CN210193412U - Activated carbon reaction equipment - Google Patents
Activated carbon reaction equipment Download PDFInfo
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- CN210193412U CN210193412U CN201921020646.0U CN201921020646U CN210193412U CN 210193412 U CN210193412 U CN 210193412U CN 201921020646 U CN201921020646 U CN 201921020646U CN 210193412 U CN210193412 U CN 210193412U
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- pipe
- circulating water
- reaction
- liquid
- circulating
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 102
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 61
- 239000007788 liquid Substances 0.000 claims abstract description 85
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 63
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 11
- 239000011521 glass Substances 0.000 claims abstract description 10
- 239000002699 waste material Substances 0.000 claims abstract description 4
- 239000003814 drug Substances 0.000 claims description 26
- 238000007599 discharging Methods 0.000 claims description 12
- 230000002421 anti-septic effect Effects 0.000 claims description 7
- 229910001335 Galvanized steel Inorganic materials 0.000 claims description 6
- 239000008397 galvanized steel Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 238000005260 corrosion Methods 0.000 claims description 4
- 239000011810 insulating material Substances 0.000 claims description 3
- 239000000428 dust Substances 0.000 abstract description 3
- 239000000126 substance Substances 0.000 description 6
- 239000002956 ash Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 239000003610 charcoal Substances 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000036632 reaction speed Effects 0.000 description 2
- 238000004887 air purification Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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Abstract
The utility model relates to an active carbon reaction device, which comprises a reaction vessel, a circulating pump, a circulating pipe, a steam pipe, a liquid discharge pipe and a dosing barrel, wherein the reaction vessel is provided with a dosing port and a liquid discharge port, and the dosing port is arranged above the liquid discharge port; the dosing pipe is connected with the reaction container, the dosing pump and the dosing barrel; the reaction container is connected with a liquid discharge pipe through a liquid discharge port, and the liquid discharge pipe is connected to a waste liquid treatment pool; a circulating water inlet and a circulating water outlet are arranged on the reaction container, and the circulating water inlet is positioned above the circulating water outlet; one end of the circulating pipe is connected with the reaction vessel, and the other end of the circulating pipe is connected with the circulating pump; the reaction vessel is provided with a steam inlet and is connected with a steam pipe through the steam inlet; a feed opening is arranged at the bottom of the reaction vessel, and a feed gate valve is arranged at the feed opening; the reaction vessel is provided with a machine glass liquid level meter. The utility model discloses the reaction is abundant, reaction efficiency is high, the ideal is got rid of to the active carbon dust, the pipeline is difficult to block up.
Description
Technical Field
The utility model relates to an active carbon production technical field especially relates to an active carbon response device.
Background
The active carbon is an adsorption material with wide application, and plays an important role in air purification and water quality purification. When the removal of specific substances by the activated carbon is not ideal, the activated carbon needs to be chemically modified so as to improve the removal performance of the corresponding substances. The modification process requires the use of activated carbon reaction equipment. There are various types of activated carbon reaction apparatuses, a reaction vessel type, a tank type, and the like. The activated carbon reaction equipment often has the problems of complex feeding and discharging operation, insufficient reaction, low reaction efficiency, unsatisfactory removal of activated carbon dust, easy blockage of pipelines and the like.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a: aiming at the defects of the prior art, an activated carbon reaction device is provided to solve the above background technical problems.
The utility model adopts the technical proposal that: an active carbon reaction device comprises a reaction container, a circulating pump, a circulating pipe, a steam pipe, a liquid discharge pipe, a dosing pump, a dosing pipe, a dosing barrel and a valve on a pipeline; wherein, a medicine feeding port and a liquid discharging port are arranged on the reaction container, and the medicine feeding port is arranged above the liquid discharging port; the dosing pipe is connected with the reaction container, the dosing pump and the dosing barrel; the reaction container is connected with a liquid discharge pipe through a liquid discharge port, and the liquid discharge pipe is connected to a waste liquid treatment pool; a circulating water inlet and a circulating water outlet are arranged on the reaction container, and the circulating water inlet is positioned above the circulating water outlet; one end of the circulating pipe is connected with the reaction vessel, and the other end of the circulating pipe is connected with the circulating pump; the reaction vessel is provided with a steam inlet and is connected with a steam pipe through the steam inlet; a feed opening is arranged at the bottom of the reaction vessel, and a feed gate valve is arranged at the feed opening; the reaction vessel is provided with a machine glass liquid level meter.
The utility model discloses in: the medicine adding barrel has 3, the bottom of each medicine adding barrel is connected with a medicine adding pipe, 1 electromagnetic valve is arranged on each medicine adding pipe, and the 3 medicine adding pipes are combined and then connected with a water inlet of the medicine adding pump.
The utility model discloses in: the liquid discharge port is positioned at the bucket part of the reaction container, a filter screen is arranged in the liquid discharge port, a Y-shaped filter and an electromagnetic valve are arranged on the liquid discharge pipe, and the Y-shaped filter is positioned on the left side of the electromagnetic valve.
The utility model discloses in: the circulating water inlet is connected with a water inlet of a circulating water pump through a circulating water pipe, and a Y-shaped filter is arranged on the circulating water pipe; the circulating water outlet is connected with the water outlet of the circulating pump through a circulating water pipe; the circulating water inlet is positioned above the circulating water outlet, and a filter screen is arranged in the circulating water outlet.
The utility model discloses in: the steam pipe is provided with an electromagnetic valve which is a high-temperature resistant electromagnetic valve; the highest point of the steam pipe is at least 20 cm higher than the top of the reaction vessel; the steam pipe is a galvanized steel pipe with the inner part subjected to antiseptic treatment, and the outer part is wrapped with a heat-insulating material.
The utility model discloses in: the steam inlet is positioned 2 cm above the hopper part of the reaction container, and the central line of the pipe orifice of the steam inlet and the central line of the pipe orifice of the circulating water inlet form a 45-degree angle.
The utility model discloses in: the device also comprises a compressed air pipe, wherein the compressed air pipe enters the reaction container in two paths, the pipe wall of the compressed air pipe is 2 cm away from the wall of the reaction container, and the elevation of the pipe bottom is consistent with the elevation of the inverted hopper of the reaction container; two rows of small holes are formed in a compressed air pipe extending into the reaction container, the diameter of each small hole is 2 millimeters, the two small holes in parallel form a 90-degree included angle, the distance between the upper small hole and the lower small hole is 2 centimeters, and the distance between the uppermost row of small holes and the top of the reaction container is 50 centimeters.
The utility model discloses in: the compressed air pipe is a high-temperature-resistant PVC pipe or a galvanized steel pipe with the interior subjected to antiseptic treatment.
The utility model discloses in: a material receiving trolley is arranged below the discharging gate valve, and the inside of the discharging gate valve is subjected to anti-corrosion treatment.
The utility model discloses in: the organic glass liquid level meter comprises a liquid level meter upper liquid port and a liquid level meter lower liquid port, the liquid level meter upper liquid port is located 10 cm below the top of the reaction container, the liquid level meter lower liquid port is located 2 cm above the bucket part of the reaction container, and the center line of the pipe orifice of the organic glass liquid level meter and the center line of the pipe orifice of the circulating water inlet are 90 degrees; the liquid level meter upper liquid port and the liquid level meter lower liquid port are both provided with filter screens.
After the technical scheme is adopted, the beneficial effects of the utility model are that: the utility model has simple and stable structure, reasonable design and convenient use, the liquid medicine continuously passes through the activated carbon layer from bottom to top through the circulating pump, the liquid medicine is more fully contacted with the carbon layer, and compressed air and high-temperature steam can be introduced in the reaction process to improve the mixing effect and the reaction temperature and accelerate the reaction speed; the floating ash in the activated carbon is intercepted by the Y-shaped filter on the circulating pipeline, so that the dust content of the activated carbon can be reduced, the intercepted floating ash can be collected to be made into other products, and the utilization rate of the activated carbon is improved; can add the reaction vessel with the charcoal through loop wheel machine or lifting machine in, open the unloading gate valve during the unloading to sweep through compressed air, can solve the easy difficult problem of unloading that hardens of wet charcoal.
Drawings
Fig. 1 is a schematic structural view of the present invention;
fig. 2 is a top view of the present invention.
Detailed Description
The present invention will be further described with reference to the accompanying drawings.
As can be seen from fig. 1-2, an activated carbon reaction apparatus includes an activated carbon reaction vessel 1, the reaction vessel 1 being open-type; the device comprises a dosing pipe 2, a dosing pump 3, dosing barrels 4a, 4b and 4c, a circulating pipe 5, a circulating pump 6, a steam heating pipe 7, a compressed air pipe 8, a material receiving trolley 10, a liquid discharge pipe 11, a plurality of Y-shaped filters and electromagnetic valves. The reaction vessel 1 is provided with a chemical inlet 2a and a liquid outlet 11a, and the chemical inlet 2a is provided above the liquid outlet 11 a. The dosing port 2a is located 5 cm below the top of the reaction vessel 1. The drain port 11a is located 5 cm above the top of the reaction vessel 1. A filter screen is installed in the liquid discharge port 11 a.
The reaction vessel 1 is provided with a circulating water inlet 5a and a circulating water outlet 5b, and the circulating water inlet 5a is positioned above the circulating water outlet 5 b. The circulation water inlet 5a is located 15 cm below the top of the reaction vessel 1. The circulating water outlet 5b and the liquid outlet 11a are symmetrical in position. A filter screen is arranged in the circulating water outlet 5 b.
The reaction vessel 1 is provided with a steam inlet 7b which is positioned 2 cm above the hopper part of the reaction vessel 1, and the central line of the pipe orifice of the reaction vessel is 45 degrees with the central line of the pipe orifice of the circulating water inlet 5 a.
The bottom of the reaction vessel 1 is provided with a feed opening 9, and the bottom of the feed opening 9 is provided with a feed gate valve 9 a.
The reaction vessel 1 is provided with an organic glass liquid level meter 12, an upper liquid port 12a of the liquid level meter is positioned 10 cm below the top of the reaction vessel 1, and a lower liquid port 12b of the liquid level meter is positioned 2 cm above the bucket part of the reaction vessel 1. The central line of the pipe orifice of the machine glass liquid level meter 12 and the central line of the pipe orifice of the circulating water inlet 5a form a 90-degree angle. The upper liquid port 12a and the lower liquid port 12b of the liquid level meter are both provided with filter screens.
The dosing port 2a is connected with the water outlet of the dosing pump 3 through a dosing pipeline 2, and the dosing pipeline 2 is a PVC pipe. Respectively connecting a dosing barrel 4a with a dosing electromagnetic valve 2b, a dosing barrel 4b with a dosing electromagnetic valve 2c, and a dosing barrel 4c with a dosing electromagnetic valve 2d by PVC pipes. The 3 dosing electromagnetic valves are connected with a water inlet of the dosing pump through a four-way joint and a PVC pipe. Different medicaments can be added into the reaction container 1 by switching different medicament adding electromagnetic valves. And stopping adding the chemicals when the chemicals reach the upper liquid level of the organic glass liquid level meter 12. Wherein the dosing pump 3 is a corrosion resistant pump.
The circulating water inlet 5a is connected with a water inlet of a circulating water pump 6 through a circulating water pipe 5, a Y-shaped filter 5c is arranged on the circulating water pipe 5, the circulating water pipe 5 is a high-temperature-resistant PVC pipe, and the Y-shaped filter 5c is made of plastic materials. The circulating water outlet 5b is connected with the water outlet of the circulating water pump 6 through a high-temperature resistant PVC pipe. The circulating water pump 6 is used for continuously conveying the liquid medicine from the bottom to the top of the carbon layer, so that the liquid medicine and the activated carbon react more fully and thoroughly. The floating ash in the water is intercepted by the Y-shaped filter 5c, so that the carbon layer becomes cleaner, and the intercepted floating ash can be processed into other products, thereby reducing the resource waste.
The steam pipe 7 is connected to the reaction vessel 1 through a steam inlet 7 b. The steam pipe 7 is provided with an electromagnetic valve 7 a. The steam pipe 7 has a highest point at least 20 cm higher than the top of the reaction vessel 1. The steam pipe 7 is a galvanized steel pipe with the inside subjected to antiseptic treatment, and the outside is wrapped with a heat-insulating material. The solenoid valve 7a is a high temperature resistant solenoid valve. The steam pipe 7 functions to increase the reaction speed by steam heating.
The compressed air pipe 8 enters the reaction container 1 in two paths, the pipe wall is 2 cm away from the wall of the reaction container, and the elevation of the pipe bottom is consistent with the elevation of the hopper part of the reaction container. Two rows of small holes are formed in a compressed air pipe extending into the container, the diameter of each small hole is 2 millimeters, the two small holes in the same row form a 90-degree included angle, the distance between the upper small hole and the lower small hole is 2 centimeters, and the distance between the uppermost row of small holes and the top of the reaction container 1 is 50 centimeters. The highest point elevation of the compressed air pipe 8 is at least 1 meter higher than the top of the reaction vessel 1. The compressed air pipe 8 is a high-temperature resistant PVC pipe or a galvanized steel pipe with the interior subjected to antiseptic treatment. The compressed air pipe 8 has the effects that compressed air is blown in during the dosing reaction to increase the mixing effect of the liquid medicine, and the problem that the carbon layer is hardened and difficult to feed can be solved by blowing the compressed air during the feeding.
The drain pipe 11 is connected to the reaction vessel 1 through a drain port 11a, and a y-filter 11b and a drain solenoid valve 11c are provided on the drain pipe. The liquid discharge pipe 11 is a high-temperature-resistant PVC pipe, the Y-shaped filter 11b is of a plastic structure, and the liquid discharge electromagnetic valve 11c is a corrosion-resistant electromagnetic valve. After the reaction is finished, the liquid discharge electromagnetic valve 11c is opened to completely discharge the liquid medicine in the reaction vessel 1, and then the discharge gate valve 9a is opened to discharge the liquid medicine. The y-strainer 11b functions to trap the fly ash and prevent clogging of the solenoid valve 11 c.
The bottom of the reaction vessel 1 is also provided with a feed opening 9 and a feed gate valve 9a, and a receiving trolley 10 is arranged below the feed gate valve 9 a. The inside of the blanking gate valve 9a is subjected to antiseptic treatment. After the reaction is finished and the liquid medicine is discharged, the discharging gate valve 9a is opened for discharging, and compressed air can be introduced to assist discharging when the material plate knots are not easy to fall.
The above description is directed to the specific embodiments of the present invention, but the present invention is not limited to the above description. Any equivalent modifications and substitutions to the present embodiments are within the scope of the present invention for those skilled in the art. Accordingly, variations and modifications in equivalents may be made without departing from the spirit and scope of the invention, which is intended to be covered by the following claims.
Claims (10)
1. An active carbon reaction equipment which characterized in that: comprises a reaction vessel, a circulating pump, a circulating pipe, a steam pipe, a liquid discharge pipe, a dosing pump, a dosing pipe, a dosing barrel and a valve on a pipeline; wherein, a medicine feeding port and a liquid discharging port are arranged on the reaction container, and the medicine feeding port is arranged above the liquid discharging port; the dosing pipe is connected with the reaction container, the dosing pump and the dosing barrel; the reaction container is connected with a liquid discharge pipe through a liquid discharge port, and the liquid discharge pipe is connected to a waste liquid treatment pool; a circulating water inlet and a circulating water outlet are arranged on the reaction container, and the circulating water inlet is positioned above the circulating water outlet; one end of the circulating pipe is connected with the reaction vessel, and the other end of the circulating pipe is connected with the circulating pump; the reaction vessel is provided with a steam inlet and is connected with a steam pipe through the steam inlet; a feed opening is arranged at the bottom of the reaction vessel, and a feed gate valve is arranged at the feed opening; the reaction vessel is provided with a machine glass liquid level meter.
2. An activated carbon reaction apparatus according to claim 1, characterized in that: the medicine adding barrel has 3, the bottom of each medicine adding barrel is connected with a medicine adding pipe, 1 electromagnetic valve is arranged on each medicine adding pipe, and the 3 medicine adding pipes are combined and then connected with a water inlet of the medicine adding pump.
3. An activated carbon reaction apparatus according to claim 1, characterized in that: the liquid discharge port is positioned at the bucket part of the reaction container, a filter screen is arranged in the liquid discharge port, a Y-shaped filter and an electromagnetic valve are arranged on the liquid discharge pipe, and the Y-shaped filter is positioned on the left side of the electromagnetic valve.
4. An activated carbon reaction apparatus according to claim 1, characterized in that: the circulating water inlet is connected with a water inlet of a circulating water pump through a circulating water pipe, and a Y-shaped filter is arranged on the circulating water pipe; the circulating water outlet is connected with the water outlet of the circulating pump through a circulating water pipe; the circulating water inlet is positioned above the circulating water outlet, and a filter screen is arranged in the circulating water outlet.
5. An activated carbon reaction apparatus according to claim 1, characterized in that: the steam pipe is provided with an electromagnetic valve which is a high-temperature resistant electromagnetic valve; the highest point of the steam pipe is at least 20 cm higher than the top of the reaction vessel; the steam pipe is a galvanized steel pipe with the inner part subjected to antiseptic treatment, and the outer part is wrapped with a heat-insulating material.
6. An activated carbon reaction apparatus according to claim 1, characterized in that: the steam inlet is positioned 2 cm above the hopper part of the reaction container, and the central line of the pipe orifice of the steam inlet and the central line of the pipe orifice of the circulating water inlet form a 45-degree angle.
7. An activated carbon reaction apparatus according to claim 1, characterized in that: the device also comprises a compressed air pipe, wherein the compressed air pipe enters the reaction container in two paths, the pipe wall of the compressed air pipe is 2 cm away from the wall of the reaction container, and the elevation of the pipe bottom is consistent with the elevation of the inverted hopper of the reaction container; two rows of small holes are formed in a compressed air pipe extending into the reaction container, the diameter of each small hole is 2 millimeters, the two small holes in parallel form a 90-degree included angle, the distance between the upper small hole and the lower small hole is 2 centimeters, and the distance between the uppermost row of small holes and the top of the reaction container is 50 centimeters.
8. An activated carbon reaction apparatus according to claim 7, characterized in that: the compressed air pipe is a high-temperature-resistant PVC pipe or a galvanized steel pipe with the interior subjected to antiseptic treatment.
9. An activated carbon reaction apparatus according to claim 1, characterized in that: a material receiving trolley is arranged below the discharging gate valve, and the inside of the discharging gate valve is subjected to anti-corrosion treatment.
10. An activated carbon reaction apparatus according to claim 1, characterized in that: the organic glass liquid level meter comprises a liquid level meter upper liquid port and a liquid level meter lower liquid port, the liquid level meter upper liquid port is located 10 cm below the top of the reaction container, the liquid level meter lower liquid port is located 2 cm above the bucket part of the reaction container, and the center line of the pipe orifice of the organic glass liquid level meter and the center line of the pipe orifice of the circulating water inlet are 90 degrees; the liquid level meter upper liquid port and the liquid level meter lower liquid port are both provided with filter screens.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921020646.0U CN210193412U (en) | 2019-07-03 | 2019-07-03 | Activated carbon reaction equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921020646.0U CN210193412U (en) | 2019-07-03 | 2019-07-03 | Activated carbon reaction equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210193412U true CN210193412U (en) | 2020-03-27 |
Family
ID=69869919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921020646.0U Active CN210193412U (en) | 2019-07-03 | 2019-07-03 | Activated carbon reaction equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210193412U (en) |
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2019
- 2019-07-03 CN CN201921020646.0U patent/CN210193412U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20231219 Address after: 315000 Hemudu Town Wulian Village, Yuyao City, Ningbo City, Zhejiang Province Patentee after: Tianyi Activated Carbon Co.,Ltd. Address before: No. 688, Dongfanghong Village, Guozhuang Town, Jurong City, Zhenjiang City, Jiangsu Province, 212400 Patentee before: Jiangsu Tongrui environmental protection technology development Limited by Share Ltd. |
|
| TR01 | Transfer of patent right |