CN204973127U - Sediment liquid autosegregation system - Google Patents
Sediment liquid autosegregation system Download PDFInfo
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- CN204973127U CN204973127U CN201520565466.6U CN201520565466U CN204973127U CN 204973127 U CN204973127 U CN 204973127U CN 201520565466 U CN201520565466 U CN 201520565466U CN 204973127 U CN204973127 U CN 204973127U
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- pump
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- rotating separator
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Abstract
The utility model provides a sediment liquid autosegregation system, including the extracting tube, extracting tube rear portion top is equipped with the extract fluid -discharge tube, and sediment liquid delivery pump is connected to the extract fluid -discharge tube, the exit linkage of sediment liquid delivery pump has cylinder separator soon, and the slag notch that revolves the cylinder separator is connected with the horizontal feeding ware, and the exit linkage of horizontal feeding ware has perpendicular feeder, the export and the extracting tube intercommunication of perpendicular feeder, the discharge gate of extracting tube is connected with drying machine, and drying machine's exit linkage has alcohol distillation plant, alcohol distillation plant's export output extract finished product, the liquid outlet that revolves the cylinder separator is connected with the extract jar of keeping in, and the bottom leakage fluid dram that the extract was kept in jar is connected with the back flush pump respectively and returns the liquid washer pump, the back flush delivery side of pump with revolve cylinder separator intercommunication, return the export and sediment liquid delivery pump intercommunication of liquid washer pump. This system has reduced pipe blockage, has realized the autosegregation of sediment liquid among the continuous production, has improved production efficiency, has reduced the operation cost.
Description
Technical field
The utility model relates to a kind of equipment be separated with extract solid slag in extract, particularly relates to a kind of slag liquid automatic separation system.
Background technology
In the production technology utilizing ultrasonic wave added ethanol continuous countercurrent extraction turmeric saponin, with tiny slag charge floating in a large number in extract, if be separated removing not in time in production, the easy occluding device pipeline of slag charge, initial operating stage, needs frequent block clearing thus causes producing to stop transport.
Originally, people by setting up buffering blasket type sedimentation and filtration device respectively before extract overflow pipe and extract temporary storage tank, mode that buffering carries blue filter is cleared up slag charge to utilize artificial time in turn to open, and to keep turmeric saponin to extract the continuity of producing, enhances productivity., also there is more drawback in the continuity that can keep producing though artificial block clearing is removed slag: one is artificial timing block clearing slagging-off, at least needs three people's operations (comprise dismounting buffering cover, drag for slag, transport, centrifugal recovery extraction solvent etc.), cause labour cost to increase; Two be drag in slag, transport, centrifugal separation processes because of evaporating, emitting, dripping or leaking of liquid or gas and centrifugal after slag charge without the de-recovery process of steaming solutions of directly anhydrating, thus cause the increase of extraction solvent unit consumption; Three is that artificial timing block clearing does not match with large industrial continuous seepage, occurs block clearing situation not in time, and due to extract dehvery pump, to export bore little thus cause equipment pipe to block simultaneously, occurs continuous seepage disruption.
For a change artificial and industrial-scale production inharmonious supporting, extract solvent unit consumption high in cost of production problem, afterwards, people have developed a kind of cagem type machine automatization dregs and liquor separation device.But due to this device there is leakage, filter screen easily blocks, filter the defects such as the easy material stock of slag charge blanking, causes its difficult problem that still slag liquid is separated automatically in the large industrial continuous seepage of unsuccessful solution turmeric saponin.
Summary of the invention
For reducing line clogging, the slag liquid realized in the large industrial continuous seepage of turmeric saponin is separated automatically, enhances productivity, and reduces production cost, the utility model proposes a kind of slag liquid automatic separation system.
For this reason, the technical solution of the utility model is: a kind of slag liquid automatic separation system, comprise extracting tube, extract discharging tube is provided with on top, extracting tube rear portion, extract discharging tube connects slag liquid delivery pump, it is characterized in that: described slag liquid conveying delivery side of pump is connected with cylinder-rotating separator, is connected with straight feeding device at the slag notch of cylinder-rotating separator, the outlet of straight feeding device is connected with vertical feed appliance, and the outlet of vertical feed appliance is communicated with described extracting tube, be connected with squeezing machine at the discharging opening of extracting tube, the outlet of squeezing machine is connected with alcohol distillation device, exports extract finished product in the outlet of alcohol distillation device, the liquid outlet of described cylinder-rotating separator is connected with extract temporary storage tank, the bottom leakage fluid dram of extract temporary storage tank is connected to backwashing pump and returns liquid flushing pump, described backwash delivery side of pump is communicated with cylinder-rotating separator, the supernatant liquor in extract temporary storage tank is made to enter cylinder-rotating separator by backwashing pump during use, the filter screen outside of cylinder-rotating separator is made to obtain backwash, described time liquid rinses delivery side of pump and is communicated with slag liquid delivery pump, precipitation slag liquid in extract temporary storage tank is circulated enter slag liquid delivery pump and cylinder-rotating separator carries out secondary filter by returning liquid flushing pump during use, and its interior of cylinder-rotating separator is just rinsed.
One for technique scheme is improved and is: for improving developing result, relay is provided with between described time liquid flushing pump and backwashing pump, by this relay, liquid flushing pump and backwashing pump timing are alternately started, to carry out positive and negative flushing to the inside and outside portion of the filter screen of cylinder-rotating separator respectively during use.
Beneficial effect:
The utility model, by arranging cylinder-rotating separator in the outlet of slag liquid delivery pump, and sets gradually straight feeding device and vertical feed appliance at cylinder-rotating separator slag notch respectively, to make in slag charge separation process all the time not material stock, to reduce mouth of pipe blocking; By arranging backwashing pump at extract temporary storage tank leakage fluid dram respectively and returning liquid flushing pump, backwashing pump is communicated with cylinder-rotating separator, and liquid flushing pump will be returned be communicated with slag liquid delivery pump, isolated slag liquid is made to obtain recycling and carry out positive backwash to cylinder-rotating separator screen inside and outside, ensure that in system operation, filter screen does not block all the time, slag charge can be continuously separated out, also can carry out secondary filter to the slag charge in temporary storage tank simultaneously, ensure that the slag charge extracted in stoste is not brought subsequent handling into and caused equipment to block, avoid stopping transport because block clearing causes to produce.The system reduces line clogging, achieve the automatic separation of slag liquid in industrialization continuous seepage, improve production efficiency, good separating effect, decrease extraction solvent consumption, reduce operation cost.
Accompanying drawing explanation
Fig. 1 is front view of the present utility model;
Fig. 2 is top view of the present utility model;
Number in the figure is: 1, extracting tube; 2, extract discharging tube; 3, slag liquid delivery pump; 4, cylinder-rotating separator; 5, straight feeding device; 6, vertical feed appliance; 7, squeezing machine; 8, alcohol distillation device; 9, extract temporary storage tank; 10, backwashing pump; 11, liquid flushing pump is returned.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1 and Figure 2, a kind of slag liquid automatic separation system, comprises extracting tube 1, and the top, rear portion of extracting tube 1 is provided with extract discharging tube 2, and extract discharging tube 2 is connected slag liquid delivery pump 3 by pipeline; Cylinder-rotating separator 4 is connected with by pipeline in the outlet of described slag liquid delivery pump 3, straight feeding device 5 is connected with at the slag notch of cylinder-rotating separator 4, be connected with vertical feed appliance 6 in the outlet of straight feeding device 5, the outlet of vertical feed appliance 6 is communicated with described extracting tube 1; Be connected with squeezing machine 7 at the discharging opening of extracting tube 1, be connected with alcohol distillation device 8 in the outlet of squeezing machine 7, export extract finished product in the exit of alcohol distillation device 8; Extract temporary storage tank 9 is connected with at the liquid outlet of described cylinder-rotating separator 4, be connected to backwashing pump 10 at the bottom leakage fluid dram of extract temporary storage tank 9 and return liquid flushing pump 11, the outlet of described backwashing pump 10 is communicated with cylinder-rotating separator 4 by pipeline, make the supernatant liquor in extract temporary storage tank 9 enter cylinder-rotating separator 4 by backwashing pump 10 during use, obtain backwash to make the filter screen outside of cylinder-rotating separator 4; The outlet of described time liquid flushing pump 11 is communicated with slag liquid delivery pump 3 by pipeline, pass through back liquid flushing pump 11 during use the precipitation slag liquid in extract temporary storage tank 9 to be circulated enter slag liquid delivery pump 3 and cylinder-rotating separator 4 carries out secondary filter, the secondary slag liquid after filtration also makes its interior of cylinder-rotating separator 4 just be rinsed.
As shown in Figure 1 and Figure 2, in order to improve developing result, between described time liquid flushing pump 11 and backwashing pump 10, relay is installed, by this relay, liquid flushing pump and backwashing pump timing are alternately started, just to rinse its interior of cylinder-rotating separator 3 respectively and to carry out backwash to filter screen outside during use.
The utility model, by arranging cylinder-rotating separator in the outlet of slag liquid delivery pump, and sets gradually straight feeding device and vertical feed appliance at cylinder-rotating separator slag notch respectively, to make in slag charge separation process all the time not material stock, to reduce mouth of pipe blocking; By arranging backwashing pump at extract temporary storage tank leakage fluid dram respectively and returning liquid flushing pump, backwashing pump is communicated with cylinder-rotating separator, and liquid flushing pump will be returned be communicated with slag liquid delivery pump, isolated slag liquid is made to obtain recycling and carry out positive backwash to cylinder-rotating separator screen inside and outside, ensure that in system operation, filter screen does not block all the time, slag charge can be continuously separated out, also can carry out secondary filter to the slag charge in temporary storage tank simultaneously, ensure that the slag charge extracted in stoste is not brought subsequent handling into and caused equipment to block, avoid stopping transport because block clearing causes to produce.The system reduces line clogging, achieve the automatic separation of slag liquid in industrialization continuous seepage, improve production efficiency, good separating effect, decrease extraction solvent consumption, reduce operation cost.
Claims (2)
1. a slag liquid automatic separation system, comprise extracting tube, extract discharging tube is provided with on top, extracting tube rear portion, extract discharging tube connects slag liquid delivery pump, it is characterized in that: described slag liquid conveying delivery side of pump is connected with cylinder-rotating separator, be connected with straight feeding device at the slag notch of cylinder-rotating separator, the outlet of straight feeding device is connected with vertical feed appliance, and the outlet of vertical feed appliance is communicated with described extracting tube, be connected with squeezing machine at the discharging opening of extracting tube, the outlet of squeezing machine is connected with alcohol distillation device, exports extract finished product in the outlet of alcohol distillation device, the liquid outlet of described cylinder-rotating separator is connected with extract temporary storage tank, the bottom leakage fluid dram of extract temporary storage tank is connected to backwashing pump and returns liquid flushing pump, described backwash delivery side of pump is communicated with cylinder-rotating separator, the supernatant liquor in extract temporary storage tank is made to enter cylinder-rotating separator by backwashing pump during use, the filter screen outside of cylinder-rotating separator is made to obtain backwash, described time liquid rinses delivery side of pump and is communicated with slag liquid delivery pump, precipitation slag liquid in extract temporary storage tank is circulated enter slag liquid delivery pump and cylinder-rotating separator carries out secondary filter by returning liquid flushing pump during use, and its interior of cylinder-rotating separator is just rinsed.
2. a kind of slag liquid automatic separation system according to claim 1, it is characterized in that: between described time liquid flushing pump and backwashing pump, be provided with relay, by this relay, liquid flushing pump and backwashing pump timing are alternately started, to carry out positive and negative flushing to the inside and outside portion of the filter screen of cylinder-rotating separator respectively during use.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520565466.6U CN204973127U (en) | 2015-07-31 | 2015-07-31 | Sediment liquid autosegregation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520565466.6U CN204973127U (en) | 2015-07-31 | 2015-07-31 | Sediment liquid autosegregation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204973127U true CN204973127U (en) | 2016-01-20 |
Family
ID=55107547
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520565466.6U Expired - Fee Related CN204973127U (en) | 2015-07-31 | 2015-07-31 | Sediment liquid autosegregation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204973127U (en) |
-
2015
- 2015-07-31 CN CN201520565466.6U patent/CN204973127U/en not_active Expired - Fee Related
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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: 20160120 Termination date: 20160731 |