CN215985925U - Device for on-line detecting sulfite content of wet desulphurization slurry - Google Patents
Device for on-line detecting sulfite content of wet desulphurization slurry Download PDFInfo
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- CN215985925U CN215985925U CN202122068441.3U CN202122068441U CN215985925U CN 215985925 U CN215985925 U CN 215985925U CN 202122068441 U CN202122068441 U CN 202122068441U CN 215985925 U CN215985925 U CN 215985925U
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Abstract
The utility model discloses a device for detecting the content of sulfite in wet desulphurization slurry on line, wherein a sampling port of a gypsum slurry main pipe is communicated with an inlet of a settling tank, an outlet on the side surface of the top of the settling tank is communicated with an inlet of a reactor, an outlet on the bottom of the settling tank is communicated with an inlet of a pit of an absorption tower, an outlet on the bottom of the reactor is communicated with an inlet of a wastewater tank, an outlet of an iodine standard solution tank is communicated with the inlet of the reactor through a first titration pump, an outlet of a sodium thiosulfate standard solution tank is communicated with the inlet of the reactor through a second titration pump, a stirrer is arranged in the reactor, an oxidation reduction electrode is inserted into the reactor, and the redox electrode is connected with a data processing center, the data processing center is connected with a control center, the control center is connected with a first titration pump and a second titration pump, and the device can detect the content of the sulfite in the wet desulphurization slurry on line.
Description
Technical Field
The utility model belongs to the technical field of chemistry, and relates to a device for detecting the content of sulfite in wet desulphurization slurry on line.
Background
At present, the thermal power plant mainly adopts a limestone-gypsum wet desulphurization process to remove SO generated in the combustion process2The by-product gypsum (CaSO) can be further produced by oxidation of an oxidation fan4·2H2O), sulfite is generated when the oxidation is insufficient, and the sulfite content of the slurry can reflect the oxidation degree of the slurry. The content of sulfite in the slurry is determined, so that the accurate adjustment of the oxidation air quantity is facilitated, the quality of gypsum is ensured, and the safe and energy-saving operation and automatic control of a desulfurization system are realized.
At present, no effective method for measuring the content of sulfite in the slurry exists, belt conveyor gypsum or absorption tower slurry is measured in a whole manner, a manual sampling-laboratory detection method is mainly adopted, and no effective method for measuring the content of sulfite in the gypsum or absorption tower slurry in a whole manner on line exists.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the defects of the prior art and provides a device for detecting the content of sulfite in wet desulphurization slurry on line, which can detect the content of sulfite in wet desulphurization slurry on line.
In order to achieve the aim, the device for detecting the content of the sulfite in the wet desulphurization slurry on line comprises a gypsum slurry main pipe, a control center, a data processing center, a settling tank, a reactor, an absorption tower pit, a wastewater tank, an iodine standard solution tank, a sodium thiosulfate standard solution tank, a first titration pump, a second titration pump, a stirrer and an oxidation-reduction electrode;
the sampling port of the gypsum slurry main pipe is communicated with the inlet of a settling tank, the outlet of the side surface of the top of the settling tank is communicated with the inlet of a reactor, the outlet of the bottom of the settling tank is communicated with the inlet of an absorption tower pit, the outlet of the bottom of the reactor is communicated with the inlet of a waste water tank, the outlet of an iodine standard solution tank is communicated with the inlet of the reactor through a first titration pump, the outlet of a sodium thiosulfate standard solution tank is communicated with the inlet of the reactor through a second titration pump, a stirrer is arranged in the reactor, an oxidation-reduction electrode is inserted into the reactor and is connected with a data processing center, the data processing center is connected with a control center, and the control center is connected with the first titration pump and the second titration pump.
The sampling port of the gypsum slurry main pipe is communicated with the inlet of the settling tank through a first peristaltic pump, and the control center is connected with the first peristaltic pump.
An outlet on the side surface of the top of the settling tank is communicated with an inlet of the reactor through a second peristaltic pump, and a control center is connected with the second peristaltic pump.
The bottom outlet of the settling tank is communicated with the inlet of the absorption tower pit through a third peristaltic pump, and the control center is connected with the third peristaltic pump.
The bottom outlet of the reactor is communicated with the inlet of the waste water tank through a fourth peristaltic pump, and the control center is connected with the fourth peristaltic pump.
The device also comprises a deionized water tank; the outlet of the deionized water tank is communicated with the inlet of the reactor.
The outlet of the deionized water tank is communicated with the inlet of the reactor through a fifth peristaltic pump, and the control center is connected with the fifth peristaltic pump.
The utility model has the following beneficial effects:
when the device for detecting the content of the sulfite in the wet desulphurization slurry on line is operated specifically, the content of sulfite in the slurry is accurately measured on the basis of an indirect iodometry, specifically, the slurry is settled firstly, then the supernatant is introduced into a reactor to improve the accuracy of measurement, then adding an iodine standard solution into the reactor, reacting the iodine standard solution with the supernatant, then dropwise adding a sodium thiosulfate standard solution, finally calculating the sulfite content of the wet desulphurization slurry according to the concentration of the iodine standard solution, the addition amount of the iodine standard solution, the concentration of the sodium thiosulfate standard solution, the dropwise adding amount of the sodium thiosulfate standard solution and the addition amount of the supernatant, to realize the online measurement of the sulfite content of the wet desulphurization slurry, it is noted that the reaction time required by the utility model is short, and meanwhile, acid is not used, SO that the conversion of sulfite into SO is reduced.2Later overflow from the system makes inaccurate measurement possible, and the volatility of iodine under an open system is fully considered, so that the test is more accurate.
Drawings
FIG. 1 is a block diagram of the present invention;
wherein, 1 is a gypsum slurry mother pipe, 2 is a control center, 3 is a data processing center, 4 is a settling tank, 5 is a reactor, 6 is an absorption tower pit, 7 is a wastewater tank, 8 is an iodine standard solution tank, 9 is a sodium thiosulfate standard solution tank, 10 is a deionized water tank, 11 is a first peristaltic pump, 12 is a second peristaltic pump, 13 is a third peristaltic pump, 14 is a fourth peristaltic pump, 15 is a fifth peristaltic pump, 16 is a first titration pump, 17 is a second titration pump, 18 is a stirrer, and 19 is an oxidation-reduction electrode.
Detailed Description
In order to make the technical solutions of the present invention better understood, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, not all of the embodiments, and are not intended to limit the scope of the present disclosure. Moreover, in the following description, descriptions of well-known structures and techniques are omitted so as to not unnecessarily obscure the concepts of the present disclosure. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
There is shown in the drawings a schematic block diagram of a disclosed embodiment in accordance with the utility model. The figures are not drawn to scale, wherein certain details are exaggerated and possibly omitted for clarity of presentation. The shapes of various regions, layers and their relative sizes and positional relationships shown in the drawings are merely exemplary, and deviations may occur in practice due to manufacturing tolerances or technical limitations, and a person skilled in the art may additionally design regions/layers having different shapes, sizes, relative positions, according to actual needs.
Referring to fig. 1, the device for detecting the content of sulfite in wet desulfurization slurry on line according to the present invention includes a gypsum slurry mother pipe 1, a control center 2, a data processing center 3, a settling tank 4, a reactor 5, an absorption tower pit 6, a wastewater tank 7, an iodine standard solution tank 8, a sodium thiosulfate standard solution tank 9, a deionized water tank 10, a first peristaltic pump 11, a second peristaltic pump 12, a third peristaltic pump 13, a fourth peristaltic pump 14, a fifth peristaltic pump 15, a first titration pump 16, a second titration pump 17, a stirrer 18, and a redox electrode 19;
the sampling port of the gypsum slurry mother pipe 1 is communicated with the inlet of a settling tank 4 through a first peristaltic pump 11, the outlet of the side surface of the top of the settling tank 4 is communicated with the inlet of a reactor 5 through a second peristaltic pump 12, the outlet of the bottom of the settling tank 4 is communicated with the inlet of an absorption tower pit 6 through a third peristaltic pump 13, the outlet of the bottom of the reactor 5 is communicated with the inlet of a waste water tank 7 through a fourth peristaltic pump 14, the outlet of an iodine standard solution tank 8 is communicated with the inlet of the reactor 5 through a first titration pump 16, the outlet of a sodium thiosulfate standard solution tank 9 is communicated with the inlet of the reactor 5 through a second titration pump 17, the outlet of a deionized water tank 10 is communicated with the inlet of the reactor 5 through a fifth peristaltic pump 15, a stirrer 18 is arranged in the reactor 5, an oxidation-reduction electrode 19 is inserted in the reactor 5, and the oxidation-reduction electrode 19 is connected with a data processing center 3, the data processing center 3 is connected with the control center 2, and the control center 2 is connected with a first peristaltic pump 11, a second peristaltic pump 12, a third peristaltic pump 13, a fourth peristaltic pump 14, a fifth peristaltic pump 15, a first titration pump 16 and a second titration pump 17.
The specific working process of the utility model is as follows:
1) starting a first peristaltic pump 11, quantitatively delivering the slurry in a 1-1.5L gypsum slurry mother pipe 1 into a settling tank 4 for settling for 15-30min, then quantitatively delivering 50-100mL of supernatant into a reactor 5 through a second peristaltic pump 12, and starting a stirrer 18, wherein the rotating speed of the stirrer 18 is 400-700 rpm;
2) starting a third peristaltic pump 13, discharging the residual slurry in the settling tank 4 into the absorption tower pit 6, and then closing the third peristaltic pump 13;
3) starting a first titration pump 16, adding a certain amount of iodine standard solution with known concentration, and fully reacting with the supernatant under the stirring of a stirrer 18, wherein the concentration of the iodine standard solution is 0.02-0.1mol/L, the addition amount of the iodine standard solution is 3-10mL, and the reaction time of the supernatant and the iodine standard solution is 10-20 min;
4) starting a second titration pump 17, dropwise adding a sodium thiosulfate standard solution with a known concentration, wherein the concentration of the sodium thiosulfate standard solution is 0.04-0.2mol/L, judging the reaction end point of the residual iodine standard solution and the sodium thiosulfate standard solution through data obtained by measuring an oxidation-reduction electrode 19 to obtain the dropwise adding amount of the sodium thiosulfate standard solution, and simultaneously closing the second titration pump 17;
5) opening a fourth peristaltic pump 14, discharging the liquid in the reactor 5 into the waste water tank 7, and then closing the fourth peristaltic pump 14; starting a fifth peristaltic pump 15, adding 150mL of deionized water, and cleaning the reactor 5, the stirrer 18 and the redox electrode 19;
6) and calculating the sulfite content of the wet desulphurization slurry according to the effective concentration of the iodine standard solution, the addition amount of the iodine standard solution, the concentration of the sodium thiosulfate standard solution, the dropwise addition amount of the sodium thiosulfate standard solution and the addition amount of the supernatant.
The process for determining the effective concentration of the iodine standard solution in the laboratory comprises the following steps:
11) adding deionized water in the same volume as the supernatant added to the reactor 5 to the beaker;
12) adding the same volume of iodine standard solution as that added to the reactor 5 into the beaker;
13) stirring for full reaction, wherein the stirring speed and the reaction time are the same as those in the step 3);
14) dropwise adding a sodium thiosulfate standard solution with the same concentration as the sodium thiosulfate standard solution added into the reactor 5 into a beaker to obtain the effective concentration of the iodine standard solution
Comprises the following steps:
wherein the content of the first and second substances,
is the addition amount of the standard iodine solution,
the concentration of the standard sodium thiosulfate is the standard,
the sodium thiosulfate standard solution is added, wherein the calculation process is realized by a multiplier and a divider.
Calculating the sulfite content c of the wet desulfurization slurrySulfite saltComprises the following steps:
wherein, cSulfite saltIs the sulfite concentration of the slurry，vSupernatant fluidFor the volume of supernatant pumped from the settling tank 4 into the reactor 5, this calculation is carried out by means of multipliers, subtractors and dividers.
The applicant states that the present invention is described by the above embodiments, but the present invention is not limited to the above embodiments, i.e. the present invention is not limited to the above embodiments. It will be apparent to those skilled in the art that any modifications of the present invention are within the scope and disclosure of the present invention.
Claims (7)
1. The device for detecting the content of sulfite in the wet desulphurization slurry on line is characterized by comprising a gypsum slurry main pipe (1), a control center (2), a data processing center (3), a settling tank (4), a reactor (5), an absorption tower pit (6), a wastewater tank (7), an iodine standard solution tank (8), a sodium thiosulfate standard solution tank (9), a first titration pump (16), a second titration pump (17), a stirrer (18) and a redox electrode (19);
a sampling port of a gypsum slurry main pipe (1) is communicated with an inlet of a settling tank (4), an outlet of the side surface of the top of the settling tank (4) is communicated with an inlet of a reactor (5), an outlet of the bottom of the settling tank (4) is communicated with an inlet of an absorption tower pit (6), an outlet of the bottom of the reactor (5) is communicated with an inlet of a waste water tank (7), an outlet of an iodine standard solution tank (8) is communicated with an inlet of the reactor (5) through a first titration pump (16), an outlet of a sodium thiosulfate standard solution tank (9) is communicated with an inlet of the reactor (5) through a second titration pump (17), a stirrer (18) is arranged in the reactor (5), an oxidation-reduction electrode (19) is inserted into the reactor (5), the oxidation-reduction electrode (19) is connected with a data processing center (3), the data processing center (3) is connected with a control center (2), the control center (2) is connected with a first titration pump (16) and a second titration pump (17).
2. The device for detecting the sulfite content of the wet desulphurization slurry on line according to claim 1, wherein a sampling port of the gypsum slurry mother pipe (1) is communicated with an inlet of the settling tank (4) through a first peristaltic pump (11), and the control center (2) is connected with the first peristaltic pump (11).
3. The device for on-line detection of the sulfite content in the wet desulfurization slurry according to claim 2, wherein an outlet on the top side of the settling tank (4) is communicated with an inlet of the reactor (5) through a second peristaltic pump (12), and the control center (2) is connected with the second peristaltic pump (12).
4. The device for on-line detection of the sulfite content in the wet desulfurization slurry according to claim 3, wherein the bottom outlet of the settling tank (4) is communicated with the inlet of the absorption tower pit (6) through a third peristaltic pump (13), and the control center (2) is connected with the third peristaltic pump (13).
5. The device for on-line detection of the sulfite content in the wet desulfurization slurry according to claim 4, wherein the bottom outlet of the reactor (5) is communicated with the inlet of the wastewater tank (7) through a fourth peristaltic pump (14), and the control center (2) is connected with the fourth peristaltic pump (14).
6. The device for detecting the sulfite content of the wet desulphurization slurry on line according to claim 5, further comprising a deionized water tank (10); the outlet of the deionized water tank (10) is communicated with the inlet of the reactor (5).
7. The device for on-line detection of the sulfite content in the wet desulfurization slurry according to claim 6, wherein an outlet of the deionized water tank (10) is communicated with an inlet of the reactor (5) through a fifth peristaltic pump (15), and the control center (2) is connected with the fifth peristaltic pump (15).
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115121099A (en) * | 2022-07-14 | 2022-09-30 | 西安热工研究院有限公司 | Integrated online control desulfurization slurry oxidation and wastewater discharge device and method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115121099A (en) * | 2022-07-14 | 2022-09-30 | 西安热工研究院有限公司 | Integrated online control desulfurization slurry oxidation and wastewater discharge device and method |
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