CN208694424U - A kind of large high-temperature centrifugation purifying plant for chemical raw material production - Google Patents
A kind of large high-temperature centrifugation purifying plant for chemical raw material production Download PDFInfo
- Publication number
- CN208694424U CN208694424U CN201820989563.1U CN201820989563U CN208694424U CN 208694424 U CN208694424 U CN 208694424U CN 201820989563 U CN201820989563 U CN 201820989563U CN 208694424 U CN208694424 U CN 208694424U
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- China
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- box
- lower box
- centrifugal
- raw material
- reaction kettle
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Abstract
The utility model discloses a kind of large high-temperatures for chemical raw material production of purification chemical field to be centrifuged purifying plant, including lower box, the top of the lower box is equipped with reaction kettle, and the right side of reaction kettle is equipped with feed inlet, first motor is fixedly installed at the top of the reaction kettle, and the output end of first motor is fixedly connected with heating tube, the bottom of the heating tube is equipped with taper blade, the centrifugal box is located in the inner cavity of lower box, the utility model structure is simple, it is novel in design, pass through the purifying plant of high-temperature cabinet and the mutual cooperation composition of centrifugal box, it is regathered after chemical raw material in solution is crystallized, so that the purity of purification is higher, traditional concentrator bowl is arranged to the centrifugal box being made of filter screen, in centrifugal operation, solution can be thrown away simultaneously, material is stayed in centrifugal box and then is collected, behaviour Facilitate, improves production efficiency.
Description
Technical field
The utility model relates to purify technical field of chemistry, specially a kind of large high-temperature for chemical raw material production from
Heart purifying plant.
Background technique
, the extent of purification of chemical raw material particularly significant to the purification of chemical raw material in chemical raw material production process, directly
The quality of finished product is affected, and different chemical raw materials carries out the method difference of most effective purification, wherein relatively effective
A kind of method of purification is centrifugation purification, but mostly volume is smaller together for centrifugation purification at this stage, the original disposably purified
Expect smaller, is served only for use when experiment mostly, it is difficult to carried out in batch production using therefore purification technique at this stage is deposited
In deficiency, while existing heating centrifugation purifying plant is nearly all using heating and centrifugal operation while to carry out, and is thus also deposited
In the factor interfered with each other, cause to purify being not thorough for operation, for this purpose, we have proposed a kind of for chemical raw material production
Large high-temperature centrifugation purifying plant comes into operation, to solve the above problems.
Utility model content
The purpose of this utility model is to provide a kind of large high-temperatures for chemical raw material production to be centrifuged purifying plant, with
Solve the problems mentioned above in the background art.
To achieve the above object, the utility model provides the following technical solutions: a kind of large size for chemical raw material production
High temperature is centrifuged purifying plant, including lower box, and the top of the lower box is equipped with reaction kettle, and the right side of reaction kettle is equipped with charging
Mouthful, it is fixedly installed with first motor at the top of the reaction kettle, and the output end of first motor is fixedly connected with heating tube, it is described
The bottom of heating tube is equipped with taper blade, and the bottom of the reaction kettle is equipped with connecting tube, and connecting tube through lower box, bearing,
Centrifugal box simultaneously extends in the inner cavity of centrifugal box, and the centrifugal box is located in the inner cavity of lower box, and the top center of centrifugal box
Place is connected by the inner cavity top of bearing and lower box, and the intracavity bottom of the centrifugal box is equipped with partition, and the bottom of centrifugal box
It is rotatablely connected by shaft and lower box intracavity bottom, the shaft is connect by belt with the second motor, and the second motor is solid
Dingan County is mounted in the right side of lower box, drainage plate is equipped at left and right sides of the intracavity bottom of the lower box, and the bottom of lower box is left
Right two sides are fixedly installed with pedestal, and two groups of liquid outlets are equipped between pedestal described in two groups, and the left side of the lower box is equipped with lid.
Preferably, the centrifugal box includes two groups of horizontally disposed fixed plates, and four are vertically equipped between two groups of fixed plates
Support rod is organized, is fixedly installed with filter screen between two adjacent groups support rod.
Preferably, the centrifugal box is equipped with space compatible with filter plate, and the filter plate is equipped with knob.
Preferably, the heating tube includes shaft, and spiral is equipped with resistive heater in shaft, on the left of the feed inlet on
Equipped with micro-filtrate membrane filtration plate, the reactor bottom is equipped with valve.
Compared with prior art, the utility model has the beneficial effects that the utility model structure is simple, and it is novel in design, lead to
The purifying plant for crossing the mutual cooperation composition of high-temperature cabinet and centrifugal box, regathers after the chemical raw material in solution is crystallized,
So that the purity of purification is higher, traditional concentrator bowl is arranged to the centrifugal box being made of filter screen, it, can in centrifugal operation
Solution is thrown away simultaneously, material is stayed in centrifugal box and then is collected, it is easy to operate, improve production efficiency.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model；
Fig. 2 is the utility model centrifugal box structural schematic diagram.
In figure: 1 lower box, 2 reaction kettles, 3 first motors, 4 heating tubes, 5 taper blades, 6 feed inlets, 7 bearings, 8 centrifugations
Case, 81 fixed plates, 82 support columns, 83 filter screens, 9 partitions, 10 shafts, 11 second motors, 12 drainage plates, 13 liquid outlets, 14 bottoms
Seat, 15 lids.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
The utility model provides a kind of technical solution referring to FIG. 1-2: a kind of large high-temperature for chemical raw material production
It is centrifuged purifying plant, including lower box 1, the top of the lower box 1 is equipped with reaction kettle 2, and the right side of reaction kettle 2 is equipped with charging
Mouth 6, the top of the reaction kettle 2 are fixedly installed with first motor 3, and the output end of first motor 3 and the fixed company of heating tube 4
It connects, the bottom of the heating tube 4 is equipped with taper blade 5, under the bottom of the reaction kettle 2 is equipped with connecting tube, and connecting tube runs through
Cabinet 1, bearing 7, centrifugal box 8 simultaneously extend in the inner cavity of centrifugal box 8, and the centrifugal box 8 is located in the inner cavity of lower box 1, and
It is connect by bearing 7 with the inner cavity top of lower box 1 at the top center of centrifugal box, the intracavity bottom of the centrifugal box 8 is equipped with
Partition 9, and the bottom of centrifugal box 8 is rotatablely connected by shaft 10 and 1 intracavity bottom of lower box, the shaft 10 by belt with
The connection of second motor 11, and the second motor 11 is fixedly mounted on the right side of lower box 1, the intracavity bottom or so of the lower box 1
Two sides are equipped with drainage plate 12, and are fixedly installed with pedestal 14 at left and right sides of the bottom of lower box 1, set between pedestal 14 described in two groups
There are two groups of liquid outlets 13, the left side of the lower box 1 is equipped with lid 15.
Wherein, the centrifugal box 8 includes two groups of horizontally disposed fixed plates 81, and is vertically equipped between two groups of fixed plates 81
Four groups of support rods 82 are fixedly installed with filter screen 83 between two adjacent groups support rod 82, and the centrifugal box 8 is equipped with and partition 9
Compatible space, the partition 9 are equipped with knob, and the heating tube 4 includes shaft, and spiral is equipped with adding thermal resistance in shaft
Thread, micro-filtrate membrane filtration plate is equipped on the left of the feed inlet 6,2 bottom of reaction kettle is equipped with valve.
Working principle: solution is entered in reaction kettle 2 from from feed inlet 6, will be miscellaneous in solution by micro-filtrate membrane filtration plate
Matter filters out, and starts first motor 3 and heating tube 4, heating tube 4 heat solution, and first motor 3 drives taper blade 5
Rotated, accelerate the crystallization rate of solution, at the same taper blade 5 can the macrocrystalline device to bottom roll, work as knot
After crystalline substance, opening valve will crystallize raw material and solution is transported to together in centrifugal box 8, starts the second motor 11, the second motor
11 are rotated centrifugal box 8 by shaft 10, and operation is centrifuged, and solution is thrown away lower box 1 by filter screen 83
In inner cavity, solution is discharged from liquid outlet 13 under the action of drainage plate 12, and the material crystal in solution stays in 8 inner cavity of centrifugal box
Partition 9 on, then open lid 15, partition 9 extracted out by shaking hands, material crystal is collected, utility model structure
Simply, design rationally, has very strong practical value.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (4)
1. a kind of large high-temperature for chemical raw material production is centrifuged purifying plant, including lower box (1), it is characterised in that: institute
The top for stating lower box (1) is equipped with reaction kettle (2), and the right side of reaction kettle (2) is equipped with feed inlet (6), the reaction kettle (2)
Top is fixedly installed with first motor (3), and the output end of first motor (3) is fixedly connected with heating tube (4), the heating tube
(4) bottom is equipped with taper blade (5), and the bottom of the reaction kettle (2) is equipped with connecting tube, and connecting tube through lower box (1),
Bearing (7), centrifugal box (8) simultaneously extend in the inner cavity of centrifugal box (8), and the centrifugal box (8) is located at the inner cavity of lower box (1)
In, and connect with the inner cavity top of lower box (1) at the top center of centrifugal box by bearing (7), the centrifugal box (8) it is interior
Bottom of chamber portion is equipped with partition (9), and the bottom of centrifugal box (8) is rotatablely connected by shaft (10) and lower box (1) intracavity bottom, institute
It states shaft (10) to connect by belt with the second motor (11), and the second motor (11) is fixedly mounted on the right side of lower box (1),
Drainage plate (12) are equipped at left and right sides of the intracavity bottom of the lower box (1), and fixed peace at left and right sides of the bottom of lower box (1)
Equipped with pedestal (14), two groups of liquid outlets (13) are equipped between pedestal described in two groups (14), the left side of the lower box (1) is equipped with lid
Sub (15).
2. a kind of large high-temperature for chemical raw material production according to claim 1 is centrifuged purifying plant, feature exists
In: the centrifugal box (8) includes two groups of horizontally disposed fixed plates (81), and four groups are vertically equipped between two groups of fixed plates (81)
Support rod (82) is fixedly installed with filter screen (83) between two adjacent groups support rod (82).
3. a kind of large high-temperature for chemical raw material production according to claim 1 is centrifuged purifying plant, feature exists
In: the centrifugal box (8) is equipped with partition (9) compatible space, and the partition (9) is equipped with knob.
4. a kind of large high-temperature for chemical raw material production according to claim 1 is centrifuged purifying plant, feature exists
In: the heating tube (4) includes shaft, and spiral is equipped with resistive heater in shaft, and feed inlet (6) left side is equipped with micro-
The bottom of membrane filtration plate, the reaction kettle (2) is equipped with valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820989563.1U CN208694424U (en) | 2018-06-26 | 2018-06-26 | A kind of large high-temperature centrifugation purifying plant for chemical raw material production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820989563.1U CN208694424U (en) | 2018-06-26 | 2018-06-26 | A kind of large high-temperature centrifugation purifying plant for chemical raw material production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208694424U true CN208694424U (en) | 2019-04-05 |
Family
ID=65937302
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820989563.1U Expired - Fee Related CN208694424U (en) | 2018-06-26 | 2018-06-26 | A kind of large high-temperature centrifugation purifying plant for chemical raw material production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208694424U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110721652A (en) * | 2019-10-29 | 2020-01-24 | 李财 | Reaction kettle for accelerating reaction speed |
| CN113069827A (en) * | 2021-01-18 | 2021-07-06 | 李志方 | Cosmetics centrifugation purification equipment |
| CN115463475A (en) * | 2022-09-02 | 2022-12-13 | 贵州成有王记善沅食品有限公司 | Preparation method of waxberry soup anthocyanin |
-
2018
- 2018-06-26 CN CN201820989563.1U patent/CN208694424U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110721652A (en) * | 2019-10-29 | 2020-01-24 | 李财 | Reaction kettle for accelerating reaction speed |
| CN110721652B (en) * | 2019-10-29 | 2021-07-27 | 福建省沙县松川化工有限公司 | Reaction kettle for accelerating reaction speed |
| CN113069827A (en) * | 2021-01-18 | 2021-07-06 | 李志方 | Cosmetics centrifugation purification equipment |
| CN115463475A (en) * | 2022-09-02 | 2022-12-13 | 贵州成有王记善沅食品有限公司 | Preparation method of waxberry soup anthocyanin |
| CN115463475B (en) * | 2022-09-02 | 2024-01-23 | 贵州成有王记善沅食品有限公司 | Preparation method of anthocyanin in waxberry soup |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190405 Termination date: 20190626 |
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| CF01 | Termination of patent right due to non-payment of annual fee |