CN207370030U - A kind of spirulina desanding system - Google Patents
A kind of spirulina desanding system Download PDFInfo
- Publication number
- CN207370030U CN207370030U CN201720452569.0U CN201720452569U CN207370030U CN 207370030 U CN207370030 U CN 207370030U CN 201720452569 U CN201720452569 U CN 201720452569U CN 207370030 U CN207370030 U CN 207370030U
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- catch
- basin
- spirulina
- basins
- liquid
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Abstract
The utility model provides a kind of spirulina desanding system, including No.1 catch-basin and No. two catch-basins, liquid-transport pipe-line is sealedly connected between No.1 catch-basin and No. two catch-basins, No.1 catch-basin and No. two catch-basins are connected by liquid-transport pipe-line, No.1 catch-basin sidewall upper is equipped with inlet tube, and No. two catch-basin upper ends are equipped with drain pipe;Its upper strata is spirulina supernatant layer in the operating condition for No.1 catch-basin and No. two catch-basins, and lower floor is sand setting layer;Inlet tube liquid outlet is located in No.1 catch-basin below spirulina supernatant layer;Liquid-transport pipe-line includes upper tubing and lower infusion tube, and upper tubing is horizontally disposed connecting tube, and lower infusion tube inlet is located at the spirulina supernatant layer of No.1 catch-basin, and lower infusion tube liquid outlet is located at below the spirulina supernatant layer of No. two catch-basins;The inlet of drain pipe is located in the spirulina supernatant layer of No. two catch-basins.The beneficial effects of the utility model are:The design possesses the advantages that simple in structure, use cost is low, and desanding capacity is strong.
Description
Technical field
The utility model is related to spirulina desanding working process technical field, more particularly, to a kind of spirulina desanding system
System.
Background technology
In recent years, as people are more and more deep to the degree of awareness of nutritive component of spirulina, therefore spirulina is possessed
Abundant nutrition is worth to have obtained being widely recognized as people.Its nutritive value, which is embodied in spirulina, can mitigate cancer radiation, chemotherapy
Toxicity, can improve the immunity of the human body, also have the function of to reduce blood fat etc..However, the size due to spirulina
Size is in micron level, so being difficult that it is thorough with the sandstone in its residing existence waters in the food processing process of spirulina
Bottom separates, and people can so be caused to decline in edible spirulina mouthfeel.Because spirulina is in loose or close well-regulated spiral
It is cylindric to revolve shape bending, and sole mass kicks the beam, so the methods of being rinsed according to traditional stirring and washing or using a large amount of water
Expected purpose is unable to reach, thus is to be difficult to the sandstone for being swept along spirulina with it thoroughly to divide using traditional cleaning device
From, and cause the excess waste of water resource when rinsing repeatedly.
It can be seen that how to work out a kind of spirulina desanding system, possess that simple in structure, use cost is low and efficient
The advantages of desanding, is a problem to be solved by those skilled in the art.
The content of the invention
To solve the above-mentioned problems, the utility model provides a kind of spirulina desanding system.
A kind of spirulina desanding system of the utility model, including No.1 catch-basin and No. two catch-basins, the No.1 sand setting
Liquid-transport pipe-line is sealedly connected between well and No. two catch-basins, the No.1 catch-basin and No. two catch-basins pass through the liquid-transport pipe-line
Connection, the No.1 catch-basin sidewall upper are equipped with inlet tube, and No. two catch-basin upper ends are equipped with drain pipe;Described one
Its upper strata is spirulina supernatant layer in the operating condition for number catch-basin and No. two catch-basins, and lower floor is sand setting layer;Institute
Inlet tube liquid outlet is stated to be located in the No.1 catch-basin below spirulina supernatant layer;The liquid-transport pipe-line include upper tubing and
Lower infusion tube, the upper tubing are horizontally disposed connecting tube, and the lower infusion tube inlet is located at the No.1 catch-basin
Spirulina supernatant layer, the lower infusion tube liquid outlet is located at below the spirulina supernatant layers of No. two catch-basins;The row
The inlet of liquid pipe is located in the spirulina supernatant layer of No. two catch-basins.
Further, the lower end of the No.1 catch-basin and No. two catch-basins is the sand trap of inverted conical.
Further, the No.1 catch-basin and No. two catch-basins are respectively positioned below ground level.
Further, the delivery pump is centrifugal pump.
A kind of spirulina desanding system of the utility model, has the following advantages compared with prior art:
First, which is to be sunk by two wells of liquid-transport pipe-line connection No.1 catch-basin and No. two catch-basins
Sand structure.Original spirulina liquid to be cleaned is entered by the inlet tube relies on sand coarse aggregate ratio spirulina in the No.1 catch-basin
The sandstone that the characteristics of quality is big makes carries out quick separating by self gravitation and spirulina, and No.1 catch-basin upper strata is obtained clear
Clear spirulina liquid carries out the separation of secondary spiral algae and sandstone by the liquid-transport pipe-line into No. two catch-basin lower parts
Journey, the upper strata of subsequent No. two catch-basins obtain the spirulina liquid of high cleanliness, therefore spirulina and sandstone point in the design
It is simple and practicable from principle, have it is simple in structure, it is easy to use, convenient for promote the advantages of.
Secondly because the No.1 catch-basin and No. two catch-basins are more much larger than traditional cleaning sump volume, so having
The advantages of spirulina flushing dose is big, therefore the utility model has high desanding capacity;Also, because of the spirulina desanding system
Without electric power stirring and manually cleaning, the self gravitation for only relying on tiny sandstone carries out natural subsidence, so it can
The labor intensity of staff is reduced, and has the advantages that save hydroelectric resources.
Finally, due to the inlet tube, liquid-transport pipe-line and drain pipe position opposite with the liquid level of the helicla flute supernatant layer
The Reasonable Regulation And Control put so that spirulina turbid solution has longer isolation of purified path, so as to promote the clean-up effect of spirulina,
Significantly reduce the content of sandstone in spirulina.Further, since two well constructions form the linker in physics, so sinking in No.1
Sand drain continually on the premise of feed flow and No. two continuous drains of catch-basin, can be realized between two wells without extra power
The automatic transport of liquid, therefore, entire spirulina settling system have certain power self-carry for ability, so that this practicality is new
Type has the advantages that reduce power consumption and saves use cost.
Description of the drawings
Fig. 1 is the structure diagram of the utility model.
In figure:1st, inlet tube, 2, No.1 catch-basin, 3, liquid-transport pipe-line, 4, No. two catch-basins, 5, sand trap, 6, sand setting layer,
7th, spirulina supernatant layer, 8, delivery pump.
Specific embodiment
In order to be better understood from the utility model, with reference to specific embodiments and the drawings to the utility model into advance one
The description of step.
As shown in Figure 1, a kind of spirulina desanding system, including No.1 catch-basin 2 and No. two catch-basins 4, the No.1 is sunk
Liquid-transport pipe-line 3 is sealedly connected between sand drain 2 and No. two catch-basins 4, the No.1 catch-basin 2 and No. two catch-basins 4 are by described
Liquid-transport pipe-line 3 connects, and 2 sidewall upper of No.1 catch-basin is equipped with inlet tube 1, and 4 upper end of No. two catch-basins is equipped with
Drain pipe.Whole system realizes the spirulina liquid conveying between two wells by liquid level difference, wherein being equipped in the drain pipe pipeline
For providing the delivery pump 8 that defeated spirulina clear liquid send power.In order to improve the cost performance of the delivery pump 8, so will be described defeated
Pump 8 is sent to be designed as centrifugal pump.
Its upper strata is spirulina supernatant layer 7 in the operating condition for the No.1 catch-basin 2 and No. two catch-basins 4,
Lower floor is sand setting layer 6, in order to realize automatic transport spirulina liquid between two wells.Since two well constructions form the connection in physics
Device, so on the premise of No.1 catch-basin 2 continually feed flow and No. two 4 continuous drains of catch-basin, nothing between two wells
Need extra power that the automatic transport of liquid can be realized, it is seen that entire spirulina settling system has certain power self-carry energy supply
Power reduces the advantage of power consumption and saving use cost so as to assign the present embodiment.
In order to extend the disjoint paths of the spirulina and sandstone, so 1 liquid outlet of inlet tube is arranged on described one
7 lower section of spirulina supernatant layer in number catch-basin 2.So small spirulina of weight floats, and the big sandstone of weight then quickly sinks, this sets
Meter so that the sandstone doping of upper strata spirulina supernatant layer 7 is less, makes purer into the spirulina clear liquid in No. two catch-basins 4
Only.
Similarly, the lower infusion tube inlet is arranged on the spirulina supernatant layer 7 of the No.1 catch-basin 2 by the present embodiment,
The lower infusion tube liquid outlet is arranged on to 7 lower section of spirulina supernatant layer of No. two catch-basins 4.The upper tubing be then for
It prevents from excessive phenomenon occurs due to liquid storage amount is excessively high and designs in No.1 catch-basin 2.In order to make the spiral shell that the drain pipe is collected
Rotation algae is cleaner, so designing the inlet of the drain pipe in the spirulina supernatant layer 7 of No. two catch-basins 4.
In order to which the original spirulina liquid to be cleaned is made more to smoothly enter in the No.1 catch-basin 2, and do not have to
The sealing situation of inlet tube 1 and 2 inlet of No.1 catch-basin is considered, so the upper end of the No.1 catch-basin 2 is offered spiral shell
Algae feed liquor 1 is revolved, and level height residing for the spirulina inlet is higher than level height residing for the lower infusion tube.
In order to which staff is made to be more convenient to grasp the working condition of the No.1 catch-basin 2 and No. two catch-basins 4, so will
The No.1 catch-basin 2 and No. two catch-basins 4 are arranged at below ground level.The conveying for being designed as seaweed liquid provides just
Profit, without being equipped with expensive high-pressure delivery equipment.
In order to which the sandstone in the No.1 catch-basin 2 and No. two catch-basins 4 is made to concentrate on the No.1 catch-basin 2 and No. two
The bottom bosom of catch-basin 4, so being inverted conical by the lower end of the No.1 catch-basin 2 and No. two catch-basins 4
Sand trap 5.
In addition, compared with traditional flat well, the design of the sand trap 5 can more facilitate staff to clear up the sand deposited
Stone, i.e. the sandstone cleaning work for being designed as the No.1 catch-basin 2 and No. two catch-basins 4 provide great convenience.
The operation principle of the embodiment is:
First, original spirulina liquid to be cleaned is entered by the inlet tube 1 in the No.1 catch-basin 2, and according to
By spirulina and sandstone gravity size there are larger difference, the two is made to be layered in the No.1 catch-basin 2, obtains upper strata
Spirulina supernatant layer 7.Then, then continuous feed liquor makes two to the No.1 catch-basin 2 due to No. two 4 continuous drains of catch-basin
The liquid level of number catch-basin 4 is less than the liquid level of the No.1 catch-basin 2, and the setting of liquid-transport pipe-line 3 makes two wells constitute linker,
So only rely on the hydraulic pressures of two wells as conveying power just by the spirulina supernatant layer 7 in No.1 catch-basin 2 by
2 smooth delivery of power of No.1 catch-basin carries out secondary sandstone sedimentation into No. two catch-basins 4, so as on No. two 4 upper stratas of catch-basin
Obtain the high spirulina clear liquid of degree of purity.
It can be seen that entire design structure is reasonable, system operation ability is stablized, the technique effect of the design and traditional spirulina
Cleaning equipment is compared to being improved, and with simple in structure, use cost is low, the strong advantage of desanding capacity.
The embodiment of the utility model is described in detail above, but the content is only the preferable of the utility model
Embodiment, it is impossible to be construed as limiting the scope of the utility model.All impartial changes made according to the scope of the utility model
Change and improvement etc., should all still belong within this patent covering scope.
Claims (4)
1. a kind of spirulina desanding system, it is characterised in that:Including No.1 catch-basin (2) and No. two catch-basins (4), the No.1
Liquid-transport pipe-line (3), the No.1 catch-basin (2) and No. two catch-basins are sealedly connected between catch-basin (2) and No. two catch-basins (4)
(4) connected by the liquid-transport pipe-line (3), No.1 catch-basin (2) sidewall upper is equipped with inlet tube (1), described No. two
Catch-basin (4) upper end is equipped with drain pipe;
Its upper strata is spirulina supernatant layer in the operating condition for the No.1 catch-basin (2) and No. two catch-basins (4)
(7), lower floor is sand setting layer (6);Inlet tube (1) liquid outlet is located at spirulina supernatant layer in the No.1 catch-basin (2)
(7) lower section;The liquid-transport pipe-line (3) includes upper tubing and lower infusion tube, and the upper tubing is horizontally disposed connecting tube,
The lower infusion tube inlet is located at the spirulina supernatant layer (7) of the No.1 catch-basin (2), the lower infusion tube liquid outlet position
Below the spirulina supernatant layer (7) of No. two catch-basins (4);The inlet of the drain pipe is located at No. two catch-basins
(4) in spirulina supernatant layer (7);
It is equipped with to provide the delivery pump (8) that defeated spirulina clear liquid send power in the drain pipe pipeline.
2. spirulina desanding system according to claim 1, it is characterised in that:The No.1 catch-basin (2) and described two
The lower end of number catch-basin (4) is the sand trap (5) of inverted conical.
3. spirulina desanding system according to claim 1, it is characterised in that:The No.1 catch-basin (2) and described two
Number catch-basin (4) is respectively positioned below ground level.
4. the spirulina desanding system according to any one in claim 1-3, it is characterised in that:The delivery pump (8)
For centrifugal pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720452569.0U CN207370030U (en) | 2017-04-27 | 2017-04-27 | A kind of spirulina desanding system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720452569.0U CN207370030U (en) | 2017-04-27 | 2017-04-27 | A kind of spirulina desanding system |
Publications (1)
Publication Number | Publication Date |
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CN207370030U true CN207370030U (en) | 2018-05-18 |
Family
ID=62298411
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201720452569.0U Expired - Fee Related CN207370030U (en) | 2017-04-27 | 2017-04-27 | A kind of spirulina desanding system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207370030U (en) |
-
2017
- 2017-04-27 CN CN201720452569.0U patent/CN207370030U/en not_active Expired - Fee Related
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Legal Events
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GR01 | Patent grant | ||
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: 20180518 Termination date: 20190427 |