Field intensity compensation method for constructing non-uniform electric field through auxiliary electrode

Abstract

Presented is an electric field intensity compensation method for constructing a non-uniform electric field through an auxiliary electrode, including steps of: in a matrix electrode unit, designing an auxiliary electrode arrangement position according to the spatial distribution of the pollutant concentration; designing the polarity of the auxiliary electrode according to the position relationship between the auxiliary electrode and matrix electrodes; and constructing a non-uniform electric field by the auxiliary electrode and the matrix electrodes to implement space compensation of the electric field intensity. In the present invention, a non-uniform electric field matching a pollutant concentration field is constructed by setting the space arrangement and polarity of the auxiliary electrodes on the basis of the matrix electrodes according to the spatial distribution of the pollutant concentration, the contradiction of consistency between the heterogeneity of the spatial distribution of the pollutants and the removal efficiency of the uniform electric field is solved, and the spatial difference of efficiency of electrokinetically remedying organic contaminated soil is avoided, thereby improving the overall space remediation efficiency of electrokinetic remediation.

Claims

1. An electric field intensity compensation method for constructing a non-uniform electric field through an auxiliary electrode, comprising the following steps: in a matrix electrode unit, determining an auxiliary electrode layout position according to a spatial distribution of a pollutant concentration, and inserting the auxiliary electrode; controlling a polarity of the auxiliary electrode according to the position relationship between the auxiliary electrode and matrix electrodes; and constructing the non-uniform electric field by the auxiliary electrode and the matrix electrodes to implement space compensation.

2. The electric field intensity compensation method for constructing a non-uniform electric field through an auxiliary electrode of claim 1, wherein the step of determining the arrangement position of the auxiliary electrode according to the spatial distribution of the pollutant concentration comprises the following steps: taking adjacent 4 matrix electrodes as a unit, wherein, when a region of which the pollutant concentration is higher than a threshold is present in the matrix electrode unit, the geometric center position of the region is an auxiliary electrode layout position.

3. The electric field intensity compensation method for constructing a non-uniform electric field through an auxiliary electrode of claim 1, wherein the step of controlling the polarity of the auxiliary electrode according to the position relationship between the auxiliary electrode and the matrix electrodes comprises the following steps: d.sub.i is the distance between an auxiliary electrode and the i.sup.th matrix electrode, where n=4; the distance between the field intensity E corresponding to the average removal rate of pollutants and the closest matrix electrode is R; when $\underset{i=1}{\overset{n}{.Math.}}\left(d_i-R\right)0,$ the polarity of adjacent matrix electrodes is made to be opposite, and the polarity of the auxiliary electrode is opposite to that of the matrix electrode closest to same; when $\underset{i=1}{\overset{n}{.Math.}}\left(d_i-R\right)>0,$ the polarity of matrix electrodes is made to be identical, and the polarity of the auxiliary electrode is opposite to that of the matrix electrode.

4. The electric field intensity compensation method for constructing a non-uniform electric field through an auxiliary electrode of claim 1, wherein the step of constructing the non-uniform electric field by the auxiliary electrode and matrix electrodes comprises the steps of: constructing the non-uniform electric field by switching between the positive electrode and the negative electrode through the polarity of the auxiliary electrode and the polarity of the matrix electrodes.

Description

DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a diagram showing an auxiliary electrode position, polarity switching and non-uniform electric field of embodiment 1;

(2) wherein FIG. 1-1 is a schematic diagram showing a matrix electrode layout and field intensity isoline of embodiment 1;

(3) FIG. 1-2 is a schematic diagram showing an auxiliary electrode layout position of embodiment 1;

(4) FIG. 1-3 is a schematic diagram showing the polarity switching between an auxiliary electrode and a matrix electrode of embodiment 1;

(5) FIG. 1-4 is a schematic diagram showing the non-uniform electric field of embodiment 1;

(6) FIG. 2 is a diagram showing an auxiliary electrode position, polarity switching and non-uniform electric field of embodiment 2;

(7) wherein FIG. 2-1 is a schematic diagram showing a matrix electrode layout and field intensity isoline of embodiment 2;

(8) FIG. 2-2 is a schematic diagram showing an auxiliary electrode layout position of embodiment 2;

(9) FIG. 2-3 is a schematic diagram showing the polarity switching between an auxiliary electrode and a matrix electrode of embodiment 2;

(10) FIG. 2-4 is a schematic diagram showing the non-uniform electric field of embodiment 2.

DETAILED DESCRIPTION

(11) The present invention will be further described in detail below in combination with the drawings and the embodiments.

(12) An electric field intensity compensation method for constructing a non-uniform electric field through an auxiliary electrode, comprising the following steps:

(13) (1) in a matrix electrode unit, designing auxiliary electrode layout positions according to the spatial distribution of the pollutant concentration;

(14) (2) designing the polarity of the auxiliary electrodes according to the position relationship between the auxiliary electrodes and matrix electrodes;

(15) (3) constructing a non-uniform electric field by the auxiliary electrode and the matrix electrodes to implement space compensation.

(16) The step of designing the auxiliary electrode layout position specifically comprises:

(17) (1) adjacent 4 matrix electrodes are taken as a unit, wherein the distance between two adjacent matrix electrodes is L;

(18) (2) when a high concentration region of pollutants is presented in the matrix electrode unit, the geometric center position of the high concentration region is an auxiliary electrode layout position;

(19) (3) if no high concentration region of pollutants is presented in the matrix electrode unit, auxiliary electrodes are not laid.

(20) The polarity of the auxiliary electrode is specifically designed as:

(21) (1) the distance between the auxiliary electrode and the matrix electrode is d, and the polarity discrimination distance R of the auxiliary electrode is determined by the field intensity E corresponding to the average removal rate of pollutants;

(22) (2) when

(23) $\underset{i=1}{\overset{n}{.Math.}}\left(d_i-R\right)0\left(n=4\right),$
supposing the polarity of adjacent matrix electrodes are opposite, the polarity of the auxiliary electrode is opposite to that of the matrix electrode closest to same, where d.sub.i is the distance between an auxiliary electrode and the i.sup.th matrix electrode;

(24) (3) when

(25) $\underset{i=1}{\overset{n}{.Math.}}\left(d_i-R\right)>0\left(n=4\right),$
supposing the polarity of adjacent matrix electrodes are identical, the polarity of the auxiliary electrode is opposite to that of the matrix electrode;

(26) The non-uniform electric field is specifically constructed as follows:

(27) (1) the non-uniform electric field is constructed by switching between the positive electrode and the negative electrode through the polarity of the auxiliary electrodes and the polarity of the matrix electrodes according to the auxiliary electrode layout position and the polarity design of the auxiliary electrode;

(28) (2) the field intensity distribution of the non-uniform electric field is essentially consistent with the field distribution of the pollutant concentration, thereby effectively reducing the spatial variability of the pollutant concentration.

(29) The spatial distribution of the pollutant concentration is specifically formed as follows:

(30) (1) continuous distribution of spatial concentration of pollutants is formed by grid sampling and measuring the concentration of pollutants of a sampling point by using a Kriging spatial interpolation;

(31) (2) by taking the sum of the mean value of the concentration of pollutants and the standard deviation as a threshold, the spatial distribution of the concentration of pollutants is divided into a high concentration region and a low concentration region.

Embodiment 1

(32) The contaminated soil remedied in this embodiment is petroleum-contaminated soil configured for the laboratory; the collected soil is clay in which visible impurities and roots of grass and trees are removed and which is air-dried naturally and then sieved using a sieve of 2 mm; petroleum is extracted from a certain petroleum pit of Shuguang Oil Production Plant, Liaohe Oil Field Company; petroleum-contaminated soil of 40 g/kg-50 g/kg is non-uniformly prepared, and is air-dried naturally for 7 days; after petroleum is uniformly mixed with soil, the moisture content is adjusted to be 25% using deionized water, and the mixture is filled in an electrokinetic remediation reaction tank (length 20 cmwidth 20 cmheight 15 cm).

(33) The spatial distribution of the concentration of petroleum pollutants is implemented as follows: 25 samples (55) are collected in total in the reaction tank through the grid distribution point method. By using infrared spectrophotometry, the concentration of petroleum pollutants is measured to have a mean value of oil content =44.5 g/kg, a standard deviation =7.2 g/kg, and a spatial variation coefficient CV=16.2%. By taking the sum of the mean value of the concentration of pollutants and the standard deviation as a threshold, i.e. by taking +=51.7 g/kg as a threshold, the spatial distribution of the concentration of pollutants is divided into a high concentration region and a low concentration region, wherein the high concentration region accounts for 10.1% of the total area, and the low concentration region accounts for 89.9% of the total area.

(34) As shown in FIG. 1-1, the matrix electrodes are arranged in a 22 matrix, the matrix electrodes are electrodes with the serial number of 1.sup.#-4.sup.# respectively, and the electrode spacing L is 20 cm. The external voltage is 36V and the uniform electric field intensity formed by the matrix electrodes is greater than or equal to 0.8V/cm. Both the auxiliary electrode and the matrix electrodes are made of graphite electrodes (1 cm in diameter, and 20 cm in height), and the external voltage is also 36V.

(35) The field intensity compensation method for constructing a non-uniform electric field through an auxiliary electrode in this embodiment specifically comprises the steps of: 1) designing the arrangement position of the auxiliary electrode according to the spatial distribution of pollutant concentration; 2) designing the polarity of the auxiliary electrode according to the position relationship between the auxiliary electrode and the matrix electrodes; and 3) constructing a non-uniform electric field by the auxiliary electrode and the matrix electrodes, to implement the space compensation of the electric field intensity.

(36) Step 1. The auxiliary electrode arrangement position is specifically designed as follow; is:

(37) As shown in FIGS. 1-1 to 1-2 in FIG. 1, in the uniform electric field formed by four matrix electrodes, the geometric center position of the high concentration region of petroleum pollutants is the arrangement position of the auxiliary electrode (5.sup.# electrode).

(38) Step 2. The auxiliary electrode polarity is specifically designed as follows:

(39) The previous research result indicates that for the petroleum pollutants, under the electrokinetic remediation condition, the pollutant removal rate is in negative correlation with the electrode distance in space, and the field intensity is also in negative correlation with the electrode distance in space. Therefore, the average removal rate of pollutants in space and corresponding field intensity values can form a set of isolines.

(40) In this embodiment, the field intensity E corresponding to the average removal rate of petroleum pollutants is 1.0V/cm, as shown in FIG. 1-1, and a set of isolines taking the matrix electrode as a centre and having a radius of R=L/2 are formed.

(41) Since the relationship of distance (d) between the auxiliary electrode and the matrix electrodes meets

(42) $\underset{i=1}{\overset{n}{.Math.}}\left(d_i-R\right)0\left(n=4\right),$
as shown in FIG. 1-3, supposing that the polarity of adjacent matrix electrodes are opposite, the polarity of the auxiliary electrode is opposite to that of the matrix electrodes closest to same, that is, the polarity of 1.sup.# electrode, 3.sup.# electrode and 5.sup.# electrode are identical, the polarity of 2.sup.# electrode and 4.sup.# electrode are identical, and the polarity of 1.sup.# electrode, 3.sup.# electrode and 5.sup.# electrode are opposite to that of 2.sup.# electrode and 4.sup.# electrode.

(43) Step 3. The non-uniform electric field is specifically constructed as follows:

(44) The polarity of the auxiliary electrode and matrix electrodes can be adjusted by a polarity switching controller. As shown in FIG. 1-3, by keeping the polarity switching between the auxiliary electrode and the matrix electrodes, the non-uniform electric field matching the pollutant concentration field is constructed (FIG. 1-4). The time period for polarity switching of electrodes, t=4 h, and the total remediation time T=60 d.

(45) See Table 1 for remediation result.

(46) TABLE-US-00001 TABLE 1 Coefficient of variation of Electrode Electric field Remediation pollutant Processing Group arrangement type efficiency (%) concentration (%) time (d) Control None None 2.7% 16.2 60 group Experimental Matrix Uniform electric 55.7% 15.2 60 group 1 electrode field Experimental Auxiliary Non-uniform 70.2% 3.5 60 group 2 electrodes + electric field matrix electrode

(47) Embodiment 2 is different from embodiment 1 in that:

(48) The mean value of the concentration of petroleum pollutants is =34.3 g/kg, the standard deviation =8.8 g/kg, and the spatial variation coefficient CV=25.7%. By taking the sum of the mean value of the concentration of pollutants and the standard deviation as a threshold, i.e. by taking +==43.1 g/kg as a threshold, the spatial distribution of the concentration of pollutants is divided into a high concentration region and a low concentration region, wherein the high concentration region accounts for 20.7% of the total area, and the low concentration region accounts for 79.3% of the total area.

(49) As shown in FIGS. 2-1 to 2-4 in FIG. 2, in this embodiment, since the relationship of distance between the auxiliary electrode and the matrix electrodes meets

(50) $\underset{i=1}{\overset{n}{.Math.}}\left(d_i-R\right)>0\left(n=4\right),$
as shown in FIG. 2-3, supposing that the polarity of matrix electrodes are identical, the polarity of the auxiliary electrode is opposite to that of the matrix electrodes, that is, the polarity of 1.sup.# electrode, 2.sup.# electrode, 3.sup.# electrode and 4.sup.# electrode are identical, and the polarity of 1.sup.# electrode, 2.sup.# electrode, 3.sup.# electrode and 4.sup.# electrode are opposite to that of 5.sup.# electrode.

(51) As shown in FIG. 2-3, by keeping the polarity switching between the auxiliary electrode and the matrix electrodes, the non-uniform electric field matching the pollutant concentration field is constructed (FIG. 2-4). See Table 2 for remediation result.

(52) TABLE-US-00002 TABLE 2 Coefficient of variation of Electrode Electric field Remediation pollutant Processing Group arrangement type efficiency (%) concentration (%) time (d) Control None None 2.4% 25.7 60 group Experimental Matrix Uniform electric 53.2% 19.7 60 group 1 electrode field Experimental Auxiliary Non-uniform 72.7% 5.8 60 group 2 electrodes + electric field matrix electrode

(53) The above contents are further detailed descriptions of the present invention in combination with specific preferential embodiments. However, it cannot be considered that the specific embodiments of the present invention are only limited to these descriptions. Several simple deductions or replacements may be made without departing from the conception of the present invention, all of which shall be considered to belong to the protection scope of the present invention.