This disclosure relates to a beta2-microglobulin concentration analyzing method and system.
Examination reports of patients with chronical renal disease often show excessive amount of uremic toxins accumulated in their body, and the concentration of beta2-microglobulin is regarded as one of the indicators for tracking concentration of middle-molecule uremic toxins in patients with chronical renal disease. Generally, labs use enzyme-linked immunosorbent assay (ELISA) to analyze the concentration of beta2-microglobulin in the specimen. However, the operation of ELISA requires intensive laboratory labor and long analysis time, and can't be used to determine the amount of uremic toxins is dialyzed out of the patient's body.
According to one or more embodiment of this disclosure, a beta2-microglobulin concentration analyzing method, performed by a processing device, includes: inputting a plurality of samples corresponding to a plurality of sampling time points into a differential mobility analyzing device for analysis to obtain a plurality of beta2-microglobulin concentrations, wherein the plurality of samples are prepared from spent dialysate; multiplying the plurality of sampling time points with a dialysate flowrate respectively to obtain a plurality of spent dialysate volumes; performing fitting on the plurality of beta2-microglobulin concentrations to obtain a concentration-spent dialysate volume fitting curve; and performing integration on the concentration-spent dialysate volume fitting curve to generate a total dialyzed weight.
According to one or more embodiment of this disclosure, a beta2-microglobulin concentration analyzing method, adapted to a differential mobility analyzing device and a processing device, wherein the differential mobility analyzing device includes an electrospray atomizer, a differential mobility analyzer and a condensation particle counter, and the method includes: inputting a plurality of samples corresponding to a plurality of sampling time points into the electrospray atomizer to obtain a plurality of aerosol samples, wherein the plurality of samples are prepared from spent dialysate; inputting the plurality of aerosol samples into the differential mobility analyzer to obtain a plurality of screened particle samples; inputting the plurality of screened particle samples into the condensation particle counter to obtain a plurality of particle counts; dividing, by the processing device, the plurality of particle counts by a volume of the dialysate entered per unit time respectively to obtain a plurality of beta2-microglobulin concentrations; multiplying, by the processing device, the plurality of sampling time points with a dialysate flowrate respectively to obtain a plurality of spent dialysate volumes; performing, by the processing device, fitting on the plurality of beta2-microglobulin concentrations to obtain a concentration-spent dialysate volume fitting curve; and performing, by the processing device, integration on the concentration-spent dialysate volume fitting curve to generate a total dialyzed weight.
According to one or more embodiment of this disclosure, a beta2-microglobulin concentration analyzing system includes: an electrospray atomizer, a differential mobility analyzer, a condensation particle counter and a processing device. The electrospray atomizer is configured to receive a plurality of samples corresponding to a plurality of sampling time points and output a plurality of aerosol samples, wherein the plurality of samples are prepared from spent dialysate. The differential mobility analyzer is configured to receive the plurality of aerosol samples and output a plurality of screened particle samples. The condensation particle counter configured to receive the plurality of screened particle samples and output a plurality of particle counts. The processing device is connected to the condensation particle counter and is configured to perform: dividing the plurality of particle counts by a volume of the dialysate entered per unit time respectively to obtain a plurality of beta2-microglobulin concentrations; multiplying the plurality of sampling time points with a dialysate flowrate respectively to obtain a plurality of spent dialysate volumes; performing fitting on the plurality of beta2-microglobulin concentrations to obtain a concentration-spent dialysate volume fitting curve; and performing integration on the concentration-spent dialysate volume fitting curve to generate a total dialyzed weight.
The present disclosure will become more fully understood from the detailed description given hereinbelow and the accompanying drawings which are given by way of illustration only and thus are not limitative of the present disclosure and wherein:
In the following detailed description, for purposes of explanation, numerous specific details are set forth in order to provide a thorough understanding of the disclosed embodiments. According to the description, claims and the drawings disclosed in the specification, one skilled in the art may easily understand the concepts and features of the present invention. The following embodiments further illustrate various aspects of the present invention, but are not meant to limit the scope of the present invention.
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The beta2-microglobulin concentration analyzing systems shown in
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The preparation device 11 may include, for example, a centrifuge machine for filtering out impurity in the spent dialysate in step S1 to obtain the sample. In step S3, the laboratory personnel places the sample into the differential mobility analyzing device 12 for analysis to obtain the beta2-microglobulin concentration. Accordingly, the beta2-microglobulin concentration of the spent dialysate may be obtained with lower costs.
To explain the method of the preparation device 11 preparing the sample in more detail, please refer to
In step S11, the laboratory personnel loads the spent dialysate into the centrifuge tube, and places the centrifuge tube into the preparation device 11 (for example, the centrifuge machine). In step S13, the laboratory personnel operates the preparation device 11 to centrifuge the centrifuge tube loaded with the spent dialysate to remove impurity from the spent dialysate, thereby obtaining the sample for analyzing the beta2-microglobulin concentration.
To further explain method of the preparation device 11 preparing the sample, and method of purifying the spent dialysate loaded in the centrifuge tube, please refer to
The predetermined rotational speed is, for example, fourteen thousand rotations per minute (14 krpm), and the predetermined duration is, for example, 15 minutes. In step S1301, the laboratory personnel may operate the preparation device 11 to perform centrifugation on the centrifuge tube CENT loaded with the dialysate DYLS at the predetermined rotational speed, wherein the centrifuge tube CENT may include a filtration membrane MEMB, and molecular weight cut off (MWCO) of the filtration membrane MEMB may be 3 kD.
After centrifugation, the centrifuged sample in the centrifuge tube CENT′ may have layers, including an impurity layer L1 and a filtered layer L2 above the filtration membrane MEMB. The impurity layer L1 is the part that needs to be removed, and the filtered layer L2 is the part that needs to be kept. In step S1303, the laboratory personnel may use pipette to remove the impurity layer L1 from the centrifuged sample.
Then, in step S1305, the laboratory personnel adds deionized water into the centrifuged sample where impurity is already removed, to perform resuspension on the centrifuged sample with added deionized water to obtain the resuspension sample. The volume of the deionized water added into the centrifuge tube may be 500 μL. In step S1307, the central controller 13 may count a purification count. That is, the central controller 13 may add 1 to the purification count to record a number of times of performing resuspension, wherein an initial value of the purification count may be 0.
In step S1309, the laboratory personnel may determine whether the purification count reaches the predetermined count, wherein the predetermined count is, for example, 5. If the purification count reaches the predetermined count, the laboratory personnel performs step S1311, to add the ammonium acetate solution into the centrifuged sample containing deionized water, wherein a concentration of the ammonium acetate solution may be 20 mM. If the purification count does not reach the predetermined count, the laboratory personnel adds the deionized water into the centrifuge tube again to perform resuspension to obtain another resuspension sample, and performs the purification procedure on the another resuspension sample. Said “reach” herein refers to a situation of being equal to or larger than.
In short, step S1301 to step S1305 may be performed repeatedly for multiple times, wherein said multiple times equals to the predetermined count. When a number of times of performing step S1301 to step S1305 reaches the predetermined count, the laboratory personnel adds the ammonium acetate solution into the resuspension sample, to obtain the sample used for analyzing the beta2-microglobulin concentration, and the impurity concentration of the sample at this stage is less than 50 ppm.
It should be noted that the present disclosure does not limit the order of performing step S1305, S1307 and S1309, as long as step S1307 is performed prior to step S1309. In addition, numerical values of the predetermined rotational speed, the predetermined duration, volume of the deionized water, the purification count, the predetermined count and concentration of the ammonium acetate solution described in the embodiment of
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As shown in
The sample outlet of the electrospray atomizer 121 may be connected to the sample inlet of the differential mobility analyzer 122, and the sample outlet of the differential mobility analyzer 122 may be connected to the sample inlet of the condensation particle counter 123. Alternatively, the laboratory personnel or the robotic arm may transfer the sample produced by the electrospray atomizer 121 to the differential mobility analyzer 122 for analysis, and then transfer the sample produced by the differential mobility analyzer 122 to the condensation particle counter 123 for counting particle number.
As shown in
In step S31, the electrospray atomizer 121 may receive the prepared sample from the preparation device 11, and apply a positive voltage to the sample for the electrosprayed liquid sample to produce positively charged aerosol sample A1, wherein an aerosol flowrate driven by the electrospray atomizer 121 may be 1.5 liters per minute (1.5 L/min), but the present disclosure does not limit the actual numerical value of the aerosol flowrate. In step S33, the laboratory personnel transfers the aerosol sample A1 from the electrospray atomizer 121 to the differential mobility analyzer 122, thereby selecting the screened particle sample A2 from the positively charged the aerosol sample A1. The screened particle sample A2 has a specified protein molecular weight and a specified protein size, and the specified protein molecular weight is, for example, 11.8 kD, and a range of the specified protein size is, for example, 3.85 nm to 4.14 nm. A sheath flowrate of the differential mobility analyzer 122 may be 20 liters per minute (20 L/min). The present disclosure does not limit the actual numerical values of the specified protein molecular weight, the specified protein size and the sheath flowrate.
In step S35, the laboratory personnel transfers the screened particle sample A2 from the differential mobility analyzer 122 to the condensation particle counter 123. The condensation particle counter 123 may be equipped with a laser optical detector, to calculate a number of particles with the specified protein molecular weight and the specified protein size through laser light. The laser wavelength of the condensation particle counter 123 may be 405 nm. The size of beta2-microglobulin (3.85 nm) is far smaller than a size range that is detectable by laser light. Therefore, general laser optical detector might not be suitable for beta2-microglobulin analysis of the present disclosure. The beta2-microglobulin screened by the differential mobility analyzer 122 should be condensed and grown on the particle surface to enlarge the size of beta2-microglobulin from 3.85 nm to micron level (>1 μm) before it can be used in the measurement and metering performed by the laser optical detector, which illustrates the necessity of using the condensation particle counter 123. In step S37, the laboratory personnel may divide the particle count of the screened particle sample A2 by the volume the spent dialysate loaded per unit time to obtain the beta2-microglobulin concentration. Step S37 may also be performed by the central controller 13.
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It should be noted that the beta2-microglobulin concentration analyzing method according to one or more embodiments of the present disclosure are explained using the beta2-microglobulin concentration analyzing system 1a shown in
In other words, in the embodiment of
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In step S41, take the dialysis process of one subject as an example, the samples are obtained from the spent dialysate of different sampling time points during the dialysis process of the subject. In other words, one sample is at least a portion of the spent dialysate, one sample corresponds to one sampling time point, and the differential mobility analyzing device 12 performs analysis on the sample to generate one beta2-microglobulin concentration. The differential mobility analyzing device 12 may be the differential mobility analyzing device 12 shown in
In step S43, the processing device 15 multiplies each one of the sampling time points with the dialysate flowrate of the hemodialysis machine to obtain the spent dialysate volume of each one of the sampling time points. In other words, the spent dialysate volume refers to a volume of the dialysate already used at the corresponding sampling time point.
In step S45, the processing device 15 performs fitting on the beta2-microglobulin concentrations corresponding to the sampling time points respectively to obtain the concentration-spent dialysate volume fitting curve. Unit of the horizontal axis of the concentration-spent dialysate volume fitting curve generated in step S45 is, for example, the spent dialysate volume, and unit of the vertical axis of the concentration-spent dialysate volume fitting curve is, for example, a particle count per unit volume. The purpose of the fitting is to find a parameter with a smallest difference from the data point representing the beta2-microglobulin concentration. Said fitting may be a logistic fitting, a Boltzmann fitting or an exponential-decay fitting etc., wherein details of the fitting are described below in reference to
In step S47, the processing device 15 performs integration on the concentration-spent dialysate volume fitting curve to calculate area under curve (AUC) of the concentration-spent dialysate volume fitting curve, and uses the AUC as the total dialyzed weight. The total dialyzed weight indicates the weight of the total amount of dialyzed beta2-microglobulin. Through the above embodiment, the cost and time required to calculate the total amount of dialyzed beta2-microglobulin of the dialysis process may be reduced, and medical personnel may check the amount of dialyzed uremic toxins of the patient.
Please refer to
wherein y is the beta2-microglobulin concentration corresponding to one sampling time point, and the unit of “y” is the number of particles per unit volume; x is the spent dialysate volume corresponding to the sampling time point; A1 is a final permeable concentration; A2 is an initial permeable concentration; x0 is a spent dialysate volume for a default permeability; and p is a factor of the dialysate flowrate. The processing device 15 may perform logistic fitting using data analysis software of Origin.
A1 is the final permeable concentration of the permeable membrane in the hemodialysis machine, and A2 is the initial permeable concentration of the permeable membrane in the hemodialysis machine. Further, the initial permeable concentration indicates the beta2-microglobulin concentration that is permeable by the permeable membrane when the dialysis process has not yet begun or when the dialysis process has just begun. The initial permeable concentration may be considered as the filtration capacity in the initial stage of dialysis. The final permeable concentration indicates the beta2-microglobulin concentration that is permeable by the permeable membrane when the dialysis process ends or is about to end. The final permeable concentration may be considered as the filtration capacity in the final stage of dialysis. It should be noted that said “the dialysis process is about to end” may be set as a situation where the volume of spent dialysate has reached (equals to or exceeds) a preset volume and/or the dialysis time has reached (equals to or exceeds) preset time (for example, a preset time point, a present duration) etc., the present disclosure is not limited thereto.
x0 indicates a volume of the spent dialysate at the default permeability of the permeable membrane. For example, assuming that the default permeability is 50%, then x0 represents the volume of the spent dialysate when the permeability of the permeable membrane decreases to 50%. p is the factor of the dialysate flowrate and may be a coefficient generated by the data analysis software (Origin) as described above, and p may be considered as a decay rate of the beta2-microglobulin concentrations.
Please refer to
wherein y is the beta2-microglobulin concentrations; x is the spent dialysate volume; A1 is the final permeable concentration; A2 is the initial permeable concentration; and x0 is the spent dialysate volume for the default permeability. Definition of the parameters in equation (2) are the same as that of equation (1), their details are not repeated herein.
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y=A
2
+A
1
×e
(−x/x
) equation (3)
wherein y is the beta2-microglobulin concentrations; x is the spent dialysate volume; A1 is the final permeable concentration; A2 is the initial permeable concentration; and x0 is the spent dialysate volume for the default permeability. Definition of the parameters in equation (3) are the same as that of equation (1), their details are not repeated herein.
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As shown in
In step S411, the processing device 15 takes the samples corresponding to the sampling time points in turn as the target sample to perform step S413 and step S415 on the target sample.
In step S413, the processing device 15 may notify the laboratory personnel to transfer the target sample to the differential mobility analyzing device 12 or control the robotic arm 14 to transfer the target sample to the differential mobility analyzing device 12 as described above. The beta2-microglobulin concentration generated accordingly may be used as the first concentration. As shown in
In step S415, the processing device 15 calculates the second concentration according to the conversion equation and the first concentration and uses the second concentration as the beta2-microglobulin concentration of the target sample. The conversion equation may be equation (4) shown below,
C2=m×C1+DF equation (4)
wherein C2 is the second concentration; C1 is the first concentration; m is a slope of a linear relationship between the first concentration and the second concentration; DF is an intercept of the linear relationship between the first concentration and the second concentration. Equation (4) is a concentration relationship using two analysis methods to measure the beta2-microglobulin concentrations of multiple samples. The first concentration is a measured value using the differential mobility analyzing device; the second concentration is a measured value using ELISA; the parameter m is, for example, 2×10−10; and the parameter DF is, for example, 0.0071. The parameters m and DF may be adjusted according to requirements, the present disclosure is not limited thereto.
Then, the processing device 15 performs step S43 of
As shown in
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Steps S51, S53, S55 and S57 shown in
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wherein β2M is the total dialyzed weight of beta2-microglobulin; β2Mpre-Hemo is the beta2-microglobulin concentration in the blood of the subject before hemodialysis; β2Mpost-Remo is the beta2-microglobulin concentration in the blood of the subject after hemodialysis; BVpre-Hemo is a volume of blood of the subject before hemodialysis; BVpost-Hemo is a volume of blood of the subject after hemodialysis; and UF is a ultrafiltration volume.
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In view of the above description, the beta2-microglobulin concentration analyzing method and system according to one or more embodiments of the present disclosure may lower the cost of analyzing the beta2-microglobulin concentration in the blood and lower time spent on sample preparation, processing and analysis, medical personnel may check the amount of dialyzed uremic toxins of the patient, and an accurate result may be obtained. In addition, the beta2-microglobulin concentration analyzing method and system according to one or more embodiments of the present disclosure may allow the particle count of screened beta2-microglobulin to be obtained by using the condensation particle counter.
Number | Date | Country | Kind |
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111132190 | Aug 2022 | TW | national |
112112459 | Mar 2023 | TW | national |
This non-provisional application claims priority under 35 U.S.C. § 119(a) on Patent Application No(s). 63/329,043 filed in the U.S. on Apr. 8, 2022, Patent Application No(s). 111132190 filed in Republic of China (ROC) on Aug. 26, 2022, patent application Ser. No. 18/096,447 filed in the U.S. on Jan. 12, 2023, and Patent Application No(s). 112112459 filed in Republic of China (ROC) on Mar. 31, 2023 the entire contents of which are hereby incorporated by reference.
Number | Date | Country | |
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63329043 | Apr 2022 | US | |
63329043 | Apr 2022 | US |
Number | Date | Country | |
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Parent | 18096447 | Jan 2023 | US |
Child | 18132341 | US |