Claims
- 1. A method of cell lysis comprising combining nucleated cells and a lysing agent to produce a liquid mixture and causing the mixture to flow in a steady stream inside a tube having an internal diameter of about 1 cm or less at a temperature of ≦60° C., wherein the flow rate of the stream is adjusted as a function of the diameter and of the length of the tube so as to obtain a substantially homogeneous cell lysate at the outlet of the said tube, and wherein at or after the meeting point of the nucleated cells and the lysing agent, a device employing a baffle or an obstacle in tubing is not employed.
- 2. The method according to claim 1, wherein the diameter of the tube is 2 to 8 mm.
- 3. The method according to claim 1, wherein the mixing of cells and of lysing agent is conducted by introducing into the tube a stream of a suspension of cells and a stream of a solution of lysing agent.
- 4. The method according to claim 1, wherein the lysing agent is an alkaline lysing agent.
- 5. The method according to claim 4, wherein the lysing agent is a sodium hydroxide/SDS mixture.
- 6. The method according to claim 4, wherein a alkaline lysing agent is added to the cell lysate at the end of the tube.
- 7. The method according to claim 6, wherein the alkaline lysing agent is sodium or potassium acetate.
- 8. The method according to claim 1, wherein the lysing agent is a hypotonic solution.
- 9. A method of extracting plasmid DNA from cells containing the DNA, the method comprising:(i) producing a cell lysate according to the method of claim 1; (ii) treating the cell lysate with a precipitating, a neutralizing, or a precipitating and neutralizing agent to obtain a preparation comprising (a) a supernatant containing the plasmid DNA and (b) a precipitated or flocculated phase containing the majority of the cellular components, including the genomic DNA.
- 10. The method of extraction according to claim 9, wherein:(i) establishing a stream of the cell suspension in a first tube; (ii) establishing a stream of the lysing agent in a second tube that flows into the first tube (or vice versa) at a first meeting point to form a third tube; (iii) establishing a stream of a precipitating agent in a fourth tube that flows into the third tube (or vice versa) at a second meeting point situated downstream of the first meeting point to form a fifth tube; (iv) establishing a stream of the cell/lysing agent mixture produced at the first meeting point in the third tube between the first and second meeting point with a flow rate adjusted as a function of the diameter and length of the third tube to allow the homogenization of the mixture and the production of a substantially homogeneous cell lysate at the second meeting point; (v) establishing a stream from the second meeting point in a fifth tube by mixing the cell/lysing agent mixture of the third tube with the precipitating agent of the fourth tube; and (vi) recovering a preparation comprising a supernatant containing the plasmid DNA and a precipitated or flocculated phase containing the majority of the cellular components, including the genomic DNA, from the fifth tube.
- 11. The method according to claim 10, wherein the length of the tube between the first and second meeting point is from about 10 cm to a few meters.
- 12. The method according to claim 9, wherein the precipitating, neutralizing, or precipitating and neutralizing agent is sodium or potassium acetate.
- 13. The method according to claim 9, further comprising separation of the supernatant from the precipitated or flocculated phase.
- 14. The method according to claim 1 or 9, wherein the cells are bacterial.
- 15. The method according to claim 1 or 9, wherein the cells are eukaryotic cells.
- 16. An apparatus for carrying out the method according to claim 1, the apparatus comprising:(i) a first tube for establishing a stream of cell suspension in fluid connection with a cell suspension source, (ii) a second tube for establishing a stream of lysing agent in fluid connection with a source of lysing agent, the first and second tubes ending at a first meeting point at which they open into each other, (iii) a third tube having an internal diameter of about 1 cm or less and a length between about 10 cm to about a few meters extending from and in fluid connection with the first meeting point, and (iv) one or more devices for establishing the streams in the said first, second and third tubes; wherein the length, the diameter, and the flow rate in the third tube provides a substantially homogeneous mixture resulting in a substantially homogeneous lysate.
- 17. The apparatus according to claim 16, further comprising:(i) a fourth tube in fluid connection with a neutralizing, precipitating, or neutralizing and precipitating agent source at one end and in fluid connection with the second meeting point such that the third tube and the fourth tube open into each other, the third tube having a length determined by the distance between the first meeting point and the said second meeting point; (ii) a fifth tube in fluid connection with the second meeting point and having a small diameter ending at a recovery and/or separation means; and (iii) a device for establishing the streams in the fourth and fifth tubes.
- 18. The apparatus according to claim 16, wherein the device is a pump.
- 19. The method according to claim 10 wherein the internal diameter of the third tube is 2 to 8 mm.
- 20. The method according to claim 10 wherein the internal diameter of the fifth tube is 2 mm to 1 cm.
- 21. The method according to claim 10 wherein the internal diameter of both the third and fifth tubes is 2 to 8 mm.
- 22. The apparatus according to claim 16 wherein the third tube has an internal diameter of 2 to 8 mm.
- 23. The apparatus according to claim 17 wherein the fifth tube has an internal diameter of 2 mm to 1 cm.
- 24. The method according to claim 9 wherein the diameter of the tube is 2 to 8 mm.
- 25. The method according to one of claim 1-8 wherein the flow rate of the stream is less than 1000 ml/min.
- 26. The method according to claim 9 wherein the flow rate of the stream is less than 1000 ml/min.
- 27. The method according to claim 10 wherein the flow rates of the streams are less than 1000 ml/min.
- 28. The method according to claim 11 wherein the flow rates of the streams are less than 1000 ml/min.
- 29. The method according to claims 14 or 15 wherein the flow rate of the stream is less than 1000 ml/min.
- 30. The apparatus according to one of claims 16-18 wherein the flow rates of the streams is less than 1000 ml/min.
- 31. The method of claim 1 wherein the temperature is room temperature.
- 32. The method of claim 1 wherein said combining of cells and lysing agent and said causing the mixture to flow in a steady stream inside a tube are done continuously.
CROSS-REFERENCES TO RELATED APPLICATIONS
This application claims right of priority to WO 99/37750 filed Jan. 20, 1999.
PCT Information
Filing Document |
Filing Date |
Country |
Kind |
PCT/FR99/00105 |
|
WO |
00 |
Publishing Document |
Publishing Date |
Country |
Kind |
WO99/37750 |
7/29/1999 |
WO |
A |
US Referenced Citations (2)
Number |
Name |
Date |
Kind |
4294824 |
Jones et al. |
Oct 1981 |
A |
20010034435 |
Nochumson et al. |
Oct 2001 |
A1 |
Foreign Referenced Citations (7)
Number |
Date |
Country |
WO 9011092 |
Oct 1990 |
WO |
WO 9602658 |
Feb 1996 |
WO |
WO 9602658 |
Feb 1996 |
WO |
WO 9636106 |
Nov 1996 |
WO |
WO 9723601 |
Jul 1997 |
WO |
WO-9723601 |
Jul 1997 |
WO |
WO 9937750 |
Jul 1999 |
WO |
Non-Patent Literature Citations (1)
Entry |
Birnboim, (1983) Methods in Enzymology, vol. 100, 243-255. |