CN106830716A - A kind of lime slaking chemicals dosing plant - Google Patents
A kind of lime slaking chemicals dosing plant Download PDFInfo
- Publication number
- CN106830716A CN106830716A CN201710111388.6A CN201710111388A CN106830716A CN 106830716 A CN106830716 A CN 106830716A CN 201710111388 A CN201710111388 A CN 201710111388A CN 106830716 A CN106830716 A CN 106830716A
- Authority
- CN
- China
- Prior art keywords
- lime
- milk
- unit
- slaking
- sand
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2/00—Lime, magnesia or dolomite
- C04B2/02—Lime
- C04B2/04—Slaking
- C04B2/08—Devices therefor
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Soil Conditioners And Soil-Stabilizing Materials (AREA)
Abstract
The invention discloses a kind of lime slaking chemicals dosing plant, it includes:It includes:Lime delivery unit, lime slaking unit, milk of lime separative element and lime dosing unit;Wherein lime delivery unit, the quick lime in refined lime tank is delivered to the charging aperture of lime slaking unit;Lime slaking unit, including cylinder, cylinder are provided with charging aperture and discharging opening, and inner barrel is divided into from charging aperture to discharging opening:Buffering area, homogeneous area, newborn slag Disengagement zone, Lao Zha areas dreg discharging area;Quick lime flows out by being digested to milk of lime sand aqueous mixtures, milk of lime sand aqueous mixtures after lime slaking unit from discharging opening;Milk of lime separative element, the milk of lime sand aqueous mixtures that will be flowed into from discharging opening are separated into milk of lime and lime mud;Milk of lime can be separated in milk of lime sand mixture 95% lime mud by being neutralized in pump to the neutralization chamber of lime dosing unit using the present apparatus, improve quick lime utilization rate more than 10%.
Description
Technical field
The present invention relates to water-treatment technology field, particularly a kind of lime slaking chemicals dosing plant.
Background technology
Existing lime slaking dosing typically uses following two modes:One is that refined lime is hung into milk of lime by warehouse to prepare
Groove, is made the lime milk solution that concentration is 20%, then with pump defeated milk of lime deliver to waste acid, one section, two sections, three sections of neutralization chambers enter
Row is neutralized.Two is that the refined lime of refined lime tank is delivered into Calcified pond by the spiral of refined lime tank, and refined lime connects in pond with water
Immersion is touched, natural cooling grabbed to intermediate bin with grab bucket, be washed with water and enter lime slaking machine afterwards for a period of time, finally by slagging tap
Spiral carries out the separation of lime mud and milk of lime, and milk of lime is sent to neutralization chamber and is neutralized, and lime mud falls in slag bucket, periodically uses
Automobile is transported;Or the refined lime of refined lime tank is formed into lime white, lime by the first elephant trunk into the tank diameter stirring that adds water
Slurry again through the second elephant trunk enter lime white sedimentation basin precipitation, the milk of lime on sedimentation basin upper strata through screen filtration, into milk of lime pond,
Milk of lime in milk of lime pond is sent into neutralization chamber to be neutralized, the lime mud in lime white sedimentation basin is periodically through digging machine or craft
Clear out, transported with automobile.
The content of the invention
The purpose of the present invention is the above-mentioned deficiency for overcoming prior art, and it is high to provide a kind of lime utilization rate, is raised without lime
Dirt, the low lime slaking chemicals dosing plant of lime mud water content.
The technical scheme is that:A kind of lime slaking chemicals dosing plant, it includes:Lime delivery unit, lime slaking
Unit, milk of lime separative element and lime dosing unit;Wherein, lime delivery unit, the quick lime in refined lime tank is sent
To the charging aperture of lime slaking unit;Lime slaking unit, including cylinder, cylinder are provided with charging aperture and discharging opening, in cylinder
Portion is divided into from charging aperture to discharging opening:Buffering area, homogeneous area, newborn slag Disengagement zone, Lao Zha areas dreg discharging area;Quick lime is by stone
Into milk of lime sand aqueous mixtures, discharging opening stream of the milk of lime sand aqueous mixtures from lime slaking unit after ash digestion unit digestion
Go out;Milk of lime separative element, the milk of lime sand aqueous mixtures that will be flowed into from discharging opening are separated into milk of lime and lime mud;Milk of lime
Neutralized in neutralization chamber by pump to lime dosing unit.
The technical scheme of an of the invention step is:Described lime delivery unit is spiral conveyer.
The technical scheme of an of the invention step is:Described milk of lime separative element is Spiral sand-water separator, and it includes sand
Water separating tank and spiral transferring sand launder;Milk of lime sand aqueous mixtures from lime slaking unit are separated into stone by girt-water separation groove
Grey breast and lime mud, milk of lime flow to milk of lime pond;Spiral transferring sand launder, the lime mud that will sink to bottom land is defeated by spiral transferring sand launder
It is sent to the outlet at the top of spiral transferring sand launder, Pai Xiangchuzha areas.
Further technical scheme is the present invention:The helical axis of described spiral transferring sand launder is with the horizontal 25 ° of angle.
Present invention beneficial effect compared with the prior art is:1st, because the present invention obtains stone using common quicklime slaking
Grey breast, obtains milk of lime, cost-effective more than 20% using refined lime digestion compared with the prior art.
2nd, due to the quick lime in refined lime tank to be directly delivered to the charging of lime slaking unit by spiral conveyer
Mouthful, lime airborne dust is greatly decreased, reduce injury of the lime airborne dust to operator's health.
3rd, due to that using Spiral sand-water separator slagging-off, in milk of lime sand mixture 95% lime mud can be separated,
Improve quick lime utilization rate more than 10%.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Reference:1st, refined lime tank, 2, spiral conveyer, 3, lime slaking unit, 4, Spiral sand-water separator, 31,
Cylinder, 32, charging aperture, 33, discharging opening, 41, spiral transferring sand launder, 42, outlet, 43, spout hole.
Specific embodiment
Detailed construction of the invention is further described below in conjunction with figure and specific embodiment.
As shown in figure 1, a kind of lime slaking chemicals dosing plant of the invention, it includes:Spiral conveyer 2, lime slaking unit 3
And Spiral sand-water separator 4;Wherein, spiral conveyer 2 is arranged on the lower section of refined lime tank 1, by the raw stone in refined lime tank 1
Ash is delivered in the charging aperture 32 of lime slaking unit 3;Lime slaking unit 3, including cylinder 31, cylinder 31 are provided with charging aperture 32
With discharging opening 33, it is divided into discharging opening 33 from charging aperture 32 inside cylinder 31:Buffering area, homogeneous area, newborn slag Disengagement zone, drag for
Slag area dreg discharging area;The cylinder 31 of lime slaking unit 3 can gyration under the low speed, quick lime and water in cylinder, due to cylinder
The revolution of body and flight are acted on, and are voluntarily stirred in cylinder, are digested by gyration, and the newborn slag of lime slaking unit 3 is separated
Area is provided with turn sieve for sieving milk of lime sand aqueous mixtures rotated together with cylinder 31, the milk of lime after turning sieve screening
In the Spiral sand-water separator 4 that slag mixture flows into the lower section of discharging opening 33 from discharging opening 33, and the lime mud of bulk stays in cylinder
31 Lao Zha areas dreg discharging area, discharges outside cylinder 31 during deslagging.Spiral sand-water separator 4 is arranged on the top in milk of lime pond, including
Girt-water separation groove and spiral transferring sand launder 41, the milk of lime sand aqueous mixtures after screening enter in girt-water separation groove, carry out newborn slag point
From milk of lime overflows the spout hole 43 of girt-water separation unit 4, and into milk of lime pond, lime sand sinks to the groove of girt-water separation groove
Bottom, the row of 41 top exit of spiral transferring sand launder 42 is transported to by the helical axis for rotating spiral transferring sand launder 41 by lime mud along helicla flute
To Chu Zha areas(It is to draw in figure), because helical axis transports lime mud upwards with the horizontal 25 ° of angles, lime mud was being conveyed
Further milk of lime is separated in journey, so as to ensure that the lime mud moisture content of discharging opening is not more than 60%, improves the utilization rate of lime
More than 10%, will be neutralized in the neutralization chamber of the milk of lime pump in Calcified pond to lime dosing unit by vertical pump, acid will be contained
The accessing pending water of property carries out dosing neutralisation treatment.
General principle of the invention and principal character has been shown and described above, it should be understood by those skilled in the art that,
The invention is not limited in any way for above-described embodiment, all technical sides obtained by the way of equivalent or equivalent transformation
Case, all falls within protection scope of the present invention.
Claims (4)
1. a kind of lime slaking chemicals dosing plant, it is characterised in that it includes:Lime delivery unit(2), lime slaking unit(3)、
Milk of lime separative element(4)And lime dosing unit;Wherein lime delivery unit(2), by refined lime tank(1)Quick lime
Deliver to lime slaking unit(3)Charging aperture(32);Lime slaking unit(3), including cylinder(31), cylinder(31)Be provided with into
Material mouth(32)And discharging opening(33), cylinder(31)It is internal from charging aperture(32)To discharging opening(33)It is divided into:Buffering area, homogeneous
Area, newborn slag Disengagement zone, Lao Zha areas dreg discharging area;Quick lime is by lime slaking unit(3)After be digested to milk of lime sand aqueous mixtures,
Milk of lime sand aqueous mixtures are from discharging opening(33)Outflow;Milk of lime separative element(4), will be from discharging opening(33)The milk of lime of inflow
Sand aqueous mixtures are separated into milk of lime and lime mud;Milk of lime in pump to the neutralization chamber of lime dosing unit by being neutralized.
2. a kind of lime slaking chemicals dosing plant according to claim 1, it is characterised in that described lime delivery unit
(2)It is spiral conveyer.
3. a kind of lime slaking chemicals dosing plant according to claim 1 and 2, it is characterised in that described milk of lime is separated
Unit(4)It is Spiral sand-water separator, it includes girt-water separation groove and spiral transferring sand launder(41);Girt-water separation groove, will be from stone
Ash digestion unit(3)Milk of lime sand aqueous mixtures be separated into milk of lime and lime mud, milk of lime flow to milk of lime pond;Spiral transferring
Sand launder(41), the lime sand that will sink to bottom land is transported to outlet at the top of spiral transferring sand launder by spiral transferring sand launder(42)Discharge.
4. a kind of lime slaking chemicals dosing plant according to claim 3, it is characterised in that described spiral transferring sand launder(41)
Helical axis with the horizontal 25 ° of angles.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710111388.6A CN106830716A (en) | 2017-02-28 | 2017-02-28 | A kind of lime slaking chemicals dosing plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710111388.6A CN106830716A (en) | 2017-02-28 | 2017-02-28 | A kind of lime slaking chemicals dosing plant |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106830716A true CN106830716A (en) | 2017-06-13 |
Family
ID=59134394
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710111388.6A Pending CN106830716A (en) | 2017-02-28 | 2017-02-28 | A kind of lime slaking chemicals dosing plant |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106830716A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115521082A (en) * | 2022-10-11 | 2022-12-27 | 华润水泥技术研发有限公司 | Method for promoting light calcium digestion process by improving digestion temperature through photo-thermal technology |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102363568A (en) * | 2011-09-19 | 2012-02-29 | 江苏海洲水务工程有限公司 | Calcium hydroxide machine |
CN104844021A (en) * | 2015-05-04 | 2015-08-19 | 湖南水口山有色金属集团有限公司 | Lime milk preparation method and lime milk preparation device |
CN104858043A (en) * | 2015-05-19 | 2015-08-26 | 李永江 | Spiral slag extraction machine |
CN105084786A (en) * | 2015-08-10 | 2015-11-25 | 成都格瑞思文化传播有限公司 | Lime slaking and chemical feeding device |
-
2017
- 2017-02-28 CN CN201710111388.6A patent/CN106830716A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102363568A (en) * | 2011-09-19 | 2012-02-29 | 江苏海洲水务工程有限公司 | Calcium hydroxide machine |
CN104844021A (en) * | 2015-05-04 | 2015-08-19 | 湖南水口山有色金属集团有限公司 | Lime milk preparation method and lime milk preparation device |
CN104858043A (en) * | 2015-05-19 | 2015-08-26 | 李永江 | Spiral slag extraction machine |
CN105084786A (en) * | 2015-08-10 | 2015-11-25 | 成都格瑞思文化传播有限公司 | Lime slaking and chemical feeding device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115521082A (en) * | 2022-10-11 | 2022-12-27 | 华润水泥技术研发有限公司 | Method for promoting light calcium digestion process by improving digestion temperature through photo-thermal technology |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110303033A (en) | A kind of shield-tunneling construction dregs processing system and processing method | |
CN104874591B (en) | The remaining sludge treatment technology of building and system | |
CN207941295U (en) | Settlement of sewage processing system | |
CN105084786B (en) | A kind of lime slaking dosing feed device | |
CN110026123A (en) | A kind of flocculation medicament quantitatively dissolves and uniformly mixes add-on system | |
CN106976999A (en) | Concrete mixing plant wastewater ocean disposal system | |
CN110025988A (en) | A kind of slime water concentration processing system of three sections of underflow discharges | |
CN104844021B (en) | The preparation method and device of lime cream | |
CN102765741B (en) | Separating and purifying device and method of white mud/carbide slag-gypsum process desulphurization gypsum slurry | |
CN209468221U (en) | A kind of concrete mixing plant Sewage treatment utilizes device | |
CN109761294B (en) | Improved crystallizer suitable for high-salt wastewater fractional crystallization | |
CN106830716A (en) | A kind of lime slaking chemicals dosing plant | |
CN103801553A (en) | Concrete waste comprehensive treatment system | |
CN203139702U (en) | Washing, sedimentation and deslagging device of recycling sand | |
CN205387918U (en) | Mud circulation clean system during drilling | |
CN106076598A (en) | A kind of scraper-type ultrasound wave deslimer | |
CN201492975U (en) | Slag-water separating and recycling device | |
CN103084264B (en) | Multistage increasing type gold gravity-flow concentrator | |
CN110025989A (en) | It is a kind of with three sections of discharge gates without rake thickener | |
CN212292831U (en) | Powdery nitratine continuous halogen making system | |
CN209507939U (en) | A kind of mud conditioning device | |
CN204194145U (en) | High grey fine slime pillar secondary flotation equipment | |
CN107572553A (en) | A kind of transformation pot | |
CN207877416U (en) | A kind of multistage waste mineral oil classification processing connection group device | |
CN207091081U (en) | A kind of modified mudpan |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170613 |