CN214622475U - Preprocessing device based on ion chromatography survey soluble salt composition - Google Patents

Preprocessing device based on ion chromatography survey soluble salt composition Download PDF

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CN214622475U
CN214622475U CN202120875770.6U CN202120875770U CN214622475U CN 214622475 U CN214622475 U CN 214622475U CN 202120875770 U CN202120875770 U CN 202120875770U CN 214622475 U CN214622475 U CN 214622475U
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sample
exchange column
ion
ion exchange
soluble salt
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高智悦
姜波
李辛庚
樊志彬
张振岳
王晓明
郭凯
田双
闫风洁
李文静
米春旭
宗立君
吴亚平
王蝶
赵洺哲
朱耿增
王倩
姚硕
王维娜
刘鑫
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State Grid Corp of China SGCC
Electric Power Research Institute of State Grid Shandong Electric Power Co Ltd
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State Grid Corp of China SGCC
Electric Power Research Institute of State Grid Shandong Electric Power Co Ltd
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Abstract

The utility model relates to an instrument analysis technical field, in particular to preprocessing device based on ion chromatography survey soluble salt composition, including sample adder, ion exchange column, filtrating collector, module connecting device and mount. Through implementing the utility model discloses, can obtain the clear transparent sample that can directly be used for ion chromatographic analysis, under the prerequisite of not introducing interference ion, can effectively get rid of colloid and organic matter in the liquid sample, and the solution acidity that awaits measuring is unchangeable basically around handling, and ion concentration is lossless, and resin regeneration and sample pretreatment go on in same device, are fit for the preliminary treatment of big batch sample.

Description

Preprocessing device based on ion chromatography survey soluble salt composition
Technical Field
The utility model relates to an instrument analysis technical field, in particular to ion chromatography's preprocessing device.
Background
The information disclosed in this background section is only for enhancement of understanding of the general background of the invention and is not necessarily to be taken as an acknowledgement or any form of suggestion that this information constitutes prior art that is already known to a person skilled in the art.
Ion chromatography is one of high performance liquid chromatography, and is widely used for component analysis of liquid samples due to its high accuracy, good selectivity, high sensitivity and rapid analysis. However, ion chromatography is highly required for the sample to be measured, and the sample is required not to contain components which may block the sampling tube, such as solids, colloids, and macromolecular organic substances. The actually obtained samples of the atmospheric sediment, the soil or the wastewater, particularly the atmospheric sediment collected near chemical plants and power plants and the dirty samples on the surfaces of the external insulation parts of transmission and transformation lines have complex sample compositions because the samples adsorb liquid and gas discharged by the plants and are mutually adhered with settled solid substances, and the obtained filtrate is difficult to directly analyze the components of the samples by using the ion chromatography even after the filtrate is dissolved and filtered.
The existing ion chromatography sample pretreatment technology comprises a membrane treatment method, a solid phase extraction treatment method, a decomposition treatment method and the like. Among them, the ion exchange resin method is widely used because of low cost. The problems faced by the prior art are:
(1) when anions are analyzed, the pH value of a sample treated by the cation exchange resin is reduced, and the peak emergence time of sample components is changed, so that the sample components cannot be identified. In order to avoid interference caused by pH change of a sample, an alkaline substance needs to be added into the sample for acid-base neutralization, and impurities are easily introduced; (2) when analyzing the cations in the sample, the pH of the sample increases after passing through the anion exchange resin, resulting in metal ions such as Fe in the sample3+、Al3+、Zn2+、Mg2+A hydroxide precipitate formed, making the sample cloudy and unable to be analyzed directly using an ion chromatography instrument. (3) Because the exchange capacity of the pretreatment column is limited and the regeneration is troublesome, the batch treatment of the samples to be detected is difficult. Therefore, it is necessary to research a batch pretreatment technology for detecting a sample containing interfering components such as colloids and organic matters by ion chromatography, improve a soluble salt component determination method, and provide an accurate detection means for further researching the characteristics of the sample.
Disclosure of Invention
In order to solve the problem, the utility model provides a preprocessing device based on ion chromatography survey soluble salt composition, through the utility model discloses the sample that the processing obtained is clarified transparently, under the prerequisite of not introducing interference ion, can effectively get rid of colloid and organic matter in the liquid sample, and treats around the processing that the liquid pH of awaiting measuring is unchangeable basically, and the ion concentration that awaits measuring is lossless, is particularly suitable for the preliminary treatment of big batch sample, and the filtrating of obtaining can directly be used for ion chromatography analysis.
In order to achieve the above object, the utility model relates to a following technical scheme:
the utility model discloses a first aspect provides a preprocessing device based on ion chromatography survey soluble salt composition, include: the device comprises a plurality of sample adding devices, a plurality of ion exchange columns, a filtrate collector and a module connecting device; the sample adder is connected with the ion exchange columns to form a group, a plurality of groups of sample adder bodies are arranged in parallel relative to the module connecting device, the module connecting device is provided with a plurality of liquid inlets and a liquid outlet, the liquid inlets are respectively connected with the ion exchange columns, and a filtrate collector is arranged below the liquid outlet.
In a second aspect of the present invention, the resin column regeneration and the sample treatment are performed in the same apparatus. Regenerating the resin according to the steps S1-S6; sample processing was performed in accordance with steps S7-S13.
The third aspect of the present invention provides a pretreatment method for measuring soluble salt components based on ion chromatography, comprising:
s1, adding deionized water into the sample adder, opening the rotary piston of the sample adder and the rotary piston of the ion exchange column in sequence, and washing the resin in the ion exchange column by using a large amount of deionized water;
s2, closing the ion exchange column rotary piston and the sample adder rotary piston in sequence;
s3, adding an HCl solution into the sample adder connected with the cation exchange column, and adding an NaOH solution into the sample adder connected with the anion exchange column;
s4, opening the sample adder rotary piston and the ion exchange column rotary piston slowly in sequence, enabling the solution in the sample adder to flow through the ion exchange column, and closing the ion exchange column rotary piston and the sample adder rotary piston in sequence;
s5, taking down the sample adder, washing the sample adder to be neutral by using deionized water, and filling the sample adder with the deionized water;
and S6, connecting the sample adder and the ion exchange column, slowly opening the rotary piston of the sample adder and the rotary piston of the ion exchange column in sequence, and repeatedly flushing the ion exchange column by using deionized water until the effluent liquid is neutral.
S7, filtering the solid solution or waste liquid to obtain a sample C to be detected;
s8, connecting the end m of the connecting pipe with the end n of the connecting pipe through a three-way pipe;
s9, adding the sample C to be detected into a sample adder connected with the cation exchange column and a sample adder connected with the anion exchange column respectively;
s10, opening the sample adder rotary piston and the ion exchange column rotary piston in sequence, making the sample flow through the ion exchange column and the connecting pipe, and entering the filtrate collector through the three-way valve;
s11, when the liquid level of the sample in the ion exchange column is reduced to the surface of the resin, rapidly adding deionized water into the sample adder, flushing the ion exchange column and the connecting device by using the deionized water, and collecting effluent by using a filtrate collector;
and S12, transferring the liquid in the filtrate collector into a volumetric flask, and carrying out constant volume to a scale to obtain a solution D.
S13, analyzing the ion content in the solution D using an ion chromatography system.
A third aspect of the present invention provides the use of any of the above-described pretreatment device instruments in the field of analysis.
The utility model has the advantages that:
(1) the device of the utility model has low cost, easy acquisition and repeatable regeneration of consumable products.
(2) The method of the utility model overcomes the defect that the acidity of the sample becomes stronger through the cation exchange resin, and overcomes the defect that the sample becomes turbid through the anion exchange resin.
(3) The method of the utility model can ensure that the pH value of the sample before and after the sample is processed is basically unchanged on the premise of not introducing impurities.
(4) The pretreatment of the sample and the regeneration of the resin are carried out in the same device, which is convenient, time-saving and labor-saving, and is especially suitable for the pretreatment of mass samples.
Drawings
FIG. 1 is a schematic view of a pretreatment apparatus for measuring a soluble salt component by ion chromatography according to an embodiment of the present invention (when a resin is regenerated).
Fig. 2 is a schematic diagram of a pretreatment device for measuring soluble salt components based on ion chromatography according to an embodiment of the present invention (in sample processing).
Fig. 3 is a schematic diagram of a module connecting device according to an embodiment of the present invention.
Fig. 4 is a schematic view of the sample adding device in the embodiment of the present invention.
Detailed Description
It should be noted that the following detailed description is exemplary and is intended to provide further explanation of the disclosure. 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 application belongs.
It is noted that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of example embodiments according to the present application. As used herein, the singular forms "a", "an" and "the" are intended to include the plural forms as well, and it should be understood that when the terms "comprises" and/or "comprising" are used in this specification, they specify the presence of stated features, steps, operations, devices, components, and/or combinations thereof, unless the context clearly indicates otherwise.
The utility model provides a preprocessing device based on soluble salt composition of ion chromatography survey, including sample adder, ion exchange column, filtrating collector, module connecting device and mount, the ion exchange column includes anion exchange column and cation exchange column. The sample adder is connected with the ion exchange column, the anion exchange column is connected with the cation exchange column through a module connecting device, and the filtrate collector is used for collecting effluent liquid flowing through the anion exchange column and the cation exchange column. Stabilizing the sample applicator, ion exchange column, and connecting device using the fixture.
In some embodiments, the sample adder has a rotary piston for controlling the sample addition rate.
In some embodiments, the sample adder is connected with the ion exchange column through a glass frosted opening, so that sample overflow is avoided and loss is avoided.
In some embodiments, the ion exchange column is a glass vessel with a rotary piston, the cation exchange column is filled with strong acid cation exchange resin, type 650C, and the anion exchange column is filled with strong base anion exchange resin, type 550A.
In some embodiments, the module connecting means includes a connecting pipe a, a connecting pipe B, and a three-way valve when the resin is regenerated. One end m of the connecting pipe A is connected with the cation exchange column, and the other end p is higher than the height of cation exchange resin filled in the cation exchange column; one end n of the connecting pipe B is connected with the anion exchange column, and the other end q is higher than the height of anion exchange resin filled in the anion exchange column. This arrangement has the advantage that the introduction of air bubbles into the resin caused by the liquid level being below the level at which the resin is filled can be avoided.
In some embodiments, the module connecting means comprises connecting tube a, connecting tube B and a three-way valve when processing a sample. One end m of the connecting pipe A is connected with the cation exchange column, and one end n of the connecting pipe B is connected with the anion exchange column; the other end of the connecting pipe A is connected with the other end of the connecting pipe B through a three-way valve, and the position of the three-way valve is lower than the m end and the n end, so that the full filtration and exchange reaction of a sample are facilitated.
The utility model discloses still provide a preliminary treatment method based on ion chromatography survey soluble salt composition, include: resin regeneration steps S1-S6; sample processing steps S7-S13;
s1, adding deionized water into the sample adder, opening the rotary piston of the sample adder and the rotary piston of the ion exchange column in sequence, and washing the resin in the ion exchange column by using a large amount of deionized water;
s2, closing the ion exchange column rotary piston and the sample adder rotary piston in sequence;
s3, adding 1 mol. L into a sample adder connected with a cation exchange column-1Adding 1 mol. L of the HCl solution into a sample adder connected with an anion exchange column-1NaOH solution of (2);
s4, opening the sample adder rotary piston and the ion exchange column rotary piston slowly in sequence, enabling the solution in the sample adder to flow through the ion exchange column, and closing the ion exchange column rotary piston and the sample adder rotary piston in sequence;
s5, taking down the sample adder, washing the sample adder to be neutral by using deionized water, and filling the sample adder with the deionized water;
and S6, connecting the sample adder and the ion exchange column, slowly opening the rotary piston of the sample adder and the rotary piston of the ion exchange column in sequence, and repeatedly flushing the ion exchange column by using deionized water until the effluent liquid is neutral. In steps S1-S6, the three-way valve is positioned as shown in FIG. 1, and the P end and the q end are higher than the height of the ion exchange resin.
S7, filtering the solid solution or waste liquid to obtain a sample C to be detected;
s8, connecting the end m of the connecting pipe with the end n of the connecting pipe through a three-way pipe, wherein the position of the three-way valve is lower than the end m and the end n;
s9, accurately transferring a sample C to be detected with a certain volume into a sample adder connected with the cation exchange column and a sample adder connected with the anion exchange column respectively;
s10, opening the sample adder rotary piston and the ion exchange column rotary piston in sequence, making the sample flow through the ion exchange column and the connecting pipe, and entering the filtrate collector through the three-way valve;
s11, when the liquid level of the sample in the ion exchange column is reduced to the surface of the resin, rapidly adding deionized water into the sample adder, flushing the ion exchange column and the connecting device by using the deionized water, and collecting effluent by using a filtrate collector;
and S12, transferring the liquid in the filtrate collector into a volumetric flask, and fixing the volume to a scale to obtain a solution D.
S13, analyzing the ion content in the solution D using an ion chromatography system.
In some embodiments, the deionized water conductivity is less than 0.1 μ S-cm-1
In some embodiments, in step S4, the ratio of the volume of the solution flowing through the ion exchange column to the volume of the resin packed is 2.5:1 to 10: 1.
In some embodiments, in step S11, the anion exchange column and the cation exchange column are washed with deionized water 4-5 times.
In some embodiments, the total volume of solution collected by the filtrate collector is 5-20 mL less than the volumetric volume.
In some embodiments, the resin surface layer is always below the liquid level.
The present invention is further illustrated by the following examples, which are not intended to limit the scope of the present invention. It should be understood that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention. The test methods in the following examples, which are not specified under specific conditions, are generally carried out under conventional conditions.
Referring to fig. 1-2, the present invention provides a pretreatment apparatus for measuring soluble salt components based on ion chromatography, comprising a sample adder 1, a fixing frame 2, a cation exchange column 3, an anion exchange column 4, a module connecting device 5 and a filtrate collector 6. The sample adder 1 is connected with the ion exchange column, the anion exchange column 4 is connected with the cation exchange column 3 through a module connecting device 5, and the module connecting device 5 comprises a three-way valve 14, a connecting pipe 7 and a connecting pipe 8; the filtrate collector 6 is used for collecting effluent liquid flowing through the anion exchange column and the cation exchange column. The sample applicator 1, the cation exchange column 3, the anion exchange column 4 and the connection means 5 are stabilized using the holder 2. One end of the connecting pipe 7 is connected with the bottom of the cation exchange column 3, when the resin is regenerated, the other end is higher than the height of the cation exchange resin filled in the cation exchange column 3, and when a sample is processed, the other end is lower than the bottom of the cation exchange column 3; one end of the connecting pipe 8 is connected with the bottom of the anion exchange column 4, when the resin is regenerated, the other end is higher than the height of the anion exchange resin filled in the anion exchange column 4, and when the sample is processed, the other end is lower than the bottom of the anion exchange column 4.
As shown in fig. 4, the sample adder 1 is provided with a rotary piston 9 for controlling the sample addition rate. The bottom of the sample adder 1 is a glass frosted opening, and is connected with the ion exchange column through a glass frosted opening 10.
The ion exchange column is a glass vessel with a rotary piston 11, and the inside of the ion exchange column is filled with ion exchange resin.
The method for performing ion chromatography pretreatment by using the pretreatment device for soluble salt components comprises the following steps:
adding deionized water into the sample adder 1, opening the sample adder rotary piston 9 and the ion exchange column rotary piston 11 in sequence, and flushing ion exchange with deionized waterControlling the flow rate of the resin in the column to be 10-25 mL/min-1And flushing until the effluent liquid is neutral.
Closing the ion exchange column rotary piston 11 and the sample adder rotary piston 9 in sequence; 1 mol. L was added to a sample adder 1 connected to a cation exchange column -11 mol. L into the sample adder 1 connected to the anion exchange column 4-1NaOH solution.
And (3) opening the sample adder rotary piston 9 and the ion exchange column rotary piston 11 slowly in sequence, continuously adding HCl solution or NaOH solution into the sample adder 1, enabling the HCl solution to flow through the cation exchange column 3, enabling the NaOH solution to flow through the anion exchange column 4, and closing the ion exchange column rotary piston 11 and the sample adder rotary piston 9 in sequence to finish the regeneration process of the ion exchange column.
Taking down the sample adder 1, flushing the sample adder 1 to neutrality by using deionized water, and filling the sample adder 1 with the deionized water; connecting the sample adder and the ion exchange column, slowly opening the rotary piston 11 of the sample adder and the rotary piston 9 of the ion exchange column in sequence, and repeatedly flushing the ion exchange column by using deionized water until the effluent liquid is neutral. One end 12 of the connection pipe 7 and one end 13 of the connection pipe 8 are connected via a three-way valve 14.
Example 1
Resin regeneration: adding deionized water into the sample adder 1, opening the sample adder rotary piston 9 and the ion exchange column rotary piston 11 in sequence, flushing the resin in the ion exchange column by using the deionized water, and controlling the flow rate to be 10-25 mL/min-1And flushing until the effluent liquid is neutral.
Closing the ion exchange column rotary piston 11 and the sample adder rotary piston 9 in sequence; 1 mol. L of the product was introduced into a sample addition apparatus 1 connected to a cation exchange column 3-11 mol. L into the sample adder 1 connected to the anion exchange column 4-1NaOH solution.
And (3) opening the sample adder rotary piston 9 and the ion exchange column rotary piston 11 slowly in sequence, continuously adding HCl solution or NaOH solution into the sample adder 1, enabling the HCl solution to flow through the cation exchange column 3, enabling the NaOH solution to flow through the anion exchange column 4, and closing the ion exchange column rotary piston 11 and the sample adder rotary piston 9 in sequence to finish the regeneration process of the ion exchange column.
Adding deionized water into the sample adder 1, opening the ion exchange column rotary piston 11 and the sample adder rotary piston 9 in sequence, flushing the resin in the ion exchange column with deionized water, and controlling the flow rate to be 10-25 mL/min-1And (4) washing until the effluent is neutral, and detecting the contents of cations and anions in the effluent by using an ion chromatograph, wherein the contents of the cations and the anions are less than 0.1 mg/L.
Example 2
Respectively transferring IC multi-element standard solution MERCK (Germany) F-、Cl-、SO4 2-、NO3 -、PO4 3-(concentrations were 100 mg. multidot.L, respectively)-1、250mg·L-1、500mg·L-1、500mg·L-1、1000mg·L-1) Transferring 4.00mL, 10.00mL, 20.00mL and 40.00mL into a 100mL volumetric flask, fixing the volume by using deionized water, shaking up to prepare 4 standard intermediate solutions A1、A2、A3、A4The concentrations are shown in Table 1,
TABLE 1 Standard intermediate solution concentrations
Figure BDA0003039656250000111
From A1Transferring 5.00mL of the standard intermediate solution into a sample adder connected with the cation exchange column 3, and adding the sample from A1Transferring 5.00mL of the standard intermediate solution into a sample adder connected with the anion exchange column 4; connecting the m end of the connecting pipe with the n end of the connecting pipe through a three-way pipe, wherein the position of the three-way pipe is lower than the lower end of the ion exchange resin; the sample adder rotary piston 9 and the ion exchange column rotary piston 11 are opened in sequence, and the flow rate of the exchange column is adjusted to 5 m.min-1The sample is passed through an ion exchange column and connecting tube through tee 14 into filtrate collector 6. When the liquid level of the sample in the ion exchange column is reduced to the surface layer of the resin, the deionized water is rapidly added into the sample adder 1, and the whole treatment processThe liquid level of the medium-pressure liquid is kept higher than the surface layer of the resin in the ion exchange column, so that air bubbles are prevented from entering the inside of the resin. Deionized water is used for replacing ions in each exchange column for 4-5 times, about 8mL of water is used for each time, and about 80mL of effluent is collected by using a filtrate collector 6.
Transferring the effluent liquid collected by the filtrate collector 6 into a volumetric flask, and using deionized water to perform constant volume to 100mL to obtain a diluted sample BB to be detected1. Repeating the steps to obtain the diluted sample BB to be detected in sequence2、BB3、BB4
Detection of BB (bulk blending) of sample to be detected by using ion chromatograph1、BB2、BB3、BB4The results obtained are shown in Table 2.
TABLE 2 ion concentration in samples to be tested after pretreatment
Figure BDA0003039656250000121
Example 3
Sample C0Is yellow and turbid industrial wastewater, is filtered by a 0.45 mu m microporous membrane to be light yellow and turbid liquid and is marked as C1Pipetting with pipette 5.00mLC1A sample feeder connected to the cation exchange column 3; then using a pipette to pipette 5.00mLC1The sample is added to a sample adder connected to the anion exchange column 4. Connecting the m end of the connecting pipe with the n end of the connecting pipe through a three-way pipe, wherein the position of the three-way pipe is lower than the liquid level of the lower end of the ion exchange resin; the sample adder rotary piston 9 and the ion exchange column rotary piston 11 are opened in sequence, and the flow rate of the exchange column is adjusted to be 5 mL/min-1The sample is passed through an ion exchange column and connecting tube through tee 14 into filtrate collector 6. When the liquid level of the sample in the ion exchange column is reduced to the surface layer of the resin, deionized water is rapidly added into the sample adder 1, and the liquid level is kept higher than the surface layer of the resin in the ion exchange column in the whole treatment process, so that air bubbles are prevented from entering the inside of the resin. Each exchange column uses deionized water to replace ions in the column for 4-5 times, each time uses about 8mL of water, and filtrate is collected by a filtrate collector 6And about 80mL of the effluent liquid is collected. Transferring the effluent liquid collected by the filtrate collector 6 into a volumetric flask, and using deionized water to perform constant volume to 100mL to obtain a diluted colorless, clear and transparent sample C to be detected2
According to the method for measuring the Chemical Oxygen Demand (COD) in HB/T399-2The COD (multiplied by 20 times) was 2.0 mg/L. The pH of the sample was measured to be 7.23 using a pH meter. The content of the inactive silicon in the sample is measured to be 0mg/L according to the method for measuring the inactive silicon in the water sample in DL/T502-2006.
Comparative example 1
In order to verify the accuracy of the pretreatment device and the analysis method of the patent, a standard solution F was carried out-、Cl-、SO4 2-、NO3 -、PO4 3-The recovery test of (1) was as described in example 2, except that each of the 4 standard intermediate solutions A described in example 2 was pipetted from the same solution1、A2、A3、A4Sequentially transferring 5.00mL of the solution to be respectively constant volume to 100mL, and marking the solution after shaking up as AA1、AA2、AA3、AA4. Detection of AA in a sample to be tested using an ion chromatograph1、AA2、AA3、AA4The results obtained are shown in Table 3. Pretreated by the patent F-、Cl-、SO4 2-、NO3 -、PO4 3-The ion concentration and recovery are shown in Table 4. The recovery rate is in the range of 93.6-105%, and the test requirements are met.
TABLE 3 ion concentration and Peak area in samples to be tested without pretreatment
Figure BDA0003039656250000141
TABLE 4 concentration and recovery of pretreated ions
Figure BDA0003039656250000142
Figure BDA0003039656250000151
Comparative example 2
Industrial wastewater sample C0Sample C filtered through a 0.45 μm microporous membrane according to the conventional method because of the high content of organic matter, colloidal silica and solid particles1The sample is light yellow and is turbid and opaque, organic matters and colloidal silica cannot be thoroughly removed, the requirement of an ion chromatographic instrument on sample analysis cannot be met, and the sample easily pollutes an ion chromatographic column, blocks a chromatographic system and damages the instrument. Therefore, it is necessary to use sample C1Further processing is carried out in order to obtain a sample suitable for the analysis requirements of the ion chromatography instrument.
According to the determination method of Chemical Oxygen Demand (COD) in HB/T399-1The COD of (1) is 27.0mg/L, and the sample C is measured according to the method for measuring the inactive silicon in the DL/T502-2006 water sample1The content of inactive silicon was 4.1 mg/L. Measurement of sample C Using a pH Meter1The pH values of (A) and (B) were 7.23, respectively.
Sample C1Through the utility model discloses obtain the sample C that awaits measuring behind the preprocessing device2The color of the sample is changed from light yellow to colorless, and the state of the sample is changed from turbid to clear and transparent; the removal rate of organic matters is 92.6 percent, and the removal rate of inactive silicon is 100 percent; the acidity of the sample is basically unchanged, and the detection requirement of an ion chromatography instrument is met.
It should be noted that the above examples are only used to illustrate the technical solution of the present invention and not to limit it. Although the present invention has been described in detail with reference to the examples given, those skilled in the art can modify the technical solutions of the present invention or substitute them with equivalents as necessary without departing from the spirit and scope of the technical solutions of the present invention.

Claims (10)

1. A pretreatment device for measuring a soluble salt component based on ion chromatography, comprising: the device comprises a plurality of sample adding devices, a plurality of ion exchange columns, a filtrate collector and a module connecting device; the sample adder is connected with the ion exchange columns to form a group, a plurality of groups are arranged in parallel relative to the module connecting device, the module connecting device is provided with a plurality of liquid inlets and a liquid outlet, the liquid inlets are respectively connected with the ion exchange columns, a filtrate collector is arranged below the liquid outlet, resin regeneration and sample pretreatment are carried out in the same device, and the device is suitable for pretreatment of samples in batches.
2. The pretreatment apparatus for measuring a soluble salt content based on ion chromatography as claimed in claim 1, wherein said ion exchange columns are provided in an even number, respectively, of cation exchange columns and anion exchange columns, alternately.
3. The pretreatment apparatus for measuring soluble salt components based on ion chromatography according to claim 1, wherein the module connection means comprises: the multi-channel ion exchange column comprises a multi-channel valve and a plurality of connecting pipes, wherein one end of each connecting pipe is connected with the multi-channel valve, and the other end of each connecting pipe is connected with the ion exchange column.
4. The pretreatment apparatus for measuring a soluble salt content based on ion chromatography as claimed in claim 3, wherein the connection tube has a connection end with the multi-channel valve having a level higher than a liquid level at an upper end of the ion exchange resin during regeneration of the resin, and a connection end with the multi-channel valve having a level lower than a liquid level at a lower end of the ion exchange resin during pretreatment of the sample.
5. The pretreatment device for measuring a soluble salt content based on ion chromatography as claimed in claim 1, wherein said sample addition means is provided with a rotary piston.
6. The pretreatment device for measuring soluble salt components based on ion chromatography as claimed in claim 1, wherein the sample addition means is connected to the ion exchange column through a glass-frosted opening.
7. The pretreatment apparatus for measuring soluble salt components based on ion chromatography as claimed in claim 1, wherein the ion exchange column is a glass vessel with a rotary piston.
8. The pretreatment device for measuring a soluble salt content based on ion chromatography as claimed in claim 1, wherein the inside of the cation exchange column is filled with a strongly acidic cation exchange resin.
9. The pretreatment device for measuring a soluble salt content based on ion chromatography as claimed in claim 1, wherein the anion exchange column is internally filled with a strongly basic anion exchange resin.
10. The pretreatment apparatus for measuring a soluble salt component based on ion chromatography as claimed in claim 1, wherein the module connection means comprises a connection pipe a, a connection pipe B and a three-way valve.
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