CN204631573U - Polymerization osamine automated production equipment - Google Patents
Polymerization osamine automated production equipment Download PDFInfo
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- CN204631573U CN204631573U CN201520143120.7U CN201520143120U CN204631573U CN 204631573 U CN204631573 U CN 204631573U CN 201520143120 U CN201520143120 U CN 201520143120U CN 204631573 U CN204631573 U CN 204631573U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/02—Total factory control, e.g. smart factories, flexible manufacturing systems [FMS] or integrated manufacturing systems [IMS]
Abstract
The utility model relates to a kind of polymerization osamine automated production equipment, belongs to chemical field.The technical scheme that this patent adopts is: comprise four groups of level meter measuring tanks and the one group of powder metering tank of expecting sensor with position fixed by platform support, first liquid test tank is wherein connected stirred pot with the discharging opening of powder metering tank by pipeline, second liquid test tank, the discharging opening of the 3rd level meter measuring tank and the 4th level meter measuring tank is connected to one by pipeline and has heating cooling power and with the reactor of temperature sensor, the discharging opening of above-mentioned stirred pot is connected to above-mentioned reactor by pipeline, connecting tube between above-mentioned reactor and stirred pot is provided with feeding pump, the middle part of reactor is also connected with a catalyst feeds and connects catalyst feeding device, the discharging opening of reactor is connected to finished pot by pipeline, pipeline between reactor and finished pot is provided with discharging pump.This patent realizes the full-automatic constant product quality of production run, indifference between batch.
Description
Technical field
The present invention relates to a kind of polymerization osamine automated production equipment, belong to chemical field.
Background technology
Polymerization osamine is as the cement grinding aid raw material of a kind of new life, and it improves the applicability of cement grinding aid and the compatibility of concrete admixture greatly, and application prospect is fine.Lack polymerization osamine automated production equipment in market, and the product homogenisation that common process is produced is poor, batch between the property of there are differences.
Summary of the invention
The object of this patent is to provide a kind of polymerization osamine automated production equipment, realizes production run full-automation, reduces error, the polymerization sugar amine product steady quality produced, indifference between batch.
For achieving the above object, the technical scheme that this patent adopts is: comprise four groups of level meter measuring tanks and the one group of powder metering tank of expecting sensor with position fixed by platform support, first liquid test tank is wherein connected stirred pot with the discharging opening of powder metering tank by pipeline, second liquid test tank, the discharging opening of the 3rd level meter measuring tank and the 4th level meter measuring tank is connected to one by pipeline and has heating cooling power and with the reactor of temperature sensor, the discharging opening of above-mentioned stirred pot is connected to above-mentioned reactor by pipeline, connecting tube between above-mentioned reactor and stirred pot is provided with feeding pump, the middle part of reactor is also connected with a catalyst feeds and connects catalyst feeding device, the discharging opening of reactor is connected to finished pot by pipeline, pipeline between reactor and finished pot is provided with discharging pump.
As preferably, the discharging opening of described level meter measuring tank is provided with pneumatic valve, and the discharging opening of powder metering tank is provided with flap valve.
As preferably, described reactor is three layers, and inside is reaction chamber, and outermost layer is cooling water layer, and middle layer is heat conduction oil reservoir.As preferably, the discharging opening of reactor is provided with pneumatic valve; The heat conduction oil reservoir of described reactor is connected to conduction oil pumping plant by pipeline, and cooling water layer is connected to circulating cooling pond by the pipeline being provided with water pump; The pipeline that described powder metering tank discharging opening connects is stainless steel pipes, and described reactor is built with stirring apparatus.
The advantage of this patent is: by metering system, discharging pneumatic valve, and stirring apparatus realizes production run full-automation, reduces error, constant product quality, indifference between batch.
Accompanying drawing explanation
Fig. 1 is the structural drawing of this patent;
Reference numeral: 1, platform support, 2, powder metering tank, 3, position material sensor, 4, pneumatic valve, 5, first liquid test tank, 6, flap valve, 7, stirred pot, 8, feeding pump, 9, reactor, 10, conduction oil pumping plant, 11, discharging pump, 12, catalyst feeding device, 13, water pump, 14, circulating cooling pond, 15, finished pot, 16, second liquid test tank, the 17, the 3rd level meter measuring tank, the 18, the 4th level meter measuring tank.
Embodiment
According to Fig. 1, platform support has the hole of 900mm diameter, each test tank is placed in 900mm hole by the foot support of position material sensor.
Fill raw water with in the level meter measuring tank that powder metering tank batch mixing stirs, this raw water selects tap water, and its excess-three level meter measuring tank is respectively charged into molasses, amino acid solution, alcohol.Pneumatic valve is equipped with in each level meter measuring tank bottom.Powder metering tank bottom dress flap valve.
Stirred pot is that the stainless steel of diameter 2.0*2.5 is made, and with motor vertical shaft reductor and paddle, paddle top is connected with reductor shaft joint, and bottom is contained in the sliding bearing groove bottom stirred pot.Stirred pot discharge pipe establishes feeding pump, and discharge pipe is the PPR pipe road of 63mm, and passes to reactor.Reactor temperature change can show from control terminal and be provided with feedback control loop.Manhole door is arranged at reactor top, for observing the change of material materials inside reaction and adding catalyzer in time.
The stirring apparatus of reactor is equipped with motor, reductor and paddle, and paddle is fixed on reductor by interlock joint.The discharging opening pneumatic valve of reactor to be fixed on reactor by flange and to be connected with feeding pump by PPR pipe road.In reactor, reacted finished product is evacuated in finished pot by discharging pump by PPR pipe road.
The implementation method of technological process is described below in conjunction with accompanying drawing:
Water is according to the weight blanking of 28wt%, and stirred pot is clicked and opened;
Powder starts the weight blanking by 3 wt %, and abundant stirring and dissolving falls in stirring machine, 5 minutes summers of conputer controlled, 10 minutes winters, stirs and stop after time of arrival;
Feeding pump motor is opened, and be extracted in reactor by the material in stirred pot, when there is vacuum, pump stops automatically;
Second liquid test tank bottom pneumatic valve is opened automatically, and material enters reactor by pipeline, closes when arriving the weight of 40.5 wt %;
When the pneumatic valve of second liquid test tank cuts out, conduction oil pumping plant unlatching work, heat-conducting oil heating reactor, squeezes into reactor by station internal circulation pump and heats, and stops ebullator working on when temperature reaches 60 DEG C;
The pneumatic valve of the 3rd level meter measuring tank starts, and the First Astronautic Research Institute for Measurement and Test needs weight liquid charging stock to flow into reactor by pipeline, when reaching the weight of 22 wt %, automatically closes;
The pneumatic valve of the 4th level meter measuring tank starts, and when reaching the weight of 4wt%, automatically closes;
Conduction oil pumping plant is opened, and when reactor temperature arrives 60 DEG C, the weight percent catalyst of metering 2.5% joins in reactor;
When reactor temperature arrives 80 DEG C, oil pump stops, and water circulating pump is automatically opened and cold water is squeezed into reactor cooling from circulating water pool, and when chilling temperature is to 30 DEG C, cooling-water pump stops automatically;
Pneumatic valve in reactor and discharging pump are opened automatically, by reactor and finished pot connecting tube, squeeze in finished pot.
When there is vacuum in reactor, the pneumatic valve in reactor and discharging pump are closed automatically.
Claims (6)
1. a polymerization osamine automated production equipment, it is characterized in that, comprise by fixing four groups of level meter measuring tanks and the one group of powder metering tank of expecting sensor (3) with position of platform support (1), first liquid test tank (5) is wherein connected stirred pot (7) with the discharging opening of powder metering tank (2) by pipeline, second liquid test tank (16), the discharging opening of the 3rd level meter measuring tank (17) and the 4th level meter measuring tank (18) is connected to one by pipeline and has heating cooling and stirring ability and with the reactor (9) of temperature sensor, the discharging opening of above-mentioned stirred pot (7) is connected to above-mentioned reactor (9) by pipeline, connecting tube between above-mentioned reactor (9) and stirred pot (7) is provided with feeding pump (8), the middle part of reactor (9) is also provided with a catalyst feeds and connects catalyst feeding device (12), the discharging opening of reactor (9) is connected to finished pot (15) by pipeline, pipeline between reactor (9) and finished pot (15) is provided with discharging pump (11).
2. polymerization osamine automated production equipment according to claim 1, is characterized in that, the discharging opening of described each group of level meter measuring tank is provided with pneumatic valve (6), and the discharging opening of powder metering tank is provided with flap valve (4).
3. polymerization osamine automated production equipment according to claim 1, is characterized in that, described reactor (9) is three layers, and inside is reaction chamber, and outermost layer is cooling water layer, and middle layer is heat conduction oil reservoir, and the discharging opening of reactor (9) is provided with pneumatic valve.
4. polymerization osamine automated production equipment according to claim 3, it is characterized in that, the heat conduction oil reservoir of described reactor is connected to conduction oil pumping plant (10) by pipeline, and cooling water layer is connected to circulating cooling pond (14) by the pipeline being provided with water pump (13).
5. polymerization osamine automated production equipment according to claim 1, is characterized in that, the pipeline that described powder metering tank discharging opening connects is stainless steel pipes.
6. polymerization osamine automated production equipment according to claim 1, is characterized in that, described reactor (9) is built with stirring apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520143120.7U CN204631573U (en) | 2015-03-13 | 2015-03-13 | Polymerization osamine automated production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520143120.7U CN204631573U (en) | 2015-03-13 | 2015-03-13 | Polymerization osamine automated production equipment |
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| Publication Number | Publication Date |
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| CN204631573U true CN204631573U (en) | 2015-09-09 |
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| CN201520143120.7U Active CN204631573U (en) | 2015-03-13 | 2015-03-13 | Polymerization osamine automated production equipment |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104765342A (en) * | 2015-03-13 | 2015-07-08 | 枣庄市荣宝莱建材科技发展有限公司 | Automated polymerized osamine production device and preparation method thereof |
| CN110132386A (en) * | 2019-06-10 | 2019-08-16 | 无锡灵鸽机械科技股份有限公司 | The liquid metering device and its application method of a kind of stirring of novel belt, heating |
-
2015
- 2015-03-13 CN CN201520143120.7U patent/CN204631573U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104765342A (en) * | 2015-03-13 | 2015-07-08 | 枣庄市荣宝莱建材科技发展有限公司 | Automated polymerized osamine production device and preparation method thereof |
| CN110132386A (en) * | 2019-06-10 | 2019-08-16 | 无锡灵鸽机械科技股份有限公司 | The liquid metering device and its application method of a kind of stirring of novel belt, heating |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 277800 Shandong city of Zaozhuang province high tech Zone Shengong Road Patentee after: Shandong Guoyuan New Material Co., Ltd. Address before: 277800 Shandong city of Zaozhuang province high tech Zone Shengong Road Patentee before: Shanghai Zople Cloud Computing Co., Ltd. |