CN205007626U - Percolating device - Google Patents
Percolating device Download PDFInfo
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- CN205007626U CN205007626U CN201520396079.4U CN201520396079U CN205007626U CN 205007626 U CN205007626 U CN 205007626U CN 201520396079 U CN201520396079 U CN 201520396079U CN 205007626 U CN205007626 U CN 205007626U
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- diacolation
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Abstract
The utility model discloses a percolating device, including solvent house steward, solvent jar, feed liquor pipe, a diacolation section of thick bamboo and drain pipe, the solvent house steward is connected with the solvent jar, the feed liquor pipe is located the bottom of solvent jar, and is connected with the top of diacolation section of thick bamboo one end, the drain pipe is located the bottom of the diacolation section of thick bamboo other end, evenly distributed has crisscross communicating baffle between interior feed liquor pipe of a diacolation section of thick bamboo and the drain pipe. When evenly distributed has crisscross communicating baffle from top to bottom between feed liquor pipe and the drain pipe in the diacolation section of thick bamboo, still be connected with the control tube between a solvent jar and the diacolation section of thick bamboo, the control tube mouth of pipe is located between the height of the feed liquor pipe mouth of pipe and below baffle in the diacolation section of thick bamboo, the control tube mouth of pipe is higher than the feed liquor pipe mouth of pipe in the solvent jar. Still be provided with adjusting valve on feed liquor pipe and the drain pipe. The utility model discloses under the condition that does not increase the long -pending size of diacolation barrel, practiced thrift manufacturing cost, reduced intensity of labour, improved production conditions. And a work efficiency is increased.
Description
Technical field
The utility model relates to a kind of mechanical equipment technical field, more particularly, particularly relates to a kind of percolating device.
Background technology
In Chinese Traditional Medicine, percolation often can be used to extract Effective Component of Chinese Medicine.Percolation is exactly that the medicinal material that appropriateness is pulverized is placed in percolator, and constantly add solvent from top, solvent infiltrate medicinal material sulfate layer flows downhill moves in process the method leaching medicinal ingredient.Diacolation belongs to Dynamic Leaching method, wants solvent utilization rate high, and the time that solvent flow process and solvent contact with medicinal material and the area contacted are the key factors determining diacolation effect.The percolating device used in prior art, its solvent flow process is all by percolator distance decision up and down, when percolator small volume, the flow process of solvent is just shorter, so be difficult to the optimum efficiency playing diacolation, if and increase cylindrical shell height can affect factory building layout, wasting space area.And adding of solvent also needs manual adjustment to control, waste of manpower resource.
Utility model content
The purpose of this utility model is for above-mentioned the deficiencies in the prior art, provides a kind of percolating device increasing diacolation effect when not changing equipment occupation space.
The technical solution adopted in the utility model is percolating device, comprises solvent house steward, solvent tank, feed tube, percolator and drain pipe; Described solvent house steward is connected with solvent tank; Described feed tube is positioned at the bottom of solvent tank, and is connected with the top of percolator one end; Described drain pipe is positioned at the bottom of the percolator other end; The staggered dividing plate communicated is evenly distributed with between feed tube with drain pipe in described percolator; Also adjustable pipe is connected with between described solvent tank and percolator; In described solvent tank, the adjustable pipe mouth of pipe is higher than the feed tube mouth of pipe.
Further, staggeredly up and down between feed tube and drain pipe in described percolator dividing plate is evenly distributed with; In described percolator, the adjustable pipe mouth of pipe is between the feed tube mouth of pipe and the height of underlay screen.
Further, in described percolator, between feed tube and drain pipe, left and right is staggered is evenly distributed with dividing plate.
Further, described feed tube and drain pipe are also provided with control valve.
The beneficial effects of the utility model are: the utility model is when increasing percolator volume size, dividing plate is uniformly distributed by staggered up and down between feed tube and drain pipe in percolator, thus serve the distance increasing solvent and flow in percolator, too increase solvent and medicinal material catalytic time simultaneously.Improve the leaching rate of medicinal material active ingredient, the optimum efficiency of the diacolation of maximized performance.
The utility model, by increasing adjustable pipe and control valve, utilizes the operation principle of negative pressure in percolator, serves oneself and artificial dual regulation effect to the influx of percolator internal solvent, inlet time.Reduce the labour intensity of workman, improve working condition, improve production efficiency.
By above-mentioned improvement, the utility model, when not increasing percolator volume size, has been saved production cost, has been reduced labour intensity, improved working condition.Improve operating efficiency.
Accompanying drawing explanation
Below in conjunction with the embodiment in accompanying drawing, the utility model is described in further detail, but do not form any restriction of the present utility model.
Fig. 1 is the structural representation that the utility model implements.
Fig. 2 is the structural representation of the utility model embodiment two.
In figure: 1, solvent house steward, 2, solvent tank, 3, feed tube, 4, adjustable pipe, 5, control valve, 6, percolator, 7, dividing plate, 8, drain pipe.
Detailed description of the invention
Embodiment one:
Consult shown in Fig. 1, percolating device of the present utility model, comprise solvent house steward 1, solvent tank 2, feed tube 3, percolator 6 and drain pipe 8.Described solvent house steward 1 is connected with solvent tank 2.Described feed tube 3 is positioned at the bottom of solvent tank 2, and is connected with the top of percolator 6 one end.Described drain pipe 8 is positioned at the bottom of percolator 6 other end.The staggered dividing plate 7 communicated is evenly distributed with between feed tube 3 with drain pipe 8 in described percolator 6.Adjustable pipe 4 is also connected with between described solvent tank 2 and percolator 6.In described solvent tank 2, adjustable pipe 4 mouth of pipe is higher than feed tube 3 mouth of pipe.
Further, staggeredly up and down between feed tube 3 and drain pipe 8 in percolator 6 described in the utility model dividing plate 7 is evenly distributed with.In described percolator 6, adjustable pipe 4 mouth of pipe is between feed tube 3 mouth of pipe and the height of underlay screen 7.
Between the inherent feed tube 3 of percolator 6 described in the utility model and drain pipe 8, be also staggeredly distributed with dividing plate 7 up and down every a segment distance and space in cylinder is isolated.Solvent flows into from the upper end feed tube 3 of percolator 6, the Clearance Flow between dividing plate 7, and abundant and medicinal material haptoreaction, finally flow out from the liquid outlet being positioned at percolator 6 other end bottom.
Embodiment two:
Further, consult Fig. 2, in percolator 6 described in the utility model, between feed tube 3 and drain pipe 8, left and right is staggered is evenly distributed with dividing plate 7.
As further improvement, feed tube 3 described in the utility model and drain pipe 8 are also provided with control valve 5.
The utility model is in the percolator 6 adding dividing plate 7, and solvent enters from the feed tube 3 of upper end, the Clearance Flow between dividing plate 7.By increasing an adjustable pipe 4 between percolator 6 and solvent tank 2.When adjustable pipe 4 communicates with air, in percolator 6, be in atmospheric pressure state.Feed tube 3 then flows into downwards in percolator 6 due to hydraulic action solvent.When solvent is raised to certain altitude (when being dipped into the lower nozzle of adjustable pipe 4), then air can not enter in percolator 6 from adjustable pipe 4.Negative pressure in such percolator 6 is increasing, and the solvent that feed tube 3 flows into will progressively slow down minimizing, finally stops.Now solvent flows between dividing plate 7, and when solvent is again lower than dividing plate 7, solvent is lower than adjustable pipe 4 mouthfuls, and air enters in percolator 6 from adjustable pipe 4 mouthfuls again, and solvent continues to flow into from feed tube 3.Go round and begin again circulation like this, thus reach the object of automatic control.
And by arranging control valve 5 on feed tube 3 with drain pipe 8, the speed of manual adjustment solvent inflow and outflow can be played again further.
The beneficial effects of the utility model are: the utility model is when increasing percolator 6 volume size, dividing plate 7 is uniformly distributed by staggered up and down between feed tube 3 and drain pipe 8 in percolator 6, thus serve the distance increasing solvent and flow in percolator 6, too increase solvent and medicinal material catalytic time simultaneously.Improve the leaching rate of medicinal material active ingredient, the diacolation effect of maximized performance.
The utility model, by increasing adjustable pipe 4 and control valve 5, utilizes the operation principle of negative pressure in percolator 6, serves oneself and/or artificial dual regulation effect to the influx of percolator 6 internal solvent, inlet time.Reduce the labour intensity of workman, improve working condition, improve production efficiency.
By above-mentioned improvement, the utility model, when not increasing percolator 6 volume size, has been saved production cost, has been reduced labour intensity, improved working condition.Improve operating efficiency.
Above illustrated embodiment is better embodiment of the present utility model, only be used for conveniently the utility model being described, not any pro forma restriction is done to the utility model, have in any art and usually know the knowledgeable, if do not depart from the utility model carry in the scope of technical characteristic, utilize the utility model disclose the Equivalent embodiments changing or modify in the done local of technology contents, and do not depart from technical characteristic content of the present utility model, all still belong in the scope of the utility model technical characteristic.
Claims (4)
1. a percolating device, comprises solvent house steward (1), solvent tank (2), feed tube (3), percolator (6) and drain pipe (8); Described solvent house steward (1) is connected with solvent tank (2); Described feed tube (3) is positioned at the bottom of solvent tank (2), and is connected with the top of percolator (6) one end; Described drain pipe (8) is positioned at the bottom of percolator (6) other end; It is characterized in that: between described percolator (6) interior feed tube (3) with drain pipe (8), be evenly distributed with the staggered dividing plate (7) communicated; Adjustable pipe (4) is also connected with between described solvent tank (2) and percolator (6); In described solvent tank (2), adjustable pipe (4) mouth of pipe is higher than feed tube (3) mouth of pipe.
2. a kind of percolating device as claimed in claim 1, is characterized in that: be evenly distributed with dividing plate (7) for staggered up and down between described percolator (6) interior feed tube (3) and drain pipe (8); Adjustable pipe (4) is also connected with between described solvent tank (2) and percolator (6); In described percolator (6), adjustable pipe (4) mouth of pipe is positioned between the height of feed tube (3) mouth of pipe and underlay screen (7); In described solvent tank (2), adjustable pipe (4) mouth of pipe is higher than feed tube (3) mouth of pipe.
3. a kind of percolating device as claimed in claim 1, is characterized in that: be evenly distributed with dividing plate (7) for left and right is staggered between described percolator (6) interior feed tube (3) and drain pipe (8); Adjustable pipe (4) is also connected with between described solvent tank (2) and percolator (6); In described solvent tank (2), adjustable pipe (4) mouth of pipe is higher than feed tube (3) mouth of pipe.
4. a kind of percolating device according to claim 1, is characterized in that: described feed tube (3) and drain pipe (8) are also provided with control valve (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520396079.4U CN205007626U (en) | 2015-06-10 | 2015-06-10 | Percolating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520396079.4U CN205007626U (en) | 2015-06-10 | 2015-06-10 | Percolating device |
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| Publication Number | Publication Date |
|---|---|
| CN205007626U true CN205007626U (en) | 2016-02-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520396079.4U Active CN205007626U (en) | 2015-06-10 | 2015-06-10 | Percolating device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106110703A (en) * | 2016-08-01 | 2016-11-16 | 中石化上海工程有限公司 | The method that continuous dynamic countercurrent extracts |
-
2015
- 2015-06-10 CN CN201520396079.4U patent/CN205007626U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106110703A (en) * | 2016-08-01 | 2016-11-16 | 中石化上海工程有限公司 | The method that continuous dynamic countercurrent extracts |
| CN106110703B (en) * | 2016-08-01 | 2018-07-27 | 中石化上海工程有限公司 | The method of continuous dynamic countercurrent extraction |
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