CN203764221U - Device for extracting high-viscosity granule-containing liquid - Google Patents
Device for extracting high-viscosity granule-containing liquid Download PDFInfo
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- CN203764221U CN203764221U CN201420049373.3U CN201420049373U CN203764221U CN 203764221 U CN203764221 U CN 203764221U CN 201420049373 U CN201420049373 U CN 201420049373U CN 203764221 U CN203764221 U CN 203764221U
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- viscosity
- jacket
- liquid
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- high viscosity
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Abstract
The utility model provides a device for extracting high-viscosity granule-containing liquid. The device comprises a jacket reaction kettle and a diaphragm pump, wherein an opening is arranged at the bottom of the jacket reaction kettle; the jacket reaction kettle and the diaphragm pump are connected through a jacket steel pipe; one end of the jacket steel pipe is connected with the opening positioned at the bottom of the jacket reaction kettle, and the other end of the jacket steel pipe is connected with the diaphragm pump; the jacket reaction kettle is internally provided with a high-speed stirrer. The device provided by the utility model can reduce the viscosity of liquid by continuously heating the high-viscosity granule-containing liquid inside the jacket reaction kettle by arranging the jacket steel pipe, thereby reducing the pressure of the diaphragm pump and ensuring the delivery efficiency of the liquid; the device provided by the utility model can be used for continuously stirring a high-viscosity granule-containing liquid material in the extracting process of the high-viscosity granule-containing liquid material by arranging a high-speed stirring device in the jacket reaction kettle, thereby ensuring the uniformity of the density of the high-viscosity granule-containing liquid material.
Description
Technical field
The utility model relates to high viscosity containing particle-liquid conveying technology field, refers to especially a kind of device for high viscosity is extracted out containing particle-liquid.
Background technology
High viscosity in reactor usually needs to extract out containing particle-liquid, conventional method is at present: filling the upper opening place insertion flexible pipe of high viscosity containing the reactor container of particle-liquid, and flexible pipe is connected with the extraneous sticky pump of height or shell pump, utilize the work of high sticky pump or shell pump that the high viscosity in reactor container is retracted to assigned address containing particle-liquid along flexible pipe.
There is following defect in said method:
High sticky pump there will be holddown phenomenon when carrying the high viscosity liquid that contains particle, causes transportation work to stop, and even can damage high sticky pump; Shell pump usually there will be idle running phenomenon when transfer of highly viscous liquid, causes liquid transporting velocity to slow down.
Because the high viscosity in reactor container is containing particle-liquid Density inhomogeneity, a lot of particles can sink to container bottom in addition, further cause the fluid density of extraction inhomogeneous, affect high viscosity containing the quality of pumping of particle-liquid.
Utility model content
The utility model proposes a kind of device for high viscosity is extracted out containing particle-liquid, solved the problem that prior art medium-high viscosity contains particle-liquid material conveying process inefficiency, takes out material Density inhomogeneity.
The technical solution of the utility model is achieved in that
A device for high viscosity is extracted out containing particle-liquid, comprising: bottom is provided with jacket reactor and the membrane pump of opening; Between described jacket reactor and described membrane pump, by chuck steel pipe, be connected; One end of described chuck steel pipe is connected with the bottom opening of described jacket reactor, and its other end is connected with described membrane pump.
In described jacket reactor, be provided with high speed agitator.
The utility model also comprises frequency converter, and the input of described high speed agitator is connected with the output of described frequency converter.
The length of described chuck steel pipe is 1～2.5 meter.
Described membrane pump is pneumatic diaphragm pump.
The course of work of the present utility model and operation principle are as follows:
Extraneous thermal source constantly passes into steam or hot water by the chuck of chuck steel pipe in the chuck of jacket reactor, and the high viscosity being used in heating jacket reactor, containing particle-liquid material, makes high viscosity contain the reduced viscosity of particle-liquid; Meanwhile, high speed agitator constantly carries out high-speed stirred to the high viscosity in jacket reactor containing particle-liquid, and the density of liquid is kept evenly.
In addition, for the liquid of different viscosities variable grain thing size, the mixing speed of high speed agitator can be set by frequency converter, to adapt to the stirring demand of different viscosities liquid, effectively utilize electric energy.
The beneficial effects of the utility model are:
By chuck steel pipe is set, can constantly to the high viscosity in jacket reactor, containing particle-liquid, heat, reduce liquid viscosity, thereby reduce the pressure to membrane pump, guarantee the transfer efficiency of liquid.
By high-speed stirring apparatus is set in jacket reactor, can containing in the extraction of particle-liquid material, constantly to it, stir in high viscosity, guarantee the uniformity of its density.
In addition, by the bottom at jacket reactor, opening is set and connects membrane pump by chuck steel pipe, make the difference in height Distance Shortened between membrane pump and reactor, reduce the power consumption of membrane pump.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, to the accompanying drawing of required use in embodiment or description of the Prior Art be briefly described below, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skills, do not paying under the prerequisite of creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is described in the utility model a kind of for the overall structure schematic diagram containing particle-liquid withdrawing device by high viscosity;
In figure:
1, jacket reactor, 2, chuck steel pipe, 3, membrane pump, 4, high speed agitator, 5, frequency converter.
The specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only the utility model part embodiment, rather than whole embodiment.Embodiment based in the utility model, those of ordinary skills are not making the every other embodiment obtaining under creative work prerequisite, all belong to the scope of the utility model protection.
Embodiment is as shown in Figure 1 known, and a kind of device for high viscosity is extracted out containing particle-liquid described in the utility model, comprising: bottom is provided with jacket reactor 1 and the membrane pump 3 of opening; Between jacket reactor 1 and membrane pump 3, by chuck steel pipe 2, be connected; One end of chuck steel pipe 2 is connected with the bottom opening of jacket reactor 1, and its other end is connected with membrane pump 3.
In above-mentioned jacket reactor 1, be provided with high speed agitator 4, outside is provided with frequency converter 5, and the input of high speed agitator 4 is connected with the output of frequency converter 5.
The length of above-mentioned chuck steel pipe 2 can be 1～2.5 meter.
Above-mentioned membrane pump 3 is pneumatic diaphragm pump.
Above-mentioned for high viscosity is as follows containing the course of work and the operation principle of the device of particle-liquid extraction:
Extraneous thermal source constantly passes into steam or hot water by the chuck of chuck steel pipe 2 in the chuck of jacket reactor 1, and the high viscosity being used in heating jacket reactor 1, containing particle-liquid material, makes high viscosity contain the reduced viscosity of particle-liquid; Meanwhile, high speed agitator 4 constantly carries out high-speed stirred to the high viscosity in jacket reactor 1 containing particle-liquid, and the density of liquid is kept evenly.
In addition, for the liquid of different viscosities variable grain thing size, the mixing speed of high speed agitator 4 can be set by frequency converter 5, to adapt to the stirring demand of different viscosities liquid, effectively utilize electric energy.
In sum, the utility model, by chuck steel pipe is set, can constantly heat containing particle-liquid the high viscosity in jacket reactor, reduces liquid viscosity, thereby reduces the pressure to membrane pump, guarantees the transfer efficiency of liquid.
By high-speed stirring apparatus is set in jacket reactor, can containing in the extraction of particle-liquid material, constantly to it, stir in high viscosity, guarantee the uniformity of its density.
In addition, by the bottom at jacket reactor, opening is set and connects membrane pump by chuck steel pipe, make the difference in height Distance Shortened between membrane pump and reactor, reduce the power consumption of membrane pump.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (5)
1. the device for high viscosity is extracted out containing particle-liquid, is characterized in that, comprising: bottom is provided with jacket reactor (1) and the membrane pump (3) of opening; Between described jacket reactor (1) and described membrane pump (3), by chuck steel pipe (2), be connected; One end of described chuck steel pipe (2) is connected with the bottom opening of described jacket reactor (1), and its other end is connected with described membrane pump (3).
2. a kind of device for high viscosity is extracted out containing particle-liquid according to claim 1, is characterized in that, is provided with high speed agitator (4) in described jacket reactor (1).
3. a kind of device for high viscosity is extracted out containing particle-liquid according to claim 2, is characterized in that, also comprise frequency converter (5), the input of described high speed agitator (4) is connected with the output of described frequency converter (5).
4. a kind of device for high viscosity is extracted out containing particle-liquid according to claim 1, is characterized in that, the length of described chuck steel pipe (2) is 1～2.5 meter.
5. a kind of device for high viscosity is extracted out containing particle-liquid according to claim 1, is characterized in that, described membrane pump (3) is pneumatic diaphragm pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420049373.3U CN203764221U (en) | 2014-01-26 | 2014-01-26 | Device for extracting high-viscosity granule-containing liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420049373.3U CN203764221U (en) | 2014-01-26 | 2014-01-26 | Device for extracting high-viscosity granule-containing liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203764221U true CN203764221U (en) | 2014-08-13 |
Family
ID=51281469
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420049373.3U Expired - Fee Related CN203764221U (en) | 2014-01-26 | 2014-01-26 | Device for extracting high-viscosity granule-containing liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203764221U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114682419A (en) * | 2020-12-25 | 2022-07-01 | 华晨宝马汽车有限公司 | Spraying material viscosity control equipment and method for vehicle spraying production line |
-
2014
- 2014-01-26 CN CN201420049373.3U patent/CN203764221U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114682419A (en) * | 2020-12-25 | 2022-07-01 | 华晨宝马汽车有限公司 | Spraying material viscosity control equipment and method for vehicle spraying production line |
| CN114682419B (en) * | 2020-12-25 | 2024-01-16 | 华晨宝马汽车有限公司 | Spray material viscosity control device and method for vehicle spray production line |
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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: 20140813 Termination date: 20210126 |