CN207401404U - A kind of flocculant prepares and adding set - Google Patents
A kind of flocculant prepares and adding set Download PDFInfo
- Publication number
- CN207401404U CN207401404U CN201721345925.5U CN201721345925U CN207401404U CN 207401404 U CN207401404 U CN 207401404U CN 201721345925 U CN201721345925 U CN 201721345925U CN 207401404 U CN207401404 U CN 207401404U
- Authority
- CN
- China
- Prior art keywords
- medicament
- flocculant
- pipe
- powder
- preparation
- 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.)
- Active
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model is related to a kind of preparation of flocculant and adding sets, it is characterised in that:It is made of a preparation system and secondary preparation and add-on system, preparation system includes base rack, flocculant powder feedstock vessel, powder slot tank diameter, a medicament stock chest and flocculant powder conveying apparatus, the flocculant powder conveying apparatus is connected with the discharge port of flocculant powder feedstock vessel and hot air blower respectively by one end by three-way pipe, and the other end extend into the powder carry bend pipe of powder slot tank diameter;The secondary preparation is prepared pipe, a medicament feed inlet, secondary agent outlet and is prepared pipe filler pipe B connected vertically with secondary medicament and formed with add-on system by secondary medicament.The utility model has the advantages that:Flocculant can be continuously added, the flocculant concentration of preparation is low, and flocculating effect is good, high degree of automation.
Description
Technical field
The utility model belongs to tailings dewatering technical field, more particularly, to a kind of preparation of flocculant and adding set.
Background technology
The most common equipment of Tailing thickening in ore dressing plant is Tailing thickening machine, and its general granularity of tailing is fine, proportion compared with
Small, the rate of settling is much smaller compared with concentrate, and in order to accelerate the rate of settling of tailing, to reach the solids for reducing overflow water
Content reduces Tailing thickening machine diameter, and so as to reduce the purpose of equipment and capital expenditure, common method is exactly in Tailing thickening
Flocculant is added in pond.The addition of current tailing flocculant is mostly manually to be prepared by a certain concentration intermittent stirring, is not only worked
Intensity is big, and to prepare vessel volume limited due to single processed interval, it is impossible to add substantial amounts of water, the flocculant often made is dense
It spends greatly, flocculating effect is bad.So we can continuously add flocculant it is necessary to develop one kind, the flocculant of preparation is dense
Spend low, flocculating effect is good, and the flocculant of high degree of automation prepares and adding set.
The content of the invention
The purpose of this utility model, which is to provide one kind, can continuously add flocculant, and the flocculant concentration of preparation is low, wadding
Solidifying effect is good, and the flocculant of high degree of automation prepares and adding set.
Prepared by a kind of flocculant of the utility model is realized with adding set by following technical proposals:
A kind of flocculant of the utility model prepares and adding set, it is characterised in that:By a preparation system and secondary
It prepares and add-on system is formed,
Preparation system includes base rack, is arranged on the flocculant powder feed of base rack top one side
Tank, the powder slot tank diameter for being arranged on base rack top opposite side, a medicament stock chest being arranged in base rack with
And flocculant powder conveying apparatus, it is equipped with meter, the flocculation in the discharge outlet of the flocculant powder feedstock vessel
Agent powder conveying apparatus is connected with the discharge port of flocculant powder feedstock vessel and hot air blower respectively by one end by three-way pipe,
The powder carry bend pipe that the other end extend into powder slot tank diameter is formed;
Feed pipe A is equipped in the top one side of the powder slot tank diameter, regulating valve A and stream are equipped on feed pipe A
To adjust the concentration for once preparing liquid medicine, drainage conduit and regulating valve B are equipped in the bottom of powder slot tank diameter by gauge A,
The drainage conduit is connected with the material inlet of a medicament storage tank, and switch valve is equipped in drainage conduit;
Eccentrie helical totorpump is equipped on a medicament stock chest, the pan feeding pipe end of the eccentrie helical totorpump is located at
Lower section in medicament storage tank, the outlet of the end of the discharge nozzle of the eccentrie helical totorpump as a medicament, with secondary system
The standby medicament feed inlet that pipe is prepared with the secondary medicament of add-on system is connected, and is equipped on the outlet of eccentrie helical totorpump
Flowmeter C;
Secondary prepare described in the utility model prepares pipe by secondary medicament with add-on system, is arranged on secondary medicament preparation pipe
Medicament feed inlet of one end, be arranged on secondary medicament prepare the pipe other end secondary medicament discharge port and with secondary medicament system
Standby pipe filler pipe B connected vertically is formed, and flowmeter B and regulating valve B is equipped on the filler pipe B, for adjusting two
The concentration of secondary liquid medicine, the secondary medicament discharge port are arranged on the top of the central tube of Tailing thickening machine, and secondary medicine
The central tube tailing material inlet of agent discharge port face Tailing thickening machine.
The concentration of the liquid medicine once prepared is controlled 0.3%~0.5%.
The concentration of the secondary liquid medicine is 0.03%~0.05%.
The powder carry bend pipe is made of horizontal material feeding section, upward conveying section and bending discharge zone, the level
Material feeding section is reducer pipe from the coarse to fine, and reducer pipe top is connected with the discharge port of flocculant powder feedstock vessel.
The change of the meter I, flowmeter A and regulating valve A, flowmeter B and regulating valve B, flowmeter C and eccentrie helical totorpump
Frequency motor is electrically connected with control cabinet.
The advantages of the utility model:
(1) the flocculant preparation of the utility model and adding set, by the way of continuously preparing twice, final flocculant
0.03%~0.05%, this greatly improved tailing wadding well below the drug concentration manually prepared for the concentration control of solution
Solidifying effect is conducive to reduce the diameter in Tailing thickening pond, improves overflow water quality, reduces equipment and capital expenditure;
(2) the flocculant preparation of the utility model and adding set, by the way of continuously preparing twice, a solution system
Standby drug concentration control for 0.3~0.5%, is greatly reducing the volume of a liquid medicine, so as to reduce one
Secondary medicament prepares set instrument size, and the integrated arrangement prepared for a medicament creates condition;
(3) prepared by the flocculant of the utility model and adding set, all subsystems prepared by a medicament are integrated in same
One is collectively formed on a base rack and once prepares station equipment entirety, not only contributes to the management of equipment, and it is compact-sized,
Occupation of land has been saved, has reduced investment;
(4) the flocculant preparation of the utility model and adding set, the side that secondary preparation is prepared with add-on system by tubular type
Formula, a medicament and water well-mixed second aqueous in pipe, it is achieved thereby that the one of the preparation and conveying of second aqueous
Change, enormously simplify preparation link, reduce investment;
(5) the flocculant preparation of the utility model and adding set, by flocculant in pipeline before prepared by a medicament
During flocculant is preheated, do not only reached increase flocculant solubility purpose, and the conveying of powder with
Preheating one carries out in delivery pipe simultaneously, enormously simplifies preheating link, reduces investment;
(6) the flocculant preparation of the utility model and adding set, powder meter, flowmeter A and regulating valve A, flowmeter
B is connected with the control signal of the frequency conversion of regulating valve B, flowmeter C and eccentrie helical totorpump with control cabinet, high degree of automation, no
It only greatly reduces hand labor and drug concentration control is accurate.
Description of the drawings
Fig. 1 is the schematic diagram of a preparation system structure of the utility model.
Fig. 2 is the secondary preparation of the utility model and the structure diagram of add-on system.
Specific embodiment
Specific embodiment of the present utility model is further illustrated below in conjunction with the accompanying drawings.
As shown in Figure 1, a kind of flocculant of the utility model prepares and adding set, it is characterised in that:By once preparing
System and secondary preparation and add-on system are formed,
Preparation system includes base rack 1, be arranged on the flocculant powder of 1 top one side of base rack to
Batch can 2, the powder slot tank diameter 6 for being arranged on 1 top opposite side of base rack, a medicament being arranged in base rack 1 storage
Hopper 9 and flocculant powder conveying apparatus are equipped with meter 3, institute in the discharge outlet of the flocculant powder feedstock vessel 2
The flocculant powder conveying apparatus stated is roused with the discharge port of flocculant powder feedstock vessel 2 and hot wind respectively by one end by three-way pipe
Wind turbine 5 connects, and the powder carry bend pipe 4 that the other end extend into powder slot tank diameter 6 is formed;
The utility model is equipped with feed pipe A14 in the top one side of the powder slot tank diameter 6, on feed pipe A14
Equipped with regulating valve A15 and flowmeter A16, to adjust the concentration for once preparing liquid medicine, in the bottom of powder slot tank diameter 6
Equipped with drainage conduit 8 and regulating valve B10, the drainage conduit 8 is connected with the material inlet of a medicament storage tank 9, and 7 be stirring in figure
Device;
The utility model is equipped with eccentrie helical totorpump 11, the eccentrie helical totorpump on a medicament stock chest 9
11 entrance pipe end 12 is located at lower section, 17 conduct of end of the discharge nozzle of the eccentrie helical totorpump 11 in a medicament storage tank 9
The outlet of medicament, the medicament feed inlet 18 that pipe is prepared with secondary preparation with the secondary medicament of add-on system are connected,
Flowmeter C13 is equipped on the outlet of eccentrie helical totorpump 11;
As shown in Fig. 2, secondary preparation described in the utility model prepares pipe 22 by secondary medicament, is arranged on two with add-on system
Secondary medicament prepares a medicament feed inlet 18 of 22 one end of pipe, is arranged on the secondary medicament discharging that secondary medicament prepares the pipe other end
It mouthfuls 23 and prepares 22 filler pipe B21 connected vertically of pipe with secondary medicament and is formed, equipped with flow on the filler pipe B21
B19 and regulating valve B20 is counted, for adjusting the concentration of secondary liquid medicine, the secondary medicament discharge port 23 is arranged on tailing
The top of the central tube 24 of thickener, and the 24 tailing material inlet of central tube of secondary medicament discharge port face Tailing thickening machine, with
It is sufficiently mixed beneficial to secondary medicament and tailing ore pulp in central tube.
The concentration control of the liquid medicine described in the utility model once prepared is 0.3%~0.5%, the secondary medicament
The concentration of solution is 0.03%~0.05%.
Powder carry bend pipe 4 described in the utility model is by horizontal material feeding section 4-1, the conveying that is inclined upwardly section and bending discharge zone
It is formed, the horizontal material feeding section is reducer pipe from the coarse to fine, and reducer pipe top goes out with flocculant powder feedstock vessel 2
Material mouth connects.
Meter 3 described in the utility model, flowmeter A14 and regulating valve A15, flowmeter B19 and regulating valve B20, flow
The variable-frequency motor for counting C13 and eccentrie helical totorpump 11 is electrically connected with control cabinet.High degree of automation, control are accurate.
Claims (4)
1. a kind of flocculant prepares and adding set, it is characterised in that:By a preparation system and secondary preparation and add-on system
It is formed,
Preparation system includes base rack, is arranged on the flocculant powder feedstock vessel of base rack top one side,
It is arranged on powder slot tank diameter, a medicament stock chest being arranged in base rack and the wadding of base rack top opposite side
Solidifying agent powder conveying apparatus is equipped with meter, the flocculant powder in the discharge outlet of the flocculant powder feedstock vessel
Material conveying device is connected with the discharge port of flocculant powder feedstock vessel and hot air blower respectively by one end by three-way pipe, another
The powder carry bend pipe that end extend into powder slot tank diameter is formed;
Feed pipe A is equipped in the top one side of the powder slot tank diameter, regulating valve A and flowmeter are equipped on feed pipe A
To adjust the concentration for once preparing liquid medicine, drainage conduit and regulating valve B are equipped in the bottom of powder slot tank diameter by A, described
Drainage conduit be connected with the material inlet of a medicament storage tank;
Eccentrie helical totorpump is equipped on a medicament stock chest, the pan feeding pipe end of the eccentrie helical totorpump is located at once
Lower section in medicament storage tank, the outlet of the end of the discharge nozzle of the eccentrie helical totorpump as a medicament, with secondary preparation with
The medicament feed inlet that the secondary medicament of add-on system prepares pipe is connected, and flow is equipped on the outlet of eccentrie helical totorpump
Count C;
The secondary preparation is prepared with add-on system by secondary medicament manages, is arranged on the medicament that secondary medicament prepares pipe one end
Feed inlet, be arranged on secondary medicament prepare the pipe other end secondary medicament discharge port and with secondary medicament prepare pipe it is connected vertically
Filler pipe B is formed, and flowmeter B and regulating valve B is equipped on the filler pipe B, for adjusting the dense of secondary liquid medicine
Degree, the secondary medicament discharge port are arranged on the top of the central tube of Tailing thickening machine, and secondary medicament discharge port face tail
The central tube tailing material inlet of ore deposit thickener.
2. flocculant according to claim 1 prepares and adding set, it is characterised in that:The medicament once prepared
The concentration of solution is controlled 0.3%~0.5%.
3. flocculant according to claim 1 prepares and adding set, it is characterised in that:The secondary liquid medicine it is dense
It spends for 0.03%~0.05%.
4. flocculant according to claim 1 prepares and adding set, it is characterised in that:The powder carry bend pipe is by water
Flat material feeding section, upward conveying section and bending discharge zone are formed, and the horizontal material feeding section is reducer pipe from the coarse to fine, is become
Footpath pipe top is connected with the discharge port of flocculant powder feedstock vessel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721345925.5U CN207401404U (en) | 2017-10-19 | 2017-10-19 | A kind of flocculant prepares and adding set |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721345925.5U CN207401404U (en) | 2017-10-19 | 2017-10-19 | A kind of flocculant prepares and adding set |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207401404U true CN207401404U (en) | 2018-05-25 |
Family
ID=62320100
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721345925.5U Active CN207401404U (en) | 2017-10-19 | 2017-10-19 | A kind of flocculant prepares and adding set |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207401404U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115624907A (en) * | 2022-12-21 | 2023-01-20 | 常州市江湖化工有限公司 | Mixing equipment for production and processing of composite corrosion and scale inhibitor |
-
2017
- 2017-10-19 CN CN201721345925.5U patent/CN207401404U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115624907A (en) * | 2022-12-21 | 2023-01-20 | 常州市江湖化工有限公司 | Mixing equipment for production and processing of composite corrosion and scale inhibitor |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN208249963U (en) | A kind of thickener medicament intelligently prepares add-on system | |
CN207401404U (en) | A kind of flocculant prepares and adding set | |
CN203613011U (en) | Water treatment reactor | |
CN107519796A (en) | A kind of flocculant prepares and adding set | |
CN205917056U (en) | Coagulating sedimentation device | |
CN202638060U (en) | A thickener feed system | |
CN212655602U (en) | Coal dressing slime water mixing adds medicine and pressure filter linked system | |
CN106362480B (en) | A kind of concentrate pulp high efficiency filter method | |
CN105797870B (en) | A kind of flotation continuous automatic chemical-feeding device | |
CN202199314U (en) | Automatic chemical feeding device | |
CN112225339A (en) | Coal preparation and slime water mixing, dosing and filter press linkage system and method | |
CN211098838U (en) | Flocculant solution preparation and metering feeding system | |
CN206645995U (en) | The medicament adding device of high-efficiency concentrator | |
CN204888310U (en) | Device of online mixing distribution fodder | |
CN210855314U (en) | Sewage treatment adds medicament device | |
CN209259944U (en) | A kind of automatic size mixing device of continuous milk of lime | |
CN209476906U (en) | A kind of cyanidation tailings harmless treatment device | |
CN207446513U (en) | A kind of microfloatation collecting agent is prepared and adding set | |
CN208115673U (en) | A kind of novel bubble medicine machine | |
CN205182531U (en) | Water treatment ration medication dosing device | |
CN107986496B (en) | Fenton equipment for continuous sewage treatment and sewage treatment method thereof | |
CN206199123U (en) | A kind of stirring filling apparatus prepared for biological medicine medicine | |
CN215028309U (en) | Flocculating agent configuration system | |
CN220214021U (en) | Novel overflow clarification device for vertical sand bin | |
CN205095471U (en) | Flocculation and sedimentation tank |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |