CN201737731U - Powdered activated carbon dry feeder - Google Patents
Powdered activated carbon dry feeder Download PDFInfo
- Publication number
- CN201737731U CN201737731U CN2010202514473U CN201020251447U CN201737731U CN 201737731 U CN201737731 U CN 201737731U CN 2010202514473 U CN2010202514473 U CN 2010202514473U CN 201020251447 U CN201020251447 U CN 201020251447U CN 201737731 U CN201737731 U CN 201737731U
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- CN
- China
- Prior art keywords
- activated carbon
- powdered activated
- speed jet
- outlet
- carbon dry
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- Water Treatment By Sorption (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a powdered activated carbon dry feeder; the upper end of a storage cabin (5) is connected with the outlet of a cyclone separator (3); the inlet of the cyclone separator (3) is connected with a feed station (1) through a suction tube (2); the cyclone separator (3) is connected with a vacuum generator (4) through a pneumatic three-way valve; the discharge port of the lower end of the storage cabin (5) is connected with a feeding machine (8); the inlet and the outlet of a high-speed jet mixer (7) are connected with a water duct (6) in series; and the water duct (6) arranged at the inlet end of the high-speed jet mixer (7) is connected with a pipeline booster pump (9) in series; and the feed port of the high-speed jet mixer (7) is connected with the outlet of the feeding machine (8). The utility model relates to a powdered activated carbon dry feeder which has high utilization rate of activated carbon and friendly working environment, and is beneficial for improving water processing effect and saving energies.
Description
Technical field
The utility model relates to a kind of adding equipment, particularly relates to a kind of Powdered Activated Carbon dry method adding equipment.
Background technology
Adding of all kinds of flocculation agents in urban life feedwater, industrial water supply processing and city domestic sewage and the Industrial Wastewater Treatment, sorbent material, water purification agent is that what to adopt is that all kinds of flocculation agents, sorbent material, water purification agent are directly thrown in a pond at present.Adopt this method, all kinds of flocculation agents, sorbent material, the water purification agent particularly utilising efficiency of gac are very low, and operator's Working environment is very abominable simultaneously, are unfavorable for improving the water treatment effect and save the energy.
The utility model content
Technical problem to be solved in the utility model provides a kind of utilising efficiency height of gac, Working environment close friend, the Powdered Activated Carbon dry method adding equipment that helps improving the water treatment effect and save the energy.
In order to solve the problems of the technologies described above, the Powdered Activated Carbon dry method adding equipment that the utility model provides, comprise hydraulic pipe, the upper end of storage bin is connected with the outlet of cyclonic separator, the import of described cyclonic separator is connected with the station that feeds intake by material sucking pipes, described cyclonic separator is connected with vacuum generator by Pneumatic three-way valve, the lower end discharge port of described storage bin is connected with the machine of adding, the import of high-speed jet mixing tank and outlet are connected on the described hydraulic pipe and the described hydraulic pipe that is in the entrance end of described high-speed jet mixing tank is in series with the pipe pressurizing pump, and the opening for feed of described high-speed jet mixing tank is connected with the described outlet that adds machine.
The described station that feeds intake is provided with microporous membrane filters.
Total system is provided with the pressurized air back-blowing device.
Adopt the Powdered Activated Carbon dry method adding equipment of technique scheme, Powdered Activated Carbon dry method dosing system is to utilize vacuum generator to bleed, make total system be in certain vacuum state, Powdered Activated Carbon together is inhaled into the station that feeds intake with outside air, form the material air-flow, arrive cyclonic separator through material sucking pipes, realize that in cyclonic separator gas, material separate, Powdered Activated Carbon after the separation enters storage bin, at last by Pneumatic three-way valve constantly open and close realize controlling suction-blowing, and the switching of Pneumatic three-way valve is controlled by control center.The pipe pressurizing pump makes the high-speed jet mixing tank produce high velocity flow, and material enters the opening for feed of high-speed jet mixing tank through the lower end of storage bin discharge port by the machine of adding, and is mixed into hydraulic pipe with high speed water in the high-speed jet mixing tank and finishes adding of material.When the pressurized air back-blowing device that total system is provided with, each blowing, the pulse of compressed air blowback total system strainer on the station that particularly feeds intake blows off the powder that is adsorbed in filter surfaces get off, and can normally move with the assurance suction.
Characteristics of the present utility model:
1, diffusion effect is good, and mixture homogeneity improves;
2, gac utilization ratio height is compared with traditional adding equipment, can save gac about 50%;
3, do not have the wearing and tearing and the line clogging of pump, running cost is low, good stability;
4, the equipment integral volume is little, and construction cost is low, and cost of use is few;
5, all processes are automatic control, and are easy and simple to handle;
6, operating process does not have the airborne dust generation, can obviously improve operator's Working environment;
The dry method of the scope of application all kinds of flocculation agents, sorbent material, water purification agent in urban life feedwater, industrial water supply processing and city domestic sewage and Industrial Wastewater Treatment adds.Powdered Activated Carbon dry method adding equipment is that conventional powder gac adding equipment is carried out product behind the major tuneup, be the adding equipment that is that specially tap water is handled and sewage treatment industry designs, and the dry method that can be used for other solid-state coagulating agent, sorbent material and water purification agent add.This equipment has adopted volute tangential feeding technology and numerical control integrated technology, has improved the utilising efficiency of gac greatly, has improved operator's Working environment simultaneously.In water supply and sewage work, obtained using widely, raising water treatment effect, the saving energy have been had the certain economic meaning.
In sum, the utility model is a kind of utilising efficiency height of gac, Working environment close friend, the Powdered Activated Carbon dry method adding equipment that helps improving the water treatment effect and save the energy.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.
Referring to Fig. 1, the upper end of storage bin 5 is connected with the outlet of cyclonic separator 3, the import of cyclonic separator 3 is connected with the station 1 that feeds intake by material sucking pipes 2, the station that feeds intake 1 is provided with microporous membrane filters, cyclonic separator 3 is connected with vacuum generator 4 by Pneumatic three-way valve, the lower end discharge port of storage bin 5 is connected with the machine of adding 8, the import of high-speed jet mixing tank 7 and outlet are connected on the hydraulic pipe 6 and the hydraulic pipe 6 that is in the entrance end of high-speed jet mixing tank 7 is in series with pipe pressurizing pump 9, and the opening for feed of high-speed jet mixing tank 9 is connected with the outlet of the machine of adding 8.Total system is provided with the pressurized air back-blowing device.
Referring to Fig. 1, cyclonic separator 3 utilizes vacuum generator 4 to bleed, make total system be in certain vacuum state, Powdered Activated Carbon together is inhaled into the station 1 that feeds intake with outside air, forms the material air-flow, arrives cyclonic separator 3 through material sucking pipes 2, realize that in cyclonic separator 3 gas, material separate, Powdered Activated Carbon after the separation enters storage bin 5, at last by Pneumatic three-way valve constantly open and close realize controlling suction-blowing, and the switching of Pneumatic three-way valve is controlled by control center.Pipe pressurizing pump 9 makes high-speed jet mixing tank 7 produce high velocity flow, material enters the opening for feed of high-speed jet mixing tank 7 through the lower end of storage bin 5 discharge port by the machine of adding 8, is mixed into hydraulic pipe 6 with high speed water in the high-speed jet mixing tank 7 and finishes adding of material.When the pressurized air back-blowing device that total system is provided with, each blowing, the microporous membrane filters that pulse of compressed air blowback total system particularly feeds intake station 1 blows off the powder that is adsorbed in the microporous membrane filters surface get off, and can normally move with the assurance suction.
Claims (3)
1. Powdered Activated Carbon dry method adding equipment, comprise hydraulic pipe (6), it is characterized in that: the upper end of storage bin (5) is connected with the outlet of cyclonic separator (3), the import of described cyclonic separator (3) is connected with the station that feeds intake (1) by material sucking pipes (2), described cyclonic separator (3) is connected with vacuum generator (4) by Pneumatic three-way valve, the lower end discharge port of described storage bin (5) is connected with the machine of adding (8), the import of high-speed jet mixing tank (7) and outlet are connected on that described hydraulic pipe (6) is gone up and the described hydraulic pipe (6) that is in the entrance end of described high-speed jet mixing tank (7) is in series with pipe pressurizing pump (9), and the opening for feed of described high-speed jet mixing tank (7) is connected with the described outlet that adds machine (8).
2. Powdered Activated Carbon dry method adding equipment according to claim 1 is characterized in that: the described station that feeds intake (1) is provided with microporous membrane filters.
3. Powdered Activated Carbon dry method adding equipment according to claim 1 and 2, it is characterized in that: total system is provided with the pressurized air back-blowing device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202514473U CN201737731U (en) | 2010-07-08 | 2010-07-08 | Powdered activated carbon dry feeder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202514473U CN201737731U (en) | 2010-07-08 | 2010-07-08 | Powdered activated carbon dry feeder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201737731U true CN201737731U (en) | 2011-02-09 |
Family
ID=43553014
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202514473U Expired - Lifetime CN201737731U (en) | 2010-07-08 | 2010-07-08 | Powdered activated carbon dry feeder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201737731U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102241423A (en) * | 2011-06-10 | 2011-11-16 | 北京市市政工程设计研究总院 | Mobile container type integrated powder dissolving and adding device |
| CN106032212A (en) * | 2015-03-20 | 2016-10-19 | 慈溪市天顺机械设备有限公司 | Novel suction feeder |
| CN106365238A (en) * | 2016-08-31 | 2017-02-01 | 潍坊和创环保设备有限公司 | Powdered activated carbon dry-method feeding system |
| CN106629976A (en) * | 2016-12-28 | 2017-05-10 | 江苏华达环境工程有限公司 | Integrated powdered activated carbon adding device and adding system thereof |
| CN107159562A (en) * | 2017-07-17 | 2017-09-15 | 苏州三峰激光科技有限公司 | Screening plant and titanium alloy powder screening system |
| CN108263695A (en) * | 2018-01-25 | 2018-07-10 | 方亨 | A kind of automatic charging production equipment of unsaturated polyester resin |
-
2010
- 2010-07-08 CN CN2010202514473U patent/CN201737731U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102241423A (en) * | 2011-06-10 | 2011-11-16 | 北京市市政工程设计研究总院 | Mobile container type integrated powder dissolving and adding device |
| CN106032212A (en) * | 2015-03-20 | 2016-10-19 | 慈溪市天顺机械设备有限公司 | Novel suction feeder |
| CN106365238A (en) * | 2016-08-31 | 2017-02-01 | 潍坊和创环保设备有限公司 | Powdered activated carbon dry-method feeding system |
| CN106629976A (en) * | 2016-12-28 | 2017-05-10 | 江苏华达环境工程有限公司 | Integrated powdered activated carbon adding device and adding system thereof |
| CN107159562A (en) * | 2017-07-17 | 2017-09-15 | 苏州三峰激光科技有限公司 | Screening plant and titanium alloy powder screening system |
| CN108263695A (en) * | 2018-01-25 | 2018-07-10 | 方亨 | A kind of automatic charging production equipment of unsaturated polyester resin |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: HU'NAN BOSSCO HUAYI ENVIRONMENTAL ENGINEERING CO., Free format text: FORMER NAME: HUNAN HUAYI MUNICIPAL ENGINEERING DESIGN CO., LTD. |
|
| CP03 | Change of name, title or address |
Address after: Yuelu District City, Wangcheng province Hunan 410205 Changsha Po Valley base Lu Tin Road No. 8 Patentee after: Hunan BOSCH, Huayi Environmental Engineering Co. Ltd. Address before: 410002, fortune 909, Fortune Center, No. 468 Furong Road, Hunan, Changsha, Hunan Patentee before: Hunan Huayi Municipal Engineering Design Co., Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Yuelu District City, Wangcheng province Hunan 410205 Changsha Po Valley base Lu Tin Road No. 8 Patentee after: Hunan BOSCH Environmental Protection Technology Co., Ltd. Address before: Yuelu District City, Wangcheng province Hunan 410205 Changsha Po Valley base Lu Tin Road No. 8 Patentee before: Hunan BOSCH, Huayi Environmental Engineering Co. Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110209 |