基板とヒーター(好ましくは平板状ヒーター)を備え、好ましい実施形態では、PCR用マイクロ流体基板はヒーターとマグネットにより挟持され、熱変性温度帯と反対側のループ部に対応するアニーリング温度帯、熱変性温度帯伸長温度帯の温度を所定の温度に安定して保持する。 The meandering channel of the present invention is formed in a PCR microfluidic substrate. This substrate is preferably flat. The nucleic acid amplification substrate of the present invention comprises a PCR microfluidic substrate and a heater (preferably a flat plate heater). In a preferred embodiment, the PCR microfluidic substrate is sandwiched between a heater and a magnet and is opposite to the heat denaturation temperature zone. The temperature in the annealing temperature zone and the heat denaturing temperature zone extension temperature zone corresponding to the loop portion of the above is stably held at a predetermined temperature.
図3aに示される実施形態では、平板状ステンレス製ヒーター上の平板状PCR用マイクロ流体基板の上にマグネットを設けている。このマグネットにより基板とヒーターが密着し、均一な温度を実現できる。 In the embodiment shown in FIG. 3a, a magnet is provided on a planar PCR microfluidic substrate on a planar stainless steel heater. With this magnet, the substrate and the heater are in close contact, and a uniform temperature can be realized.
本発明を実施するための核酸増幅装置の模式図を図1に示す。この装置は、PCR試薬の入口、蛇行流路、PCR反応後の液(試料プラグ液)の出口を備える。PCRの1サイクルは、両側の1対のループ部分(高温の熱変性部と低温のアニーリング部)、ループ部分を結ぶ2つの直線部分(伸長部と冷却部)からなる1つのユニットにより行うことができる。 A schematic view of a nucleic acid amplification apparatus for carrying out the present invention is shown in FIG. This apparatus includes an inlet for a PCR reagent, a meandering channel, and an outlet for a solution (sample plug solution) after the PCR reaction. One cycle of PCR can be performed by one unit consisting of a pair of loop parts (high temperature heat denaturing part and low temperature annealing part) on both sides and two linear parts (extension part and cooling part) connecting the loop parts. it can.
図4に示すように、熱変性部は「熱変性温度帯(95℃のヒーターブロック)」に対応し、アニーリング部は、「アニーリング温度帯(30℃のヒーターブロック)」に対応し、ループ部分を結ぶ2つの直線部分(伸長部と冷却部)は、「伸長温度帯(72℃のヒーターブロック)」に対応する。本発明で使用する核酸増幅装置は、このユニットが多数連結された蛇行流路において核酸増幅反応を行う。1つのPCR試料液が蛇行流路を進んでいくと、蛇行流路のユニット数に応じて多数のサイクルのPCR反応が行われ、必要な数のPCR産物が形成されて蛇行流路の出口から放出される。 As shown in FIG. 4, the heat denaturing part corresponds to “thermal denaturing temperature zone (95 ° C. heater block)”, and the annealing part corresponds to “annealing temperature zone (30 ° C. heater block)”. The two straight line sections (extension part and cooling part) connecting the two lines correspond to the “extension temperature zone (72 ° C. heater block)”. The nucleic acid amplification apparatus used in the present invention performs a nucleic acid amplification reaction in a meandering channel in which a large number of these units are connected. When one PCR sample solution advances through the meandering channel, a number of cycles of PCR reaction are performed according to the number of units in the meandering channel, and a necessary number of PCR products are formed from the outlet of the meandering channel. Released.
本発明の蛇行流路の伸長部は流路断面積が最も小さく、空間に余裕があるので、伸長部のデザインを例えば図2bに示すように蛇行させることで、伸長部の体積を増加させることができる。伸長部の流路断面積は小さいので、粘性の力によって試料プラグ液は伸長部を遅く流動する。大量の試料プラグ液を熱変性部(95℃)に流動させると、長い時間(例えば1分間以上)熱変性部(95℃)に残留し、気泡が発生するおそれがあるが、熱変性部を流動する時間が気泡が発生しない程度の時間(通常30秒以下、好ましくは20秒以下、より好ましくは10秒以下)であれば、試料プラグ液の液量が増大しても核酸増幅反応を問題なく行うことができる。 Since the elongated portion of the meandering channel of the present invention has the smallest channel cross-sectional area and has enough space, the volume of the elongated portion can be increased by meandering the elongated portion design as shown in FIG. 2b, for example. Can do. Since the channel cross-sectional area of the extension portion is small, the sample plug liquid slowly flows through the extension portion due to the viscous force. If a large amount of sample plug solution is flowed to the heat-denaturing part (95 ° C), it may remain in the heat-denaturing part (95 ° C) for a long time (for example, 1 minute or more) and bubbles may be generated. If the flow time is such that no bubbles are generated (usually 30 seconds or less, preferably 20 seconds or less, more preferably 10 seconds or less), the nucleic acid amplification reaction may be a problem even if the amount of the sample plug solution increases. Can be done without.
なお、試料プラグ液の液量が増加すれば、核酸増幅に時間がかかり、アニーリング部における残留時間も長くなるため、アニーリング部の温度は30℃(図2)から55℃程度の温度に上昇させればよい。アニーリング部から伸長部に供給される試料プラグ液の温度は55〜60℃程度が望ましく、このような温度になるようにアニーリング部の温度を適宜設定できる。例えば、試料プラグ液の液量に応じてアニーリング部の温度を30℃〜60℃程度の温度範囲で設定すればよい。 If the volume of the sample plug solution increases, nucleic acid amplification takes longer and the remaining time in the annealing section also becomes longer. Therefore, the temperature of the annealing section is increased from 30 ° C (Fig. 2) to about 55 ° C. Just do it. The temperature of the sample plug solution supplied from the annealing part to the extension part is preferably about 55 to 60 ° C., and the temperature of the annealing part can be appropriately set so as to be such a temperature. For example, the temperature of the annealing part may be set in a temperature range of about 30 ° C. to 60 ° C. according to the amount of the sample plug solution.
本発明の核酸増幅装置の蛇行流路は伸長部、熱変性部、冷却部及びアニーリング部から構成され、流路断面積は、伸長部<冷却部<熱変性部≦アニーリング部となっている。特に流路断面積が伸長部<冷却部であることが重要である。このような構成とすることで、伸長部を移動する時間が長くなり、冷却部を移動する時間は短くなり、伸長部における核酸の伸長反応に十分な時間が確保し、冷却部における送液の時間短縮が行われる。プラグ状の試料液の量が少ないときには図2aに示されるように伸長部は直線状の流路でも十分であるが、プラグ状の試料液の量が多くなった場合、伸長部の流路は図2bに示されるように蛇行させてもよい。本発明ではプラグ状の試料液は各部(熱変性部、伸長部、冷却部、アニーリング部)に単独で存在し得ることが重要であり、最も流路断面積の小さい伸長部の流路内体積は各プラグ状の試料液の体積よりも大きくする必要がある。伸長部は最も流路断面積が小さく流路内の体積が小さいので、図2bに示されるように流路を蛇行させて流路内の体積を増加させることができる。 The meandering flow path of the nucleic acid amplification device of the present invention is composed of an extending part, a heat denaturing part, a cooling part, and an annealing part, and the cross-sectional area of the flow path is extending part <cooling part <thermal denaturing part ≦ annealing part. In particular, it is important that the cross-sectional area of the flow path is the extension portion <the cooling portion. By adopting such a configuration, the time for moving the extension part is lengthened, the time for moving the cooling part is shortened, a sufficient time is secured for the nucleic acid extension reaction in the extension part, and the liquid feeding in the cooling part is performed. Time is reduced. When the amount of the plug-like sample liquid is small, a linear flow path is sufficient as shown in FIG. 2a. However, when the amount of the plug-like sample liquid is large, the flow path of the elongated part is It may be meandered as shown in FIG. 2b. In the present invention, it is important that the plug-like sample solution can exist independently in each part (thermal denaturation part, extension part, cooling part, annealing part), and the volume in the extension part of the extension part having the smallest channel cross-sectional area. Needs to be larger than the volume of each plug-like sample solution. Since the elongated portion has the smallest channel cross-sectional area and the volume in the channel, the volume in the channel can be increased by meandering the channel as shown in FIG. 2b.
図4aに示されるように、95℃のヒーターブロック内の熱変性部の伸長部側端部は流路断面積を伸長部と同様に細くしている。これは、この95℃の細い流路部分を試料液がゆっくり通過することで熱変性を行うのに十分な時間を確保するためである。伸長部と冷却部の流路断面積が熱変性部、アニーリング部の流路断面積よりも小さいことは、図1a,bの断面図にも示されている。 As shown in FIG. 4a, the end of the heat denaturing part in the heater block at 95 ° C. has a channel cross-sectional area that is narrower than that of the extending part. This is because the sample solution slowly passes through the thin channel portion at 95 ° C. to ensure a sufficient time for heat denaturation. It is also shown in the cross-sectional views of FIGS. 1A and 1B that the cross-sectional areas of the extension part and the cooling part are smaller than the cross-sectional areas of the heat-denaturing part and the annealing part.
図5に本発明の装置における送液原理の概略を示す。アニーリング部ではPCR試料プラグ液はポンプの陽圧により流動されて移動し(i)、流路断面積が大きいアニーリング部から流路断面積の小さい伸長部への送液は毛管力により素早く移動する(ii)。伸長部では流路断面積が小さいのでプラグ液は粘性によりゆっくり移動し、十分な伸長時間が確保されるようになっている(iii)。伸長部と熱変性部の境界を熱変性温度域に設定すると、この領域での送液が非常にゆっくり行われるために熱変性に必要な時間がこの部分で十分に確保される(iv)。プラグ液が流路断面積の大きな熱変性部に送液されると、その前のゆっくりした移動時に高められたポンプの陽圧によりプラグ液は素早く移動する(v)。熱変性部から冷却部への移動及び冷却部内の移動は高い陽圧と毛管力により素早く行われる(vi)、(vii)。アニーリング部は流路断面積が大きくなっているので、試料プラグ液は冷却部よりもゆっくり移動し、アニーリングに必要な時間が確保される。図6a、図9aに示すように、本発明の核酸増幅装置の蛇行流路は、流路断面積を、伸長部<冷却部<熱変性部≦アニーリング部とすることで、試料プラグ液の移動時間は伸長部>アニーリング部>熱変性部>冷却部となり、核酸増幅反応を行うのに理想的な反応時間の配分となるため、高速化を実現しつつ核酸増幅反応を確実に行うことができる。 FIG. 5 shows an outline of the liquid feeding principle in the apparatus of the present invention. In the annealing section, the PCR sample plug solution is moved and moved by the positive pressure of the pump (i), and the liquid feeding from the annealing section having a large channel cross-sectional area to the extension section having a small channel cross-sectional area moves quickly by capillary force. (ii). Since the cross-sectional area of the flow path is small in the extension part, the plug liquid moves slowly due to the viscosity, and a sufficient extension time is secured (iii). When the boundary between the extension portion and the heat denaturation portion is set in the heat denaturation temperature region, the liquid feeding in this region is performed very slowly, so that the time necessary for the heat denaturation is sufficiently secured in this portion (iv). When the plug liquid is sent to the heat-denaturing part having a large flow path cross-sectional area, the plug liquid quickly moves due to the positive pressure of the pump that is raised during the slow movement before the plug liquid (v). The movement from the heat denaturing part to the cooling part and the movement in the cooling part are quickly performed by a high positive pressure and capillary force (vi), (vii). Since the annealing section has a larger channel cross-sectional area, the sample plug liquid moves more slowly than the cooling section, and the time required for annealing is secured. As shown in FIGS. 6a and 9a, the meandering channel of the nucleic acid amplification device of the present invention has a cross-sectional area of the extension part <cooling part <thermal denaturing part ≦ annealing part so that the sample plug liquid moves. The time is extended part> annealing part> thermal denaturing part> cooling part, and the reaction time distribution is ideal for performing nucleic acid amplification reaction, so that nucleic acid amplification reaction can be performed reliably while realizing high speed. .
本発明で使用するポンプは通常のポンプが使用でき、特に限定されないが、例えば小型のダイヤフラム式ポンプ(mp6 piezoelectric diaphragm micropump)を好ましく使用できる。このダイヤフラム式ポンプは、気体・液体の吐出・吸引の両方が可能なポンプであり、蛇行流路の入口での吐出と出口での吸引の両方に使用できる。 The pump used in the present invention can be a normal pump, and is not particularly limited. For example, a small diaphragm pump (mp6 piezoelectric diaphragm micropump) can be preferably used. This diaphragm pump is a pump capable of both discharging and sucking gas and liquid, and can be used for both discharging at the inlet of the meandering channel and suction at the outlet.
図6は室温における試料プラグ液の残留時間分布であり、図9aはサーマルサイクル時の残留時間分布である。流路の形状を活用しなかったとき、すなわち流路断面積が伸長部=冷却部=熱変性部=アニーリング部の場合、室温(図6a)では残留時間は全て同一であるが、サーマルサイクル時には残留時間は大きく変化する(図9a)。流路形状を活用したとき、プラグ液の蒸気圧の寄与がない室温条件で伸長部と熱変性部の残留時間は長くなり、冷却部、アニーリング部の残留時間は短くなる。この残留時間パターンの変化は、核酸増幅反応を確実に行いながら高速化を実現するために理想的である。図9aに示されるように、サーマルサイクル時には本発明の流路形状を活用しなくても室温(図6a)と比較して伸長部とアニーリング部の残留時間は大きく延長され、熱変性部の残留時間はやや減少し、冷却部の残留時間は大きく低下する。これは蛇行流路内の蒸気圧による効果である。これに流路形状の効果を重ね合わせることで、伸長部、熱変性部、冷却部、アニーリング部における試料プラグ液の残留時間をさらに理想的なものにすることができる。 FIG. 6 shows the residual time distribution of the sample plug liquid at room temperature, and FIG. 9A shows the residual time distribution during the thermal cycle. When the shape of the channel is not utilized, that is, when the channel cross-sectional area is the extension portion = cooling portion = thermal denaturing portion = annealing portion, the remaining time is all the same at room temperature (FIG. 6a). The remaining time varies greatly (FIG. 9a). When the flow path shape is utilized, the remaining time of the extension part and the heat-denaturing part becomes longer and the remaining time of the cooling part and the annealing part becomes shorter under room temperature conditions where the vapor pressure of the plug liquid does not contribute. This change in the residual time pattern is ideal for achieving high speed while reliably performing the nucleic acid amplification reaction. As shown in FIG. 9a, the remaining time of the extension part and the annealing part is greatly extended compared to room temperature (FIG. 6a) without using the flow path shape of the present invention during the thermal cycle, and the residual heat denaturation part. The time is slightly reduced and the remaining time of the cooling part is greatly reduced. This is an effect due to the vapor pressure in the meandering flow path. By superimposing the effect of the channel shape on this, the remaining time of the sample plug liquid in the extension part, the heat denaturing part, the cooling part, and the annealing part can be made more ideal.
図20に示すように、本発明の核酸増幅装置を用いたPCRでは、増幅された核酸が得られているが、流路断面積を一定にした図19bの装置を用いた場合増幅された核酸は得られなかった。これは、各サイクルにおける残留時間が一定である本発明の効果である。
なお、PCRの試料液としては、PCRの標準的なキットを利用することができる。核酸の増幅反応(PCR)は、リアルタイムPCR法、RT-PCR法などを利用することができる。
As shown in FIG. 20, in the PCR using the nucleic acid amplification device of the present invention, an amplified nucleic acid is obtained, but the amplified nucleic acid is obtained when the device of FIG. Was not obtained. This is an effect of the present invention in which the remaining time in each cycle is constant.
As a PCR sample solution, a standard PCR kit can be used. For the amplification reaction (PCR) of nucleic acid, a real-time PCR method, an RT-PCR method or the like can be used.
次に、40サイクルの蛇行流路を有する本発明の核酸増幅装置、及び流路断面積が一定の比較対象の核酸増幅装置を用い、室温で試料プラグ液を送液したときの各サイクルにおける残留時間分布を図7に示す。図7aと図7bに示されるように、本発明の核酸増幅装置は、入口から出口にかけて1サイクルの合計の残留時間と冷却部、アニーリング部、伸長部、熱変性部の各々の残留時間はほとんど変わらないが、流路断面積が一定の装置(図7b)では、サイクル数が20前後のときに残留時間が最も長くなり、出口(40サイクル)に近づくと残留時間は急速に短くなっている。この残留時間の変化は、サーマルサイクル下での送液の場合にも同様に生じ(図10)、本発明の装置はサーマルサイクル下の方が残留時間の変動がさらに小さくなり(図7a、図10aの比較)。流路断面積が一定の比較例の装置ではサーマルサイクル下の方が残留時間の変動がさらに大きくなっている(図7b、図10bの比較)。このように本発明の装置及び方法は、多数のPCRサイクルを行った場合、確実に核酸の増幅を行うことができるが、流路断面積が一定であると特に出口付近で必要な残留時間が確保されなくなり増幅不良になるだけでなく、蛇行流路の中央付近では必要以上に長い残留時間になり、高速化の妨げになる。 Next, using the nucleic acid amplification device of the present invention having a 40-cycle meandering channel and the comparison target nucleic acid amplification device having a constant channel cross-sectional area, the remaining in each cycle when the sample plug solution is fed at room temperature The time distribution is shown in FIG. As shown in FIGS. 7a and 7b, the nucleic acid amplification apparatus of the present invention has almost one cycle of remaining time from the inlet to the outlet and the remaining time of each of the cooling part, annealing part, extension part and heat denaturing part. Although it does not change, in a device with a constant channel cross-sectional area (FIG. 7b), the remaining time becomes the longest when the number of cycles is around 20, and the remaining time rapidly decreases when approaching the outlet (40 cycles). . This change in the remaining time similarly occurs in the case of liquid feeding under the thermal cycle (FIG. 10), and in the apparatus of the present invention, the variation in the remaining time becomes smaller under the thermal cycle (FIG. 7a, FIG. 10a comparison). In the device of the comparative example in which the flow path cross-sectional area is constant, the fluctuation of the remaining time is further larger under the thermal cycle (comparison of FIGS. 7b and 10b). As described above, the apparatus and method of the present invention can reliably amplify a nucleic acid when a large number of PCR cycles are performed. However, if the flow path cross-sectional area is constant, the required remaining time particularly near the outlet is obtained. Not only is it not ensured, but the amplification becomes poor, and the remaining time is longer than necessary near the center of the meandering flow path, which hinders speeding up.
伸長部と冷却部の流路断面積が残留時間に及ぼす影響を図11、図16に示す。伸長部と冷却部の流路断面積が同一(0.25mm2)であってもサーマルサイクル下では冷却部の残留時間は十分短くなっているが、反応の高速化の観点では伸長部と冷却部の流路断面積が同一では不十分であり、冷却部の断面積を伸長部よりも大きくして冷却部の残留時間を伸長部よりも十分短くすることが反応の高速化に重要である。 The influence of the channel cross-sectional area of the extension part and the cooling part on the remaining time is shown in FIGS. Even if the flow path cross-sectional area of the extension part and the cooling part is the same (0.25 mm 2 ), the remaining time of the cooling part is sufficiently short under the thermal cycle, but the extension part and the cooling part are from the viewpoint of speeding up the reaction. It is not sufficient if the flow path cross-sectional areas are the same, and it is important for speeding up the reaction that the cross-sectional area of the cooling part is made larger than that of the extension part and the remaining time of the cooling part is sufficiently shorter than that of the extension part.
図12には、室温・吸引下での残留時間を示す。図6(室温吐出下)と比較すると、吸引及び吐出により残留時間は同様に変化すること、図6の吐出下の方が残留時間の変化の程度がやや大きいことを示す。 FIG. 12 shows the remaining time at room temperature and under suction. Compared with FIG. 6 (under room temperature discharge), the remaining time changes in the same manner due to suction and discharge, and the degree of change in the remaining time is slightly larger under discharge in FIG.
さらに、図14、15には、サーマルサイクル・吸引下での残留時間の変化を示す。図14から、本発明の流路形状を活用すると冷却部の残留時間が大幅に短縮されることがわかる。まら、図15と図10を比較すると、サーマルサイクル吸引下(図15)の方がサーマルサイクル吐出下(図10)よりもサイクル数による残留時間の変化率は小さいことがわかる。 Further, FIGS. 14 and 15 show changes in the remaining time under thermal cycling and suction. From FIG. 14, it can be seen that the remaining time of the cooling section is greatly shortened when the flow channel shape of the present invention is utilized. Furthermore, comparing FIG. 15 and FIG. 10, it can be seen that the rate of change in the remaining time depending on the number of cycles is smaller when the thermal cycle is sucked (FIG. 15) than when the thermal cycle is discharged (FIG. 10).
図17、18は、流路の形状を流体制御に活用したPCR用マイクロ流体装置と流路の形状を流体制御に活用しないPCR用マイクロ流体装置を用いて、PCR試料プラグ液の液量を変化させて入口からの吐出によりPCRを行った結果、リアルタイムPCRキットのDNA断片の増幅に伴って得られた蛍光強度の比較を示す。伸長部の流路体積は、2〜3μLである。1μLまたは2μLの試料プラグ液の場合、十分な蛍光強度が得られるが、試料プラグ液の量が3μL以上になると伸長部での残留時間が短くなることで蛍光強度が徐々に減少する。したがって、試料プラグ液の液量によって、図2a、図2bに示されるような流路形状の装置を使い分けることができる。 17 and 18 show changes in the amount of PCR sample plug solution using a PCR microfluidic device that utilizes the shape of the flow channel for fluid control and a PCR microfluidic device that does not utilize the shape of the flow channel for fluid control. As a result of performing PCR by discharging from the inlet, a comparison of the fluorescence intensities obtained with the amplification of the DNA fragment of the real-time PCR kit is shown. The channel volume of the extension is 2 to 3 μL. In the case of a 1 μL or 2 μL sample plug solution, a sufficient fluorescence intensity can be obtained. However, when the amount of the sample plug solution is 3 μL or more, the remaining time in the extension portion is shortened, so that the fluorescence intensity gradually decreases. Therefore, a device having a channel shape as shown in FIGS. 2a and 2b can be used depending on the amount of the sample plug solution.
図17は入口にシリンジでPCR用試料プラグ液を入れて、入口からポンプで吐出したとき。図18は入口にシリンジでPCR用試料プラグ液を入れて、出口からポンプで吸引したときの結果を示す。入口からのポンプでの吐出と出口からのポンプでの吸引のいずれでも核酸増幅産物が得られることが確認された。 FIG. 17 shows the case where the PCR sample plug solution is put into the inlet with a syringe and discharged from the inlet with a pump. FIG. 18 shows the results when the sample plug solution for PCR is put into the inlet with a syringe and sucked with a pump from the outlet. It was confirmed that a nucleic acid amplification product can be obtained by either discharging from the pump from the inlet or suction from the pump from the outlet.
図19は、セグメントフローにより流動させた試料プラグ液の残留時間分布を比較したものであり、本発明の流路構造(図19a)が比較対象の流路構造(図19b)よりも残留時間の変動の少なさにおいて優れていることと、セグメントフローによる複数の試料プラグ液は、同じ間隔(位相)で送液することが重要であることを示す。図20は、図19aによる試料液1,2では核酸増幅産物である蛍光物質が十分な量で得られるが、図19bによる試料液3,4では核酸増幅産物である蛍光物質が十分な量で得られないことを示す。この結果は、蛇行流路の構造(特に流路断面積)と試料プラグ液間の間隔の制御が非常に重要であることを示す。 FIG. 19 compares the residual time distribution of the sample plug fluid flowed by the segment flow. The flow path structure of the present invention (FIG. 19a) has a longer remaining time than the flow path structure of the comparison target (FIG. 19b). It shows that it is excellent in the small fluctuation, and that it is important to send a plurality of sample plug liquids by the segment flow at the same interval (phase). FIG. 20 shows that a sufficient amount of the fluorescent substance as a nucleic acid amplification product is obtained in the sample liquids 1 and 2 according to FIG. 19a, whereas a sufficient amount of the fluorescent substance as a nucleic acid amplification product is obtained in the sample liquids 3 and 4 according to FIG. Indicates that it cannot be obtained. This result shows that control of the structure of the meandering channel (particularly the channel cross-sectional area) and the distance between the sample plug liquids is very important.
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| JP6195211B2 (en) * | 2013-08-08 | 2017-09-13 | パナソニックIpマネジメント株式会社 | Microfluidic device |
| CN108291184B (en) * | 2015-12-01 | 2022-07-01 | 日本板硝子株式会社 | PCR reaction vessel, PCR device, and PCR method |
| JP6584373B2 (en) * | 2016-08-01 | 2019-10-02 | 日本板硝子株式会社 | Reaction processing apparatus and reaction processing method |
| CN109844091B (en) | 2016-11-01 | 2022-12-30 | 日本板硝子株式会社 | Reaction processing container and reaction processing device |
| CN111601876B (en) | 2018-01-15 | 2024-04-05 | 光技光电集团日本分公司 | Reaction treatment device |
| JP7132158B2 (en) * | 2019-03-08 | 2022-09-06 | 株式会社日立ハイテク | Temperature controller and nucleic acid amplifier |
| JP6652673B1 (en) * | 2019-06-07 | 2020-02-26 | 日本板硝子株式会社 | Reaction processing vessel |
| JP6652677B2 (en) * | 2019-09-03 | 2020-02-26 | 日本板硝子株式会社 | Reaction treatment apparatus and reaction treatment method |
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| US8263392B2 (en) * | 2006-11-14 | 2012-09-11 | University Of Utah Research Foundation | Methods and compositions related to continuous flow thermal gradient PCR |
| JP5224801B2 (en) * | 2007-12-21 | 2013-07-03 | キヤノン株式会社 | Nucleic acid amplification equipment |
| JP5717235B2 (en) * | 2010-03-26 | 2015-05-13 | 独立行政法人産業技術総合研究所 | Nucleic acid amplification method |
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