CN204848396U - System sand sewage treatment tower - Google Patents

System sand sewage treatment tower Download PDF

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Publication number
CN204848396U
CN204848396U CN201520530645.6U CN201520530645U CN204848396U CN 204848396 U CN204848396 U CN 204848396U CN 201520530645 U CN201520530645 U CN 201520530645U CN 204848396 U CN204848396 U CN 204848396U
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CN
China
Prior art keywords
sewage treatment
tower
reaction channel
processed
sand sewage
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201520530645.6U
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Chinese (zh)
Inventor
王天
陈翔铭
黄日昌
黄红金
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujian Tianyufangyuan Mining Industry Co Ltd
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Fujian Tianyufangyuan Mining Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
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Priority to CN201520530645.6U priority Critical patent/CN204848396U/en
Application granted granted Critical
Publication of CN204848396U publication Critical patent/CN204848396U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a system sand sewage treatment tower, including the king -tower body, set firmly in the reaction portion of the internal portion of king -tower through the fixed part, support the supporting part of the king -tower body, king -tower body bottom is the portion of gathering materials, open the bottom of the portion of gathering materials has the reactant export of taking connecting portion, the king -tower body is opened to have near the top edge and is made the clear water export that purifies the clear water outflow, its characterized in that, reaction portion includes reaction channel and spiral track, the spiral track is vertical to be installed in the reaction channel, makes the liquid that flows in from the reaction channel top along the spiral track from the last helicoidal flow of doing under to in the reaction channel, the utility model discloses system sand sewage treatment tower is equipped with the spiral track in the reaction channel, medicament and sewage pass through the orbital drainage of spiral, utilizes the principle of spiral stirring to make sewage and medicament mix the stirring in the short time, 3 times of left and right sides that improvement reaction time is fast.

Description

A kind of sand sewage treatment tower processed
Technical field
The utility model relates to a kind of sand sewage treatment tower processed, belongs to mine system engineering processing technology field.
Background technology
Can produce a large amount of sewage in the process of the Machine-made Sand and washing rubble that wash method with water, sewage is with after crossing fine sand recovery device process, and sewage is still containing mud.Traditional processing mode is filtered step by step by settling tank, precipitates and allow silt be separated with water, and this mode floor space is many, sedimentation time is long, does not have efficient Machine-made Sand and washing rubble sewage treatment tower in the market.
Utility model content
The utility model discloses a kind of sand sewage treatment tower processed, to solve the problem mentioned in background technology.
In order to reach above-mentioned object, the utility model adopts following concrete technical scheme:
A kind of sand sewage treatment tower processed, comprise main tower, the reacting part of main tower inside is fixedly arranged on by fixed part, support the support portion of main tower, it is the portion of gathering materials bottom described main tower, the lowermost end in the described portion that gathers materials has the reactant outlet of band connection section, described main tower has the clear water output that purification clear water is flowed out near top, it is characterized in that, described reacting part comprises reaction channel and helical orbit, described helical orbit is vertically installed in reaction channel, the liquid that flows into above reaction channel to be spinned from top to bottom flowing along helical orbit reaction channel.
Further, the desilting mouth at through helical orbit center from top to bottom is also comprised.
Further, also comprise unhurried current portion, described reaction channel bottom is connected with the unhurried current portion reducing flow velocity.
Further, described unhurried current portion is and the amplification mouth be connected bottom reaction channel.
Further, also comprise spreader plate and boatswain chair, the outline of described spreader plate is close with the similar size of amplification mouth bottom end outlet shape, and described spreader plate is fixedly arranged near amplifying immediately below mouth bottom end outlet by boatswain chair.
Further, described spreader plate is dull and stereotyped or the sharp centrum plate upward of vertebra.
Further, the cone angle of described spreader plate is 120 ° ~ 175 °.
Further, the cone angle of described spreader plate is 150 °.
Further, also comprise overflow groove, described overflow groove to be surrounded near upper port medial surface, groove inwall and groove bottom by main tower and forms, and described clear water output is positioned on groove bottom, and the clear water after filtration is flowed out from overflow groove.
Further, also comprise separation net, described separation net is fixedly arranged in the annulus that groove inwall and reaction channel be encircled into.
Further, also comprise pressure relief opening and ladder, described pressure relief opening is arranged at main tower on the external cylindrical surface of lower end, and described ladder extends to top from main tower bottom and is arranged at this main tower external cylindrical surface.
Further, described main tower diameter is 2500mm.
The utility model advantage is compared with prior art:
1, at reaction channel built with there being helical orbit, medicament and sewage, by the drainage of helical orbit, utilize the principle of helical stir to make sewage and medicament mix and blend at short notice, improve the reaction times fast about 3 times.
2, separation net is housed, the effect of separation net is: the flow velocity that 1, can slow down water, stops the flocculence suspended substance that a below part floats; 2, can prevent external object waft into, fall into reaction tower, in order to avoid it blocks pipeline affect pumping of reactant; 3, the safety operation of workman on reaction tower can be protected.
3, current enter to flow out through unhurried current portion from osculum, make current reduced velocity flow in moving process, allow medicament and mud have the sufficient time to carry out reaction precipitation, allow completely reacted floss not easily be taken out of the water surface in the current slowed down.
4, arrive spreader plate through the good floss of unhurried current portion initial reaction to utilize reflection to refund the principle slowing down current to have slowed down the speed of current, the prolongation reaction times makes current overflow from side in this process, utilize the Angulation changes water (flow) direction of spreader plate, current are flowed down with reacted floss above reaction tower tapering mouth.Advantage 1: the throw out that current directly can not impact below rushes the full-blown flowers condensed broken; 2: current down allow reactant precipitate below spreader plate from periphery, thing, water are separated relatively more thorough, and clear water overflows, and underflow precipitation bottom is extracted out with the best effect reaching squeezing; 3: the water (flow) direction utilizing spreader plate Angulation changes; the difficult problem that can play throw out caking at the bottom of purge column is flowed down above cone mouth; solve popular response tower and can produce the blocking of material caking in use for some time, the problem that cleaning is time-consuming, require great effort be shut down, reach energy-conservation, efficient effect.
5, main tower intended diameter is 2500mm, and general mine road flat-bed trailer can transport, and is convenient to transport and installs.Because main tower diameter is little, floor space is little can be placed on each place, place flexibly.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is the part sectioned view of Fig. 1 along A-A face;
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Embodiment 1:
As shown in FIG. 1 to 3, a kind of sand sewage treatment tower processed, comprise main tower 1, the reacting part of main tower inside is fixedly arranged on by fixed part 21, support the support portion 10 of main tower, it is the portion of gathering materials 9 bottom main tower, the lowermost end in portion 9 of gathering materials has the reactant outlet 11 of band connection section, main tower has the clear water output 73 that purification clear water is flowed out near top, reacting part comprises reaction channel 2 and helical orbit 3, helical orbit 3 is vertically installed in reaction channel 2, the liquid flowed into above reaction channel 2 to be spinned from top to bottom flowing along helical orbit 3 reaction channel 2,
For convenience of regularly removing the mud overstock in helical orbit 3, helical orbit 3 center is provided with desilting mouth 4 through from top to bottom;
Also be provided with overflow groove 7, overflow groove 7 to be surrounded near upper port medial surface, groove inwall 71 and groove bottom 72 by main tower 1 and forms, and clear water output 73 is positioned on groove bottom 72, and the clear water after filtration is flowed out from overflow groove 7;
In order to stop flocculence suspended substance that a below part floats, prevent from foreign material from falling in tower resulting in blockage and improve processing safety, also comprising separation net 8, separation net 8 is fixedly arranged on groove inwall 71 with the 2-in-1 annulus surrounded of reaction channel;
Also comprise pressure relief opening 12 and ladder 13, pressure relief opening 12 is arranged at main tower 1 on the external cylindrical surface of lower end, and ladder 13 extends to top and is arranged at this main tower 1 external cylindrical surface from main tower 1 bottom;
For convenience of the transport of this sewage treatment tower, main tower 1 diameter is preferably designed for 2500mm.
Embodiment 2:
As shown in FIG. 1 to 3, on the basis of embodiment 1, also comprise unhurried current portion, described reaction channel 2 bottom is connected with unhurried current portion, and this unhurried current portion can be the amplification mouth 5 be connected bottom 2 roads logical with reaction.
Embodiment 3:
As shown in FIG. 1 to 3, on the basis of embodiment 2, also comprise spreader plate 6 and boatswain chair 61, the outline of spreader plate 6 is close with the similar size of amplification mouth 5 bottom end outlet shape, and spreader plate 6 is fixedly arranged near amplifying immediately below mouth 5 bottom end outlet by boatswain chair 61; Spreader plate 6 can be dull and stereotyped or the sharp centrum plate upward of vertebra;
When spreader plate 6 is centrum plates, its cone angle scope is 120 ° ~ 175 °, is preferably 150 °.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this specification sheets is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.

Claims (12)

1. a sand sewage treatment tower processed, comprise main tower (1), the reacting part of main tower inside is fixedly arranged on by fixed part (21), support the support portion (10) of main tower, bottom described main tower be the portion of gathering materials (9), the lowermost end of the described portion that gathers materials (9) has reactant outlet (11) of band connection section, described main tower has the clear water output (73) that purification clear water is flowed out near top, it is characterized in that, described reacting part comprises reaction channel (2) and helical orbit (3), described helical orbit (3) is vertically installed in reaction channel (2), the liquid flowed into from reaction channel (2) top to be spinned from top to bottom flowing along helical orbit (3) reaction channel (2).
2. a kind of sand sewage treatment tower processed as claimed in claim 1, is characterized in that, also comprise the desilting mouth (4) at through helical orbit (3) center from top to bottom.
3. the one sand sewage treatment tower as described in as arbitrary in claim 1 or 2, is characterized in that, also comprise unhurried current portion, and described reaction channel (2) bottom is connected with the unhurried current portion reducing flow velocity.
4. a kind of sand sewage treatment tower processed as claimed in claim 3, is characterized in that, described unhurried current portion is the amplification mouth (5) be connected bottom (2) road logical with reaction.
5. a kind of sand sewage treatment tower processed as claimed in claim 4, it is characterized in that, also comprise spreader plate (6) and boatswain chair (61), the outline of described spreader plate (6) is close with the similar size of amplification mouth (5) bottom end outlet shape, and described spreader plate (6) is fixedly arranged near amplifying immediately below mouth (5) bottom end outlet by boatswain chair (61).
6. a kind of sand sewage treatment tower processed as claimed in claim 5, is characterized in that, described spreader plate (6) is dull and stereotyped or the sharp centrum plate upward of vertebra.
7. a kind of sand sewage treatment tower processed as claimed in claim 6, it is characterized in that, the cone angle of described spreader plate (6) is 120 ° ~ 175 °.
8. a kind of sand sewage treatment tower processed as claimed in claim 7, it is characterized in that, the cone angle of described spreader plate (6) is 150 °.
9. a kind of sand sewage treatment tower processed as claimed in claim 1, it is characterized in that, also comprise overflow groove (7), described overflow groove (7) is surrounded by main tower (1) close upper port medial surface, groove inwall (71) and groove bottom (72) and forms, described clear water output (73) is positioned on groove bottom (72), and the clear water after filtration is flowed out from overflow groove (7).
10. sand sewage treatment tower processed as claimed in claim 9 a kind of, is characterized in that, also comprise separation net (8), and described separation net (8) is fixedly arranged in the annulus that groove inwall (71) and reaction channel (2) be encircled into.
11. a kind of sand sewage treatment towers processed as claimed in claim 1, it is characterized in that, also comprise pressure relief opening (12) and ladder (13), described pressure relief opening (12) is arranged at main tower (1) on the external cylindrical surface of lower end, and described ladder (13) extends to top from main tower (1) bottom and is arranged at this main tower (1) external cylindrical surface.
12. a kind of sand sewage treatment towers processed as claimed in claim 1, it is characterized in that, described main tower (1) diameter is 2500mm.
CN201520530645.6U 2015-07-22 2015-07-22 System sand sewage treatment tower Expired - Fee Related CN204848396U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520530645.6U CN204848396U (en) 2015-07-22 2015-07-22 System sand sewage treatment tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520530645.6U CN204848396U (en) 2015-07-22 2015-07-22 System sand sewage treatment tower

Publications (1)

Publication Number Publication Date
CN204848396U true CN204848396U (en) 2015-12-09

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Application Number Title Priority Date Filing Date
CN201520530645.6U Expired - Fee Related CN204848396U (en) 2015-07-22 2015-07-22 System sand sewage treatment tower

Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105084478A (en) * 2015-07-22 2015-11-25 福建省天玉方圆矿业有限公司 Sand making sewage treatment tower

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105084478A (en) * 2015-07-22 2015-11-25 福建省天玉方圆矿业有限公司 Sand making sewage treatment tower

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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

Granted publication date: 20151209

Termination date: 20170722

CF01 Termination of patent right due to non-payment of annual fee