CN108046398A - Sedimentation separation pulping equipment and sedimentation separation pulping system - Google Patents
Sedimentation separation pulping equipment and sedimentation separation pulping system Download PDFInfo
- Publication number
- CN108046398A CN108046398A CN201810039042.4A CN201810039042A CN108046398A CN 108046398 A CN108046398 A CN 108046398A CN 201810039042 A CN201810039042 A CN 201810039042A CN 108046398 A CN108046398 A CN 108046398A
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- Prior art keywords
- cylinder
- sedimentation separation
- connecting tube
- separation pulping
- sedimentation
- Prior art date
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Links
- 238000004062 sedimentation Methods 0.000 title claims abstract description 65
- 238000000926 separation method Methods 0.000 title claims abstract description 58
- 238000004537 pulping Methods 0.000 title claims abstract description 49
- 239000000463 material Substances 0.000 claims abstract description 74
- 238000005243 fluidization Methods 0.000 claims abstract description 15
- 238000005520 cutting process Methods 0.000 claims abstract description 12
- 239000012530 fluid Substances 0.000 claims abstract description 7
- 239000004576 sand Substances 0.000 claims description 27
- 239000007788 liquid Substances 0.000 claims description 9
- 239000010865 sewage Substances 0.000 claims description 8
- 229920002472 Starch Polymers 0.000 claims description 5
- 235000019698 starch Nutrition 0.000 claims description 5
- 239000008107 starch Substances 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000001727 in vivo Methods 0.000 claims description 2
- 239000010813 municipal solid waste Substances 0.000 abstract description 12
- 238000012545 processing Methods 0.000 abstract description 9
- 238000005265 energy consumption Methods 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 description 14
- 239000000126 substance Substances 0.000 description 9
- 239000002002 slurry Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 230000009471 action Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 238000013019 agitation Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 210000000988 bone and bone Anatomy 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 235000002566 Capsicum Nutrition 0.000 description 2
- 240000008574 Capsicum frutescens Species 0.000 description 2
- 239000001390 capsicum minimum Substances 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 244000052769 pathogen Species 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000255925 Diptera Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 244000302909 Piper aduncum Species 0.000 description 1
- 235000016761 Piper aduncum Nutrition 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000010980 cellulose Nutrition 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000011081 inoculation Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 244000000010 microbial pathogen Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Abstract
The present invention provides a kind of sedimentation separation pulping equipment and sedimentation separation pulping systems, belong to kitchen garbage and technical field of domestic garbage treatment.Sedimentation separation pulping equipment includes fluidization separator, sedimentation buffer unit and the 3rd connecting tube, fluidization separator includes the first cylinder and classification is managed, settling buffer unit includes the second cylinder, second cylinder is vertically arranged, 3rd connecting tube is provided with cutting machine and pump, for cutting machine for being cut to the material in the 3rd connecting tube, the 3rd connecting tube has input terminal and output terminal, pumps for by the fluid input/output terminal in input terminal.The sedimentation separation pulping equipment specific aim is stronger, and applicability is preferable, and work efficiency is high, low energy consumption, greatly reduces its processing cost, drastically increases technology stability.Sedimentation separation pulping system includes sedimentation separation pulping equipment, has the repertoire of the sedimentation separation pulping equipment.
Description
Technical field
The present invention relates to kitchen garbage and technical field of domestic garbage treatment, in particular to a kind of sedimentation separation system
Starch equipment and sedimentation separation pulping system.
Background technology
Kitchen garbage is the sanitary waste that resident is formed during personal consumption, is easily rotted, and distributes stench, is passed
Broadcast bacterium and virus.Kitchen garbage main component includes rice and flour group food remnants, vegetables, vegetable and animals oils, meat bone etc., from change
It learns on composition, there is starch, cellulose, protein, lipid and inorganic salts.
Kitchen garbage has the dual character of significant harm and resource, and feature can be summarized as：
(1) moisture content height, reachable 80% -95%.
(2) salt content is high, some areas are high containing capsicum, acetic acid.
(3) high organic content, protein, cellulose, starch, fat etc..
(4) nitrogen, phosphorus, potassium, calcium and various trace elements are rich in.
(5) there are pathogen, pathogenic microorganisms.
(6) perishable, rotten, smelly, growth mosquito.
Kitchen garbage contains more rich nutriment, it is possible to provide starch, cellulose, carbohydrate that microorganism growth needs etc.
Substance ferments to it with microorganism, those harmful pathogens on the one hand can be killed by the high-temperature sterilization before inoculation, separately
On the one hand constituent is gone by being inoculated with beneficial microorganism improvement, in addition generates substantial amounts of unicellular thallus albumen and accumulated
It is tired, in addition also avoid kitchen garbage to environment and human body institute may caused by threat, so as to fulfill diet and kitchen wastes it is innoxious,
Recycling.
There are substantial amounts of weight foreign substances, such as glass fragment, potsherd, bone, shell, sandstone, capsicum in kitchen garbage
Seed, wild pepper seed etc., this kind of nondegradable foreign matter are not readily separated in the processing procedure of kitchen garbage because grain size is smaller, but
That this kind of heavy foreign substances generate equipment in the processing procedure of kitchen slurry serious abrasion or damage, easily block pipeline and
Valve reduces the service life of equipment, while it easily deposits in subsequent processing structures and facility function is caused to lose very
To halt production.
Inventor has found in practical application and research, is at least had the following disadvantages in traditional correlation technique：
Specific aim is not strong, and applicability is poor, and treatment effect is bad；
Equipment loss is serious, and operation stability is poor；
Scarfing cinder is frequent, and labor intensity of operating staff is big.
The content of the invention
Object of the present invention is to provide a kind of sedimentation separation pulping equipments, improve the deficiencies in the prior art, are directed to
Property it is stronger, applicability is preferable, and work efficiency is high, low energy consumption, greatly reduces its processing cost, and it is steady to drastically increase technique
It is qualitative.
Another object of the present invention is to provide a kind of sedimentation separation pulping system, including sedimentation mentioned above point
From pulping equipment, the repertoire with the sedimentation separation pulping equipment.
What the embodiment of the present invention was realized in：
The embodiment provides a kind of sedimentation separation pulping equipment, including：
Fluidization separator, the fluidization separator includes the first cylinder and classification is managed, the first cylinder tool
There is accommodating chamber, the classification pipe is positioned partially or entirely in the accommodating chamber, and first cylinder is connected with the classification pipe
And it is vertically arranged, first cylinder is provided with feed inlet, and the classification pipe is provided with the water conservancy diversion connected with the accommodating chamber
Mouthful, the bottom of the classification pipe is provided with the first sand removing hole；
Buffer unit is settled, the sedimentation buffer unit includes the second cylinder, and second cylinder is vertically arranged, and described the
The first connecting tube connected with the top of the classification pipe is provided at the top of two cylinders, the bottom of second cylinder is provided with
With the second connecting tube for connecting of bottom of the classification pipe, discharge port is provided at the top of second cylinder, described second
The bottom of body is provided with sewage draining exit；
3rd connecting tube, the 3rd connecting tube are provided with cutting machine and pump, and the cutting machine is used to connect to the described 3rd
Material in taking over is cut, and the 3rd connecting tube has input terminal and an output terminal, and the pump is for by the input terminal
Interior fluid inputs the output terminal, and the input terminal includes first input end and the second input terminal, and the first input end connects
The top of the classification pipe is connected to, second input terminal is connected to the bottom of second cylinder, and the output terminal is connected to
The bottom of second cylinder.
Specifically, the sedimentation separation pulping equipment specific aim is stronger, applicability is preferable, and work efficiency is high, low energy consumption, greatly
Its processing cost is reduced greatly, drastically increases technology stability.
Optionally, the sedimentation separation pulping equipment further includes swirl-flow devices, and the swirl-flow devices include the 3rd cylinder, institute
State that the 3rd cylinder is vertically arranged, the side of the 3rd cylinder is provided with material inlet, and the material inlet connects with the described 3rd
Connection is taken over, drainage conduit is provided at the top of the 3rd cylinder, one end of the drainage conduit is stretched into the 3rd cylinder, institute
State the material outlet that is connected with the 3rd connecting tube of other end formation of drainage conduit, the bottom of the 3rd cylinder is provided with the
Two sand removing holes.
Optionally, the drainage conduit stretches into the height of the height less than the material inlet of described 3rd in vivo one end
Degree.
Optionally, the swirl-flow devices further include the first sand collecting tank and two the first motor-operated control valves, two described first
Motor-operated control valve is connected and is connected between the bottom of first sand collecting tank and the 3rd cylinder.
Optionally, the bottom of the 3rd cylinder is provided with the first backwash mouth.
Optionally, the sedimentation separation pulping equipment further includes multiple guiding devices, and multiple guiding devices are distributed in
The surrounding of the classification pipe, one end of the guiding device are connected to the classification pipe, and the guiding device is used for the appearance
The material of intracavitary received imports the flow-guiding mouth.
Optionally, the fluidization separator further includes the second sand collecting tank and two the second motor-operated control valves, two institutes
It states the series connection of the second motor-operated control valve and is connected between the bottom of second sand collecting tank and first cylinder.
Optionally, the bottom of the classification pipe is provided with the second backwash mouth.
Optionally, the sedimentation buffer unit further includes control valve, and the control valve is located at the bottom of second cylinder
And the sewage draining exit blowdown is controlled, manhole, foul smell collection port and liquid level gauge installing port are provided at the top of second cylinder,
The bottom of second cylinder is provided with thermometer installing pipe.
The embodiment of the present invention additionally provides a kind of sedimentation separation pulping system, including sedimentation separation system mentioned above
Equipment is starched, the repertoire with the sedimentation separation pulping equipment.
Compared with prior art, the advantageous effect of the embodiment of the present invention includes：
The sedimentation separation pulping equipment specific aim is stronger, and applicability is preferable, and work efficiency is high, low energy consumption, substantially reduces
Its processing cost, drastically increases technology stability.
Description of the drawings
It in order to illustrate the technical solution of the embodiments of the present invention more clearly, below will be to needed in the embodiment attached
Figure is briefly described, it should be understood that the following drawings illustrates only certain embodiments of the present invention, therefore is not construed as pair
The restriction of scope, for those of ordinary skill in the art, without creative efforts, can also be according to this
A little attached drawings obtain other relevant attached drawings.
Fig. 1 is the structure diagram for the sedimentation separation pulping equipment that the embodiment of the present invention 1 provides；
Fig. 2 is the structure diagram of fluidization separator shown in FIG. 1；
Fig. 3 is the structure diagram of sedimentation buffer unit shown in FIG. 1；
Fig. 4 is the structure diagram of swirl-flow devices shown in FIG. 1.
Icon：100- sedimentation separation pulping equipments；10- fluidization separators；101- first ports；102- second ends
Mouthful；103- third ports；The first cylinders of 11-；111- accommodating chambers；112- feed inlets；12- classification pipes；The first sand removing holes of 121-；
122- second backwashes mouth；The second motor-operated control valves of 13-；The second sand collecting tanks of 14-；20- settles buffer unit；The 4th ends of 201-
Mouthful；202- fifth ports；The 6th ports of 203-；The second cylinders of 21-；211- discharge ports；212- sewage draining exits；213- manholes；
214- foul smell collection ports；215- liquid level gauge installing ports；216- thermometer installing pipes；22- control valves；30- swirl-flow devices；31-
Three cylinders；311- material inlets；312- drainage conduits；313- material outlets；The second sand removing holes of 314-；315- first backwashes mouth；
The first motor-operated control valves of 32-；The first sand collecting tanks of 33-；40- guiding devices；The first connecting tubes of 50-；The second connecting tubes of 60-；70-
Three connecting tubes；71- cutting machines；72- is pumped；731- first input ends；The second input terminals of 732-；74- output terminals.
Specific embodiment
To make the purpose, technical scheme and advantage of the embodiment of the present invention clearer, below in conjunction with the embodiment of the present invention
In attached drawing, the technical solution in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is
Part of the embodiment of the present invention, instead of all the embodiments.The present invention implementation being usually described and illustrated herein in the accompanying drawings
The component of example can configure to arrange and design with a variety of.
Therefore, below the detailed description of the embodiment of the present invention to providing in the accompanying drawings be not intended to limit it is claimed
The scope of the present invention, but be merely representative of the present invention selected embodiment.Based on the embodiments of the present invention, this field is common
Technical staff's all other embodiments obtained without creative efforts belong to the model that the present invention protects
It encloses.
It should be noted that：Similar label and letter represents similar terms in following attached drawing, therefore, once a certain Xiang Yi
It is defined, then it further need not be defined and explained in subsequent attached drawing in a attached drawing.
In the description of the present invention, it is necessary to explanation, term " " center ", " on ", " under ", " vertical ", " interior ", " outer " etc.
The orientation or position relationship of instruction are usual when being used based on orientation shown in the drawings or position relationship or the invention product
The orientation or position relationship put, are for only for ease of the description present invention and simplify description rather than instruction or imply meaning
Device or element must have specific orientation, with specific azimuth configuration and operation, therefore it is not intended that the present invention's
Limitation.
In addition, term " first ", " second ", " the 3rd " etc. are only used for distinguishing description, and it is not intended that instruction or hint
Relative importance.
In the description of the present invention, it is also necessary to explanation, unless otherwise clearly defined and limited, term " setting ",
" installation ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected or integrally connect
It connects；Can be mechanical connection or electrical connection；It can be directly connected, can also be indirectly connected by intermediary, it can
To be the connection inside two elements.For the ordinary skill in the art, can above-mentioned term be understood with concrete condition
Concrete meaning in the present invention.
Embodiment 1
- Fig. 4 is please referred to Fig.1, present embodiments provides a kind of sedimentation separation pulping equipment 100, including：
Fluidization separator 10, fluidization separator 10 include the first cylinder 11 and classification pipe 12, the first cylinder 11
With accommodating chamber 111, classification pipe 12 is positioned partially or entirely in accommodating chamber 111, the first cylinder 11 be connected with being classified pipe 12 and
Vertically arranged, the first cylinder 11 is provided with feed inlet 112, and classification pipe 12 is provided with the flow-guiding mouth connected with accommodating chamber 111, point
The bottom of grade pipe 12 is provided with the first sand removing hole 121；
Buffer unit 20 is settled, sedimentation buffer unit 20 includes the second cylinder 21, and the second cylinder 21 is vertically arranged, second
The top of body 21 is provided with the first connecting tube 50 connected with being classified the top of pipe 12, and the bottom of the second cylinder 21 is provided with dividing
Second connecting tube 60 of the bottom connection of grade pipe 12, the top of the second cylinder 21 is provided with discharge port 211, the bottom of the second cylinder 21
Portion is provided with sewage draining exit 212；
3rd connecting tube 70, the 3rd connecting tube 70 are provided with cutting machine 71 and pump 72, and cutting machine 71 is used to connect to the 3rd
Material in pipe 70 is cut, and the 3rd connecting tube 70 has input terminal and output terminal 74, and pump 72 is used for the stream in input terminal
Body input/output terminal 74, input terminal include 731 and second input terminal 732 of first input end, and first input end 731 is connected to classification
The top of pipe 12, the second input terminal 732 are connected to the bottom of the second cylinder 21, and output terminal 74 is connected to the bottom of the second cylinder 21
Portion.
It needs exist for illustrating, the material in the present embodiment refers to kitchen garbage, generally comprises slurry, sand, bone
Deng.In other embodiment or the fluid slurry of any required sedimentation separation.
Material enters from feed inlet 112 in the first cylinder 11, is entered by flow-guiding mouth in classification pipe 12, is classified in pipe 12
Partial material is entered by first input end 731 in the 3rd connecting tube 70, and partial material enters second by the first connecting tube 50
In cylinder 21, the heavier foreign substances precipitation in part is discharged into the bottom of classification pipe 12 by the first sand removing hole 121.
Meanwhile the second partial material in cylinder 21 by the second input terminal 732 into the 3rd connecting tube 70, part object
Material is back to by the second connecting tube 60 in classification pipe 12, carries out local circulation, forms upper up-flow effect.
Meanwhile first pass through cutting machine 71 into the material of the 3rd connecting tube 70 and cut, then the supercharging by pump 72, it will
It is sent into output terminal 74, and output terminal 74 is located relatively at the bottom of the second cylinder 21, is repeatedly cycled.
The slurry for being finally reached requirement is discharged by discharge port 211.
Generally, slurry mainly enters from first input end 731 in the 3rd connecting tube 70, part size passes through the first connection
Pipe 50 enters in the second cylinder 21, primarily serves overflow protective effect.
Material uses tangential admission mode from feed inlet 112 into the first cylinder 11, that is to say, that the first cylinder 11 is in circle
Cylinder, the input direction of material is along its tangential direction, the material being more advantageous in the first cylinder 11 of agitation.
Similarly, the first connecting tube 50 inputs the material in the second cylinder 21, and tangential admission mode equally may be employed, have
Beneficial to the material in the second cylinder 21 of agitation.
Similarly, output terminal 74 inputs the material in the second cylinder 21, also using tangential admission mode, is conducive to stir bottom
Deposit.
In the present embodiment, pump 72 can select impeller pump, Pulp pump etc..
In this way, be conducive to material and sedimentation buffering is realized in the second cylinder 21, into after classification pipe 12, stir
Material in dynamic classification pipe 12, and upper up-flow effect is formed, fluidization separation is advantageously implemented, lighter material floats, passes through
First connecting tube 50 realizes overflow protective effect, and heavier material sinking is deposited in the bottom for being classified pipe 12, eventually by first
Sand removing hole 121 is discharged.
Slurry mainly forms upper up-flow, lighter object by the liquid of 60 circulating reflux of the second connecting tube in classification pipe 12
Material is in fluidized state, with fluid circulation；Heavier material cannot rise with fluid, drop to spigot.
With reference to Fig. 2 and Fig. 3, classification pipe 12 is provided with first port 101, second port 102 and third port 103, and second
Cylinder 21 is provided with the 4th port 201,202 and the 6th port 203 of fifth port.
First port 101 coordinates with first input end 731, realizes that classification pipe 12 is connected with the 3rd connecting tube 70.
Second port 102 coordinates with the 4th port 201, forms the first connecting tube 50, realizes the top and the of classification pipe 12
The top connection of two cylinders 21, so that the material of classification 12 overflow of pipe enters in the second cylinder 21.
103 and the 6th port 203 of third port coordinates, and forms the second connecting tube 60, realizes the bottom and the of classification pipe 12
The bottom connection of two cylinders 21, so that the feed back in the second cylinder 21 is extremely classified the bottom of pipe 12.
Fifth port 202 coordinates with the second input terminal 732, realizes that the second cylinder 21 is connected with the 3rd connecting tube 70.
In the present embodiment, the top of classification pipe 12 is located in accommodating chamber 111, and its underpart is located at outside the first cylinder 11, whole
Body is located at the center of the first cylinder 11.Sewage draining exit 212 is located at the bottom centre position of the second cylinder 21.
It of courses, in other embodiment, classification pipe 12 can be entirely located in the first cylinder 11, and bottom carries out sediment outflow.
100 specific aim of sedimentation separation pulping equipment is stronger, and applicability is preferable, and work efficiency is high, low energy consumption, drops significantly
Its low processing cost, drastically increases technology stability.It has the characteristics that sedimentation separation function and slurrying are integrated.
With reference to Fig. 4, in the present embodiment, sedimentation separation pulping equipment 100 further includes swirl-flow devices 30, and swirl-flow devices 30 include
3rd cylinder 31, the 3rd cylinder 31 is vertically arranged, and the side of the 3rd cylinder 31 is provided with material inlet 311, material inlet 311 with
3rd connecting tube 70 connects, and the top of the 3rd cylinder 31 is provided with drainage conduit 312, and the 3rd cylinder is stretched into one end of drainage conduit 312
In 31, the other end of drainage conduit 312 forms the discharge material outlet 313 connected with the 3rd connecting tube 70, the bottom of the 3rd cylinder 31
Portion is provided with the second sand removing hole 314.
The top of 3rd cylinder 31 be in cylinder, bottom be in taper cone barrel, 70 outputting material of the 3rd connecting tube, by material into
Mouthfuls 311 into the 3rd cylinders 31, and tangential admission generates cyclonic action, make material in centrifugal force by internal structure and again
Separation is realized under the action of power.The cone base angle degree of taper cone barrel is generally located between 10 ° -20 °.
The lighter material in part is discharged by drainage conduit 312 from the discharge material outlet 313 at top simultaneously, enters the 3rd
In connecting tube 70, enter output terminal 74 with the material in the 3rd connecting tube 70.The heavier material in part under gravity precipitation,
Into bottom, discharged by the second sand removing hole 314.
Generally, these lighter materials are organic matter, heavier material is the foreign substances in kitchen raw material.
The drainage conduit 312 can be external tube body or the 3rd cylinder 31 carries, as long as being capable of outputting material
.
In the present embodiment, the 3rd cylinder 31 can be understood as being connected in parallel in the 3rd connecting tube 70, that is to say, that material
In the 3rd cylinder 31 of entrance that can be selective or do not enter and directly exported by output terminal 74.
The tangential material into the 3rd cylinder 31 carries out centrifugal cyclone separation, and charging rate is more than the first cylinder 11
Charging rate is conducive to increase cycle-index of the material in local circulation, increases desanding effect.
Optionally, drainage conduit 312 stretches into the height of the height less than material inlet 311 of one end in the 3rd cylinder 31.
Such setting can effectively prevent material from the phenomenon that short stream occur, improve it in 31 inward turning flow point of the 3rd cylinder
From efficiency.
Optionally, swirl-flow devices 30 further include the first sand collecting tank 33 and two the first motor-operated control valves 32, two first electricity
Dynamic control valve 32 is connected and is connected between the first sand collecting tank 33 and the bottom of the 3rd cylinder 31.
In the present embodiment, two the first motor-operated control valves 32 are connected, and the material of discharge effectively can be controlled, one
As, the first motor-operated control valve 32 of top is first opened, enters heavier material, is then shut off the first Electronic control of top
Valve 32 and the first motor-operated control valve 32 for opening lower section make this partial material enter in the first sand collecting tank 33 and are kept in.
By the setting of series connection, complete equipment can be preferably protected, while the normal fluidised form of fluid can not be destroyed.
Optionally, the bottom of the 3rd cylinder 31 is provided with the first backwash mouth 315.
It backwashes mouth and accesses external pipeline, the bottom of the 3rd cylinder 31 is rinsed, avoids blocking.
With reference to Fig. 1 and Fig. 2, sedimentation separation pulping equipment 100 further includes multiple guiding devices 40, and multiple guiding devices 40 are equal
The surrounding of classification pipe 12 is distributed in, one end of guiding device 40 is connected to classification pipe 12, and guiding device 40 is used for will be in accommodating chamber 111
Material import flow-guiding mouth.
The material that feed inlet 112 inputs flows downward under the action of tangential swirl and gravity, along guiding device 40
Into in classification pipe 12, under the booster action of guiding device 40, material enters classification pipe 12, runs into from the second cylinder 21
Feed back upper up-flow, occurs fluidization centrifugation, and the slurry of light specific gravity obtains upward acceleration in ascending current, is being classified
It is flowed up in pipe 12, as recycle feed by being delivered to after 72 sucking of pump in the 3rd cylinder 31, the foreign substances of weight are being classified
Pipe 12 continues to be deposited to the first sand removing hole 121.
Guiding device 40 can be understood as flow deflector in the present embodiment, and its one end is connected on classification pipe 12, other end position
In in accommodating chamber 111, flow-guiding mouth can be understood as opening up through hole on classification pipe 12, be conducive to carry out water conservancy diversion.
Optionally, fluidization separator 10 further includes the second sand collecting tank 14 and two the second motor-operated control valves 13, two
Second motor-operated control valve 13 is connected and is connected between the bottom of the second sand collecting tank 14 and the first cylinder 11.
Effect, effect, principle of second motor-operated control valve 13 etc. may be referred to the first motor-operated control valve 32.
Optionally, the bottom for being classified pipe 12 is provided with the second backwash mouth 122.
Effect, effect, principle of second backwash mouth 122 etc. may be referred to the first backwash mouth 315.
Optionally, sedimentation buffer unit 20 further includes control valve 22, and control valve 22 is located at the bottom of the second cylinder 21 and control
212 blowdown of sewage draining exit processed, the top of the second cylinder 21 are provided with manhole 213, foul smell collection port 214 and liquid level gauge installing port
215, the bottom of the second cylinder 21 is provided with thermometer installing pipe 216.
Manhole 213 overhauls the second cylinder 21 convenient for user, and foul smell collection port 214 can be with external pipeline
The foul smell generated in second cylinder 21 is collected by connection, and liquid level gauge is installed by the liquid level gauge installing port 215, is had
Beneficial to the liquid level in the second cylinder 21 of monitoring, thermometer is installed by the thermometer installing pipe 216, is conducive to monitor
The temperature of material, is conducive to the monitoring of subsequent treatment process condition in second cylinder 21.
A kind of sedimentation separation pulping equipment 100 provided according to embodiments of the present invention, the original of sedimentation separation pulping equipment 100
Reason is：
Material enters from feed inlet 112 in the first cylinder 11, into classification pipe under the guiding role of guiding device 40
In 12, under the action of Flow of Goods and Materials, material stirs and generates effect of settling, and heavier foreign substances enter the bottom of classification pipe 12
Portion, a lighter part, which floats and passes through first input end 731, to be entered in the 3rd connecting tube 70, and another part passes through the first connection
In 50 overflow of pipe to the second cylinder 21.
Heavier material generates effect of settling in second cylinder 21, and part of it is flowed back by the second connecting tube 60 of bottom
To classification pipe 12, so as to continue the material in agitation classification pipe 12 and form upper up-flow effect, another part passes through second
Input terminal 732 enters in the 3rd connecting tube 70, and the lighter material in part is discharged by discharge port 211, into next process.
The material of 731 and second input terminal 732 of first input end input is cut by cutting machine 71, realizes broken system
Slurry acts on, then the effect by pump 72, it is made to transfer to output terminal 74, during output, partial material passes through material inlet
311 enter in the 3rd cylinder 31, under the action of centrifugal cyclone, realize sedimentation, heavier foreign substances enter the 3rd cylinder 31
Bottom, lighter material is entered by discharge material outlet 313 in the 3rd connecting tube 70, defeated with the material in the 3rd connecting tube 70
To output terminal 74, the material of output stirs the liquid in the second cylinder 21, so as to fulfill cycling.
This equipment specificity is strong, and equipment is not allowed to be also easy to produce clogging, and weight foreign substances separative efficiency is higher, input cost
Relatively low, whole energy consumption is relatively low.Equipment design is reasonable, and overall effect is preferable.
Embodiment 2
The present embodiment also provides a kind of sedimentation separation pulping system, including sedimentation separation pulping equipment mentioned above
100, there is the repertoire of the sedimentation separation pulping equipment 100.
The structure of sedimentation separation pulping equipment 100 may be referred to embodiment 1.
Sedimentation separation pulping system further includes control device, the first motor-operated control valve 32 of control, the second motor-operated control valve
13rd, cutting machine 71 and pump 72, realize and rationalize operation.
The control device can be PLC, or computer board.
In conclusion the present invention provides a kind of sedimentation separation pulping equipment 100,100 pins of sedimentation separation pulping equipment
Stronger to property, applicability is preferable, and work efficiency is high, low energy consumption, greatly reduces its processing cost, drastically increases technique
Stability.
The foregoing is only a preferred embodiment of the present invention, is not intended to limit the invention, for the skill of this field
For art personnel, the invention may be variously modified and varied.Within the spirit and principles of the invention, that is made any repaiies
Change, equivalent substitution, improvement etc., should all be included in the protection scope of the present invention.
Claims (10)
1. a kind of sedimentation separation pulping equipment, which is characterized in that including：
Fluidization separator, the fluidization separator includes the first cylinder and classification is managed, and first cylinder, which has, to be held
Receive chamber, the classification pipe is positioned partially or entirely in the accommodating chamber, and first cylinder is connected and equal with the classification pipe
Vertically arranged, first cylinder is provided with feed inlet, and the classification pipe is provided with the flow-guiding mouth connected with the accommodating chamber, institute
The bottom for stating classification pipe is provided with the first sand removing hole；
Buffer unit is settled, the sedimentation buffer unit includes the second cylinder, and second cylinder is vertically arranged, described second
The first connecting tube connected with the top of the classification pipe is provided at the top of body, the bottom of second cylinder is provided with and institute
The second connecting tube of the bottom connection of classification pipe is stated, discharge port is provided at the top of second cylinder, second cylinder
Bottom is provided with sewage draining exit；
3rd connecting tube, the 3rd connecting tube are provided with cutting machine and pump, and the cutting machine is used for the 3rd connecting tube
Interior material is cut, and the 3rd connecting tube has input terminal and output terminal, and the pump is for will be in the input terminal
Fluid inputs the output terminal, and the input terminal includes first input end and the second input terminal, and the first input end is connected to
The top of the classification pipe, second input terminal are connected to the bottom of second cylinder, and the output terminal is connected to described
The bottom of second cylinder.
2. sedimentation separation pulping equipment according to claim 1, which is characterized in that the sedimentation separation pulping equipment also wraps
Swirl-flow devices are included, the swirl-flow devices include the 3rd cylinder, and the 3rd cylinder is vertically arranged, and the side of the 3rd cylinder is set
Material inlet is equipped with, the material inlet is connected with the 3rd connecting tube, and drainage conduit is provided at the top of the 3rd cylinder,
One end of the drainage conduit is stretched into the 3rd cylinder, and the other end formation of the drainage conduit is connected with the 3rd connecting tube
Material outlet, the bottom of the 3rd cylinder is provided with the second sand removing hole.
3. sedimentation separation pulping equipment according to claim 2, which is characterized in that the drainage conduit stretches into described 3rd
The height of in vivo one end is less than the height of the material inlet.
4. sedimentation separation pulping equipment according to claim 2, which is characterized in that the swirl-flow devices further include the first collection
Silo and two the first motor-operated control valves, two first motor-operated control valves series connection and are connected to first sand collecting tank and institute
Between the bottom for stating the 3rd cylinder.
5. sedimentation separation pulping equipment according to claim 2, which is characterized in that the bottom of the 3rd cylinder is provided with
First backwash mouth.
6. according to claim 1-5 any one of them sedimentation separation pulping equipments, which is characterized in that the sedimentation separation slurrying
Equipment further includes multiple guiding devices, and multiple guiding devices are distributed in the surrounding of the classification pipe, the guiding device
One end is connected to the classification pipe, and the guiding device is used to the material in the accommodating chamber importing the flow-guiding mouth.
7. according to claim 1-5 any one of them sedimentation separation pulping equipments, which is characterized in that the fluidization separation dress
It puts and further includes the second sand collecting tank and two the second motor-operated control valves, two second motor-operated control valves are connected and are connected to described
Between the bottom of second sand collecting tank and first cylinder.
8. according to claim 1-5 any one of them sedimentation separation pulping equipments, which is characterized in that the bottom of the classification pipe
It is provided with the second backwash mouth.
9. according to claim 1-5 any one of them sedimentation separation pulping equipments, which is characterized in that the sedimentation buffer unit
Control valve is further included, the control valve is located at the bottom of second cylinder and controls the sewage draining exit blowdown, described second
Manhole, foul smell collection port and liquid level gauge installing port are provided at the top of body, the bottom of second cylinder is provided with thermometer
Installing pipe.
10. a kind of sedimentation separation pulping system, which is characterized in that including claim 1-9 any one of them sedimentation separation systems
Starch equipment.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810039042.4A CN108046398B (en) | 2018-01-16 | 2018-01-16 | Sedimentation separation pulping equipment and sedimentation separation pulping system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201810039042.4A CN108046398B (en) | 2018-01-16 | 2018-01-16 | Sedimentation separation pulping equipment and sedimentation separation pulping system |
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| CN108046398B CN108046398B (en) | 2024-02-27 |
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| WO2002028786A2 (en) * | 2000-10-04 | 2002-04-11 | Great Circle Technologies, Inc. | Process and apparatus for treating wastewater |
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| CN102225354A (en) * | 2011-03-15 | 2011-10-26 | 太原理工大学 | Re-flotation hybrid selecting process and selecting device thereof |
| CN206027853U (en) * | 2016-08-26 | 2017-03-22 | 耐德三井造船（重庆）环境装备有限公司 | Broken humidifying pulping system of kitchen garbage |
| CN207891105U (en) * | 2018-01-16 | 2018-09-21 | 青海洁神环境能源产业有限公司 | Sedimentation separation pulping equipment and sedimentation separation pulping system |
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2018
- 2018-01-16 CN CN201810039042.4A patent/CN108046398B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002028786A2 (en) * | 2000-10-04 | 2002-04-11 | Great Circle Technologies, Inc. | Process and apparatus for treating wastewater |
| CN1360978A (en) * | 2000-12-27 | 2002-07-31 | 松下电器产业株式会社 | Renewable resources treatment apparatus for waste electric appliances |
| CN102225354A (en) * | 2011-03-15 | 2011-10-26 | 太原理工大学 | Re-flotation hybrid selecting process and selecting device thereof |
| CN206027853U (en) * | 2016-08-26 | 2017-03-22 | 耐德三井造船（重庆）环境装备有限公司 | Broken humidifying pulping system of kitchen garbage |
| CN207891105U (en) * | 2018-01-16 | 2018-09-21 | 青海洁神环境能源产业有限公司 | Sedimentation separation pulping equipment and sedimentation separation pulping system |
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| CN108046398B (en) | 2024-02-27 |
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