CN204816527U - Circulating device in glass cleaning agent production - Google Patents
Circulating device in glass cleaning agent production Download PDFInfo
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- CN204816527U CN204816527U CN201520561984.0U CN201520561984U CN204816527U CN 204816527 U CN204816527 U CN 204816527U CN 201520561984 U CN201520561984 U CN 201520561984U CN 204816527 U CN204816527 U CN 204816527U
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- pipeline
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- vavuum pump
- reation kettle
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Abstract
The utility model discloses a circulating device in glass cleaning agent production, include: reation kettle, locate agitator among the reation kettle, drive the driving motor of agitator, through first pipeline with discharge gate that reation kettle bottom is connected, locate filter on the first pipeline between discharge gate and the reation kettle, locate vacuum pump on the first pipeline between filter and the discharge gate, locate ejection of compact valve and circulation valve on the first pipeline between vacuum pump and the discharge gate, the reation kettle top is equipped with a feed inlet, the feed inlet pass through the second pipeline with first pipeline intercommunication between vacuum pump, the ejection of compact valve, the circulation valve install in on the second pipeline. Has following advantage: shorten the material time of dissolving, promote the degree of consistency that the material reaction mixes, greatly reduced equipment and workman's intensity, can accelerate the filling time and save the filling time.
Description
Technical field
The utility model relates to glass cleaner production technical field, particularly relates to the EGR in the production of a kind of glass cleaner.
Background technology
Along with the extensive use in the industry of touch-screen, mobile phone sheet glass, sapphire glass, the use amount of glass cleaner is also increasing.As the manufacturer of glass cleaner, how to enhance productivity, economize energy cost, reduce the labour intensity of direct labor, be the target that each manufacturer works hard always.
Glass cleaner is a kind of alkaline, still or low foaming transparency liquid; it is produced raw material and is generally solid particle, powder and a part of liquid; in actual production, often there will be solid particle indissoluble solution, stir uneven, the upper and lower uneven first-class phenomenon of the rear standing easily appearance of cleaning agent production, how effectively to solve the problem is a challenging task.
Refer to Fig. 1, it is existing glass cleaner production equipment, form primarily of reactor 102, motor 104, agitator 106, filter 108, electric pump 202 and valve 204, this reactor 102 top is provided with the dog-house 206 for feeding intake, and the agitator 106 in reactor 102 generally adopts paddle, adjustable speed and agitating device moving up and down.There is following defect in this glass cleaner production equipment:
(1), workman will feed intake from the dog-house 206 of reactor 102 to reactor 102 operating platform, therefore, all raw material needs the equipment delivery such as fork truck, lifting platform on operating platform, considerably increases the intensity of equipment and workman, also there is certain danger;
(2), solid material is easily adsorbed on bottom reactor 102, occurs dissolving difficulty, dissolving the problems such as uneven, and reductor will be adopted in addition to carry out speed governing and move up and down stirring, and this can considerably increase equipment cost;
(3), produced rear filling general employing gravity flow, filling speed is slow, and reactor 102 underflow is unclean, causes difficulty to cleaning equipment.
Therefore, prior art existing defects, needs to improve.
Utility model content
The purpose of this utility model overcomes the deficiencies in the prior art, the EGR in providing a kind of glass cleaner to produce.
The technical solution of the utility model is as follows: the EGR during the utility model provides a kind of glass cleaner to produce, comprise: reactor, be located at the agitator in described reactor, drive the drive motors of described agitator, by the first pipeline and the discharging opening be connected bottom described reactor, be located at the filter on the first pipeline between described discharging opening and reactor, be located at the vavuum pump on the first pipeline between described filter and discharging opening, be located at the discharge valve on the first pipeline between described vavuum pump and discharging opening and circulation valve, described reactor top is provided with a charging aperture, described charging aperture is by second pipe and described vavuum pump, the first pipeline communication between discharge valve, described circulation valve is installed on described second pipe.
EGR in described glass cleaner production also comprises: the 3rd pipeline being located at the gravity flow valve on the first pipeline between described filter and reactor and the first pipeline communication between described filter and gravity flow valve and the material inlet valve be located on described 3rd pipeline.
Described discharge valve, circulation valve, gravity flow valve and material inlet valve are acid and alkali-resistance ball valve.
Described vavuum pump is acid and alkali-resistance vavuum pump.
Adopt such scheme, the EGR in glass cleaner production of the present utility model, has the following advantages:
1, shorten the material dissolution time, shorten to 1/3rd of existing normal agitation dissolution velocity required time, improve the uniformity of material reaction mixing;
2, can directly carry liquid material to reactor from ground, without the need to the equipment such as fork truck, lifting platform by feedstock delivery on operating platform, greatly reduce the intensity of equipment and workman;
3, adopt vavuum pump to carry in filling bucket fast, the filling time can be accelerated and save the filling time, can reduce by the filling time of 3/4ths.
Accompanying drawing explanation
Fig. 1 is the structural representation producing glass cleaner reactor used in prior art.
Fig. 2 is the structural representation of the EGR during the utility model glass cleaner is produced.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in detail.
Refer to Fig. 2, EGR during the utility model provides a kind of glass cleaner to produce, comprise: reactor 2, be located at the agitator 4 in described reactor 2, drive the drive motors 6 of described agitator 4, by the first pipeline 8 and the discharging opening 12 be connected bottom described reactor 2, be located at the filter 14 on the first pipeline 8 between described discharging opening 12 and reactor 2, be located at the vavuum pump 16 on the first pipeline 8 between described filter 14 and discharging opening 12, be located at the discharge valve 18 on the first pipeline 8 between described vavuum pump 16 and discharging opening 12 and circulation valve 22, described reactor 2 top is provided with a charging aperture 24, described charging aperture 24 is by second pipe 26 and described vavuum pump 16, the first pipeline 8 between discharge valve 18 is communicated with, described circulation valve 22 is installed on described second pipe 26.
Further, the EGR in described glass cleaner production also comprises: be located at the 3rd pipeline 32 that described filter 14 is communicated with the gravity flow valve 28 on the first pipeline 8 between reactor 2 and the first pipeline 8 between described filter 14 with gravity flow valve 28 and the material inlet valve 34 be located on described 3rd pipeline 32.
According to the needs used, described discharge valve 18, circulation valve 22, gravity flow valve 28 and material inlet valve 34 are acid and alkali-resistance ball valve.Described vavuum pump 16 is acid and alkali-resistance vavuum pump.
EGR in the glass cleaner production that the utility model provides has the following advantages and realizes principle:
(1), shorten the material dissolution time, shorten to 1/3rd of existing normal agitation dissolution velocity required time, improve the uniformity of material reaction mixing.Concrete operations are: close material inlet valve 34 and discharge valve 18, open circulation valve 22 and gravity flow valve 28, open vavuum pump 16, the material in reactor 2 can be made to carry out systemic circulation, thus accelerate the dissolution velocity of solid material.
(2), can directly carry liquid material to reactor from ground, without the need to the equipment such as fork truck, lifting platform by feedstock delivery on operating platform, greatly reduce the intensity of equipment and workman.Concrete operations are: close gravity flow valve 28 and discharge valve 18, open circulation valve 22 and material inlet valve 34, open vavuum pump 16, utilize vavuum pump 14 to be pumped in reactor 2 through second pipe 26 by material.Owing to carrying out absorbing material by the 3rd pipeline 32, therefore can directly carry liquid material to reactor 2 from ground.
(3), adopt vavuum pump 16 to carry in filling bucket fast, the filling time can be accelerated and save the filling time, can reduce by the filling time of 3/4ths.Concrete operations are: close material inlet valve 34 and circulation valve 22, open gravity flow valve 28 and discharge valve 18, open vavuum pump 16, the liquid material in reactor 2 can be made to be transported to fast in filling bucket, reach the object of Quick-filling.
These are only preferred embodiment of the present utility model, be not limited to the utility model, all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (4)
1. the EGR in a glass cleaner production, it is characterized in that, comprise: reactor, be located at the agitator in described reactor, drive the drive motors of described agitator, by the first pipeline and the discharging opening be connected bottom described reactor, be located at the filter on the first pipeline between described discharging opening and reactor, be located at the vavuum pump on the first pipeline between described filter and discharging opening, be located at the discharge valve on the first pipeline between described vavuum pump and discharging opening and circulation valve, described reactor top is provided with a charging aperture, described charging aperture is by second pipe and described vavuum pump, the first pipeline communication between discharge valve, described circulation valve is installed on described second pipe.
2. the EGR in glass cleaner production according to claim 1, it is characterized in that, also comprise: the 3rd pipeline being located at the gravity flow valve on the first pipeline between described filter and reactor and the first pipeline communication between described filter and gravity flow valve and the material inlet valve be located on described 3rd pipeline.
3. the EGR in glass cleaner production according to claim 2, it is characterized in that, described discharge valve, circulation valve, gravity flow valve and material inlet valve are acid and alkali-resistance ball valve.
4. the EGR in glass cleaner production according to claim 1, it is characterized in that, described vavuum pump is acid and alkali-resistance vavuum pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520561984.0U CN204816527U (en) | 2015-07-30 | 2015-07-30 | Circulating device in glass cleaning agent production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520561984.0U CN204816527U (en) | 2015-07-30 | 2015-07-30 | Circulating device in glass cleaning agent production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204816527U true CN204816527U (en) | 2015-12-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520561984.0U Active CN204816527U (en) | 2015-07-30 | 2015-07-30 | Circulating device in glass cleaning agent production |
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| CN (1) | CN204816527U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109225097A (en) * | 2018-09-07 | 2019-01-18 | 佛山市科顺建筑材料有限公司 | A kind of reaction kettle cleaning system and cleaning method |
-
2015
- 2015-07-30 CN CN201520561984.0U patent/CN204816527U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109225097A (en) * | 2018-09-07 | 2019-01-18 | 佛山市科顺建筑材料有限公司 | A kind of reaction kettle cleaning system and cleaning method |
| CN109225097B (en) * | 2018-09-07 | 2024-02-20 | 佛山市科顺建筑材料有限公司 | Reaction kettle cleaning system and method |
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| GR01 | Patent grant |