Method and Microfluidic Device for Studying Cell Deformations
US-2024210301-A1 · Jun 27, 2024 · US
US9592483B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9592483-B2 |
| Application number | US-201313922635-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 20, 2013 |
| Priority date | Jun 7, 2012 |
| Publication date | Mar 14, 2017 |
| Grant date | Mar 14, 2017 |
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Disclosed is a system that can mix deionized water and concentrated sheath fluid to provide sheath fluid in a flow cytometer system having a desired concentration. Flow rates are low, which substantially match the flow rate of sheath fluid through the nozzle, so that turbulence and air bubbles are not formed in the sheath fluid. The available deionized water is then used for back flushing and removal of sample cells and deposited salts from the sheath fluid.
Opening claim text (preview).
What is claimed is: 1. A system for mixing deionized water and sheath fluid concentrate comprising: a first container to contain deionized water; a second container to contain concentrated sheath fluid having a first concentration, wherein the first container and the second container are configured to simultaneously contain different fluids; a pressurized reservoir; a valve that has a first input, a second input, and an output, wherein: the first input is fluidically coupled to the first container, the second input is fluidically coupled to the second container, the valve is configured to allow deionized water in the first container to flow through the output to the pressurized reservoir when in a first position, and the valve is configured to allow concentrated sheath fluid in the second container to flow through the output to the pressurized reservoir when in a second position; a pump that is fluidically interposed between the valve and the pressurized reservoir and configured to flow deionized water in the first container and concentrated sheath fluid in the second container into the pressurized reservoir at a flowrate that is sufficiently slow that substantially no bubbles form in the pressurized reservoir; and a controller that is configured to maintain a concentration of a mixture of the deionized water and the concentrated sheath fluid in the pressurized reservoir such that the mixture has a concentration of sheath fluid less than the first concentration by repeatedly switching the valve between the first position, thereby supplying a first amount of deionized water by the pump to the pressurized reservoir, and the second position, thereby supplying a second amount of concentrated sheath fluid by the pump to the pressurized reservoir. 2. The system of claim 1 wherein the controller comprises a rate integrator that is configured to: sample a pump control signal, create a sampled pump control signal, and sum the sampled pump control signal to determine when the first amount of deionized water has been delivered to the pressurized container and to determine when the second amount of concentrated sheath fluid has been delivered to the pressurized container. 3. The system of claim 1 wherein: the pressurized reservoir is configured to flow the mixture out of the pressurized reservoir at an outflow rate, and the pump is configured to cause deionized water in the first container and concentrated sheath fluid in the second container to flow to the pressurized reservoir at a flowrate that is substantially equal to the outflow rate. 4. The system of claim 3 further comprising: a rinse pump fluidically connected to the first container; a second valve fluidically connected to the rinse pump; and a nozzle of a flow cytometer that is fluidically connected to the second valve, wherein: the rinse pump is fluidically interposed between the second valve and the first container, the second valve is fluidically interposed between the nozzle and the rinse pump, the rinse pump is configured to cause deionized water in the first container to flow through the second valve to the nozzle. 5. The system of claim 1 , wherein the concentration of sheath fluid in the pressurized reservoir is nominally seven parts deionized water to one part concentrated sheath fluid. 6. The system of claim 1 , wherein the first container contains deionized water and the second container contains concentrated sheath fluid. 7. The system of claim 1 , wherein the flowrate of the pump is about 8 milliliters per minute. 8. The system of claim 1 , wherein the first amount is about 7 milliliters of deionized water and the second amount is about 1 milliliter of concentrated sheath fluid. 9. The system of claim 2 , wherein the controller is further configured to, based on the determination, generate a valve control signal to cause the valve to switch between the first position and the second position. 10. The system of claim 3 , further comprising a level sensor communicatively connected to the controller and configured to generate a level sensor signal that is representative of a level of the mixture in the pressurized reservoir, wherein the controller is further configured to, based on the level sensor signal from the level sensor, change the flowrate of the pump. 11. The system of claim 10 , wherein the controller is further configured to cause, based on a determination that the level of the mixture in the pressurized reservoir is below a first level, the flowrate of the pump to increase. 12. The system of claim 10 , wherein the controller is further configured to cause, based on a determination that the level of the mixture in the pressurized reservoir is above a second level, the flowrate of the pump to decrease. 13. The system of claim 4 , further comprising one or more of: an injector needle, a sample tube, and a sample uptake tube, wherein: each of the injector needle, the sample tube, and the sample update tube are fluidically connected to the second valve, and the rinse pump is configured to cause deionized water in the first container to flow through the second valve to the one or more of: the injector needle, the sample tube, and the sample uptake tube. 14. The system of claim 4 , further comprising a waste collector fluidically connected to the nozzle, wherein: the nozzle is fluidically interposed between the second valve and the waste collector, and the rinse pump is further configured to cause deionized water in the first container to flow through the second valve, through the nozzle, and to the waste collector.
for cytology · CPC title
Handling flow, e.g. hydrodynamic focusing · CPC title
Physics · mapped topic
by measuring the values related to the quantity of the individual components (G05D11/139 takes precedence) · CPC title
Operations & Transport · mapped topic
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