CN106799268B - Compensation liquid separation operating method for pipettor - Google Patents

Compensation liquid separation operating method for pipettor Download PDF

Info

Publication number
CN106799268B
CN106799268B CN201710062089.8A CN201710062089A CN106799268B CN 106799268 B CN106799268 B CN 106799268B CN 201710062089 A CN201710062089 A CN 201710062089A CN 106799268 B CN106799268 B CN 106799268B
Authority
CN
China
Prior art keywords
liquid separation
volume
pipettor
drain
time
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201710062089.8A
Other languages
Chinese (zh)
Other versions
CN106799268A (en
Inventor
罗耿荣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shunde District Foshan City Sieve Grace Scientific Instrument Co Ltd
Original Assignee
Shunde District Foshan City Sieve Grace Scientific Instrument Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shunde District Foshan City Sieve Grace Scientific Instrument Co Ltd filed Critical Shunde District Foshan City Sieve Grace Scientific Instrument Co Ltd
Priority to CN201710062089.8A priority Critical patent/CN106799268B/en
Publication of CN106799268A publication Critical patent/CN106799268A/en
Application granted granted Critical
Publication of CN106799268B publication Critical patent/CN106799268B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L3/00Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
    • B01L3/02Burettes; Pipettes
    • B01L3/021Pipettes, i.e. with only one conduit for withdrawing and redistributing liquids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2300/00Additional constructional details
    • B01L2300/02Identification, exchange or storage of information
    • B01L2300/025Displaying results or values with integrated means

Abstract

The present invention relates to pipettor technical fields, the more particularly, to compensation liquid separation operating method of pipettor, comprising the following steps: A, obtains Δ V in advanceIt is first、ΔVIt is residual;B, imbibition operation is carried out: setting pipettor imbibition volume VIt inhales, VIt inhales=liquid separation total volume VA+ΔVIt is first+ΔVIt is residual, then make pipettor imbibition;C, the 1st liquid separation operation: setting the 1st drain volume V of pipettor is carried out1, the 1st drain volume=1st time liquid separation volume V1+ΔVIt is first, then make pipettor drain;D, the 2nd time~n-th liquid separation operation: setting pipettor secondary drain volume, the secondary drain volume=secondary liquid separation volume V is successively carried outi, then make pipettor drain;Wherein;E, residual liquid is emptied, the present invention is by increasing Δ VIt is first、ΔVIt is residualIt compensates and corrects, guarantees liquid separation for the first time and last time liquid separation is all accurately, to improve liquid separation precision, reduce the wasting of resources, reduce experimental cost.

Description

Compensation liquid separation operating method for pipettor
Technical field:
The present invention relates to pipettor technical field more particularly to a kind of compensation liquid separation operating methods for pipettor.
Background technique:
In medical treatment, drug, gene and protein research, biological study, drug development laboratories and other biotechnologys In application field, it is often necessary to manipulate laboratory in various laboratory procedures using liquid metering devices such as pipettors Fluid sample, if pipettor is that liquid is then distributed into one or more points in the liquid sucking pipette by certain volume With volume.Existing pipettor carry out liquid separation mode process in, start imbibition when and when drain for the first time, due to pipettor inner cavity Air pressure and external pressure there are pressure difference so that the volume of practical imbibition can the imbibition volume less than normal in setting, drain for the first time Actual volume also can the liquid separation volume less than normal for the first time in setting, in addition, pipettor inner cavity has liquid after last time liquid separation Residual, i.e., the actual volume of last time drain can the last time liquid separation volume less than normal in setting.Therefore existing pipettor point Liquid separation for the first time when liquid, last time liquid separation can all have an error, and people can will liquid separation liquid for the first time when using pipettor liquid separation Body, last time liquid separation body abandon, and cause the waste of resource, especially biology, many liquid reagents of pharmaceuticals industry are very precious , considerably increase the cost of experiment.
Summary of the invention:
One kind is provided the purpose of the present invention is to the shortcomings of the prior art can be improved liquid separation precision, reduces The wasting of resources, the compensation liquid separation operating method for pipettor for reducing experimental cost.
To achieve the goals above, the technical solution adopted by the present invention is that:
Compensation liquid separation operating method for pipettor, comprising the following steps:
A, compensation rate volume delta V when the 1st liquid separation is obtained ahead of timeIt is first, liquid remaining balance body after last time liquid separation Product Δ VIt is residual
B, imbibition operation is carried out: setting pipettor imbibition volume VIt inhales, VIt inhales=liquid separation total volume VA+ΔVIt is first+ΔVIt is residual, then make Pipettor imbibition;
C, the 1st liquid separation operation: setting the 1st drain volume of pipettor, the 1st drain volume=1st time liquid separation is carried out Volume V1+ΔVIt is first, then make pipettor drain;
D, the 2nd time~n-th liquid separation is successively carried out to operate: setting pipettor secondary drain volume, the secondary drain volume= The secondary liquid separation volume Vi, then make pipettor drain;Wherein, n is liquid separation total degree, and n is natural number greater than 1, i be no more than The natural number of n;
E, residual liquid is emptied.
Pass through the compensation of head drop of liquid when measurement and calculating the 1st liquid separation of acquisition in the step A by the way of experiment Measure volume delta VIt is first, liquid remaining balance volume delta V after last time liquid separationIt is residual
Preferably, the step A specifically:
A1, the operation of liquid separation each time, each drain volume of the pipettor=secondary liquid separation are successively carried out by uncompensated mode Volume;
A2, measurement obtain practical drain volume, the practical drain volume of last time liquid separation of the 1st liquid separation;
A3, the 1st liquid separation volume compares with the practical drain volume of the 1st liquid separation calculates difference, which is For Δ VIt is first;Last time liquid separation volume is compared with the practical drain volume of last time liquid separation and calculates difference, the difference As Δ VIt is residual
It can also be previously according to Δ V corresponding to different air pressures, temperature in the step AIt is first、ΔVIt is residualData are made in numerical value Table, liquid separation operation by tables of data obtain corresponding Δ V according to air pressure at that time, temperatureIt is first、ΔVIt is residualNumerical value.
After completing a pipetting, automatic Memory is when time operating process and parameter and returns to start-up operation state, when When pipetting does not change operating process and parameter setting next time, automatically by the operating process and ginseng of last pipetting Number is arranged to the operating process and parameter of pipetting next time.
The beneficial effects of the invention are that: the present invention is used for the compensation liquid separation operating method of pipettor, comprising the following steps: A, compensation rate volume delta V when the 1st liquid separation is obtained ahead of timeIt is first, liquid remaining balance volume delta V after last time liquid separationIt is residual;B, Carry out imbibition operation: setting pipettor imbibition volume VIt inhales, VIt inhales=liquid separation total volume VA+ΔVIt is first+ΔVIt is residual, then inhale pipettor Liquid;C, the 1st liquid separation operation: setting the 1st drain volume of pipettor, the 1st drain volume=1st time liquid separation volume V is carried out1 +ΔVIt is first, then make pipettor drain;D, the 2nd time~n-th liquid separation operation: setting pipettor secondary drain volume is successively carried out, The secondary drain volume=secondary liquid separation volume Vi, then make pipettor drain;Wherein;E, residual liquid is emptied, the present invention passes through Increase compensation rate volume delta VIt is first1st liquid separation volume is compensated and corrected, by increasing liquid remaining balance volume delta VIt is residualIt is right Last time liquid separation volume compensates and corrects, and guarantees liquid separation for the first time and last time liquid separation is all accurately, to improve liquid separation essence Degree reduces the wasting of resources, reduces experimental cost.
Specific embodiment:
Below with reference to embodiment, the present invention is further illustrated, the compensation liquid separation operation side for pipettor Method, the compensation liquid separation operating method for pipettor, comprising the following steps:
One, compensation rate volume delta V when the 1st liquid separation is obtained ahead of timeIt is first, liquid remaining balance body after last time liquid separation Product Δ VIt is residual
Two, imbibition operation is carried out: setting pipettor imbibition volume VIt inhales, VIt inhales=liquid separation total volume VA+ΔVIt is first+ΔVIt is residual, then Make pipettor imbibition;
Three, the 1st liquid separation operation: setting the 1st drain volume of pipettor, the 1st drain volume=1st time liquid separation is carried out Volume V1+ΔVIt is first, then make pipettor drain;
Four, the 2nd time~n-th liquid separation is successively carried out to operate: setting pipettor secondary drain volume, the secondary drain volume= The secondary liquid separation volume Vi, then make pipettor drain;Wherein, n is liquid separation total degree, and n is natural number greater than 1, i be no more than The natural number of n;Specifically:
Set the 2nd drain volume of pipettor, the 2nd drain volume=2nd time liquid separation volume V2, then arrange pipettor Liquid;
Set the 3rd drain volume of pipettor, the 3rd drain volume=3rd time liquid separation volume V3, then arrange pipettor Liquid;
…………
Set pipettor n-th drain volume, n-th drain volume=n-th liquid separation volume Vn, then arrange pipettor Liquid;
Five, residual liquid is emptied.
The compensation of head drop of liquid when can obtain the 1st liquid separation by measurement and calculating by the way of experiment in step 1 Measure volume delta VIt is first, liquid remaining balance volume delta V after last time liquid separationIt is residual, specifically:
1, the operation of liquid separation each time, each drain volume of the pipettor=secondary liquid separation body are successively carried out by uncompensated mode Product;
2, measurement obtains practical drain volume, the practical drain volume of last time liquid separation of the 1st liquid separation;
3, the 1st liquid separation volume is compared with the practical drain volume of the 1st liquid separation and calculates difference, which is ΔVIt is first;Last time liquid separation volume is compared with the practical drain volume of last time liquid separation and calculates difference, which is For Δ VIt is residual
It can also be previously according to Δ V corresponding to different air pressures, temperature in step 1It is first、ΔVIt is residualTables of data is made in numerical value, point Liquid operation by tables of data obtains corresponding Δ V according to air pressure at that time, temperatureIt is first、ΔVIt is residualNumerical value.
After completing a pipetting, automatic Memory is when time operating process and parameter and returns to start-up operation state, when When pipetting does not change operating process and parameter setting next time, automatically by the operating process and ginseng of last pipetting Number is arranged to the operating process and parameter of pipetting next time.
The present invention is by increasing compensation rate volume delta VIt is first1st liquid separation volume is compensated and corrected, by increasing liquid Remaining balance volume delta VIt is residualLast time liquid separation volume is compensated and corrected, guarantees liquid separation for the first time and last time liquid separation is all Accurately, liquid separation precision is improved, the wasting of resources is reduced, reduces experimental cost.
Certainly, the above is only presently preferred embodiments of the present invention, therefore all according to structure described in present patent application range It makes, the equivalent change or modification that feature and principle are done, is included in the scope of the patent application of the present invention.

Claims (3)

1. being used for the compensation liquid separation operating method of pipettor, which comprises the following steps:
A, in advance by the way of experiment by measuring and calculating compensation rate volume delta V when obtaining the 1st liquid separationIt is first, last Liquid remaining balance volume delta V after secondary liquid separationIt is residual;Specifically:
A1, the operation of liquid separation each time, each drain volume of the pipettor=secondary liquid separation volume are successively carried out by uncompensated mode;
A2, measurement obtain practical drain volume, the practical drain volume of last time liquid separation of the 1st liquid separation;
A3, the 1st liquid separation volume compares with the practical drain volume of the 1st liquid separation calculates difference, which is Δ VIt is first;Last time liquid separation volume is compared with the practical drain volume of last time liquid separation and calculates difference, which is ΔVIt is residual
B, imbibition operation is carried out: setting pipettor imbibition volume VIt inhales, VIt inhales=liquid separation total volume VA+ΔVIt is first+ΔVIt is residual, then make liquid relief Device imbibition;
C, the 1st liquid separation operation: setting the 1st drain volume of pipettor, the 1st drain volume=1st time liquid separation volume V is carried out1 +ΔVIt is first, then make pipettor drain;
D, the 2nd time~n-th liquid separation operation: setting pipettor secondary drain volume, secondary drain volume=this time is successively carried out Liquid separation volume Vi, then make pipettor drain;Wherein, n is liquid separation total degree, and n is the natural number greater than 1, and i is no more than n's Natural number;
E, residual liquid is emptied.
2. the compensation liquid separation operating method according to claim 1 for pipettor, it is characterised in that: the step A In previously according to Δ V corresponding to different air pressures, temperatureIt is first、ΔVIt is residualTables of data is made in numerical value, and liquid separation operation is according to gas at that time Pressure, temperature obtain corresponding Δ V by tables of dataIt is first、ΔVIt is residualNumerical value.
3. the compensation liquid separation operating method of pipettor is used for described in -2 any one according to claim 1, it is characterised in that: After completing a pipetting, automatic Memory is when time operating process and parameter and returns to start-up operation state, moves when next time Liquid operation without changing operating process and when parameter setting, automatically by the operating process of last pipetting and parameter setting at The operating process and parameter of pipetting next time.
CN201710062089.8A 2017-01-31 2017-01-31 Compensation liquid separation operating method for pipettor Active CN106799268B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710062089.8A CN106799268B (en) 2017-01-31 2017-01-31 Compensation liquid separation operating method for pipettor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710062089.8A CN106799268B (en) 2017-01-31 2017-01-31 Compensation liquid separation operating method for pipettor

Publications (2)

Publication Number Publication Date
CN106799268A CN106799268A (en) 2017-06-06
CN106799268B true CN106799268B (en) 2019-06-04

Family

ID=58987232

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710062089.8A Active CN106799268B (en) 2017-01-31 2017-01-31 Compensation liquid separation operating method for pipettor

Country Status (1)

Country Link
CN (1) CN106799268B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115770631B (en) * 2022-12-07 2023-08-15 深圳市恒永达科技股份有限公司 Environment-adaptive air type liquid transfer pump and control method thereof

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7770475B2 (en) * 2007-06-29 2010-08-10 Rainin Instrument, Llc Hybrid manual-electronic pipette
CN103008040B (en) * 2012-09-05 2015-08-05 罗耿荣 The electric pipettor of auto modification precision and precision correcting method thereof
CN103495442B (en) * 2013-10-16 2015-12-23 佛山市顺德区罗恩科学仪器有限公司 Electric pipettor and automatic gauge method, automatic liquid separation method
CN103480441B (en) * 2013-10-16 2015-08-05 佛山市顺德区罗恩科学仪器有限公司 Auxiliary aspirator
CN203620655U (en) * 2013-10-16 2014-06-04 佛山市顺德区罗恩科学仪器有限公司 Electric pipette

Also Published As

Publication number Publication date
CN106799268A (en) 2017-06-06

Similar Documents

Publication Publication Date Title
EP3600668B1 (en) Modular organ microphysiological system with microbiome
US10545155B2 (en) Mass-spectrometer systems and methods
EP2490810B1 (en) Test set for a photometric measuring device and photometric measuring method for a sample liquid
JP2019505214A (en) Modular organ microphysiological system with integrated pumping, leveling and sensing
US9804095B2 (en) Test set for a photometric measuring device, and photometric measuring method for a sample liquid
CN101329358A (en) Sample dispensing treatment apparatus
CN108373969A (en) A kind of digital pcr chip and preparation method thereof and application method
CN106799268B (en) Compensation liquid separation operating method for pipettor
KR20220052911A (en) Dispensing compounds in microfluidic devices
CN103495442B (en) Electric pipettor and automatic gauge method, automatic liquid separation method
CN108459171A (en) A kind of high-precision sample adding system
Fan et al. Fed-batch CHO cell culture for lab-scale antibody production
DE102005045393A1 (en) Apparatus and method for dosing solutions
US20120031176A1 (en) Sample storage in microfluidics devices
CN203620655U (en) Electric pipette
CN203436330U (en) Blood sampling and containing component and blood sampling device
WO2019183038A1 (en) Organ-on-chip platforms with reduced fluid volume
CN112345680B (en) Method for simultaneously detecting eight sterols in ganoderma lucidum
CN108676924A (en) The segmentation loading methods of small space small size sample-adding pipe
US9989503B2 (en) Apparatus for quantitatively analyzing gas components with automatic feed control function of gas
US10730046B2 (en) Fluid handling systems for application of fluid shear stress to a fluid sample
CN103954727A (en) Quality control and detection method of jinming tablet
Shovkova et al. Development and validation of GLC/FID-and GLC/MSprocedures of secnidazole determination by the methods of additions
DE102004023053A1 (en) Device for performing parallel reactions under sterile conditions, useful e.g. for culturing microorganisms, comprises two modules, one of sterilizable and the other of non-sterilizable components
CN103226142A (en) Method for detecting leucogen concentration in blood plasma

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant