CN106830715A - A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide - Google Patents

A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide Download PDF

Info

Publication number
CN106830715A
CN106830715A CN201611211011.XA CN201611211011A CN106830715A CN 106830715 A CN106830715 A CN 106830715A CN 201611211011 A CN201611211011 A CN 201611211011A CN 106830715 A CN106830715 A CN 106830715A
Authority
CN
China
Prior art keywords
auger
lime
calcium hydroxide
waste residue
waste
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
Application number
CN201611211011.XA
Other languages
Chinese (zh)
Inventor
傅志全
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.)
Jiande Quanxin Calcium Industry Co Ltd
Original Assignee
Jiande Quanxin Calcium 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 Jiande Quanxin Calcium Industry Co Ltd filed Critical Jiande Quanxin Calcium Industry Co Ltd
Priority to CN201611211011.XA priority Critical patent/CN106830715A/en
Publication of CN106830715A publication Critical patent/CN106830715A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2/00Lime, magnesia or dolomite
    • C04B2/02Lime
    • C04B2/04Slaking
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2/00Lime, magnesia or dolomite
    • C04B2/02Lime
    • C04B2/04Slaking
    • C04B2/045After-treatment of slaked lime

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide, the present invention relates to calcium hydroxide production field;Its procedure of processing is as follows:First, waste residue is unloaded:After haulage vehicle reaches using the auxiliary equipments such as auger of cutting into slices by material dispersion after matched with quick lime;2nd, lime is unloaded broken:Quick lime is unloaded material bin by haulage vehicle, and lime silo is promoted to after being crushed to 1mm~20mm;3rd, it is homogenized:4th, static digestion:By the material of homogenization stage, static state digests more than 2h in being promoted to homogenizing bin by elevator, quick lime and moisture is fully reacted complete;5th, roughing is got the raw materials ready;6th, process:The material in storehouse of getting the raw materials ready enters the ultra-fine grey calcium machine of alloy or pneumatic separator by charging auger, and calcium hydroxide after processing is preserved into product storehouse.The production method high degree of automation, good airproof performance can be by discarded object cycling and reutilization, energy-conserving and environment-protective.

Description

A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide
Technical field
The present invention relates to calcium hydroxide production field, and in particular to the stone that a kind of utilization precipitated calcium carbonate factory production shuttle is produced The method that mortar and waste residue waste material produce calcium hydroxide.
Background technology
Calcium hydroxide is a kind of white powdery solids.Chemical formula Ca (OH) 2, is commonly called as white lime, calcium hydroxide, and the aqueous solution claims Make clarification limewash.Calcium hydroxide has the general character of alkali, is a kind of highly basic.Calcium hydroxide is binary highly basic, but is only capable of being slightly soluble in Water.Calcium hydroxide is widely used in the industry.
Many lime whites and waste residue waste material are generated during current precipitated calcium carbonate industry production, it is impossible to obtain effectively Treatment, causes some available resources to waste, and pole is not environmentally.
The content of the invention
Defect and deficiency it is an object of the invention to be directed to prior art, there is provided a kind of simple structure, it is reasonable in design, make With the convenient method for producing calcium hydroxide using lime white and waste residue waste material, the production method high degree of automation, sealing It is good, can be by discarded object cycling and reutilization, energy-conserving and environment-protective.
To achieve the above object, the technical solution adopted by the present invention is:Its procedure of processing is as follows:
First, waste residue is unloaded:
Material is discharged into a trapezoidal hopper by haulage vehicle;
2nd, using the leftover bits and pieces in lime leasing;
3rd, it is homogenized:
Lime white and waste residue waste material are conveyed by auger and tentatively mixed, and add 1mm~10mm's in first order auger end Quick lime carries out digestion reaction with wet stock, and quick lime and wet stock ratio are 0.1~0.5:1, and can be according to the dry and wet of material The a small amount of water of degree supplement, then auger is homogenized by two-stage(Total length is not less than 20m)Stirring homogenizing(30min~60min), make to do Wet stock is evenly distributed, and homogenizing and digestion reaction have been carried out in whipping process, makes material dry and wet suitable, into loose sprills; The bottom of homogenizing auger is deposited in through digesting again for a long time without complete calcium oxide is digested, because volume after digestion is complete Expanding and become fluffy can progressively be delivered to elevator by auger;
4th, static digestion:
By the material of homogenization stage, static state digests more than 2h in being promoted to homogenizing bin by elevator, makes quick lime and moisture Fully reaction is complete;
5th, roughing is got the raw materials ready:
After by the static digestion of more than 2h, material conveying auger to elevator is screened out simultaneously crushed stone by drum sieve Discharge, then will tail over material and be delivered to the standby production in storehouse of getting the raw materials ready by auger;
6th, process:
The material in storehouse of getting the raw materials ready enters the ultra-fine grey calcium machine of alloy or pneumatic separator by charging auger, and the calcium hydroxide after processing enters Enter product storehouse preservation.
Further, waste discharge slag, cinder device are equipped with described step five and step 6, can be with improve product quality And content.
Further, pulsed dust-removing device is provided with described step two and step 3, to reach purify air, protection ring The target in border.
The present invention has the beneficial effect that:A kind of utilization lime white of the present invention and waste residue waste material produce the side of calcium hydroxide Method, the production method high degree of automation, good airproof performance can have discarded object cycling and reutilization, energy-conserving and environment-protective, the present invention Simple structure, it is reasonable to set, the advantages of low manufacture cost.
Specific embodiment
This specific embodiment use technical scheme be:Its procedure of processing is as follows:
First, waste residue is unloaded:
Material is discharged into a trapezoidal hopper by haulage vehicle;
2nd, using the leftover bits and pieces in lime leasing;
3rd, it is homogenized:
Lime white and waste residue waste material are conveyed by auger and tentatively mixed, and the quick lime of 5mm is added in first order auger end Digestion reaction is carried out with wet stock, quick lime and wet stock ratio are 0.1~0.5, and can be few according to the humidity of material supplement The water of amount, then auger is homogenized by two-stage(Total length is not less than 20m)Stirring homogenizing 50min, makes dry and wet material be evenly distributed, Homogenizing and digestion reaction are carried out in whipping process, has made material dry and wet suitable, into loose sprills;Without the complete oxidation of digestion Calcium precipitate in the bottom of homogenizing auger through digesting again for a long time, after because of volumetric expansion and becoming fluffy meeting after digestion completely Elevator is progressively delivered to by auger;
4th, static digestion:
By the material of homogenization stage, static state digests more than 2h in being promoted to homogenizing bin by elevator, makes quick lime and moisture Fully reaction is complete;
5th, roughing is got the raw materials ready:
After by the static digestion of more than 2h, sample conveying auger to elevator is screened out simultaneously crushed stone by drum sieve Discharge, then will tail over material and be delivered to the standby production in storehouse of getting the raw materials ready by auger;
6th, process:
Get the raw materials ready storehouse material by charging auger enter the ultra-fine grey calcium machine of FZQ type alloys or pneumatic separator, the hydrogen-oxygen after processing Change calcium to be preserved into product storehouse;
7th, packed and transported:
The calcium hydroxide of production can now be wrapped into existing entrucking according to 25kg inner wrappings, also can bulk vehicle entrucking directly transport;In packaging In-site installation has pulsed dust-removing device, to reach purify air, the target of environmental protection.
Further, waste discharge slag, cinder device are equipped with described step five and step 6, can be with improve product quality And content.
Further, the exit leaked is provided with pulsed dust-removing device in described step two and step 3, to reach Purify air, the target of environmental protection.
This specific embodiment has the beneficial effect that:It is a kind of using lime white and waste residue waste material described in this specific embodiment The method for producing calcium hydroxide, the production method high degree of automation, good airproof performance can save discarded object cycling and reutilization Can environmental protection, the present invention has simple structure, and it is reasonable to set, the advantages of low manufacture cost.
The above, is merely illustrative of the technical solution of the present invention and unrestricted, and those of ordinary skill in the art are to this hair Other modifications or equivalent that bright technical scheme is made, without departing from the spirit and scope of technical solution of the present invention, All should cover in the middle of scope of the presently claimed invention.

Claims (3)

1. a kind of method that utilization lime white and waste residue waste material produce calcium hydroxide, it is characterised in that:Its procedure of processing is as follows:
(1), waste residue is unloaded:
Material is discharged in hopper using grabbing the auxiliary equipments such as palladium, auger after haulage vehicle reaches;
(2), lime is unloaded broken:
Quick lime is unloaded material bin by haulage vehicle, and lime silo is promoted to after being crushed to 1mm~20mm;
(3), it is homogenized:
Lime white and waste residue waste material are conveyed by auger and tentatively mixed, and add 1mm~10mm's in first order auger end Quick lime carries out digestion reaction with wet stock, and quick lime and wet stock ratio are 0.1~0.5:1, and can be according to the dry and wet of material The a small amount of water of degree supplement, then auger is homogenized by two-stage, total length is not less than 20m, and stirring homogenizing, 30min~60min makes to do Wet stock is evenly distributed, and homogenizing and digestion reaction have been carried out in whipping process, makes material dry and wet suitable, into loose sprills; The bottom of homogenizing auger is deposited in through digesting again for a long time without complete calcium oxide is digested, because volume after digestion is complete Expanding and become fluffy can progressively be delivered to elevator by auger;
(4), static digestion:
By the material of homogenization stage, static state digests more than 2h in being promoted to homogenizing bin by elevator, makes quick lime and moisture Fully reaction is complete;
(5), roughing is got the raw materials ready:
After by the static digestion of more than 2h, sample conveying auger to elevator is screened out simultaneously crushed stone by drum sieve Discharge, then will tail over material and be delivered to the standby production in storehouse of getting the raw materials ready by auger;
(6), process:
The material in storehouse of getting the raw materials ready enters the ultra-fine grey calcium machine of alloy or pneumatic separator by charging auger, and the calcium hydroxide after processing enters Enter product storehouse preservation.
2. the method that a kind of utilization lime white according to claim 1 and waste residue waste material produce calcium hydroxide, its feature exists In:Waste discharge slag, cinder device, improve product quality and content are equipped with described step (five) and step (6).
3. the method that a kind of utilization lime white according to claim 1 and waste residue waste material produce calcium hydroxide, its feature exists In:Pulsed dust-removing device is provided with described step (two) and step (3), for purify air, environmental protection.
CN201611211011.XA 2016-12-24 2016-12-24 A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide Pending CN106830715A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611211011.XA CN106830715A (en) 2016-12-24 2016-12-24 A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611211011.XA CN106830715A (en) 2016-12-24 2016-12-24 A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide

Publications (1)

Publication Number Publication Date
CN106830715A true CN106830715A (en) 2017-06-13

Family

ID=59136080

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611211011.XA Pending CN106830715A (en) 2016-12-24 2016-12-24 A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide

Country Status (1)

Country Link
CN (1) CN106830715A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112624647A (en) * 2019-09-24 2021-04-09 尹诗东 Method for recycling aluminum sulfate waste residues and product thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103508478A (en) * 2013-06-05 2014-01-15 池州灵芝化建材料科技有限公司 Method used for preparing calcium hydroxide from light calcium carbonate and active calcium oxide defective products
CN105541136A (en) * 2016-01-20 2016-05-04 湖州浙宝冶金辅料有限公司 Production process and system of calcium hydroxide
CN105776298A (en) * 2016-05-17 2016-07-20 长沙市望城区湘怡钙业有限公司 Preparation method of calcium hydroxide
CN105879742A (en) * 2015-01-26 2016-08-24 建德市全新钙业有限公司 Stirring device of dedusting digester

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103508478A (en) * 2013-06-05 2014-01-15 池州灵芝化建材料科技有限公司 Method used for preparing calcium hydroxide from light calcium carbonate and active calcium oxide defective products
CN105879742A (en) * 2015-01-26 2016-08-24 建德市全新钙业有限公司 Stirring device of dedusting digester
CN105541136A (en) * 2016-01-20 2016-05-04 湖州浙宝冶金辅料有限公司 Production process and system of calcium hydroxide
CN105776298A (en) * 2016-05-17 2016-07-20 长沙市望城区湘怡钙业有限公司 Preparation method of calcium hydroxide

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112624647A (en) * 2019-09-24 2021-04-09 尹诗东 Method for recycling aluminum sulfate waste residues and product thereof

Similar Documents

Publication Publication Date Title
CN102114379B (en) Desulfurizing agent and preparation and application thereof
CN110078389A (en) A kind of high response and high-specific surface area calcium hydroxide raw powder's production technology
CN205762896U (en) A kind of aluminium cell slag from delining innocuity disposal system
CN106219586A (en) A kind of be raw material production nanometer grade calcium carbonate with carbide slag device and method
CN203469801U (en) Desulfurized ash-limestone mixing and slurrying device
CN106830715A (en) A kind of method that utilization lime white and waste residue waste material produce calcium hydroxide
CN109384400A (en) A kind of calcium carbide residues processing technique and system
CN211936365U (en) System for utilize cement kiln tail to return ash and carry out flue gas desulfurization
CN104790240A (en) Low-carbon environmental protection clean paper making technology
CN106630689A (en) Preparation method of building paint grade ash calcium powder
CN207167116U (en) Forage cuts briquetting dryer
CN214360288U (en) Production line of calcium oxide and calcium hydroxide
CN212701298U (en) Wet-process desulfurizer preparation system
CN104209073B (en) A kind of modified starch production equipment
CN205443069U (en) Adopt magnesite ore crushing production magnesite clinker's device
CN211415552U (en) Production system for bleaching lignocellulose
CN103614180A (en) Device for producing biomass fuel particles
CN211871806U (en) High-efficient lime slaker
CN114197028A (en) Continuous preparation method of calcium sulfate whiskers
CN206476911U (en) A kind of line production system of mineral matter functional fertilizer
CN205528455U (en) Industrial grade calcium hydrate production facility
CN111229011A (en) System and method for performing flue gas desulfurization by using cement kiln tail return ash
CN205550491U (en) Environment -friendly slay adds lancing concrete brick factory supplies hybrid system
CN218903034U (en) Reutilization system for waste carbon dioxide and steel slag
CN113117490A (en) Integrated process for flue gas desulfurization and denitrification and cementing material production

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
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20170613