CN204644190U - A kind of heat circulation production line of concrete admixture - Google Patents
A kind of heat circulation production line of concrete admixture Download PDFInfo
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- CN204644190U CN204644190U CN201520324572.5U CN201520324572U CN204644190U CN 204644190 U CN204644190 U CN 204644190U CN 201520324572 U CN201520324572 U CN 201520324572U CN 204644190 U CN204644190 U CN 204644190U
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Abstract
The utility model relates to concrete admixture production technical field, discloses a kind of heat circulation production line of concrete admixture.Raw material storage unit comprises acrylic acid measuring tank, A material-compound tank and B material-compound tank.Acrylic acid measuring tank is connected with A material-compound tank, and A material-compound tank is connected with water inlet pipe with B material-compound tank.Raw material drips unit and comprises A dropping tank, B dropping tank, hydrogen peroxide dropping tank and liquid caustic soda dropping tank.A drips tank, B drips tank and is connected with A material-compound tank, B material-compound tank respectively.Reaction member comprises reactor, and its opening for feed drips tank with A respectively, B drips tank, hydrogen peroxide drips tank, liquid caustic soda drips tank and water inlet pipe is connected.Composite unit comprises resin polymerization still, and C drips tank and batch mixing stirred pot, and resin polymerization still, C drip tank and be all connected with batch mixing stirred pot with reactor, and finished product storage element comprises product storage tank, and it is connected with batch mixing stirred pot.The utility model level of automation is high, energy-saving and emission-reduction, and production efficiency is high.
Description
Technical field
The utility model relates to concrete admixture production technical field, particularly relates to a kind of heat circulation production line of concrete admixture.
Background technology
In recent years, every infrastructure construction of China is more and more faster, and corresponding material of construction have also been obtained very fast development.In the face of huge market demand, the production technology of the building material product of domestic most building supplies business is obviously unable to catch up with current trend.
In the production technology of concrete admixture, domestic many manufacturers still adopt comparatively traditional, that level of automation is low production line, although there is part producing producer to carry out automatic improving to a certain extent, still there is the problems such as production line automation degree is not high enough, Design of Production Line is complicated, unreasonable in the concrete admixture after transformation and upgrade.
Therefore, the production line of concrete admixture still needs the upgrading that keeps, and improves level of automation and production efficiency.
Utility model content
In order to solve the problems of the technologies described above, the utility model provides a kind of heat circulation production line of concrete admixture, and this production line automation degree is high, and production efficiency is high, controls accurately the consumption of material and each reaction conditions.
Concrete technical scheme of the present utility model is: a kind of heat circulation production line of concrete admixture, comprises raw material storage unit, raw material drips unit, reaction member, composite unit and finished product storage element.
Described raw material storage unit comprises acrylic acid measuring tank, A material-compound tank and B material-compound tank, described acrylic acid measuring tank is provided with opening for feed, pressure control mouth and discharge port, described A material-compound tank is provided with water-in, opening for feed and discharge port, and described B material-compound tank is provided with water-in and discharge port.
Wherein, the discharge port of acrylic acid measuring tank is connected with the opening for feed of A material-compound tank, and A material-compound tank is connected with water inlet pipe with the water-in on B material-compound tank.
Described raw material drips unit and comprises A dropping tank, B dropping tank, hydrogen peroxide dropping tank and liquid caustic soda dropping tank, described A drips tank, B drips tank, hydrogen peroxide drips tank and liquid caustic soda dropping tank is equipped with opening for feed and discharge port, and A drips tank, B drips tank, hydrogen peroxide drips on tank and is also provided with pressure control mouth.
Wherein, the opening for feed that A drips tank is connected with the discharge port of A material-compound tank, and the opening for feed that B drips tank is connected with the discharge port of B material-compound tank; Pressure control mouth on acrylic acid measuring tank, A dropping tank, B dropping tank, hydrogen peroxide dropping tank and vacuum pump are connected by pneumatic tube.
Described reaction member comprises reactor, and described reactor is provided with 5 opening for feeds and 1 discharge port, and reactor is also provided with cooling system, and described cooling system comprises recirculated water spiral cold-finger, water-in, water outlet and thermometer.
5 opening for feeds on reactor drip tank with A respectively, B drips tank, hydrogen peroxide drips tank, liquid caustic soda drips tank and water inlet pipe is connected, and water-in, the water outlet of reactor are connected with outside circulating pipe;
Described composite unit comprises resin polymerization still, C drips tank and batch mixing stirred pot, described resin polymerization still is provided with 2 opening for feeds and 1 discharge port, described C drips tank and is provided with an opening for feed and a discharge port, and batch mixing stirred pot is provided with 3 opening for feeds and a discharge port.
Discharge port, the C of resin polymerization still drip the discharge port of tank, the discharge port of reactor is connected with the opening for feed of 3 on batch mixing stirred pot respectively, whipping appts is provided with in batch mixing stirred pot, the section of tubing of described circulating pipe is located in resin polymerization still, and is located at the circulating pipe helically type in resin polymerization still.
Described finished product storage element comprises product storage tank, and product storage tank is provided with opening for feed and is connected with the discharge port of batch mixing stirred pot.
As preferably, described A dropping tank, B dropping tank, acrylic acid measuring tank, hydrogen peroxide dropping tank, liquid caustic soda dropping tank and C dropping tank are equipped with weighing device.
As preferably, described raw material drips unit and includes 2 A in parallel and drip tank and 2 B in parallel drip tank.
As preferably, described reaction member comprises 2 reactors in parallel.
Be compared with the prior art, the beneficial effects of the utility model are: production line automation degree of the present utility model is high, whole process can pass through conputer controlled, pass through conputer controlled, accurately can control the consumption to material and the control of each reaction conditions, not only production efficiency is high, and the concrete admixture performance of preparation is good.In addition, the setting of circulating pipe, makes the water after heating up in reactor flow through in resin polymerization still through circulating pipe, heats, take full advantage of heat, energy-saving and emission-reduction to material in resin polymerization still.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of the present utility model.
Reference numeral is: acrylic acid measuring tank 1, A material-compound tank 2, B material-compound tank 3, water inlet pipe 4, A drip tank 5, B drips tank 6, hydrogen peroxide drips tank 7, liquid caustic soda drips tank 8, vacuum pump 9, gas transmission 710, reactor 11, recirculated water spiral cold-finger 12, thermometer 13, circulating pipe 14, resin polymerization still 15, C drip tank 16, batch mixing stirred pot 17, product storage tank 18, weighing device 19.
Embodiment
Below in conjunction with embodiment, the utility model will be further described.
Embodiment 1
As shown in Figure 1: a kind of heat circulation production line of concrete admixture, comprise raw material storage unit, raw material drips unit, reaction member, composite unit and finished product storage element.
Described raw material storage unit comprises acrylic acid measuring tank 1, A material-compound tank 2 and B material-compound tank 3, described acrylic acid measuring tank is provided with opening for feed, pressure control mouth and discharge port, described A material-compound tank is provided with water-in, opening for feed and discharge port, and described B material-compound tank is provided with water-in and discharge port;
Wherein, the discharge port of acrylic acid measuring tank is connected with the opening for feed of A material-compound tank, and A material-compound tank is connected with water inlet pipe 4 with the water-in on B material-compound tank;
Described raw material dropping unit comprises 2 A dropping tank 5,2 B in parallel dropping tanks 6 in parallel, hydrogen peroxide drips tank 7 and liquid caustic soda drip tank 8, described A drips tank, B drips tank, hydrogen peroxide drips tank and liquid caustic soda dropping tank is equipped with opening for feed and discharge port, and A drips tank, B drips tank, hydrogen peroxide drips on tank and is also provided with pressure control mouth.
Wherein, the opening for feed that A drips tank is connected with the discharge port of A material-compound tank, and the opening for feed that B drips tank is connected with the discharge port of B material-compound tank; Pressure control mouth on acrylic acid measuring tank, A dropping tank, B dropping tank, hydrogen peroxide dropping tank and vacuum pump 9 are connected by pneumatic tube 10.
Described reaction member comprises 2 reactors 11 in parallel, and described reactor is provided with 5 opening for feeds and 1 discharge port, and reactor is also provided with cooling system, and described cooling system comprises recirculated water spiral cold-finger 12, water-in, water outlet and thermometer 13.
5 opening for feeds on reactor drip tank with A respectively, B drips tank, hydrogen peroxide drips tank, liquid caustic soda drips tank and water inlet pipe is connected, and water-in, the water outlet of reactor are connected with outside circulating pipe 14;
Described composite unit comprises resin polymerization still 15, C drips tank 16 and batch mixing stirred pot 17, described resin polymerization still is provided with 2 opening for feeds and 1 discharge port, described C drips tank and is provided with an opening for feed and a discharge port, and batch mixing stirred pot is provided with 3 opening for feeds and a discharge port.
Discharge port, the C of resin polymerization still drip the discharge port of tank, the discharge port of reactor is connected with the opening for feed of 3 on batch mixing stirred pot respectively, whipping appts is provided with in batch mixing stirred pot, the section of tubing of described circulating pipe is located in resin polymerization still, and is located at the circulating pipe helically type in resin polymerization still.
Described finished product storage element comprises product storage tank 18, and product storage tank is provided with opening for feed and is connected with the discharge port of batch mixing stirred pot.
Described A drips tank, B drips tank, acrylic acid measuring tank, hydrogen peroxide drip tank, liquid caustic soda drips tank and C dropping tank is equipped with weighing device 19.
During the work of this production line, vinylformic acid is stored in acrylic acid measuring tank, fed in raw material to A material-compound tank by acrylic acid measuring tank, B material-compound tank stores other raw materials.Water inlet pipe and A material-compound tank are communicated with the water-in of B material-compound tank and add water to it.
Drip tank by A material-compound tank and B material-compound tank respectively to each A dropping tank and B to feed in raw material.
Then, drip tank by A, B drips tank, hydrogen peroxide drips tank and liquid caustic soda dropping tank adds materials to reactor.A dropping tank, B dropping tank, acrylic acid measuring tank, hydrogen peroxide drip tank and are all connected with vacuum pump with liquid caustic soda dropping tank, and vacuum pump control A dropping tank, B dropping tank, acrylic acid measuring tank, hydrogen peroxide dropping tank and liquid caustic soda drip the pressure in tank.Be provided with cooling system in reactor, temperature control can be carried out to the material in reactor.And the water after heating up in reactor flows through in resin polymerization still through circulating pipe, heats, take full advantage of heat, energy-saving and emission-reduction to material in resin polymerization still.
The polymerization of resin is carried out in resin polymerization still, C drips in tank and stores the raw material such as accelerating component, viscosity reduction component, reactor, resin polymerization and still C drip the discharge port of tank and the opening for feed of batch mixing stirred pot, and mixture is after batch mixing stirred pot stirs, and its product transfers to finished product memotron.
The opening for feed of each test tank of the present utility model, material-compound tank, dropping tank, reactor and hold-up vessel, water-in, discharge port are equipped with valve, and these valves can be regulated by conputer controlled, realize accurately feeding in raw material.
The above; it is only preferred embodiment of the present utility model; not the utility model is imposed any restrictions; every above embodiment is done according to the utility model technical spirit any simple modification, change and equivalent structure transformation, all still belong to the protection domain of technical solutions of the utility model.
Claims (4)
1. a heat circulation production line for concrete admixture, is characterized in that: comprise raw material storage unit, raw material drips unit, reaction member, composite unit and finished product storage element;
Described raw material storage unit comprises acrylic acid measuring tank (1), A material-compound tank (2) and B material-compound tank (3), described acrylic acid measuring tank is provided with opening for feed, pressure control mouth and discharge port, described A material-compound tank is provided with water-in, opening for feed and discharge port, and described B material-compound tank is provided with water-in and discharge port;
Wherein, the discharge port of acrylic acid measuring tank is connected with the opening for feed of A material-compound tank, and A material-compound tank is connected with water inlet pipe (4) with the water-in on B material-compound tank;
Described raw material drips unit and comprises A dropping tank (5), B dropping tank (6), hydrogen peroxide dropping tank (7) and liquid caustic soda dropping tank (8), described A drips tank, B drips tank, hydrogen peroxide drips tank and liquid caustic soda dropping tank is equipped with opening for feed and discharge port, and A drips tank, B drips tank, hydrogen peroxide drips on tank and is also provided with pressure control mouth
Wherein, the opening for feed that A drips tank is connected with the discharge port of A material-compound tank, and the opening for feed that B drips tank is connected with the discharge port of B material-compound tank; Pressure control mouth on acrylic acid measuring tank, A dropping tank, B dropping tank, hydrogen peroxide dropping tank and vacuum pump (9) are connected by pneumatic tube (10);
Described reaction member comprises reactor (11), described reactor is provided with 5 opening for feeds and 1 discharge port, reactor is also provided with cooling system, and described cooling system comprises recirculated water spiral cold-finger (12), water-in, water outlet and thermometer (13); 5 opening for feeds on reactor drip tank with A respectively, B drips tank, hydrogen peroxide drips tank, liquid caustic soda drips tank and water inlet pipe is connected, and water-in, the water outlet of reactor are connected with outside circulating pipe (14);
Described composite unit comprises resin polymerization still (15), C drips tank (16) and batch mixing stirred pot (17), described resin polymerization still is provided with 2 opening for feeds and 1 discharge port, described C drips tank and is provided with an opening for feed and a discharge port, and batch mixing stirred pot is provided with 3 opening for feeds and a discharge port;
Discharge port, the C of resin polymerization still drip the discharge port of tank, the discharge port of reactor is connected with the opening for feed of 3 on batch mixing stirred pot respectively, are provided with whipping appts in batch mixing stirred pot; The section of tubing of described circulating pipe is located in resin polymerization still, and is located at the circulating pipe helically type in resin polymerization still;
Described finished product storage element comprises product storage tank (18), and product storage tank is provided with opening for feed and is connected with the discharge port of batch mixing stirred pot.
2. the heat circulation production line of concrete admixture as claimed in claim 1, is characterized in that, described A drips tank, B drips tank, acrylic acid measuring tank, hydrogen peroxide dropping tank, liquid caustic soda dropping tank and C drip on tank and be equipped with weighing device (19).
3. the heat circulation production line of concrete admixture as claimed in claim 1, is characterized in that, described raw material drips unit and includes 2 A in parallel and drip tank and 2 B in parallel drip tank.
4. the heat circulation production line of concrete admixture as claimed in claim 1, it is characterized in that, described reaction member comprises 2 reactors in parallel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520324572.5U CN204644190U (en) | 2015-05-16 | 2015-05-16 | A kind of heat circulation production line of concrete admixture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520324572.5U CN204644190U (en) | 2015-05-16 | 2015-05-16 | A kind of heat circulation production line of concrete admixture |
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| CN204644190U true CN204644190U (en) | 2015-09-16 |
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| CN201520324572.5U Expired - Fee Related CN204644190U (en) | 2015-05-16 | 2015-05-16 | A kind of heat circulation production line of concrete admixture |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109954456A (en) * | 2017-12-25 | 2019-07-02 | 宜兴市兴南复合材料厂有限公司 | Resin reaction kettle with automatic recipe maker |
-
2015
- 2015-05-16 CN CN201520324572.5U patent/CN204644190U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109954456A (en) * | 2017-12-25 | 2019-07-02 | 宜兴市兴南复合材料厂有限公司 | Resin reaction kettle with automatic recipe maker |
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| 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: 20150916 Termination date: 20160516 |