CN202688017U - Powdered activated carbon dosing equipment used for water treatment - Google Patents
Powdered activated carbon dosing equipment used for water treatment Download PDFInfo
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- CN202688017U CN202688017U CN 201220388720 CN201220388720U CN202688017U CN 202688017 U CN202688017 U CN 202688017U CN 201220388720 CN201220388720 CN 201220388720 CN 201220388720 U CN201220388720 U CN 201220388720U CN 202688017 U CN202688017 U CN 202688017U
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Abstract
The utility model discloses powdered activated carbon dosing equipment used for water treatment. The powdered activated carbon dosing equipment comprises a dry powder storage feeding system, a solution stirring system and a slurry feeding system. A discharging port of the dry powder storage feeding system is connected with a feeding port of the solution stirring system. A discharging port of the solution stirring system is connected with a feeding port of the slurry feeding system. The powdered activated carbon dosing equipment is a complete set of equipment which can automatically carry out quantitative mix proportioning and quantitative feeding for powdered activated carbon, and has the advantages of being high in the automation degree, little in manual operation, visual in human-computer interface, easy and convenient to operate, simple in structure, attractive in appearance, stable and reliable in system, little in powder pollution, high in powder utilization rate, high in working efficiency, uniform and precise in feeding, and the like.
Description
Technical field
The utility model relates to a kind of pharmacy and liquid chemical feeding equipment, relates in particular to a kind of Powdered Activated Carbon medicine machine for water treatment.
Background technology
The organic pollutant of Powdered Activated Carbon to dissolving in the water has stronger adsorptive power such as haloform and precursor substance, tetracol phenixin, benzene class, phenolic compound etc.Organic compound of colourity, foreign odor, peculiar smell, methylenum coeruleum surfactant, weedicide, sterilant, agricultural chemicals, synthetic detergent, synthetic dyestuff, aminated compounds and many synthetic etc. there is preferably removal effect.To some heavy metal compound, such as mercury, lead, iron, nickel, chromium, zinc, cobalt etc. stronger adsorptive power is arranged also, therefore in the situation that present former water is subject to organism, algae, colourity, heavy metal contamination or have foreign odor to distinguish the flavor of, adding Powdered Activated Carbon has become a kind of efficient solution, its effectively deodorizing, except look with reduce organic content.And the Powdered Activated Carbon medicine machine carries out the nucleus equipment of water treatment just with Powdered Activated Carbon.
In the prior art, the Powdered Activated Carbon adding equipment that each water factory uses, exist serious such as dust pollution, operational condition is abominable, the serious harm workman's is healthy, affect simultaneously the integrated environment of water factory, manual operation is many, and manipulation strength is large, the utilising efficiency of Powdered Activated Carbon is low, the problem such as can not realize continuously, add accurately.
Summary of the invention
The purpose of this utility model provides a kind of Powdered Activated Carbon medicine machine for water treatment with regard to being in order to address the above problem.
The utility model is achieved through the following technical solutions above-mentioned purpose:
The utility model comprises that dry powder stores feeding system, solution stirring system and slurries dosing system, the discharge port of described dry powder storage feeding system is connected with the opening for feed of described solution stirring system, and the discharge port of described solution stirring system is connected with the opening for feed of described slurries dosing system.
Described dry powder stores feeding system and comprises vacuum feeder, hopper, storage bin, level gage, shaking device, discharge valve and quantitative worm conveyor, the discharge port of described vacuum feeder is connected with the entrance of described hopper, the outlet of described hopper is connected with the entrance of described storage bin, the discharge port of described storage bin is provided with described discharge valve, the discharge port of described storage bin is connected with the feeding mouth of described quantitative worm conveyor, the discharge port of described quantitative worm conveyor is the discharge port that described dry powder stores feeding system, and described shaking device and described level gage all are installed on the described storage bin.
Described solution stirring system comprises the first feed valve, the second feed valve, the first stirrer, the second stirrer, the first water intaking valve, the second water intaking valve, the first NaOH solution tank NaOH, the second NaOH solution tank NaOH, the first liquidometer, the second liquidometer, the first bleeder valve, the second bleeder valve and solution are filled with shutdown valve, the discharge port that described dry powder stores feeding system simultaneously with described the first feed valve be connected the opening for feed of the second feed valve and be connected, the discharge port of described the first feed valve 9 is connected with the opening for feed of described the first NaOH solution tank NaOH, the upper end of described the first NaOH solution tank NaOH is equipped with described the first stirrer, the epimere of described the first NaOH solution tank NaOH is equipped with described the first water intaking valve, the hypomere of described the first NaOH solution tank NaOH is equipped with described the first bleeder valve, the discharge port of described the second feed valve is connected with the opening for feed of described the second NaOH solution tank NaOH, the upper end of described the second NaOH solution tank NaOH is equipped with described the second stirrer, the epimere of described the second NaOH solution tank NaOH is equipped with described the second water intaking valve, the hypomere of described the second NaOH solution tank NaOH is equipped with described the second bleeder valve, the discharge port of described the first bleeder valve is connected with the opening for feed of described shutdown valve by pipeline, the discharge port of described shutdown valve is connected by the discharge port of pipeline with described the second bleeder valve, described the first liquidometer is installed on described the first NaOH solution tank NaOH, described the second liquidometer is installed on described the second NaOH solution tank NaOH, described the first water intaking valve all is connected with the water source with the water-in of described the second water intaking valve, and the discharge port of described the second bleeder valve is the discharge port of described solution stirring system.
Described slurries dosing system comprises spiral pump shutdown valve and spiral pump, the opening for feed of described spiral pump shutdown valve is connected with the discharge port of described solution stirring system, the discharge port of described spiral pump shutdown valve is connected with the opening for feed of described spiral pump, and the discharge port of described spiral pump is the discharge port of described Powdered Activated Carbon medicine machine for water treatment.
The beneficial effects of the utility model are:
The utility model is the suite of equipment that Powdered Activated Carbon is automatically carried out quantitative proportioning, quantitatively adds, have level of automation high, manual operation is few, intuitively man-machine interface, simple, convenient, simple in structure, handsome in appearance, system stability is reliable, dust pollution is little, powder using efficiency is high, high efficiency, and the advantage such as feed intake even, accurate.
Description of drawings
Fig. 1 is the structural representation of the Powdered Activated Carbon medicine machine for water treatment described in the utility model.
Among the figure: the 1-vacuum feeder, the 2-hopper, the 3-storage bin, the 4-level gage, the 5-shaking device, the 6-discharge valve, the quantitative worm conveyor of 7-, 8-the first stirrer, 9-the first feed valve, 10-the second feed valve, 11-the second stirrer, 12-the second NaOH solution tank NaOH, 13-spiral pump shutdown valve, the 14-spiral pump, 15-the second bleeder valve, 16-the second liquidometer, 17-the second water intaking valve, 18-solution is filled with shutdown valve, 19-the first NaOH solution tank NaOH, 20-the first bleeder valve, 21-the first liquidometer, 22-the first water intaking valve.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing:
As shown in Figure 1: the utility model comprises that dry powder stores feeding system, solution stirring system and slurries dosing system, the discharge port of dry powder storage feeding system is connected with the opening for feed of solution stirring system, and the discharge port of solution stirring system is connected with the opening for feed of slurries dosing system.
As shown in Figure 1: dry powder stores feeding system and comprises vacuum feeder 1, hopper 2, storage bin 3, level gage 4, shaking device 5, discharge valve 6 and quantitative worm conveyor 7, the discharge port of vacuum feeder 1 is connected with the entrance of hopper 2, the outlet of hopper 2 is connected with the entrance of storage bin 3, the discharge port of storage bin 3 is provided with discharge valve 6, the discharge port of storage bin 3 is connected with the feeding mouth of quantitative worm conveyor 7, quantitatively the discharge port of worm conveyor 7 is the discharge port that dry powder stores feeding system, and shaking device 5 and level gage 4 all are installed on the storage bin 3.The material level of storage bin 3 is detected by the level gage 4 of installing on the storage bin 3, when level gage 4 detects Powdered Activated Carbon in the storage bin 3 and is in low material level, automatic-prompting (warning) needs reinforced, manually the active carbon powder material is utilized vacuum feeder 1 that active carbon powder is sucked in the storage bin 3, after the Powdered Activated Carbon in the storage bin 3 reached high charge level, automatic-prompting stopped to feed in raw material.When level gage 4 detects that Powdered Activated Carbon is in low material level in the feed bin of metering conveyor, automatically open storage bin 3 bottom discharge valves 6, Powdered Activated Carbon is flowed automatically in the opening for feed of quantitative worm conveyor 7, when quantitatively the Powdered Activated Carbon in the worm conveyor 7 is in high charge level, discharge valve 6 autoshutdowns.
As shown in Figure 1: the solution stirring system comprises the first feed valve 9, the second feed valve 10, the first stirrer 8, the second stirrer 11, the first water intaking valve 22, the second water intaking valve 17, the first NaOH solution tank NaOH 19, the second NaOH solution tank NaOH 12, the first liquidometer 21, the second liquidometer 16, the first bleeder valve 20, the second bleeder valve 15 and solution are filled with shutdown valve 18, the discharge port that dry powder stores feeding system simultaneously with the first feed valve 9 be connected the opening for feed of feed valve 10 and be connected, the discharge port of the first feed valve 9 is connected with the opening for feed of the first NaOH solution tank NaOH 19, the upper end of the first NaOH solution tank NaOH 19 is equipped with the first stirrer 8, the epimere of the first NaOH solution tank NaOH 19 is equipped with the first water intaking valve 22, the hypomere of the first NaOH solution tank NaOH 19 is equipped with the first bleeder valve 20, the discharge port of the second feed valve 10 is connected with the opening for feed of the second NaOH solution tank NaOH 12, the upper end of the second NaOH solution tank NaOH 12 is equipped with the second stirrer 11, the epimere of the second NaOH solution tank NaOH 12 is equipped with the second water intaking valve 17, the hypomere of the second NaOH solution tank NaOH 12 is equipped with the second bleeder valve 15, the discharge port of the first bleeder valve 20 is connected by the opening for feed of pipeline with NaOH solution tank NaOH shutdown valve 18, the discharge port that solution is filled with shutdown valve 18 is connected by the discharge port of pipeline with the second bleeder valve 15, the first liquidometer 21 is installed on the first NaOH solution tank NaOH 19, the second liquidometer 16 is installed on the second NaOH solution tank NaOH 12, the first water intaking valve 22 all is connected with the water source with the water-in of the second water intaking valve 17, and the discharge port of the second bleeder valve 15 is the discharge port of solution stirring system.Open the first water intaking valve 22 and the second water intaking valve 17, when the first NaOH solution tank NaOH 19 and the second NaOH solution tank NaOH 12 interior liquid levels during to middle liquid level, open the first stirrer 8 and the second stirrer 11, open the first bleeder valve 20 and the second bleeder valve 15, quantitative worm conveyor 7 autoshutdowns when the active carbon powder that adds reaches set amount, when the first NaOH solution tank NaOH 19 and the second NaOH solution tank NaOH 12 interior liquid levels autoshutdown the first water intaking valve 22 and the second water intaking valve 17 after the high liquid level, after slurry agitation dilution evenly, can enter the state of adding.Agitator is continuously operation.
As shown in Figure 1: the slurries dosing system comprises spiral pump shutdown valve 13 and spiral pump 14, the opening for feed of spiral pump shutdown valve 13 is connected with the discharge port of solution stirring system, the discharge port of spiral pump shutdown valve 13 is connected with the opening for feed of spiral pump 14, and the discharge port of spiral pump 14 is the discharge port that is used for the Powdered Activated Carbon medicine machine of water treatment.Open the first bleeder valve 20 and second bleeder valve 15 of the first NaOH solution tank NaOH 19 and the second NaOH solution tank NaOH 12, start spiral pump 14, according to raw water flow, by the automatic adjusting screw(rod) pump 14 of frequency transformer, the control dosage.When the first NaOH solution tank NaOH 19 is intact to low liquid level and the second NaOH solution tank NaOH 12 inner liquid medicine proportionings, automatically switch to the second NaOH solution tank NaOH 12.If the first NaOH solution tank NaOH 19 and the second NaOH solution tank NaOH 12 are low liquid level, then termination of pumping is reported to the police.
The utility model also has automatic control and test section, is mainly used in the electrical equipment of a whole set of chemicals dosing plant and control and the monitoring of instrument.
Claims (4)
1. Powdered Activated Carbon medicine machine that is used for water treatment, it is characterized in that: comprise that dry powder stores feeding system, solution stirring system and slurries dosing system, the discharge port of described dry powder storage feeding system is connected with the opening for feed of described solution stirring system, and the discharge port of described solution stirring system is connected with the opening for feed of described slurries dosing system.
2. the Powdered Activated Carbon medicine machine for water treatment according to claim 1, it is characterized in that: described dry powder stores feeding system and comprises vacuum feeder, hopper, storage bin, level gage, shaking device, discharge valve and quantitative worm conveyor, the discharge port of described vacuum feeder is connected with the entrance of described hopper, the outlet of described hopper is connected with the entrance of described storage bin, the discharge port of described storage bin is provided with described discharge valve, the discharge port of described storage bin is connected with the feeding mouth of described quantitative worm conveyor, the discharge port of described quantitative worm conveyor is the discharge port that described dry powder stores feeding system, and described shaking device and described level gage all are installed on the described storage bin.
3. the Powdered Activated Carbon medicine machine for water treatment according to claim 1, it is characterized in that: described solution stirring system comprises the first feed valve, the second feed valve, the first stirrer, the second stirrer, the first water intaking valve, the second water intaking valve, the first NaOH solution tank NaOH, the second NaOH solution tank NaOH, the first liquidometer, the second liquidometer, the first bleeder valve, the second bleeder valve and NaOH solution tank NaOH shutdown valve, the discharge port that described dry powder stores feeding system simultaneously with described the first feed valve be connected the opening for feed of the second feed valve and be connected, the discharge port of described the first feed valve is connected with the opening for feed of described the first NaOH solution tank NaOH, the upper end of described the first NaOH solution tank NaOH is equipped with described the first stirrer, the epimere of described the first NaOH solution tank NaOH is equipped with described the first water intaking valve, the hypomere of described the first NaOH solution tank NaOH is equipped with described the first bleeder valve, the discharge port of described the second feed valve is connected with the opening for feed of described the second NaOH solution tank NaOH, the upper end of described the second NaOH solution tank NaOH is equipped with described the second stirrer, the epimere of described the second NaOH solution tank NaOH is equipped with described the second water intaking valve, the hypomere of described the second NaOH solution tank NaOH is equipped with described the second bleeder valve, the discharge port of described the first bleeder valve is connected with the opening for feed of described shutdown valve by pipeline, the discharge port of described shutdown valve is connected by the discharge port of pipeline with described the second bleeder valve, described the first liquidometer is installed on described the first NaOH solution tank NaOH, described the second liquidometer is installed on described the second NaOH solution tank NaOH, described the first water intaking valve all is connected with the water source with the water-in of described the second water intaking valve, and the discharge port of described the second bleeder valve is the discharge port of described solution stirring system.
4. the Powdered Activated Carbon medicine machine for water treatment according to claim 1, it is characterized in that: described slurries dosing system comprises spiral pump shutdown valve and spiral pump, the opening for feed of described spiral pump shutdown valve is connected with the discharge port of described solution stirring system, the discharge port of described spiral pump shutdown valve is connected with the opening for feed of described spiral pump, and the discharge port of described spiral pump is the discharge port of described Powdered Activated Carbon medicine machine for water treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220388720 CN202688017U (en) | 2012-08-07 | 2012-08-07 | Powdered activated carbon dosing equipment used for water treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220388720 CN202688017U (en) | 2012-08-07 | 2012-08-07 | Powdered activated carbon dosing equipment used for water treatment |
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| Publication Number | Publication Date |
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| CN202688017U true CN202688017U (en) | 2013-01-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201220388720 Expired - Lifetime CN202688017U (en) | 2012-08-07 | 2012-08-07 | Powdered activated carbon dosing equipment used for water treatment |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152624A (en) * | 2015-07-31 | 2015-12-16 | 李兴 | Solidification method and system of waste incineration fly ash |
| CN105836401A (en) * | 2016-05-26 | 2016-08-10 | 广东众和化塑有限公司 | Feeding machine |
| CN106430355A (en) * | 2016-11-13 | 2017-02-22 | 安徽省环境科学研究院 | Powder form water treatment medicament pneumatic dosing system |
| CN110902790A (en) * | 2019-12-10 | 2020-03-24 | 重庆振冉环保技术开发有限公司 | Automatic quantitative dosing equipment |
| CN113600076A (en) * | 2021-06-25 | 2021-11-05 | 南通派菲克水务技术有限公司 | Powdered activated carbon adding system |
-
2012
- 2012-08-07 CN CN 201220388720 patent/CN202688017U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152624A (en) * | 2015-07-31 | 2015-12-16 | 李兴 | Solidification method and system of waste incineration fly ash |
| CN105836401A (en) * | 2016-05-26 | 2016-08-10 | 广东众和化塑有限公司 | Feeding machine |
| CN106430355A (en) * | 2016-11-13 | 2017-02-22 | 安徽省环境科学研究院 | Powder form water treatment medicament pneumatic dosing system |
| CN110902790A (en) * | 2019-12-10 | 2020-03-24 | 重庆振冉环保技术开发有限公司 | Automatic quantitative dosing equipment |
| CN113600076A (en) * | 2021-06-25 | 2021-11-05 | 南通派菲克水务技术有限公司 | Powdered activated carbon adding system |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130123 |
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| CX01 | Expiry of patent term |