CN204752411U - System sand hydrologic cycle clean system - Google Patents

System sand hydrologic cycle clean system Download PDF

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Publication number
CN204752411U
CN204752411U CN201520432308.3U CN201520432308U CN204752411U CN 204752411 U CN204752411 U CN 204752411U CN 201520432308 U CN201520432308 U CN 201520432308U CN 204752411 U CN204752411 U CN 204752411U
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CN
China
Prior art keywords
reaction tower
tower
sewage
sand
order reaction
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
CN201520432308.3U
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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
Original Assignee
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
Publication date
Application filed by Fujian Tianyufangyuan Mining Industry Co Ltd filed Critical Fujian Tianyufangyuan Mining Industry Co Ltd
Priority to CN201520432308.3U priority Critical patent/CN204752411U/en
Application granted granted Critical
Publication of CN204752411U publication Critical patent/CN204752411U/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 hydrologic cycle clean system, a serial communication port, including the sediment stuff pump of pumping sewage, the shale shaker of screening granule, the straight line shaker of dehydration, be used for the sand grain to wash, the spiral classifier of plastic and dehydration, the swirler of separation sewage, a chemicals tank for storing the medicament, the mixed pond of combined sewage and medicament, the reaction tower of silt particle granule in the separation sewage, deposit the precipitator tower of silt particle granule, a squeezer for squeezing reaction tower and precipitator tower discharge mud, a cycling use of water pond for collecting precipitator tower outflow clear water, this practical system sand hydrologic cycle clean system, it makes sewage react rapidly to add the medicament according to various quality of water, deposit, the deposit time is shortened, accelerate the separation of muddy water, make full use of water, play energy saving and emission reduction's effect.

Description

A kind of sand water cycle purification system processed
Technical field
The utility model relates to a kind of sand water cycle purification system 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, and in earth, water content is high, and waste water serious, earth is unfavorable for transport.
Utility model content
The utility model discloses a kind of sand water cycle purification system 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 water cycle purification system processed, it is characterized in that, comprise the Pulp pump pumping sewage, the vibratory screening apparatus of screening particle, the straight line shaker of dehydration, rinse for sand grains, the screw classifier of shaping and dehydration, be separated the swirler of sewage, for storing the pharmacy jar of medicament, the mixing pit of combined sewage and medicament, be separated the reaction tower of silt particle particle in sewage, the settling tower of precipitation silt particle particle, the squeezing machine of mud is discharged for squeezing reaction tower and settling tower, the cycling use of water pond of clear water is flowed out for collecting precipitation tower, the particle that composite demand is sifted out in described vibration falls into the initiating terminal of screw classifier, sand grains is sieved by current punching in screw classifier, shaping, dehydration obtains the clean coarse sand granule of composite demand, the sewage that screw classifier is discharged is delivered to swirler by Pulp pump and is separated, isolated sewage input mixing pit, isolated fine sand is delivered to straight line shaker and is dewatered, the end that fine sand after dehydration sends into spiral separator mixes with coarse sand, the valve for controlling to discharge mud is provided with bottom described reaction tower, the 3rd valve for controlling to discharge mud is provided with bottom described settling tower, described pharmacy jar attached bag draws together the first pharmacy jar and the second pharmacy jar, drug delivery in described second pharmacy jar is to mixing pit, the Liquid transfer of mixing pit mixing is to reaction tower, the medicament of described first pharmacy jar is directly delivered to reaction tower, the clear water that reaction tower flows out is delivered to settling tower and carries out precipitation purification.
Further, described reaction tower comprises first order reaction tower and second order reaction tower, described first order reaction tower bottom is provided with the first valve for controlling to discharge mud, described second order reaction tower bottom is provided with the second valve for controlling to discharge mud, drug delivery in described second pharmacy jar is to mixing pit, the liquid of mixing pit mixing is delivered to first order reaction tower and second order reaction tower respectively, the medicament of described first pharmacy jar is delivered to first order reaction tower and second order reaction tower respectively, the clear water that first order reaction tower and second order reaction tower flow out is delivered to settling tower and carries out precipitation purification.
Further, described first valve and the second valve are Pneumatic butterfly valve.
Further, described Pneumatic butterfly valve adopts the time relay to control.
The utility model advantage is compared with prior art: the utility model carrys out alternative traditional settling tank by reaction tower, add medicament according to various water quality sewage to be reacted rapidly, precipitates, reduce sedimentation time, accelerate the separation of muddy water, clear water after purification is stored into water reservoir recycle, make full use of water resources, play the effect of energy-saving and emission-reduction; Because the content of mud is different with composition, the time of reaction precipitation is also different, by the control Pneumatic butterfly valve of the time relay, to control sedimentary discharge, makes throw out reach the optimum concn of squeezing.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is schema of the present utility model;
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 depicted in figs. 1 and 2, a kind of sand water cycle purification system processed, it is characterized in that, comprise the Pulp pump 1 pumping sewage, the vibratory screening apparatus 2 of screening particle, the straight line shaker 3 of dehydration, rinse for sand grains, the screw classifier 4 of shaping and dehydration, be separated the swirler 5 of sewage, for storing the pharmacy jar of medicament, the mixing pit 8 of combined sewage and medicament, be separated the reaction tower of silt particle particle in sewage, the settling tower 11 of precipitation silt particle particle, the squeezing machine 12 of mud is discharged for squeezing reaction tower and settling tower, the cycling use of water pond 13 of clear water is flowed out for collecting precipitation tower 11, the particle that described vibratory screening apparatus 2 goes out composite demand falls into the initiating terminal of screw classifier 4, sand grains is sieved by current punching in screw classifier 4, shaping, dehydration obtains the clean coarse sand granule of composite demand, the sewage that screw classifier 4 is discharged is delivered to swirler 5 by Pulp pump and is separated, isolated sewage input mixing pit, isolated fine sand is delivered to straight line shaker 3 and is dewatered, the end that fine sand after dehydration sends into spiral separator mixes with coarse sand, the valve for controlling to discharge mud is provided with bottom described reaction tower, the 3rd valve 111 for controlling to discharge mud is provided with bottom described settling tower, described pharmacy jar attached bag draws together the first pharmacy jar 7 and the second pharmacy jar 6, drug delivery in described second pharmacy jar 6 is to mixing pit 8, the Liquid transfer that mixing pit 8 mixes is to reaction tower, the medicament of described first pharmacy jar 7 is directly delivered to reaction tower, the clear water that reaction tower flows out is delivered to settling tower 11 and carries out precipitation purification.
In order to reach better decontamination effect improving, described reaction tower comprises first order reaction tower 9 and second order reaction tower 10, the first valve 91 for controlling to discharge mud is provided with bottom described first order reaction tower 9, the second valve 101 for controlling to discharge mud is provided with bottom described second order reaction tower 10, drug delivery in described second pharmacy jar 6 is to mixing pit 8, the liquid that mixing pit 8 mixes is delivered to first order reaction tower 9 and second order reaction tower 10 respectively, the medicament of described first pharmacy jar 7 is delivered to first order reaction tower 9 and second order reaction tower 10 respectively, the clear water that first order reaction tower 9 and second order reaction tower 10 flow out is delivered to settling tower 11 and carries out precipitation purification.
Preferably described first valve 91 and the second valve 101 are Pneumatic butterfly valve, and described Pneumatic butterfly valve adopts the time relay to control.
During use, in washed-out sand process, the sewage produced pumps on swirler by Pulp pump, be separated by swirler, stream of relatively coarse particles to straight line shaker dewaters, thin flows to mixing pit by the overflow port of swirler, the existing mixing of medicament is added in mixing pit, controlled by the time relay, temporally flow to two reaction towers respectively and carry out reaction precipitation, then pump mud by sludge pump and carry out press dewatering to squeezing machine, the clear water separated after reaction precipitation flow back into cycling use of water pond and carries out recycle, supplementary external clear water is also carried out by external water reservoir in cycling use of water pond, to offset the damage by water consumption of sand process processed, whole system reaches zero release no pollution.
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 (4)

1. a sand water cycle purification system processed, it is characterized in that, comprise the Pulp pump (1) pumping sewage, the vibratory screening apparatus (2) of screening particle, the straight line shaker (3) of dehydration, rinse for sand grains, the screw classifier (4) of shaping and dehydration, be separated the swirler (5) of sewage, for storing the pharmacy jar of medicament, the mixing pit (8) of combined sewage and medicament, be separated the reaction tower of silt particle particle in sewage, the settling tower (11) of precipitation silt particle particle, the squeezing machine (12) of mud is discharged for squeezing reaction tower and settling tower, the cycling use of water pond (13) of clear water is flowed out for collecting precipitation tower (11), the particle that described vibratory screening apparatus (2) goes out composite demand falls into the initiating terminal of screw classifier (4), sand grains is sieved by current punching in screw classifier (4), shaping, dehydration obtains the clean coarse sand granule of composite demand, the sewage that screw classifier (4) is discharged is delivered to swirler (5) by Pulp pump and is separated, isolated sewage input mixing pit, isolated fine sand is delivered to straight line shaker (3) and is dewatered, the end that fine sand after dehydration sends into spiral separator mixes with coarse sand, the valve for controlling to discharge mud is provided with bottom described reaction tower, the 3rd valve (111) for controlling to discharge mud is provided with bottom described settling tower, described pharmacy jar attached bag draws together the first pharmacy jar (7) and the second pharmacy jar (6), drug delivery in described second pharmacy jar (6) is to mixing pit (8), the Liquid transfer that mixing pit (8) mixes is to reaction tower, the medicament of described first pharmacy jar (7) is directly delivered to reaction tower, the clear water that reaction tower flows out is delivered to settling tower (11) and carries out precipitation purification.
2. a kind of sand water cycle purification system processed as claimed in claim 1, it is characterized in that, described reaction tower comprises first order reaction tower (9) and second order reaction tower (10), described first order reaction tower (9) bottom is provided with the first valve (91) for controlling to discharge mud, described second order reaction tower (10) bottom is provided with the second valve (101) for controlling to discharge mud, drug delivery in described second pharmacy jar (6) is to mixing pit (8), the liquid that mixing pit (8) mixes is delivered to first order reaction tower (9) and second order reaction tower (10) respectively, the medicament of described first pharmacy jar (7) is delivered to first order reaction tower (9) and second order reaction tower (10) respectively, the clear water that first order reaction tower (9) and second order reaction tower (10) flow out is delivered to settling tower (11) and carries out precipitation purification.
3. a kind of sand water cycle purification system processed as claimed in claim 2, it is characterized in that, described first valve (91) and the second valve (101) are Pneumatic butterfly valve.
4. a kind of sand water cycle purification system processed as claimed in claim 3, is characterized in that, described Pneumatic butterfly valve adopts the time relay to control.
CN201520432308.3U 2015-06-23 2015-06-23 System sand hydrologic cycle clean system Expired - Fee Related CN204752411U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520432308.3U CN204752411U (en) 2015-06-23 2015-06-23 System sand hydrologic cycle clean system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520432308.3U CN204752411U (en) 2015-06-23 2015-06-23 System sand hydrologic cycle clean system

Publications (1)

Publication Number Publication Date
CN204752411U true CN204752411U (en) 2015-11-11

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CN201520432308.3U Expired - Fee Related CN204752411U (en) 2015-06-23 2015-06-23 System sand hydrologic cycle clean system

Country Status (1)

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CN (1) CN204752411U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110252641A (en) * 2019-06-21 2019-09-20 山东诚邦重工有限公司 Washed-out sand equipment
CN111359304A (en) * 2020-04-02 2020-07-03 中国天楹股份有限公司 Slag water recovery system and recovery method for waste incineration slag separation plant

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110252641A (en) * 2019-06-21 2019-09-20 山东诚邦重工有限公司 Washed-out sand equipment
CN111359304A (en) * 2020-04-02 2020-07-03 中国天楹股份有限公司 Slag water recovery system and recovery method for waste incineration slag separation plant

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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: 20151111

Termination date: 20170623