CN114709288B - A kind of solar cell and diffusion method thereof - Google Patents
A kind of solar cell and diffusion method thereof Download PDFInfo
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- H10F10/00—Individual photovoltaic cells, e.g. solar cells
- H10F10/10—Individual photovoltaic cells, e.g. solar cells having potential barriers
- H10F10/14—Photovoltaic cells having only PN homojunction potential barriers
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- H—ELECTRICITY
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- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P32/00—Diffusion of dopants within, into or out of wafers, substrates or parts of devices
- H10P32/10—Diffusion of dopants within, into or out of semiconductor bodies or layers
- H10P32/12—Diffusion of dopants within, into or out of semiconductor bodies or layers between a solid phase and a gaseous phase
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- H10P32/00—Diffusion of dopants within, into or out of wafers, substrates or parts of devices
- H10P32/10—Diffusion of dopants within, into or out of semiconductor bodies or layers
- H10P32/17—Diffusion of dopants within, into or out of semiconductor bodies or layers characterised by the semiconductor material
- H10P32/171—Diffusion of dopants within, into or out of semiconductor bodies or layers characterised by the semiconductor material being group IV material
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Abstract
The application provides a solar cell and a diffusion method thereof, and belongs to the technical field of photovoltaics. A solar cell and a diffusion method thereof, comprising: and sequentially performing first pre-oxidation treatment, first power supply treatment, second pre-oxidation treatment, second power supply treatment and third power supply treatment on the silicon wafer. The oxygen inflow amount of the first pre-oxidation treatment and the second pre-oxidation treatment is increased. The temperature of the first time of the source treatment, the second time of the source treatment and the third time of the source treatment and the nitrogen carrying phosphorus oxychloride are gradually increased. According to the diffusion method of the solar cell, the shallow junction can be prepared through the cooperation of the two pre-oxidation treatments and the three power supply treatments, meanwhile, the doping non-uniformity is improved, and the blue light response of the solar cell can be improved by the shallow junction, so that the photoelectric conversion efficiency of the solar cell is improved.
Description
Technical Field
The application relates to the technical field of photovoltaics, in particular to a solar cell and a diffusion method thereof.
Background
The environmental pollution caused by non-renewable energy consumption is serious, and the development of renewable clean energy of photovoltaics is accelerated. At present, the solar battery is widely regarded as renewable energy sources, conforms to the trend of global photovoltaic development, and is important in cost reduction and synergy. The efficiency of the crystalline silicon solar cell is improved, and the production process of the cell slice is more required to be improved from the crystalline silicon raw material.
In the preparation process of the single crystal PERC solar cell, a selective emitter manufactured by diffusion is the core. The diffusion forms a P-N junction, and the junction depth and the surface concentration of the P-N junction directly influence the photoelectric conversion efficiency of the solar cell.
At present, the common diffusion process realizes phosphorus source doping through the steps of pre-deposition, high-temperature junction pushing, temperature reduction, impurity absorption, source post-supplementing and the like. The P-N junction after diffusion mainly causes uneven distribution of phosphorus sources on the surface of a silicon wafer and uneven doping, poor uniformity and other problems due to uneven distribution of air flow and over-dense arrangement of silicon wafers during diffusion, so that the efficiency of a battery piece is poor, the conventional large-size monocrystalline silicon wafer is generally provided with two-step through sources in the diffusion process, the diffusion time is longer, the manufactured P-N junction is deeper, the uniformity of sheet resistance in a single sheet is poor, and the surface recombination is larger.
Disclosure of Invention
The application provides a solar cell and a diffusion method thereof, which can prepare shallow junctions and improve the technical problem of uneven doping.
Embodiments of the present application are implemented as follows:
in a first aspect, an example of the present application provides a solar cell and a diffusion method thereof, including: and sequentially performing first pre-oxidation treatment, first power supply treatment, second pre-oxidation treatment, second power supply treatment and third power supply treatment on the silicon wafer.
The first pre-oxidation treatment and the second pre-oxidation treatment are both carried out under the condition of introducing oxygen, the oxygen introducing amount of the first pre-oxidation treatment is 500-600 sccm, and the oxygen introducing amount of the second pre-oxidation treatment is 800-1000 sccm.
The first time of the source treatment, the second time of the source treatment and the third time of the source treatment are all carried out under the conditions of oxygen and nitrogen carrying phosphorus oxychloride, the temperature of the first time of the source treatment is 790-795 ℃, the nitrogen inlet amount of the first time of the source treatment is 800-900 sccm, the temperature of the second time of the source treatment is 800-805 ℃, the nitrogen inlet amount of the second time of the source treatment is 1000-1100 sccm, the temperature of the third time of the source treatment is 810-815 ℃, and the nitrogen inlet amount of the third time of the source treatment is 1500-2000 sccm.
In the technical scheme, the diffusion method of the solar cell can prepare the shallow junction through the cooperation of the two pre-oxidation treatments and the three power supply treatments, and meanwhile, the doping non-uniformity is improved, and the shallow junction can improve the blue light response of the solar cell so as to improve the photoelectric conversion efficiency of the solar cell.
In the diffusion method of the solar cell, the oxygen inlet amount of the second pre-oxidation treatment is larger than that of the first pre-oxidation treatment, so that an oxide layer of a semiconductor substrate is formed, a shallow junction is formed, the surface concentration is reduced, the impurity concentration in the oxide layer of the semiconductor substrate is uniformly distributed, and the phosphorus source doping in the shallow junction is also further uniformly distributed.
In the diffusion method of the solar cell, the temperature of the first time of the through source treatment, the temperature of the second time of the through source treatment and the temperature of the third time of the through source treatment are sequentially increased, the nitrogen inlet amount of the first time of the through source treatment, the nitrogen inlet amount of the second time of the through source treatment and the nitrogen inlet amount of the third time of the through source treatment are sequentially increased, the high-concentration diffusion is carried out on the surface layer of the silicon wafer in a short time, so that a phosphorus-silicon glass layer with high doping concentration is formed on the surface of the silicon wafer only, and phosphorus atoms are uniformly distributed to push a system knot through high Wen Tongyang, thereby remarkably improving the diffusion uniformity and forming N + -N-P structure, reducing surface concentration.
With reference to the first aspect, in a first possible example of the first aspect of the present application, the first pre-oxidation treatment includes heat preservation at 780-785 ℃ and oxygen ventilation for 2-3 min.
With reference to the first aspect, in a second possible example of the first aspect of the present application, the first-pass source treatment includes heat-preservation for 2 to 3min at 790 to 795 ℃ under the condition of introducing oxygen and nitrogen carrying phosphorus oxychloride.
Optionally, the oxygen gas is introduced into the reactor at an amount of 500-600 sccm in the first source introduction treatment.
With reference to the first aspect, in a third possible example of the first aspect of the present application, the second pre-oxidation treatment includes heat preservation at 800-805 ℃ and oxygen ventilation for 2-3 min.
With reference to the first aspect, in a fourth possible example of the first aspect of the present application, the second-pass source treatment includes heat preservation for 2 to 3min at 800 to 805 ℃ under the condition of introducing oxygen and nitrogen carrying phosphorus oxychloride.
Optionally, the oxygen gas is introduced into the reactor at 700-800 sccm in the second time of source introduction treatment.
With reference to the first aspect, in a fifth possible example of the first aspect of the present application, the third-pass source treatment includes heat preservation for 2 to 2.5min at 810 to 815 ℃ under the condition of introducing oxygen and nitrogen carrying phosphorus oxychloride.
Optionally, the oxygen gas inlet amount in the third time of the source passing treatment is 100-1200 sccm.
With reference to the first aspect, in a sixth possible example of the first aspect of the present application, after the third-pass source treatment is completed, the temperature is raised to 845 to 850 ℃, and then high-temperature oxidation treatment is performed at this temperature.
Optionally, the oxygen gas is introduced into the high-temperature oxidation treatment at 400-500 sccm.
Optionally, the high temperature oxidation treatment time is 4-4.5 min.
Optionally, after the high-temperature oxidation treatment is completed, stopping introducing oxygen, and continuing to keep the temperature at 845-850 ℃ for 5-6 min.
With reference to the first aspect, in a seventh possible example of the first aspect of the present application, after the heat preservation is performed at 845-850 ℃ for 5-6 min, the temperature is reduced to 780-795 ℃, and then the post-source treatment is performed, wherein the post-source treatment comprises heat preservation at 790-795 ℃ and under the condition of introducing oxygen and nitrogen carrying phosphorus oxychloride for 12-13 min.
Optionally, the oxygen gas inlet amount in the post-source treatment is 800-900 sccm.
Optionally, the nitrogen gas is introduced into the post-source treatment at 1400-1500 sccm.
Optionally, after finishing the post-source treatment, performing post-oxidation treatment, wherein the post-oxidation treatment comprises heat preservation for 5-5.5 min at 780-785 ℃ under the condition of introducing oxygen.
Optionally, the oxygen gas in the post-oxidation treatment is introduced in an amount of 3000-3500 sccm.
In the above example, the post-oxidation step is performed under an oxygen-enriched condition, so that a layer of high-quality silicon-silicon dioxide interface with lower surface state density can be generated on the surface of the diffused silicon wafer, thereby effectively reducing surface recombination and further improving minority carrier lifetime and short-wave response.
With reference to the first aspect, in an eighth possible example of the first aspect of the present application, the above-mentioned first pre-oxidation treatment, first-pass source treatment, second pre-oxidation treatment, second-pass source treatment, and third-pass source treatment are all performed at a pressure of 60 to 80Pa.
In a second aspect, the present example provides a solar cell manufactured according to the above-described diffusion method of a solar cell.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present application, the drawings that are needed in the embodiments will be briefly described below, it being understood that the following drawings only illustrate some embodiments of the present application and therefore should not be considered as limiting the scope, and other related drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a flow chart of a diffusion method of a solar cell of the present application;
fig. 2 is an ECV graph of the solar cell manufactured in example 1 and comparative example 1 according to the present application.
Detailed Description
Embodiments of the present application will be described in detail below with reference to examples, but it will be understood by those skilled in the art that the following examples are only for illustrating the present application and should not be construed as limiting the scope of the present application. The specific conditions are not noted in the examples and are carried out according to conventional conditions or conditions recommended by the manufacturer. The reagents or apparatus used were conventional products commercially available without the manufacturer's attention.
The following specifically describes a solar cell and a diffusion method thereof according to an embodiment of the present application:
the application provides a diffusion method of a solar cell, fig. 1 is a flow chart of the diffusion method of the solar cell, and the diffusion method comprises the following steps: and sequentially performing first pre-oxidation treatment, first power supply treatment, second pre-oxidation treatment, second power supply treatment and third power supply treatment on the silicon wafer.
Wherein the silicon wafer is a silicon wafer with a textured surface.
The texturing process comprises the step of texturing the silicon wafer by alkali to form a textured surface with a pyramid-like structure with a light trapping effect on the surface of the silicon wafer.
Before the first pre-oxidation treatment, vertically placing the silicon wafer with the textured silicon surface into a quartz boat clamping groove, moving the silicon wafer into a low-pressure diffusion furnace tube by depending on a silicon carbide paddle, and heating to 780-785 ℃.
In one embodiment of the application, after the wafer is moved into the low pressure diffuser tube, the temperature is raised to 782 ℃. In other embodiments of the application, after the wafer is moved into the low pressure diffuser tube, it is warmed to 780 ℃, 781 ℃, 783 ℃, 784 ℃, or 785 ℃.
The pressure in the low-pressure diffusion furnace tube is 60-80 Pa.
In one embodiment of the application, the pressure in the low pressure diffuser tube is 60Pa. In other embodiments of the application, the pressure in the low pressure diffusion furnace tube may also be 65Pa, 70Pa, 75Pa, or 80Pa.
Optionally, when the silicon wafer with the textured silicon surface is vertically placed in the quartz boat clamping groove, a back-to-back manner is adopted, that is, the back surface of the silicon wafer is abutted against the back surface.
The first pre-oxidation treatment comprises the steps of introducing oxygen into a low-pressure diffusion furnace for 2-3 min at the temperature of 780-785 ℃.
The oxygen inlet amount in the first pre-oxidation treatment is 500-600 sccm.
In one embodiment of the present application, the oxygen aeration rate in the first pre-oxidation treatment is 550sccm. In other embodiments of the present application, the oxygen aeration rate in the first pre-oxidation treatment is 500sccm, 510sccm, 520sccm, 530sccm, 540sccm, 560sccm, 570sccm, 580sccm, 590sccm, or 600sccm.
The first surface pre-oxidation treatment is performed in advance before diffusion to form a thinner oxide layer, so that the speed of a phosphorus source reaching a silicon substrate is slowed down, the junction depth is reduced, and the surface concentration is reduced.
Heating to 790-795 ℃ and carrying out primary power-on treatment. The first source-passing treatment comprises the steps of introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into a low-pressure diffusion furnace for 2-3 min at the temperature of 790-795 ℃.
In one embodiment of the present application, the first power-on treatment is performed after the temperature is raised to 792 ℃. In other embodiments of the application, the first energizing treatment is performed after heating to 790 ℃, 791 ℃, 793 ℃, 794 ℃ or 795 ℃.
The oxygen inlet amount in the first time of the source treatment is 500-600 sccm.
In one embodiment of the present application, the oxygen aeration rate in the first aeration treatment is 550sccm. In other embodiments of the present application, the oxygen gas is introduced at 500sccm, 510sccm, 520sccm, 530sccm, 540sccm, 560sccm, 570sccm, 580sccm, 590sccm, or 600sccm in the first pass source treatment.
The carrying amount of phosphorus oxychloride in the nitrogen is 7-10wt%.
The nitrogen gas carrying phosphorus oxychloride in the first source treatment has the inlet amount of 800-900 sccm.
In one embodiment of the application, the nitrogen gas carrying phosphorus oxychloride in the first source passing treatment has a nitrogen gas inlet of 850sccm. In other embodiments of the present application, the nitrogen gas carrying phosphorus oxychloride in the first pass source treatment is at 800sccm, 810sccm, 820sccm, 830sccm, 840sccm, 860sccm, 870sccm, 880sccm, 890sccm or 900sccm.
The first pass source process can pre-deposit a shallow diffusion layer with smaller concentration.
Heating to 800-805 deg.c and pre-oxidizing for the second time. The second pre-oxidation treatment comprises the step of introducing oxygen into a low-pressure diffusion furnace for 2-3 min at the temperature of 800-805 ℃.
In one embodiment of the application, a second pre-oxidation treatment is performed after the temperature is raised to 802 ℃. In other embodiments of the application, the second pre-oxidation treatment is performed after the temperature is raised to 800 ℃, 801 ℃, 803 ℃, 804 ℃, or 805 ℃.
The oxygen inlet amount in the second pre-oxidation treatment is 800-1000 sccm.
In one embodiment of the present application, the oxygen aeration rate in the second pre-oxidation treatment is 900sccm. In other embodiments of the present application, the oxygen gas is introduced at 800sccm, 810sccm, 820sccm, 830sccm, 840sccm, 850sccm, 860sccm, 870sccm, 880sccm, 890sccm, 910sccm, 920sccm, 930sccm, 940sccm, 950sccm, 960sccm, 970sccm, 980sccm, 990sccm or 1000sccm in the second pre-oxidation treatment.
The second pre-oxidation treatment forms an oxide layer with the thickness of 1-2 nm through the oxygen with higher flow rate, on one hand, the inactive phosphorus source (PCl) formed by the first through-source treatment is reacted 5 ),PCl 5 Will corrode the silicon substrate; on the other hand, the effect of the subsequent high-concentration phosphorus source on the surface concentration is further slowed down.
The second time of source passing treatment comprises that the mixed gas of oxygen and nitrogen carrying phosphorus oxychloride is introduced into a low-pressure diffusion furnace for 2-3 min at the temperature of 800-805 ℃.
The oxygen inlet amount in the second time of the source treatment is 700-800 sccm.
In one embodiment of the present application, the oxygen aeration rate in the second aeration treatment is 750sccm. In other embodiments of the present application, the oxygen gas is introduced at 700sccm, 710sccm, 720sccm, 730sccm, 740sccm, 760sccm, 770sccm, 780sccm, 790sccm, or 800sccm in the second pass source treatment.
The nitrogen gas carrying phosphorus oxychloride in the second pass source treatment has the inlet amount of 1000-1100 sccm.
In one embodiment of the application, the nitrogen carrying phosphorus oxychloride in the second pass source treatment has a nitrogen inlet of 1050sccm. In other embodiments of the present application, the nitrogen gas carrying phosphorus oxychloride in the second pass source treatment is introduced at a rate of 1000sccm, 1010sccm, 1020sccm, 1030sccm, 1040sccm, 1060sccm, 1070sccm, 1080sccm, 1090sccm or 1100sccm.
The second pass source treatment is the doping of the phosphorus source with higher temperature, the reaction is more active, and the generation of impurities such as an inactive phosphorus source can be reduced.
Heating to 810-815 deg.c and the third power-on treatment. The third time of source passing treatment comprises that the mixed gas of oxygen and nitrogen carrying phosphorus oxychloride is introduced into a low-pressure diffusion furnace for 2 to 2.5min at the temperature of 810 to 815 ℃.
In one embodiment of the present application, the third pass source treatment is performed after the temperature is raised to 812 ℃. In other embodiments of the application, the third pass source treatment is performed after heating to 810 ℃, 811 ℃, 813 ℃, 814 ℃ or 815 ℃.
The nitrogen gas inlet amount of the oxygen in the third time of the source treatment is 1000-1200 sccm.
In one embodiment of the present application, the oxygen aeration rate in the third aeration treatment is 1100sccm. In other embodiments of the present application, the oxygen gas is introduced at 1000sccm, 1010sccm, 1020sccm, 1030sccm, 1040sccm, 1050sccm, 1060sccm, 1070sccm, 1080sccm, 1090sccm, 1110sccm, 1120sccm, 1130sccm, 1140sccm, 1150sccm, 1160sccm, 1170sccm, 1180sccm, 1190sccm, or 1200sccm in the second pass source treatment.
The nitrogen gas carrying phosphorus oxychloride in the third pass source treatment has the inlet amount of 1500-2000 sccm.
In one embodiment of the application, the nitrogen gas carrying phosphorus oxychloride in the third pass source treatment has a nitrogen gas inlet amount of 1750sccm. In other embodiments of the present application, the nitrogen gas carrying phosphorus oxychloride in the third pass source treatment is introduced at a rate of 1500sccm, 1550sccm, 1600sccm, 1650sccm, 1700sccm, 1800sccm, 1850sccm, 1900sccm, 1950sccm or 2000sccm.
The third pass source treatment is high-concentration phosphorus source doping, and can be matched with the first pass source treatment and the second pass source treatment, the concentration is from low to high, a concentration gradient is formed, the phosphorus sources are uniformly distributed, and the uniformity of phosphorus simple substances is improved.
After the third power-on treatment is completed, the temperature is raised to 845-850 ℃ for 5-5.5 min, and high-temperature oxidation treatment is carried out. The high-temperature oxidation treatment comprises the step of introducing oxygen into a low-pressure diffusion furnace for 4-4.5 min at the temperature of 845-850 ℃.
In one embodiment of the present application, the elevated temperature is raised to 847 ℃ and then subjected to a high temperature oxidation treatment. In other embodiments of the application, the elevated temperature is at 845 ℃, 846 ℃, 848 ℃, 849 ℃, or 850 ℃ followed by a high temperature oxidation treatment.
The oxygen inlet amount in the high-temperature oxidation treatment is 500-600 sccm.
In one embodiment of the present application, the oxygen aeration rate in the high temperature oxidation treatment is 550sccm. In other embodiments of the present application, the oxygen aeration rate in the high temperature oxidation treatment is 500sccm, 510sccm, 520sccm, 530sccm, 540sccm, 560sccm, 570sccm, 580sccm, 590sccm, or 600sccm.
And forming a phosphosilicate glass layer after the first-time source passing treatment, the second-time source passing treatment and the third-time source passing treatment, introducing oxygen in the high-temperature oxidation treatment, reacting with an inactive phosphorus source, reducing partial areas with uneven phosphorus source distribution, and further improving uniformity.
After the high-temperature oxidation treatment is finished, stopping introducing oxygen, and continuously preserving the temperature at 845-850 ℃ for 5-6 min.
The diffusion method of the solar cell shortens the duration of the height Wen Bu on the basis of the existing method, and the push junction is shallower.
After the heat preservation is completed, the temperature is reduced to 790-795 ℃ for 15-16 min for impurity removal.
In one embodiment of the application, the temperature is reduced to 792 ℃ for impurity removal. In other embodiments of the application, the temperature is reduced to 790 ℃, 791 ℃, 793 ℃, 794 ℃ or 795 ℃ for impurity removal.
And (5) after cooling and impurity separation are completed, performing post-source-passing treatment. The post-source treatment comprises the step of introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into a low-pressure diffusion furnace for 12-13 min at the temperature of 790-795 ℃.
The oxygen gas is introduced into the reactor at a rate of 800-900 sccm.
In one embodiment of the present application, the oxygen gas is introduced into the post-feed treatment at 850sccm. In other embodiments of the present application, the oxygen is introduced at 800sccm, 810sccm, 820sccm, 830sccm, 840sccm, 860sccm, 870sccm, 880sccm, 890sccm or 900sccm in the post-pass source treatment.
The nitrogen gas carrying phosphorus oxychloride in the post-source treatment has the inlet amount of 1400-1500 sccm.
In one embodiment of the application, the nitrogen gas carrying phosphorus oxychloride in the post-source treatment is introduced at 1450sccm. In other embodiments of the present application, the nitrogen gas carrying phosphorus oxychloride in the post-source treatment is introduced at 1400sccm, 1410sccm, 1420sccm, 1430sccm, 1440sccm, 1460sccm, 1470sccm, 1480sccm, 1490sccm or 1500sccm.
Cooling to 780-785 ℃ and performing post-oxidation treatment. The post-oxidation treatment comprises the step of introducing oxygen into a low-pressure diffusion furnace for 5-5.5 min at the temperature of 780-785 ℃.
In one embodiment of the application, the post-oxidation treatment is performed after the temperature is reduced to 782 ℃. In other embodiments of the application, the post-oxidation treatment is performed after cooling to 780 ℃, 781 ℃, 783 ℃, 784 ℃, or 785 ℃.
The oxygen inlet amount in the post-oxidation treatment is 3000-3500 sccm.
In one embodiment of the present application, the oxygen aeration rate in the post-oxidation treatment was 3250sccm. In other embodiments of the application, the oxygen aeration rate in the post-oxidation treatment is 3000sccm, 3050sccm, 3100sccm, 3150sccm, 3200sccm, 3300sccm, 3350sccm, 3400sccm, 3450sccm, or 3500sccm.
The post oxidation treatment is to generate a layer of silicon-silicon dioxide interface with high quality and lower surface state density on the surface of the diffused silicon wafer under the oxygen-enriched condition, so that the surface recombination can be effectively reduced, and the minority carrier lifetime is prolonged.
Cooling and taking out the boat after finishing the post-oxidation treatment.
And (3) sequentially carrying out laser SE doping, chain oxygen removal, PSG removal, alkali polishing, annealing oxidation, back coating, forward coating, laser grooving, screen printing and sintering on the silicon wafer subjected to the diffusion method, and then sorting and testing the efficiency of the finished battery piece.
According to the diffusion method of the solar cell, the shallow junction can be prepared through the cooperation of the two pre-oxidation treatments and the three power supply treatments, meanwhile, the doping non-uniformity is improved, and the blue light response of the solar cell can be improved by the shallow junction, so that the photoelectric conversion efficiency of the solar cell is improved. The diffusion method of the solar cell is simple in process and low in cost.
In the diffusion method of the solar cell, the oxygen inlet amount of the second pre-oxidation treatment is larger than that of the first pre-oxidation treatment, so that an oxide layer of a semiconductor substrate is formed, a shallow junction is formed, the surface concentration is reduced, the impurity concentration in the oxide layer of the semiconductor substrate is uniformly distributed, and the phosphorus source doping in the shallow junction is also further uniformly distributed.
In the diffusion method of the solar cell, the temperature of the first time of the through source treatment, the temperature of the second time of the through source treatment and the temperature of the third time of the through source treatment are sequentially increased, the nitrogen inlet amount of the first time of the through source treatment, the nitrogen inlet amount of the second time of the through source treatment and the nitrogen inlet amount of the third time of the through source treatment are sequentially increased, the high-concentration diffusion is carried out on the surface layer of the silicon wafer in a short time, so that a phosphorus-silicon glass layer with high doping concentration is formed on the surface of the silicon wafer only, and phosphorus atoms are uniformly distributed to push a system knot through high Wen Tongyang, thereby remarkably improving the diffusion uniformity and forming N + -N-P structure, reducing surface concentration. The post oxidation step is carried out under the oxygen-enriched condition, so that a layer of high-quality silicon-silicon dioxide interface with lower surface state density can be generated on the surface of the diffused silicon wafer, thereby effectively reducing surface recombination and further improving minority carrier lifetime and short-wave response.
The application also provides a solar cell which is manufactured according to the diffusion method of the solar cell.
A solar cell and a diffusion method thereof according to the present application are described in further detail below with reference to examples.
Example 1
The embodiment of the application provides a solar cell and a diffusion method thereof, which comprises the following steps:
s1, pretreatment
And (3) selecting 210 mm-diameter P-type monocrystalline silicon wafers, performing alkali texturing to form a texture similar to a pyramid structure on the surfaces of the silicon wafers, preparing surface textured silicon, vertically inserting the surface textured silicon wafers back to back into a quartz boat clamping groove, moving the silicon wafers into a low-pressure diffusion furnace tube by depending on a silicon carbide paddle, and wherein the pressure in the low-pressure diffusion furnace tube is 60Pa.
S2, first pre-oxidation treatment
And heating to 780 ℃, and introducing oxygen into the low-pressure diffusion furnace for 3min, wherein the oxygen inlet amount is 600sccm.
S3, first-time source processing
And heating to 790 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 5min, wherein the oxygen introducing amount is 600sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 800sccm.
S4, a second pre-oxidation treatment
And heating to 800 ℃, and introducing oxygen into the low-pressure diffusion furnace for 2min, wherein the oxygen inlet amount is 1000sccm.
S5, second-time source connection processing
At 800 ℃, introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into a low-pressure diffusion furnace for 2min, wherein the oxygen introducing amount is 800sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 1100sccm.
S6, third-time source processing
And heating to 810 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 2min, wherein the oxygen introducing amount is 1000sccm, and the nitrogen carrying phosphorus oxychloride introducing amount is 2000sccm.
S7, high-temperature oxidation treatment
Heating to 850 ℃ for 5min, and introducing oxygen into the low-pressure diffusion furnace for 4min, wherein the oxygen inlet amount is 600sccm.
S8, heat preservation
Stopping introducing oxygen, and maintaining the temperature at 850 ℃ for 5min.
S9, cooling and impurity removing
Cooling to 790 ℃ for 16 min.
S10, post-power processing
At 790 ℃, the mixed gas of oxygen and nitrogen carrying phosphorus oxychloride is introduced into the low-pressure diffusion furnace for 13min, the oxygen introduction amount is 800sccm, and the nitrogen carrying phosphorus oxychloride introduction amount is 1400sccm.
S11, post-oxidation treatment
Cooling to 780 ℃, introducing oxygen into the low-pressure diffusion furnace for 5min, wherein the oxygen inlet amount is 3500sccm, and then cooling to leave the boat.
S12, post-treatment
And (3) sequentially carrying out laser SE doping, chain oxygen removal, PSG removal, alkali polishing, annealing oxidation, back coating, forward coating, laser grooving, screen printing and sintering on the silicon wafer subjected to the diffusion method, and then sorting and testing the efficiency of the finished battery piece.
Example 2
The embodiment of the application provides a solar cell and a diffusion method thereof, which comprises the following steps:
s1, pretreatment
And (3) selecting 210 mm-diameter P-type monocrystalline silicon wafers, performing alkali texturing to form a texture similar to a pyramid structure on the surfaces of the silicon wafers, preparing surface textured silicon, vertically inserting the surface textured silicon wafers back to back into a quartz boat clamping groove, moving the silicon wafers into a low-pressure diffusion furnace tube by depending on a silicon carbide paddle, and wherein the pressure in the low-pressure diffusion furnace tube is 80Pa.
S2, first pre-oxidation treatment
And heating to 780 ℃, and introducing oxygen into the low-pressure diffusion furnace for 3min, wherein the oxygen inlet amount is 500sccm.
S3, first-time source processing
And heating to 790 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 3min, wherein the oxygen introducing amount is 500sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 800sccm.
S4, a second pre-oxidation treatment
And heating to 800 ℃, and introducing oxygen into the low-pressure diffusion furnace for 3min, wherein the oxygen inlet amount is 800sccm.
S5, second-time source connection processing
At 800 ℃, introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into a low-pressure diffusion furnace for 3min, wherein the oxygen introducing amount is 700sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 1000sccm.
S6, third-time source processing
And heating to 810 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 2.5min, wherein the oxygen introducing amount is 1000sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 1500sccm.
S7, high-temperature oxidation treatment
Heating to 845 ℃ for 5min, and introducing oxygen into the low-pressure diffusion furnace for 4.5min, wherein the oxygen inlet amount is 500sccm.
S8, heat preservation
Oxygen was stopped and incubated at 845℃for 6min.
S9, cooling and impurity removing
Cooling to 790 ℃ for 16 min.
S10, post-power processing
At 790 ℃, the mixed gas of oxygen and nitrogen carrying phosphorus oxychloride is introduced into the low-pressure diffusion furnace for 13min, the oxygen introduction amount is 800sccm, and the nitrogen carrying phosphorus oxychloride introduction amount is 1400sccm.
S11, post-oxidation treatment
Cooling to 780 ℃, introducing oxygen into the low-pressure diffusion furnace for 5.5min, wherein the oxygen inlet amount is 3000sccm, and then cooling to leave the boat.
S12, post-treatment
And (3) sequentially carrying out laser SE doping, chain oxygen removal, PSG removal, alkali polishing, annealing oxidation, back coating, forward coating, laser grooving, screen printing and sintering on the silicon wafer subjected to the diffusion method, and then sorting and testing the efficiency of the finished battery piece.
Example 3
The embodiment of the application provides a solar cell and a diffusion method thereof, which comprises the following steps:
s1, pretreatment
And (3) selecting 210 mm-diameter P-type monocrystalline silicon wafers, performing alkali texturing to form a texture similar to a pyramid structure on the surfaces of the silicon wafers, preparing surface textured silicon, vertically inserting the surface textured silicon wafers back to back into a quartz boat clamping groove, moving the silicon wafers into a low-pressure diffusion furnace tube by depending on a silicon carbide paddle, and wherein the pressure in the low-pressure diffusion furnace tube is 70Pa.
S2, first pre-oxidation treatment
And heating to 785 ℃, and introducing oxygen into the low-pressure diffusion furnace for 2min, wherein the oxygen inlet amount is 600sccm.
S3, first-time source processing
And heating to 795 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 2min, wherein the oxygen introducing amount is 600sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 900sccm.
S4, a second pre-oxidation treatment
And heating to 805 ℃, and introducing oxygen into the low-pressure diffusion furnace for 2min, wherein the oxygen inlet amount is 1000sccm.
S5, second-time source connection processing
At the temperature of 805 ℃, the mixed gas of oxygen and nitrogen carrying phosphorus oxychloride is introduced into the low-pressure diffusion furnace for 2min, the oxygen introduction amount is 800sccm, and the nitrogen carrying phosphorus oxychloride introduction amount is 1100sccm.
S6, third-time source processing
And heating to 815 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 2min, wherein the oxygen introducing amount is 1200sccm, and the nitrogen carrying phosphorus oxychloride introducing amount is 2000sccm.
S7, high-temperature oxidation treatment
Heating to 850 ℃ for 4min, and introducing oxygen into the low-pressure diffusion furnace for 4min, wherein the oxygen inlet amount is 600sccm.
S8, heat preservation
Stopping introducing oxygen, and maintaining the temperature at 850 ℃ for 5min.
S9, cooling and impurity removing
Cooling to 795 ℃ for 15 min.
S10, post-power processing
At the temperature of 795 ℃, introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into a low-pressure diffusion furnace for 12min, wherein the oxygen introducing amount is 900sccm, and the nitrogen carrying phosphorus oxychloride introducing amount is 1500sccm.
S11, post-oxidation treatment
Cooling to 785 ℃, introducing oxygen into the low-pressure diffusion furnace for 5min, wherein the oxygen inlet amount is 3500sccm, and then cooling to leave the boat.
S12, post-treatment
And (3) sequentially carrying out laser SE doping, chain oxygen removal, PSG removal, alkali polishing, annealing oxidation, back coating, forward coating, laser grooving, screen printing and sintering on the silicon wafer subjected to the diffusion method, and then sorting and testing the efficiency of the finished battery piece.
Comparative example 1
The comparative example of the present application provides a solar cell and a diffusion method thereof, which includes the steps of:
s1, pretreatment
And (3) selecting 210 mm-diameter P-type monocrystalline silicon wafers, performing alkali texturing to form a texture similar to a pyramid structure on the surfaces of the silicon wafers, preparing surface textured silicon, vertically inserting the surface textured silicon wafers back to back into a quartz boat clamping groove, moving the silicon wafers into a low-pressure diffusion furnace tube by depending on a silicon carbide paddle, and wherein the pressure in the low-pressure diffusion furnace tube is 60Pa.
S2, pre-oxidation treatment
And heating to 795 ℃, and introducing oxygen into the low-pressure diffusion furnace for 4min, wherein the oxygen inlet amount is 660sccm and the oxygen inlet amount is 1045sccm.
S3, first-time source processing
At 795 ℃, introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into a low-pressure diffusion furnace for 5min, wherein the oxygen introducing amount is 660sccm, and the nitrogen carrying phosphorus oxychloride introducing amount is 1250sccm.
S4, second-time source processing
And heating to 800 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 2min, wherein the oxygen inlet amount is 660sccm, and the nitrogen inlet amount carrying phosphorus oxychloride is 1250sccm.
S5, high-temperature oxidation treatment
Heating to 845 ℃ for 5min, and introducing oxygen into the low-pressure diffusion furnace for 4min, wherein the oxygen inlet amount is 600sccm.
S6, heat preservation
Oxygen was stopped and incubated at 845℃for 6min.
S7, cooling and impurity removing
The temperature is reduced to 780 ℃ during the use for 16 min.
S8, post-power processing
At 770 ℃, the mixed gas of oxygen and nitrogen carrying phosphorus oxychloride is introduced into the low-pressure diffusion furnace for 13min, wherein the introduced amount of the oxygen is 800sccm, and the introduced amount of the nitrogen carrying phosphorus oxychloride is 1400sccm.
S9, post-oxidation treatment
Oxygen was introduced into the low pressure diffusion furnace for 3min at an oxygen introduction rate of 1500sccm, and then cooled off the boat.
S10, post-treatment
And (3) sequentially carrying out laser SE doping, chain oxygen removal, PSG removal, alkali polishing, annealing oxidation, back coating, forward coating, laser grooving, screen printing and sintering on the silicon wafer subjected to the diffusion method, and then sorting and testing the efficiency of the finished battery piece.
Comparative example 2
The comparative example of the present application provides a solar cell and a diffusion method thereof, which includes the steps of:
s1, pretreatment
And (3) selecting 210 mm-diameter P-type monocrystalline silicon wafers, performing alkali texturing to form a texture similar to a pyramid structure on the surfaces of the silicon wafers, preparing surface textured silicon, vertically inserting the surface textured silicon wafers back to back into a quartz boat clamping groove, moving the silicon wafers into a low-pressure diffusion furnace tube by depending on a silicon carbide paddle, and wherein the pressure in the low-pressure diffusion furnace tube is 60Pa.
S2, first pre-oxidation treatment
And heating to 780 ℃, and introducing oxygen into the low-pressure diffusion furnace for 3min, wherein the oxygen inlet amount is 600sccm.
S3, first-time source processing
And heating to 790 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 5min, wherein the oxygen introducing amount is 600sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 800sccm.
S4, second-time source processing
And heating to 800 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 2min, wherein the oxygen inlet amount is 800sccm, and the nitrogen inlet amount carrying phosphorus oxychloride is 1100sccm.
S5, third-time source processing
And heating to 810 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 2min, wherein the oxygen introducing amount is 1000sccm, and the nitrogen carrying phosphorus oxychloride introducing amount is 2000sccm.
S6, high-temperature oxidation treatment
Heating to 850 ℃ for 5min, and introducing oxygen into the low-pressure diffusion furnace for 4min, wherein the oxygen inlet amount is 600sccm.
S7, heat preservation
Stopping introducing oxygen, and maintaining the temperature at 850 ℃ for 5min.
S8, cooling and impurity removing
Cooling to 790 ℃ for 16 min.
S9, post-power processing
At 790 ℃, the mixed gas of oxygen and nitrogen carrying phosphorus oxychloride is introduced into the low-pressure diffusion furnace for 13min, the oxygen introduction amount is 800sccm, and the nitrogen carrying phosphorus oxychloride introduction amount is 1400sccm.
S10, post-oxidation treatment
Cooling to 780 ℃, introducing oxygen into the low-pressure diffusion furnace for 5min, wherein the oxygen inlet amount is 3500sccm, and then cooling to leave the boat.
S11, post-treatment
And (3) sequentially carrying out laser SE doping, chain oxygen removal, PSG removal, alkali polishing, annealing oxidation, back coating, forward coating, laser grooving, screen printing and sintering on the silicon wafer subjected to the diffusion method, and then sorting and testing the efficiency of the finished battery piece.
Comparative example 3
The comparative example of the present application provides a solar cell and a diffusion method thereof, which includes the steps of:
s1, pretreatment
And (3) selecting 210 mm-diameter P-type monocrystalline silicon wafers, performing alkali texturing to form a texture similar to a pyramid structure on the surfaces of the silicon wafers, preparing surface textured silicon, vertically inserting the surface textured silicon wafers back to back into a quartz boat clamping groove, moving the silicon wafers into a low-pressure diffusion furnace tube by depending on a silicon carbide paddle, and wherein the pressure in the low-pressure diffusion furnace tube is 60Pa.
S2, first pre-oxidation treatment
And heating to 780 ℃, and introducing oxygen into the low-pressure diffusion furnace for 3min, wherein the oxygen inlet amount is 600sccm.
S3, first-time source processing
And heating to 790 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 5min, wherein the oxygen introducing amount is 600sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 800sccm.
S4, a second pre-oxidation treatment
And heating to 800 ℃, and introducing oxygen into the low-pressure diffusion furnace for 2min, wherein the oxygen inlet amount is 600sccm.
S5, second-time source connection processing
At 800 ℃, introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into a low-pressure diffusion furnace for 2min, wherein the oxygen introducing amount is 800sccm, and the nitrogen introducing amount carrying phosphorus oxychloride is 1100sccm.
S6, third-time source processing
And heating to 810 ℃, and introducing mixed gas of oxygen and nitrogen carrying phosphorus oxychloride into the low-pressure diffusion furnace for 2min, wherein the oxygen introducing amount is 1000sccm, and the nitrogen carrying phosphorus oxychloride introducing amount is 2000sccm.
S7, high-temperature oxidation treatment
Heating to 850 ℃ for 5min, and introducing oxygen into the low-pressure diffusion furnace for 4min, wherein the oxygen inlet amount is 600sccm.
S8, heat preservation
Stopping introducing oxygen, and maintaining the temperature at 850 ℃ for 5min.
S9, cooling and impurity removing
Cooling to 790 ℃ for 16 min.
S10, post-power processing
At 790 ℃, the mixed gas of oxygen and nitrogen carrying phosphorus oxychloride is introduced into the low-pressure diffusion furnace for 13min, the oxygen introduction amount is 800sccm, and the nitrogen carrying phosphorus oxychloride introduction amount is 1400sccm.
S11, post-oxidation treatment
Cooling to 780 ℃, introducing oxygen into the low-pressure diffusion furnace for 5min, wherein the oxygen inlet amount is 3500sccm, and then cooling to leave the boat.
S12, post-treatment
And (3) sequentially carrying out laser SE doping, chain oxygen removal, PSG removal, alkali polishing, annealing oxidation, back coating, forward coating, laser grooving, screen printing and sintering on the silicon wafer subjected to the diffusion method, and then sorting and testing the efficiency of the finished battery piece.
Test example 1
The solar cell sheets prepared in example 1 and comparative examples 1 to 3 were each measured for sheet resistance and ECV curve, the sheet resistance is shown in table 1, and the ECV curve is shown in fig. 2.
Table 1 sheet resistance of solar cell sheets produced in example 1 and comparative examples 1 to 3
As is clear from table 1, the non-uniformity of the sheet resistance of the solar cell manufactured by the diffusion method of the solar cell of the present application was significantly reduced as is evident from the comparison of example 1 and comparative example 1.
As can be seen from the comparison between example 1 and comparative example 2, comparative example 2 does not have the second pre-oxidation treatment, and the non-uniformity of the sheet resistance of the solar cell manufactured by the diffusion method of the solar cell of comparative example 2 is significantly improved as compared to example 1.
As is clear from the comparison between example 1 and comparative example 3, the second pre-oxidation treatment and the first pre-oxidation treatment in comparative example 3 have the same oxidation introduction amount, and the non-uniformity of the sheet resistance of the solar cell manufactured by the diffusion method of the solar cell of comparative example 3 is significantly improved as compared with example 1.
As is clear from FIG. 2, the junction depth of the solar cell manufactured by the diffusion method of the solar cell of the present application is significantly reduced, and the junction depth is 0.20 to 0.25. Mu.m.
Test example 2
The solar cell sheets obtained in example 1 and comparative examples 1 to 3 were taken out, respectively, and the properties thereof were measured as shown in table 2.
Table 2 properties of solar cell sheets produced in example 1 and comparative examples 1 to 3
| Project | Ncell | Uoc | Isc | FF | Rser | Rsh | IRev2 |
| Example 1 | 23.065 | 0.6923 | 18.296 | 80.30 | 0.00156 | 436.89 | 0.08977 |
| Comparative example 1 | 23.021 | 0.6905 | 18.284 | 80.40 | 0.00151 | 419.65 | 0.09114 |
| Comparative example 2 | 23.011 | 0.6915 | 18.291 | 80.22 | 0.00149 | 444.23 | 0.08989 |
| Comparative example 3 | 22.982 | 0.6910 | 18.256 | 80.33 | 0.00151 | 423.45 | 0.0889 |
As can be seen from table 2, the comparison of example 1 and comparative example 1 shows that the open circuit voltage, short circuit current and photoelectric conversion efficiency of the solar cell manufactured by the diffusion method of the solar cell of the present application are significantly improved.
The above description is only of specific embodiments of the application and is not intended to limit the application, but various modifications and variations can be made by those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present application should be included in the protection scope of the present application.
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