CN204661567U - A kind of production system of diminishing recombiner - Google Patents
A kind of production system of diminishing recombiner Download PDFInfo
- Publication number
- CN204661567U CN204661567U CN201520224708.5U CN201520224708U CN204661567U CN 204661567 U CN204661567 U CN 204661567U CN 201520224708 U CN201520224708 U CN 201520224708U CN 204661567 U CN204661567 U CN 204661567U
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- tank
- storage tank
- reducer
- reaction still
- enamel reaction
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Abstract
The utility model relates to a kind of production system of diminishing recombiner, comprises polymerization single polymerization monomer storage tank, initiator storage tank, nitrogen storage tank, composite tank, enamel reaction still; Described polymerization single polymerization monomer storage tank, initiator storage tank are connected respectively by the feed-pipe of a flow director and described enamel reaction still, minim pipette, described nitrogen storage tank is connected by the inlet pipe of gas flow controller with described enamel reaction still, the discharge nozzle of described enamel reaction still is connected with polycarboxylate water-reducer hold-up vessel, and described polycarboxylate water-reducer hold-up vessel forms tank by the pipeline being provided with transferpump with mixing addition material and is connected; The discharge nozzle that mixing addition material admission port and the described mixing addition material of described composite tank form tank communicates, and the clear water admission port of described composite tank is connected with clear water storage tank by the pipeline being provided with water pump.The utility model can control automatically, guarantees water reducer reliable product quality.
Description
Technical field
The utility model belongs to the production system of diminishing recombiner, is specifically related to a kind of production system of diminishing recombiner.
Background technology
Polycarboxylate water-reducer is a kind of admixture be of wide application in concrete admixture, proposes more and higher requirement with fundamental construction development to concrete performance.
High performance Water-reducing Admixtures To Cements has high dissemination, can keep concrete bright degree of falling preferably.Infiltrating this kind of admixture can make concrete have high-performance, can obtain high-strength high-performance concrete.
Polycarboxylate water-reducer is high efficiency water reducing agent conventional at present, and the bitter edible plant based water reducer that its working condition is more general is more harsh, if in polymerization process, monomer polymerization is incomplete, not only has environmental protection hidden danger, and can affect concrete performance.
Utility model content
The production system of the diminishing recombiner that the purpose of this utility model is to solve above-mentioned technical problem and provides a kind of high-efficient automatic to control.
The utility model is achieved in that a kind of production system of diminishing recombiner, comprises polymerization single polymerization monomer storage tank, initiator storage tank, nitrogen storage tank, composite tank, enamel reaction still; Described polymerization single polymerization monomer storage tank, initiator storage tank are connected respectively by the feed-pipe of a flow director and described enamel reaction still, minim pipette, described nitrogen storage tank is connected by the inlet pipe of gas flow controller with described enamel reaction still, the discharge nozzle of described enamel reaction still is connected with polycarboxylate water-reducer hold-up vessel, and described polycarboxylate water-reducer hold-up vessel forms tank by the pipeline being provided with transferpump with mixing addition material and is connected; The discharge nozzle that mixing addition material admission port and the described mixing addition material of described composite tank form tank communicates, and the clear water admission port of described composite tank is connected with clear water storage tank by the pipeline being provided with water pump.
Described enamel reaction still is made up of enamel internal layer still wall and the outer still wall of stainless steel, and form chuck layer between described enamel internal layer still wall and the outer still wall of described stainless steel, described chuck layer is provided with heating medium import and Crude product input; Described kettle top is also provided with electric motor, and described motor output shaft is connected with reducer input shaft, and described reducer output shaft is connected with the rotating shaft stretched in tank body, described in turn the tip of the axis and be provided with agitator.
Described polycarboxylate water-reducer hold-up vessel, mixing addition material are formed bottom tank, clear water storage tank and are equipped with gage probe.
The advantage such as the production system of the utility model diminishing recombiner has efficiently, environmental protection, production cost are low, economize in raw materials, can to flow information, and then conservative control is carried out to electric motor, flow, guarantee that in still, material is in strict accordance with the polymerization of setting operating mode, each material after accurate-metering can be carried out Homogeneous phase mixing by composite tank, guarantees water reducer reliable product quality.
Accompanying drawing explanation
Figure 1 shows that the schematic diagram of the production system of the diminishing recombiner that the utility model provides.
Embodiment
Below, in conjunction with example, substantive distinguishing features of the present utility model and advantage are further described, but the utility model is not limited to listed embodiment.
Shown in Figure 1, a kind of production system of diminishing recombiner, comprises polymerization single polymerization monomer storage tank 8, initiator storage tank 9, nitrogen storage tank 10, composite tank 4, enamel reaction still 1; Described polymerization single polymerization monomer storage tank 8, initiator storage tank 9 are connected respectively by the feed-pipe of a first flow controller 11, second amount controller 12 and described enamel reaction still 1, minim pipette, described nitrogen storage 10 tank is connected with the inlet pipe of described enamel reaction still 1 by gas flow controller 13, the discharge nozzle of described enamel reaction still 1 is connected with polycarboxylate water-reducer hold-up vessel 2, and described polycarboxylate water-reducer hold-up vessel 2 forms tank 3 by the pipeline being provided with transferpump 6 with mixing addition material and is connected; The discharge nozzle that mixing addition material admission port and the described mixing addition material of described composite tank 4 form tank 3 communicates, and the clear water admission port of described composite tank 4 is connected with clear water storage tank 5 by the pipeline being provided with water pump 7.
Described enamel reaction still is made up of enamel internal layer still wall and the outer still wall of stainless steel, and form chuck layer between described enamel internal layer still wall and the outer still wall of described stainless steel, described chuck layer is provided with heating medium import and Crude product input; Described kettle top is also provided with electric motor, and described motor output shaft is connected with reducer input shaft, and described reducer output shaft is connected with the rotating shaft stretched in tank body, described in turn the tip of the axis and be provided with agitator.
Described polycarboxylate water-reducer hold-up vessel 2, mixing addition material are formed bottom tank 3, clear water storage tank 5 and are equipped with gage probe.
Be provided with agitator in the tank body of described mixing addition material formation tank 3, connect with the output shaft of motor and step-down gear, in the tank body of described composite tank 4, be provided with agitator device, and the output shaft of the motor and step-down gear that are arranged on tank body top connect.
The feed end of described composite tank 4 and described polycarboxylate water-reducer hold-up vessel 2, mix addition material and form the material pipe that tank 3 connects and be provided with electrically-controlled valve, be connected with controller respectively.
The water inlet pipe of described clear water storage tank 5 and the clear water transfer lime connected with described composite tank 4 have been provided with magnetic valve, connect respectively with described controller.
Described controller, by gage probe, judges the amount of material in each tank body, and Controlling solenoid valve or electrically-controlled valve are opened or closed, and realize the automatic control added material etc., thus achieve the production control of automatization.
The advantage such as the utility model has efficiently, environmental protection, production cost are low, economize in raw materials, can to flow information, and then conservative control is carried out to electric motor, flow, guarantee that in still, material is in strict accordance with the polymerization of setting operating mode, each material after accurate-metering can be carried out Homogeneous phase mixing by composite tank, guarantees water reducer reliable product quality.
The high-performance polycarboxylic acids water reducing agent that the utility model is produced has good water-reducing effect, and water-reducing rate can reach more than 45%, therefore has good promotional value and market outlook.
Claims (3)
1. a production system for diminishing recombiner, is characterized in that, comprises polymerization single polymerization monomer storage tank, initiator storage tank, nitrogen storage tank, composite tank, enamel reaction still; Described polymerization single polymerization monomer storage tank, initiator storage tank are connected respectively by the feed-pipe of a flow director and described enamel reaction still, minim pipette, described nitrogen storage tank is connected by the inlet pipe of gas flow controller with described enamel reaction still, the discharge nozzle of described enamel reaction still is connected with polycarboxylate water-reducer hold-up vessel, and described polycarboxylate water-reducer hold-up vessel forms tank by the pipeline being provided with transferpump with mixing addition material and is connected; The discharge nozzle that mixing addition material admission port and the described mixing addition material of described composite tank form tank communicates, and the clear water admission port of described composite tank is connected with clear water storage tank by the pipeline being provided with water pump.
2. the production system of diminishing recombiner according to claim 1, it is characterized in that, described enamel reaction still is made up of enamel internal layer still wall and the outer still wall of stainless steel, form chuck layer between described enamel internal layer still wall and the outer still wall of described stainless steel, described chuck layer is provided with heating medium import and Crude product input; Described kettle top is also provided with electric motor, and described motor output shaft is connected with reducer input shaft, and described reducer output shaft is connected with the rotating shaft stretched in tank body, described in turn the tip of the axis and be provided with agitator.
3. the production system of diminishing recombiner according to claim 2, is characterized in that, described polycarboxylate water-reducer hold-up vessel, mixing addition material are formed bottom tank, clear water storage tank and be equipped with gage probe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520224708.5U CN204661567U (en) | 2015-04-10 | 2015-04-10 | A kind of production system of diminishing recombiner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520224708.5U CN204661567U (en) | 2015-04-10 | 2015-04-10 | A kind of production system of diminishing recombiner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204661567U true CN204661567U (en) | 2015-09-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520224708.5U Expired - Fee Related CN204661567U (en) | 2015-04-10 | 2015-04-10 | A kind of production system of diminishing recombiner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204661567U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107488837A (en) * | 2017-09-20 | 2017-12-19 | 大连理工大学 | Material microcosmic surface syntype coating system |
| CN111151212A (en) * | 2020-01-20 | 2020-05-15 | 安徽昌宁新材料有限公司 | Integrated water reducer synthesis and compounding equipment, control system and leasing method |
| CN114259966A (en) * | 2021-12-31 | 2022-04-01 | 重庆助扬建材有限公司 | Polycarboxylic acid water reducing agent and amino water reducing agent composite production system |
-
2015
- 2015-04-10 CN CN201520224708.5U patent/CN204661567U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107488837A (en) * | 2017-09-20 | 2017-12-19 | 大连理工大学 | Material microcosmic surface syntype coating system |
| CN107488837B (en) * | 2017-09-20 | 2019-04-16 | 大连理工大学 | Material microcosmic surface syntype coating system |
| CN111151212A (en) * | 2020-01-20 | 2020-05-15 | 安徽昌宁新材料有限公司 | Integrated water reducer synthesis and compounding equipment, control system and leasing method |
| CN114259966A (en) * | 2021-12-31 | 2022-04-01 | 重庆助扬建材有限公司 | Polycarboxylic acid water reducing agent and amino water reducing agent composite production system |
| CN114259966B (en) * | 2021-12-31 | 2024-01-16 | 重庆助扬建材有限公司 | Polycarboxylate water reducing agent and amino water reducing agent composite production system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150923 Termination date: 20200410 |