CN203990654U - Normal temperature asphalt modifier is produced reactor - Google Patents
Normal temperature asphalt modifier is produced reactor Download PDFInfo
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- CN203990654U CN203990654U CN201420445034.7U CN201420445034U CN203990654U CN 203990654 U CN203990654 U CN 203990654U CN 201420445034 U CN201420445034 U CN 201420445034U CN 203990654 U CN203990654 U CN 203990654U
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- agitator tank
- normal temperature
- asphalt modifier
- reactor
- temperature asphalt
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Abstract
The utility model discloses a kind of normal temperature asphalt modifier and produce reactor, comprise agitator tank and frame, agitator tank is rotatably installed in frame and drives rotation by motor, offers material mouthful on agitator tank, and agitator tank inwall is provided with fin.The utility model is simple in structure, reasonable in design, adopts this production reactor to stir raw material production asphalt modifier operating efficiency high, and labor strength is little, stirs more even.
Description
Technical field
The utility model relates to a kind of modifier production equipment, particularly relates to a kind of normal temperature asphalt modifier and produces reactor.
Background technology
In the time producing normal temperature asphalt modifier, all needing raw material to stir, is all to adopt Traditional Man hand operated mixing raw material at present, and not only labor strength is large, and production efficiency is low, and stirs even not.This problem that how to solve prior art existence becomes the direction that these those skilled in the art make great efforts.
Utility model content
The purpose of this utility model is just to provide a kind of normal temperature asphalt modifier and produces reactor, automation mechanized operation, and production efficiency significantly improves, and stirs, and can address the above problem completely.
The purpose of this utility model realizes by following technical proposals:
A kind of normal temperature asphalt modifier is produced reactor, comprises agitator tank and frame, and agitator tank is rotatably installed in frame and drives rotation by motor, offers material mouthful on agitator tank, and agitator tank inwall is provided with fin.
As preferably, also comprise rotating shaft, rotating shaft is axially passed agitator tank and is connected and fixed with agitator tank, and rotating shaft two ends are arranged in frame by bearing, and motor is fixed in frame, and motor is by one end of belt transmission connection rotating shaft.
As preferably, described frame bottom is provided with the roller of brake device, between roller and frame bottom, Weighing sensor is installed, the corresponding display screen of installing for showing the interior weight of material of agitator tank in frame.
As preferably, described agitator tank is horizontal cylindrical tube shape, and material mouthful is arranged on the position of agitator tank one end apart from sidewall certain distance, and agitator tank sidewall is provided with impurity mouth.
As preferably, this reactor also disposes drawing mechanism, and this drawing mechanism comprises material pipe, colloid mill and motor, and one end of material pipe is provided with and expects the joint that mouth mates, and the other end is connected with colloid mill, and motor is connected with colloid mill.
As preferably, described fin is arranged on agitator tank inwall in the shape of a spiral vertically.
As preferably, described agitator tank inwall is arranged fin along circumferential interval.
As preferably, the cross section of described fin is trapezoidal.
As preferably, described fin is L shaped flap.
As preferably, described agitator tank exterior contour is to become gradually the reducer diminishing gradually again greatly from one end.
Compared with prior art, the beneficial effects of the utility model are:
1. simple in structure, reasonable in design, adopt this production reactor to stir raw material production asphalt modifier operating efficiency high, labor strength is little.
2. utilize roller convenient mobile, and the changes in weight of material in can Real-Time Monitoring reactor.
3. impurity is discharged separately, avoids impurity to export with the asphalt modifier of having produced.
4. agitator tank inwall is provided with fin, strengthens mixing effect, mixes more even.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the cross-sectional view of agitator tank, is provided with helical rib in agitator tank, and fin cross section is trapezoidal;
Fig. 3 is the cross-sectional structure schematic diagram that the agitator tank of arc fin is set along circumferential interval;
Fig. 4 is the structural representation of L shaped flap;
Fig. 5 is the structural representation of embodiment bis-;
Fig. 6 is the structural representation of embodiment tri-;
Fig. 7 is the structural representation of embodiment tetra-;
Fig. 8 is the structural representation of embodiment five.
Detailed description of the invention
Below in conjunction with specific embodiments and the drawings, the utility model is further described.
Embodiment mono-
As shown in Figure 1, a kind of normal temperature asphalt modifier is produced reactor, comprise agitator tank 1, rotating shaft 2, motor 3 and frame 4, described agitator tank 1 is horizontal cylindrical tube shape, material mouth 5 is offered in one end of agitator tank 1, and rotating shaft 2 is axially passed agitator tank 1 and is connected and fixed with agitator tank 1, and rotating shaft 2 two ends are arranged in frame 4 by bearing, motor 3 is fixed in frame 4, and motor 3 is by one end of belt transmission connection rotating shaft 2.Described frame 4 bottoms are provided with the roller 6 of brake device.
Referring to Fig. 2 to Fig. 4, agitator tank 1 inwall arranges vertically spiral helicine fin 7 or along circumferential interval, arc fin 7 is set, and the cross section of this fin 7 is trapezoidal, or fin 7 is L shaped flap.
In use, raw material is put into agitator tank 1 from material mouth 5, motor 3 drive shafts 2 drive agitator tank 1 to rotate raw material mixing, and then produce asphalt modifier.The fin 7 of agitator tank 1 inwall can be assisted mixed material, raw material is mixed more even.
Embodiment bis-
Difference referring to Fig. 5 the present embodiment and embodiment mono-is, described frame 4 bottoms are provided with the roller 6 of brake device, between roller 6 and frame 4 bottoms, Weighing sensor 8 is installed, the corresponding display screen 9 of installing for showing weight of material in agitator tank in frame 4.Utilize Weighing sensor 8 to obtain the interior weight of material of agitator tank 1, and show by display screen 9, thus the changes in weight of material in can Real-Time Monitoring reactor.
Embodiment tri-
Referring to Fig. 6, the difference of the present embodiment and embodiment bis-is, described material mouth 5 is arranged on the position of agitator tank 1 one end apart from sidewall certain distance, and agitator tank 1 sidewall is provided with impurity mouth 10.
Complete and be uniformly mixed after operation, the impurity in this reactor can be deposited in agitator tank 1 bottom, can not be output together with asphalt modifier, and impurity is discharged from impurity mouth 10.
Embodiment tetra-
Referring to Fig. 7, the difference of the present embodiment and embodiment tri-is, this reactor also disposes drawing mechanism, this drawing mechanism comprises material pipe 11, colloid mill 12 and motor 13, one end of material pipe 11 is provided with and expects mouthful 5 joints that mate, the other end is connected with colloid mill 12, and motor 13 is connected with colloid mill 12.
Utilize this material pipe 11 to be connected with material mouth 5, in the time of discharging, asphalt modifier enters colloid mill 12, and the product quality of generation is better.
Embodiment five
Referring to Fig. 8, the difference of the present embodiment and embodiment tetra-is, described agitator tank 1 exterior contour is to become gradually the reducer diminishing gradually again greatly from one end, and impurity mouth 10 is opened in the position of profile maximum.This structure is more conducive to impurity piles up at agitator tank inner bottom part, thereby obtains purer asphalt modifier.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all any amendments of doing within spirit of the present utility model and principle, be equal to and replace and improvement etc., within all should being included in protection domain of the present utility model.
Claims (10)
1. normal temperature asphalt modifier is produced a reactor, it is characterized in that: comprise agitator tank and frame, agitator tank is rotatably installed in frame and drives rotation by motor, offers material mouthful on agitator tank, and agitator tank inwall is provided with fin.
2. normal temperature asphalt modifier according to claim 1 is produced reactor, it is characterized in that: also comprise rotating shaft, rotating shaft is axially passed agitator tank and is connected and fixed with agitator tank, rotating shaft two ends are arranged in frame by bearing, motor is fixed in frame, and motor is by one end of belt transmission connection rotating shaft.
3. normal temperature asphalt modifier according to claim 2 is produced reactor, it is characterized in that: described frame bottom is provided with the roller of brake device, between roller and frame bottom, Weighing sensor is installed, the corresponding display screen of installing for showing weight of material in agitator tank in frame.
4. normal temperature asphalt modifier according to claim 1 is produced reactor, it is characterized in that: described agitator tank is horizontal cylindrical tube shape, and material mouthful is arranged on the position of agitator tank one end apart from sidewall certain distance, and agitator tank sidewall is provided with impurity mouth.
5. normal temperature asphalt modifier according to claim 4 is produced reactor, it is characterized in that: this reactor also disposes drawing mechanism, this drawing mechanism comprises material pipe, colloid mill and motor, one end of material pipe is provided with and the joint of expecting that mouth mates, the other end is connected with colloid mill, and motor is connected with colloid mill.
6. normal temperature asphalt modifier according to claim 1 is produced reactor, it is characterized in that: described fin is arranged on agitator tank inwall in the shape of a spiral vertically.
7. normal temperature asphalt modifier according to claim 1 is produced reactor, it is characterized in that: described agitator tank inwall is arranged fin along circumferential interval.
8. produce reactor according to the normal temperature asphalt modifier described in claim 6 or 7, it is characterized in that: the cross section of described fin is trapezoidal.
9. produce reactor according to the normal temperature asphalt modifier described in claim 6 or 7, it is characterized in that: described fin is L shaped flap.
10. normal temperature asphalt modifier according to claim 1 is produced reactor, it is characterized in that: described agitator tank exterior contour is to become gradually the reducer diminishing gradually again greatly from one end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420445034.7U CN203990654U (en) | 2014-08-08 | 2014-08-08 | Normal temperature asphalt modifier is produced reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420445034.7U CN203990654U (en) | 2014-08-08 | 2014-08-08 | Normal temperature asphalt modifier is produced reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203990654U true CN203990654U (en) | 2014-12-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201420445034.7U Active CN203990654U (en) | 2014-08-08 | 2014-08-08 | Normal temperature asphalt modifier is produced reactor |
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| CN (1) | CN203990654U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109173972A (en) * | 2018-10-15 | 2019-01-11 | 河南省科学院地理研究所 | A kind of efficient reclaiming organic waste utilizes reactor tank |
| CN110270274A (en) * | 2019-07-19 | 2019-09-24 | 中国科学院北京综合研究中心 | A kind of quick preparation loads the movable fixture of the modified material of micro-nano oxygen bubbles |
| CN113769700A (en) * | 2021-08-30 | 2021-12-10 | 长沙缔仑生物科技有限公司 | DNA/RNA industrial full-automatic synthesizer |
-
2014
- 2014-08-08 CN CN201420445034.7U patent/CN203990654U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109173972A (en) * | 2018-10-15 | 2019-01-11 | 河南省科学院地理研究所 | A kind of efficient reclaiming organic waste utilizes reactor tank |
| CN110270274A (en) * | 2019-07-19 | 2019-09-24 | 中国科学院北京综合研究中心 | A kind of quick preparation loads the movable fixture of the modified material of micro-nano oxygen bubbles |
| CN113769700A (en) * | 2021-08-30 | 2021-12-10 | 长沙缔仑生物科技有限公司 | DNA/RNA industrial full-automatic synthesizer |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Sichuan Xingda Investment Co., Ltd. Assignor: Sichuan Xinggao Polymer Resin Co., Ltd. Contract record no.: 2018510000064 Denomination of utility model: Reaction kettle for manufacturing asphalt modifier at room temperature Granted publication date: 20141210 License type: Exclusive License Record date: 20181115 |