CN204543727U - A kind of for the filtration drying device in glyphosate production technique - Google Patents
A kind of for the filtration drying device in glyphosate production technique Download PDFInfo
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- CN204543727U CN204543727U CN201520222599.3U CN201520222599U CN204543727U CN 204543727 U CN204543727 U CN 204543727U CN 201520222599 U CN201520222599 U CN 201520222599U CN 204543727 U CN204543727 U CN 204543727U
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- filter cloth
- micropore filter
- annular micropore
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Abstract
The utility model relates to a kind of for the filtration drying device in glyphosate production technique, comprises annular micropore filter cloth, and for locating and drive the first power axle and the second power axle that annular micropore filter cloth rotates; Annular micropore filter cloth is the clinohedral vibrational power flow of right low left high; Annular micropore filter cloth inner chamber is provided with filtrate collection chamber, and annular micropore filter cloth top is provided with water conservancy diversion wind chamber, arranges vacuum drying chamber bottom annular micropore filter cloth.The mode that the utility model is combined by micropore filter-cloth filtering and vacuum drying is removed fast to moisture remaining in glyphosate products, and make the moisture in glyphosate products reach expection standard, improving product purity and concentration, improve the quality of products.
Description
Technical field
The utility model relates to glyphosate production technical field, particularly a kind of for the filtration drying device in glyphosate production technique.
Background technology
Glyphosate, as a kind of spectrum herbicide, is worldwide used widely.It is reported, glyphosate effectively can eliminate 76 kinds in 78 kinds of the most serious weeds of the harm of having announced in world wide.As the environmentally friendly herbicide of one, glyphosate obtains wide popularization and application in China.Existing technique, in the glyphosate production later stage, needs to remove the micro-moisture residued in glyphosate products, carries out purification concentrate product, and to ensure that obtaining glyphosate finished product water content meets expection standard, purity is high.Existing production technology is when removing glyphosate products residual moisture, the mode that main employing industrial centrifugal machine is centrifugal, residual moisture is separated with glyphosate particle, obtain the standard compliant glyphosate finished product of water content, this kind dewaters mode inefficiency, the cost that dewaters is high, and needs multistage centrifugal the residual water in glyphosate could to be reduced in critical field.
Based on above analysis, the existing equipment for removing glyphosate residual water is improved, design a kind of modified removes residual water filtration drying device for glyphosate later-period purification, the mode combined by micropore filter-cloth filtering and vacuum drying is removed fast to moisture remaining in glyphosate products, the moisture in glyphosate products is made to reach expection standard, improving product purity and concentration, improve the quality of products, and seems particularly important.
Utility model content
The purpose of this utility model is, for the existing equipment for removing glyphosate residual water above-mentioned technical problem, a kind of modified is provided to remove the filtration drying device of residual water for glyphosate later-period purification, the mode combined by micropore filter-cloth filtering and vacuum drying is removed fast to moisture remaining in glyphosate products, the moisture in glyphosate products is made to reach expection standard, improving product purity and concentration, improve the quality of products.
The utility model is achieved through the following technical solutions:
For the filtration drying device in glyphosate production technique, it is characterized in that, structure comprises annular micropore filter cloth (1), and for location and the first power axle (2) of driving annular micropore filter cloth (1) to rotate and the second power axle (3); The clinohedral vibrational power flow of described annular micropore filter cloth (1) in right low left high;
Described annular micropore filter cloth (1) inner chamber top is provided with the roller (4) for supporting annular micropore filter cloth (1);
Described annular micropore filter cloth (1) inner chamber is provided with filtrate collection chamber (5), and filtrate collection chamber (5) top is provided with the first vacuum pumping pump (51), and filtrate collection chamber (5) bottom is provided with filtrate suction pump (52);
Described annular micropore filter cloth (1) top is provided with water conservancy diversion wind chamber (6), water conservancy diversion wind chamber (6) top is provided with high pressure air blowing machine (61), water conservancy diversion wind chamber (6) is upper is provided with feed cavity (62) near the second power axle (3) one end, and feed cavity (62) upper end connects glyphosate and quantitatively drips tank (63);
Described first power axle (2) upper left side is provided with discharging wheel (7), and discharging wheel (7) contacts with annular micropore filter cloth (1), and discharging wheel (7) is connected with the high-frequency drive motor (71) for driving discharging to take turns (7);
Described discharging wheel (7) is rotated along clockwise direction, and annular micropore filter cloth (1) is rotated in the counterclockwise direction;
Described annular micropore filter cloth (1) bottom arranges vacuum drying chamber (8), is provided with rail type material delivery roll (81), arranges heat radiation heater (82) directly over rail type material delivery roll (81) in vacuum drying chamber (8);
Described vacuum drying chamber (8) upper right side connects the second vacuum pumping pump (83);
Described rail type material delivery roll (81) end connects Material collecting box for harvesting (84).
Further, described filtrate suction pump (52) end connects filtrate collecting pit (5201).
Further, described first vacuum pumping pump (51) end connects the first dust arrester (5101).
Further, described second vacuum pumping pump (83) end connects the second dust arrester (8301).
Further, described heat radiation heater (82) is carbon fiber infrared heating device.
Further, described discharging wheel (7) is integrated with the hairbrush for auxiliary scraper.
Further, described water conservancy diversion wind chamber (6) and annular micropore filter cloth (1) form the cavity body structure of opposing seal.
Further, described filtrate collection chamber (5) forms the cavity body structure of opposing seal in annular micropore filter cloth (1) inner chamber with annular micropore filter cloth (1).
Further, described vacuum drying chamber (8) and annular micropore filter cloth (1) form the cavity body structure of opposing seal.
The utility model provides a kind of for the filtration drying device in glyphosate production technique, and compared with prior art, beneficial effect is:
1, the utility model is provided with water conservancy diversion wind chamber (6) on annular micropore filter cloth (1) top, and water conservancy diversion wind chamber (6) top is provided with high pressure air blowing machine (61), and water conservancy diversion wind chamber (6) and annular micropore filter cloth (1) form the cavity body structure of opposing seal, annular micropore filter cloth (1) inner chamber is provided with filtrate collection chamber (5), filtrate collection chamber (5) top is provided with the first vacuum pumping pump (51), filtrate collection chamber (5) bottom is provided with filtrate suction pump (52), and filtrate collection chamber (5) forms the cavity body structure of opposing seal in annular micropore filter cloth (1) inner chamber with annular micropore filter cloth (1), annular micropore filter cloth (1) bottom arranges vacuum drying chamber (8), rail type material delivery roll (81) is provided with in vacuum drying chamber (8), heat radiation heater (82) is set directly over rail type material delivery roll (81), vacuum drying chamber (8) upper right side connects the second vacuum pumping pump (83), vacuum drying chamber (8) and annular micropore filter cloth (1) form the cavity body structure of opposing seal, this kind of project organization, utilize the downward high-pressure blast that water conservancy diversion wind chamber (6) produces, the upper glyphosate of annular micropore filter cloth (1) will be positioned over to blowing down, downward high-pressure blast makes the residual water in glyphosate fall in filtrate collection chamber (5) via the micropore on annular micropore filter cloth (1), meanwhile, filtrate collection chamber (5) top is provided with the first vacuum pumping pump (51), the first vacuum pumping pump (51) is utilized to vacuumize process to filtrate collection chamber (5), make mineralization pressure between annular micropore filter cloth (1) upper and lower sides poor, the residual water be conducive in glyphosate hurtles down to filtrate collection chamber (5), heat radiation heater (82) and the second vacuum pumping pump (83) is provided with in vacuum drying chamber (8), utilize heat radiation heater (82) and the second vacuum pumping pump (83) rapidly and efficiently dehumidification treatments can be carried out to the glyphosate entered in vacuum drying chamber (8), reduce the water content in glyphosate, improve the quality of products.
2, the utility model annular micropore filter cloth (1) is set to the clinohedral structure of right low left high, water conservancy diversion wind chamber (6) is upper is provided with feed cavity (62) near the second power axle (3) one end, feed cavity (62) upper end connects glyphosate and quantitatively drips tank (63), annular micropore filter cloth (1) is rotated along clockwise direction, this kind of project organization, glyphosate to be dehumidified is moved to height point by by low spot on annular micropore filter cloth (1), this kind of project organization, with be beneficial to residual water and glyphosate particle separation, promote dehumidification rate.
3, in the utility model, the first power axle (2) upper left side is provided with discharging wheel (7), discharging wheel (7) contacts with annular micropore filter cloth (1), discharging wheel (7) is connected with the high-frequency drive motor (71) for driving discharging to take turns (7), discharging wheel (7) is rotated along clockwise direction, annular micropore filter cloth (1) is rotated in the counterclockwise direction, this kind of project organization is conducive to upper for annular micropore filter cloth (1) glyphosate particle fast transfer in vacuum drying chamber (8), discharging wheel (7) is integrated with the hairbrush for auxiliary scraper, utilize hairbrush can carry out block clearing process to annular micropore filter cloth (1), avoid the upper filter bores blocking of annular micropore filter cloth (1), ensure that the smooth and easy of whole device carries out.
Accompanying drawing explanation
Fig. 1 is that the utility model is for the filtration drying apparatus structure schematic diagram in glyphosate production technique.
Fig. 2 is the package assembly schematic diagram of the utility model annular micropore filter cloth and filtrate collection chamber.
Detailed description of the invention
Accompanying drawings 1 and Fig. 2 are described further the utility model.
The utility model relates to a kind of for the filtration drying device in glyphosate production technique, it is characterized in that, structure comprises annular micropore filter cloth (1), and for location and the first power axle (2) of driving annular micropore filter cloth (1) to rotate and the second power axle (3); The clinohedral vibrational power flow of described annular micropore filter cloth (1) in right low left high;
Described annular micropore filter cloth (1) inner chamber top is provided with the roller (4) for supporting annular micropore filter cloth (1);
Described annular micropore filter cloth (1) inner chamber is provided with filtrate collection chamber (5), and filtrate collection chamber (5) top is provided with the first vacuum pumping pump (51), and filtrate collection chamber (5) bottom is provided with filtrate suction pump (52);
Described annular micropore filter cloth (1) top is provided with water conservancy diversion wind chamber (6), water conservancy diversion wind chamber (6) top is provided with high pressure air blowing machine (61), water conservancy diversion wind chamber (6) is upper is provided with feed cavity (62) near the second power axle (3) one end, and feed cavity (62) upper end connects glyphosate and quantitatively drips tank (63);
Described first power axle (2) upper left side is provided with discharging wheel (7), and discharging wheel (7) contacts with annular micropore filter cloth (1), and discharging wheel (7) is connected with the high-frequency drive motor (71) for driving discharging to take turns (7);
Described discharging wheel (7) is rotated along clockwise direction, and annular micropore filter cloth (1) is rotated in the counterclockwise direction;
Described annular micropore filter cloth (1) bottom arranges vacuum drying chamber (8), is provided with rail type material delivery roll (81), arranges heat radiation heater (82) directly over rail type material delivery roll (81) in vacuum drying chamber (8);
Described vacuum drying chamber (8) upper right side connects the second vacuum pumping pump (83);
Described rail type material delivery roll (81) end connects Material collecting box for harvesting (84).
Preferably, as improvement, described filtrate suction pump (52) end connects filtrate collecting pit (5201).
Preferably, as improvement, described first vacuum pumping pump (51) end connects the first dust arrester (5101).
Preferably, as improvement, described second vacuum pumping pump (83) end connects the second dust arrester (8301).
Preferably, as improvement, described heat radiation heater (82) is carbon fiber infrared heating device.
Preferably, as improvement, described discharging wheel (7) is integrated with the hairbrush for auxiliary scraper.
Preferably, as improvement, described water conservancy diversion wind chamber (6) and annular micropore filter cloth (1) form the cavity body structure of opposing seal.
Preferably, as improvement, described filtrate collection chamber (5) forms the cavity body structure of opposing seal in annular micropore filter cloth (1) inner chamber with annular micropore filter cloth (1).
Preferably, as improvement, described vacuum drying chamber (8) and annular micropore filter cloth (1) form the cavity body structure of opposing seal.
Compared with prior art, the utility model is provided with water conservancy diversion wind chamber (6) on annular micropore filter cloth (1) top, water conservancy diversion wind chamber (6) top is provided with high pressure air blowing machine (61), and water conservancy diversion wind chamber (6) and annular micropore filter cloth (1) form the cavity body structure of opposing seal, annular micropore filter cloth (1) inner chamber is provided with filtrate collection chamber (5), filtrate collection chamber (5) top is provided with the first vacuum pumping pump (51), filtrate collection chamber (5) bottom is provided with filtrate suction pump (52), and filtrate collection chamber (5) forms the cavity body structure of opposing seal in annular micropore filter cloth (1) inner chamber with annular micropore filter cloth (1), annular micropore filter cloth (1) bottom arranges vacuum drying chamber (8), rail type material delivery roll (81) is provided with in vacuum drying chamber (8), heat radiation heater (82) is set directly over rail type material delivery roll (81), vacuum drying chamber (8) upper right side connects the second vacuum pumping pump (83), vacuum drying chamber (8) and annular micropore filter cloth (1) form the cavity body structure of opposing seal, this kind of project organization, utilize the downward high-pressure blast that water conservancy diversion wind chamber (6) produces, the upper glyphosate of annular micropore filter cloth (1) will be positioned over to blowing down, downward high-pressure blast makes the residual water in glyphosate fall in filtrate collection chamber (5) via the micropore on annular micropore filter cloth (1), meanwhile, filtrate collection chamber (5) top is provided with the first vacuum pumping pump (51), the first vacuum pumping pump (51) is utilized to vacuumize process to filtrate collection chamber (5), make mineralization pressure between annular micropore filter cloth (1) upper and lower sides poor, the residual water be conducive in glyphosate hurtles down to filtrate collection chamber (5), heat radiation heater (82) and the second vacuum pumping pump (83) is provided with in vacuum drying chamber (8), utilize heat radiation heater (82) and the second vacuum pumping pump (83) rapidly and efficiently dehumidification treatments can be carried out to the glyphosate entered in vacuum drying chamber (8), reduce the water content in glyphosate, improve the quality of products.
The utility model annular micropore filter cloth (1) is set to the clinohedral structure of right low left high, water conservancy diversion wind chamber (6) is upper is provided with feed cavity (62) near the second power axle (3) one end, feed cavity (62) upper end connects glyphosate and quantitatively drips tank (63), annular micropore filter cloth (1) is rotated along clockwise direction, this kind of project organization, glyphosate to be dehumidified is moved to height point by by low spot on annular micropore filter cloth (1), this kind of project organization, with be beneficial to residual water and glyphosate particle separation, promote dehumidification rate.
In the utility model, the first power axle (2) upper left side is provided with discharging wheel (7), discharging wheel (7) contacts with annular micropore filter cloth (1), discharging wheel (7) is connected with the high-frequency drive motor (71) for driving discharging to take turns (7), discharging wheel (7) is rotated along clockwise direction, annular micropore filter cloth (1) is rotated in the counterclockwise direction, this kind of project organization is conducive to upper for annular micropore filter cloth (1) glyphosate particle fast transfer in vacuum drying chamber (8), discharging wheel (7) is integrated with the hairbrush for auxiliary scraper, utilize hairbrush can carry out block clearing process to annular micropore filter cloth (1), avoid the upper filter bores blocking of annular micropore filter cloth (1), ensure that the smooth and easy of whole device carries out.
The utility model in use, glyphosate to be dehumidified quantitatively drips tank (63) via glyphosate successively and feed cavity (62) enters annular micropore filter cloth (1), first power axle (2) and the second power axle (3) drive annular micropore filter cloth (1) to rotate counterclockwise, annular micropore filter cloth (1) is rotated and is driven glyphosate to be dehumidified to be moved to height point by low spot, portion of residual water in glyphosate to be dehumidified enters filtrate collection chamber (5) by the micropore on annular micropore filter cloth (1), when glyphosate to be dehumidified moves to the first power axle (2), discharging wheel (7) and annular micropore filter cloth (1) contact, glyphosate is transferred in vacuum drying chamber (8), glyphosate warp after vacuum drying chamber (8) further dehumidifying enters Material collecting box for harvesting (84) by rail type material delivery roll (81).
As described above, can apply the utility model.
The above; be only the utility model preferably detailed description of the invention; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; be equal to according to the technical solution of the utility model and utility model design thereof and replace or change, all should be encompassed within protection domain of the present utility model.
Claims (9)
1. for the filtration drying device in glyphosate production technique, it is characterized in that, structure comprises annular micropore filter cloth (1), and for location and the first power axle (2) of driving annular micropore filter cloth (1) to rotate and the second power axle (3); The clinohedral vibrational power flow of described annular micropore filter cloth (1) in right low left high;
Described annular micropore filter cloth (1) inner chamber top is provided with the roller (4) for supporting annular micropore filter cloth (1);
Described annular micropore filter cloth (1) inner chamber is provided with filtrate collection chamber (5), and filtrate collection chamber (5) top is provided with the first vacuum pumping pump (51), and filtrate collection chamber (5) bottom is provided with filtrate suction pump (52);
Described annular micropore filter cloth (1) top is provided with water conservancy diversion wind chamber (6), water conservancy diversion wind chamber (6) top is provided with high pressure air blowing machine (61), water conservancy diversion wind chamber (6) is upper is provided with feed cavity (62) near the second power axle (3) one end, and feed cavity (62) upper end connects glyphosate and quantitatively drips tank (63);
Described first power axle (2) upper left side is provided with discharging wheel (7), and discharging wheel (7) contacts with annular micropore filter cloth (1), and discharging wheel (7) is connected with the high-frequency drive motor (71) for driving discharging to take turns (7);
Described discharging wheel (7) is rotated along clockwise direction, and annular micropore filter cloth (1) is rotated in the counterclockwise direction;
Described annular micropore filter cloth (1) bottom arranges vacuum drying chamber (8), is provided with rail type material delivery roll (81), arranges heat radiation heater (82) directly over rail type material delivery roll (81) in vacuum drying chamber (8);
Described vacuum drying chamber (8) upper right side connects the second vacuum pumping pump (83);
Described rail type material delivery roll (81) end connects Material collecting box for harvesting (84).
2. according to claim 1ly it is characterized in that for the filtration drying device in glyphosate production technique, described filtrate suction pump (52) end connects filtrate collecting pit (5201).
3. according to claim 1ly it is characterized in that for the filtration drying device in glyphosate production technique, described first vacuum pumping pump (51) end connects the first dust arrester (5101).
4. according to claim 1ly it is characterized in that for the filtration drying device in glyphosate production technique, described second vacuum pumping pump (83) end connects the second dust arrester (8301).
5. according to claim 1ly it is characterized in that for the filtration drying device in glyphosate production technique, described heat radiation heater (82) is carbon fiber infrared heating device.
6. according to claim 1ly to it is characterized in that for the filtration drying device in glyphosate production technique, described discharging wheel (7) is integrated with the hairbrush for auxiliary scraper.
7. according to claim 1ly it is characterized in that for the filtration drying device in glyphosate production technique, described water conservancy diversion wind chamber (6) and annular micropore filter cloth (1) form the cavity body structure of opposing seal.
8. according to claim 1ly it is characterized in that for the filtration drying device in glyphosate production technique, described filtrate collection chamber (5) forms the cavity body structure of opposing seal in annular micropore filter cloth (1) inner chamber with annular micropore filter cloth (1).
9. according to claim 1ly it is characterized in that for the filtration drying device in glyphosate production technique, described vacuum drying chamber (8) and annular micropore filter cloth (1) form the cavity body structure of opposing seal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520222599.3U CN204543727U (en) | 2015-04-14 | 2015-04-14 | A kind of for the filtration drying device in glyphosate production technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520222599.3U CN204543727U (en) | 2015-04-14 | 2015-04-14 | A kind of for the filtration drying device in glyphosate production technique |
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| Publication Number | Publication Date |
|---|---|
| CN204543727U true CN204543727U (en) | 2015-08-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520222599.3U Active CN204543727U (en) | 2015-04-14 | 2015-04-14 | A kind of for the filtration drying device in glyphosate production technique |
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| CN (1) | CN204543727U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108144355A (en) * | 2018-03-16 | 2018-06-12 | 内江市川威特殊钢有限公司 | Scraper and filter |
| CN108533198A (en) * | 2018-06-04 | 2018-09-14 | 中国海洋石油集团有限公司 | A kind of negative pressure micro-vibration drilling fluid three-phase separating device |
-
2015
- 2015-04-14 CN CN201520222599.3U patent/CN204543727U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108144355A (en) * | 2018-03-16 | 2018-06-12 | 内江市川威特殊钢有限公司 | Scraper and filter |
| CN108533198A (en) * | 2018-06-04 | 2018-09-14 | 中国海洋石油集团有限公司 | A kind of negative pressure micro-vibration drilling fluid three-phase separating device |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Device for a filtration drying for $drafting in sweet phosphine production technology Effective date of registration: 20170111 Granted publication date: 20150812 Pledgee: Chengdu Jinpeng Xiang Petrochemical Co. Ltd. Pledgor: Sichuan Beier Chemical Group Co., Ltd. Registration number: 2016510000082 |
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Effective date of registration: 20170925 Granted publication date: 20150812 |
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Date of cancellation: 20190325 Granted publication date: 20150812 |
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| PP01 | Preservation of patent right |
Effective date of registration: 20190325 Granted publication date: 20150812 |