CN204454657U - A kind of leaded cullet resource utilization remanufacture line - Google Patents
A kind of leaded cullet resource utilization remanufacture line Download PDFInfo
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- CN204454657U CN204454657U CN201420838662.1U CN201420838662U CN204454657U CN 204454657 U CN204454657 U CN 204454657U CN 201420838662 U CN201420838662 U CN 201420838662U CN 204454657 U CN204454657 U CN 204454657U
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Abstract
The utility model discloses a kind of leaded cullet resource utilization remanufacture line, comprise shredding unit, melting granulating unit, dissolver and meticulous extraction element, described shredding unit, melting granulating unit, dissolver are connected successively with meticulous extraction element.The process such as the production line that the utility model provides can be pulverized leaded cullet successively, melting, shrend, dissolving, hybrid reaction generation lead sulfide, are then separated and obtain solid-state lead sulfide and water glass, effectively leaded cullet is carried out resource utilization recovery.
Description
Technical field
The utility model relates to glass remanufacture line, particularly relates to a kind of leaded cullet resource utilization remanufacture line.
Background technology
Lead is widely used in television picture tube, computer picture tube with its feature that can reduce X-radiation.Research shows, China's production television picture tubes in 1998 and computer picture tube amount to 4,100 ten thousand, and reached 6,600 ten thousand to China's picture tube output in 2005, product major part is large gauge picture tube, on average often props up weight 23.5kg.Waste image tube glass is the melt be made up of the oxide compound of the compositions such as silicon, lead, sodium, potassium, aluminium, magnesium and calcium, and wherein plumbous content occupies second.According to research measuring and calculating, pipe cone flint glass accounts for greatly about 40% of whole glass bulb weight, often prop up CRT picture tube weight in average 23.5kg, annual yield is by 5,350 ten thousand, every annual meeting produces 50.3 ten thousand tons of leaded cullet, the metallic lead wherein contained just reaches 93539 tons more than, and metallic lead is important strategic resource.In addition to lead, also other a large amount of silicate mineralss are contained in cullet.
Reclaim plumbous significant from leaded cullet.The lead-zinc deposit of China based on lead, independent lead deposit are less, and most of lead-zinc deposit is generally total to nearly 20 kinds of elements such as association copper, iron, sulphur, silver, gold.The grade of lead deposit based on the lean ore being less than 3%, higher than 3% verify that plumbous reserves only account for whole proven reserve about 30%.And when flint glass runs into sour environment, even corrosion plumbous oxide can be gone out under rainwater condition.Lead is heavy metal element, and can damage maincenter and peripheral nervous system, circulatory system irrespective of size kidney after taking in human body, Endocrine system has impact, has a strong impact on brain development.Meanwhile, the material after leaded cullet extracts lead can be made into water glass, can bring the economic product of considerable income.Visible, the resource utilization of leaded cullet reclaims has important economic benefit, social benefit and environmental benefit.
At present, the treatment process proposing leaded cullet both at home and abroad mainly contains recycle method, acid pasting, smelting method, landfill method, directly manufactures building material etc.Recycle method due to leaded cullet main source CRT gradually substitute by liquid-crystal display, limit the use of the method; Smelting method processing cost is high, and the slag viscosity that glass is formed increases, and easily causes difficulty of skimming; Acid pasting leaches because adopting the solution such as hydrofluoric acid, there is the problems such as seriously polluted and the glass wasting of resources; Direct employing high-temperature melting method or sintering process prepare glass-ceramic building materials, then not only can not efficient recovery metallic lead, Lead contamination is endangered still exist, be from a kind of transferred product to another kind of product by heavy metals such as the lead in glass, and due to the glass-ceramic of preparation, leaded in multicellular glass, affect the use of its product; There is the problem easily causing secondary pollution in landfill method, be also the waste to plumbous and glass resource simultaneously.
Summary of the invention
The purpose of this utility model aims to provide a kind of leaded cullet resource utilization remanufacture line.
The purpose of this utility model is achieved through the following technical solutions: a kind of leaded cullet resource utilization remanufacture line, comprise shredding unit, melting granulating unit, dissolver and meticulous extraction element, described shredding unit, melting granulating unit, dissolver are connected successively with meticulous extraction element.
Described shredding unit is two cover shredding units, comprise primary mill and type fine disintegrating machine, between described primary mill and type fine disintegrating machine, lift is set, the discharge port of described type fine disintegrating machine is connected with described melting granulating unit by lift, the material through fine crushing process is delivered to the process of melting granulating unit.
Described melting granulating unit comprises dosing case, molten bath, shrend discharge device and water circle device, the bottom of described dosing case is provided with discharge port, and described molten bath is positioned at immediately below the discharge port of dosing case, the material dosing after fine crushing process drops in molten bath and carries out melting by dosing case; Discharge gate is established in the bottom in described molten bath, and described shrend discharge device comprises water quenching box, and opening for feed, water-in and water port are established in the bottom of this water quenching box, and top is provided with the discharge gate for being connected with dissolver; The top of described water circle device is provided with water outlet, for being connected with the water-in of shrend discharge device, its underpart is then provided with water-in, for being connected with the water port of described shrend discharge device, described water circle device constantly send water toward shrend discharge device, and carry out shrend to the liquation entering water quenching box, liquation meets cold formation frit, frit is discharged from discharge gate, enters dissolver.
Described dissolver comprises frit pulverizer, dosing case, autoclave and water supply installation, lift is provided with between described frit pulverizer and dosing case, frit powder after pulverizing is sent in dosing case by lift, described autoclave is positioned at the below of dosing case discharge port, its opening for feed is connected with the discharge port of dosing case, quantitative frit powder is sent in autoclave and processes, described water supply installation is connected with autoclave, for supplying water in still, the dissolving of hydro-thermal high pressure is carried out to material.
Described meticulous extraction element comprises the first separating centrifuge, there is the hybrid reaction groove of stirring rake, water supply installation and the second separating centrifuge, opening for feed established by described first separating centrifuge, liquid outlet and discharge port, described opening for feed is connected with the discharge gate of autoclave, material from autoclave is separated in the first separating centrifuge, described liquid outlet connected drainage pipe, the leakage fluid dram of liquid discharge pipe is positioned at the top of hybrid reaction groove, the liquid that first separating centrifuge is separated is entered in hybrid reaction groove to react with chemical reagent and generates sulfuration lead, the slag charge that first separating centrifuge is separated then is discharged from discharge port, described water supply installation is connected with hybrid reaction groove, for reaction provides solvent, described second separating centrifuge establishes opening for feed, liquid outlet and discharge port, the opening for feed that the discharge gate of described hybrid reaction groove is connected with the second separating centrifuge connects, sent in the second separating centrifuge by the material that reaction generates and carry out centrifugation, the liquid of gained and solid are discharged from liquid outlet and discharge port respectively.
Ball mill is provided with between described first separating centrifuge and hybrid reaction groove, filter vat and pressure filter, described ball mill, filter vat is connected along Flow of Goods and Materials direction successively with pressure filter, the described discharge port of the first separating centrifuge is connected with the opening for feed of ball mill, the liquid outlet of pressure filter is connected with hybrid reaction groove, filter screen is provided with in wherein said filter vat, described filter screen tilts to liquid flow direction, slag charge from the first separating centrifuge enters grinding in ball grinder, then enter filter vat filtering separation slurry and ball-milling medium, slurry out enters pressure filter afterwards from filter vat and carries out press filtration, liquid enters in hybrid reaction groove, filter residue is disposed to the tailings receiving tank of slag-drip opening placement from the slag-drip opening of pressure filter as tailings.
Filter screen one end in described filter vat is fixed on the bottom land of that side of filter vat feed end, the other end is fixed on the top of filter vat, filter screen becomes 30 ° with the left surface of filter vat, when ball-milling medium and slurry constantly flow in filter vat, ball-milling medium is deposited on the left side of filter screen, and slurry flows in the space of opposite side by filter screen, ball-milling medium is separated fully with slurry.
The utility model also comprises water glass concentrating unit, this water glass concentrating unit is the open container being provided with well heater, described well heater is arranged on container outer wall, fluid inlet and liquid outlet are established in the bottom of described open container, the liquid outlet connected drainage pipe of described second separating centrifuge, the outlet end of described liquid discharge pipe is positioned at the top of described open container, the liquid separated is entered heating in open container concentrated.
Rinse bath and pressure filter is provided with between described second separating centrifuge and water glass concentrating unit, described rinse bath is a casing, opening for feed and water-in are established in its top, bottom sets out the mouth of a river, described opening for feed is connected with the slag notch of the second separating centrifuge, water-in is then connected with water supply installation, add water in rinse bath and solid lead sulfide cleaned, water after cleaning and solid lead sulfide flow into press filtration in pressure filter, in influent liquid stream glass concentrating unit, solid lead sulfide is then disposed to from the slag-drip opening of pressure filter in the lead sulfide receiving tank of slag-drip opening placement.
As an embodiment of the present utility model, water supply installation in above-mentioned dissolver, extraction element and water glass concentrating unit is the water circle device of melting granulating unit, its water outlet establishes an arm, this arm establishes three secondary arms, these three secondary arms are connected with autoclave, hybrid reaction groove and rinse bath respectively, and secondary arm is provided with valve.
The utility model can do following improvement: also comprise gas treating system, this gas treating system comprises exhaust duct, condenser and gas-cleaning installation, the exhaust outlet of exhaust duct connects condenser, condenser is then connected with gas-cleaning installation, described exhaust duct is arranged on the ceiling of workshop, the blast inlet of this exhaust duct is provided with several extraction hood, for absorbing the waste gas produced in operation process, waste gas successively enters condenser and gas-cleaning installation process through exhaust duct, is then disposed in air.
In the utility model, can adopt and manually send in shredding unit by leaded cullet, so only need establish stair on shredding unit side, operator can take the stairs up, and are poured in shredding unit by leaded cullet.Also can feeding unit be set, as lift, conveying belt etc., leaded cullet be sent in shredding unit.
The utility model also comprises means of illumination and camera, and described means of illumination and camera are arranged on the ceiling of workshop.Means of illumination is used for providing illumination to workshop if desired, and the effect of camera is used to Real Time Observation workshop operation state, conveniently finds problem fast when production line breaks down and keeps in repair.
The utility model also comprises online component detection apparatus and intelligent controlling device, described online component detection apparatus is connected with control device, described intelligent controlling device controls operation and the stopping of each device, described online component detection apparatus detects the composition in slag charge or solution, detected result is delivered to control device, and control device calculates material throwing amount according to detected result.
Compared with prior art, the utility model has following beneficial effect:
(1) process such as the production line that the utility model provides can be pulverized leaded cullet successively, melting, shrend, dissolving, hybrid reaction generation lead sulfide, then be separated and obtain solid-state lead sulfide and water glass, effectively leaded cullet is carried out resource utilization recovery.
(2) the utility model is provided with online composition detection system, to pulverizing, melting, dissolving, etc. the material in treatment step carry out sampling and carry out composition detection, for the charging capacity determined in melting, dissolving, hybrid reaction.
(3) the utility model is provided with gas-cleaning installation, absorbs the waste gas produced in operation process, ensure that plant working environmental nonpollution, realizes environmental protection and produces.
(4) the utility model arranges intelligent controlling device, controls each device, realizes full-automatic production.
(5) each device of the present utility model is existing standard equipment, common and cheap, and the laid down cost of production line is low.
Accompanying drawing explanation
Fig. 1 is the structural representation of the leaded cullet resource utilization remanufacture line of the utility model embodiment.
Embodiment
Leaded cullet resource utilization remanufacture line shown in Fig. 1 is an embodiment of the present utility model, mainly comprises online component detection apparatus 37, intelligent controlling device 1, shredding unit, melting granulating unit, dissolver and meticulous extraction element.Wherein, shredding unit, melting granulating unit, dissolver are connected successively with meticulous extraction element.
Shredding unit is two cover shredding units, comprises primary mill 5 and type fine disintegrating machine 7.Arrange screw lift(elevator) 6 between primary mill 5 and type fine disintegrating machine 7, the discharge port of type fine disintegrating machine 7 is connected with melting granulating unit by screw lift(elevator) 8, the material through fine crushing process is delivered to the process of melting granulating unit.
Melting granulating unit comprises dosing case 9, molten bath 10, shrend discharge device and water circle device, and the bottom of dosing case 9 is provided with discharge port, and molten bath 10 is positioned at immediately below the discharge port of dosing case 9.Material after fine crushing process and reagent quantitative drop in molten bath 10 and carry out melting by dosing case 9.Discharge gate is established in the bottom in molten bath 10, and shrend discharge device comprises water quenching box 11, and opening for feed, water-in and water port are established in the bottom of this water quenching box 11, and the discharge gate be connected with dissolver is established on top.Water circle device comprises a water tank 12 and pump (not shown), the top of water tank 12 sets out the mouth of a river, this water outlet is connected with the water-in of pump with the water quenching box 11 of shrend discharge device through pipeline, and the bottom of water tank 12 is then provided with water-in, is connected with the water port of water quenching box 11.Water circle device constantly send water toward water quenching box 11, and carry out shrend to the liquation entering water quenching box 11, liquation meets cold formation frit, and frit is discharged from discharge gate, enters dissolver.
Dissolver comprises frit pulverizer 13, dosing case 15, autoclave 16 and water supply installation.Be provided with screw lift(elevator) 14 between frit pulverizer 13 and dosing case 15, the frit powder after pulverizing is sent in dosing case 15 by screw lift(elevator) 14.Autoclave 16 is positioned at immediately below dosing case 15 discharge port, its opening for feed is connected with the discharge port of dosing case 15, frit powder materials quantitative is sent in autoclave 16 and processes, water supply installation is connected with autoclave 16, for supplying water in still, the dissolving of hydro-thermal high pressure is carried out to material.
Extraction element comprises the first separating centrifuge 17, has the hybrid reaction groove 21 of stirring rake 27, water supply installation and the second separating centrifuge 22.First separating centrifuge 17 establishes opening for feed, liquid outlet and discharge port, its opening for feed is connected with the discharge gate of autoclave 16, material from autoclave 16 enters in the first separating centrifuge 17 and is separated, the liquid outlet connected drainage pipe of the first separating centrifuge 17, the leakage fluid dram of liquid discharge pipe is positioned at the top of hybrid reaction groove 21, is entered by the liquid that the first separating centrifuge 17 is separated in hybrid reaction groove 21 to react with chemical reagent to generate solid lead sulfide.The slag charge that first separating centrifuge 17 is separated then is discharged from discharge port.Water supply installation is connected with hybrid reaction groove 21, for reaction provides solvent.Second separating centrifuge 22 establishes opening for feed, liquid outlet and discharge port.The opening for feed that the discharge gate of hybrid reaction groove 21 is connected with the second separating centrifuge 22 connects, and is sent in the second separating centrifuge 22 by the material that reaction generates and carries out centrifugation, and the liquid of gained and solid are discharged from liquid outlet and discharge port respectively.
Ball mill 18, filter vat 19 and pressure filter 20 is provided with between first separating centrifuge 17 and hybrid reaction groove 21.Ball mill 18, filter vat 19 are connected along Flow of Goods and Materials direction successively with pressure filter 20.The discharge port of the first separating centrifuge 17 is connected with the opening for feed of ball mill 18.The liquid outlet of pressure filter 20 is connected with hybrid reaction groove 21, and be wherein provided with filter screen 26 in filter vat 19, filter screen 26 is obliquely installed to fluid flow direction.Slag charge from the first separating centrifuge 17 enters in ball mill 18 and grinds, then enter filter vat 19 filtering separation slurry and ball-milling medium, slurry out enters pressure filter 20 afterwards from filter vat 19 and carries out press filtration, liquid enters in hybrid reaction groove 21, and filter residue is disposed to the tailings receiving tank 29 of slag-drip opening placement from the slag-drip opening of pressure filter 20 as tailings.
Filter screen 26 one end in filter vat 19 is fixed on the bottom land of that side of filter vat feed end, and the other end is then fixed on groove top.Filter screen 26 becomes 30 ° with the left surface of filter vat, and when ball-milling medium and slurry constantly flow in filter vat 19, ball-milling medium is deposited on the left side of filter screen 26, and slurry flows in the space of opposite side by filter screen, and ball-milling medium is separated fully with slurry.
Also comprise water glass concentrating unit in the present embodiment, this water glass concentrating unit is the open container 25 being provided with well heater 28.Well heater 28 is arranged on container outer wall.Fluid inlet and liquid outlet are established in the bottom of open container 25, the liquid outlet connected drainage pipe of the second separating centrifuge 22, the outlet end of liquid discharge pipe is positioned at the top of open container 25, the liquid separated is entered heating in open container 25 concentrated, be then disposed to water glass gathering barrel 31 from liquid outlet.
Rinse bath 23 and pressure filter 24 is provided with between second separating centrifuge 22 and water glass concentrating unit.Rinse bath 23 is a casing, opening for feed and water-in are established in its top, bottom sets out the mouth of a river, its opening for feed is connected with the slag notch of the second separating centrifuge 22, water-in is then connected with water supply installation, adds water to clean solid lead sulfide in rinse bath 23, and the water after cleaning and solid lead sulfide flow into press filtration in pressure filter 24, in influent liquid stream glass concentrating unit, solid lead sulfide is then disposed to the lead sulfide receiving tank 30 placed below slag-drip opening from the slag-drip opening of pressure filter 24.
Water supply installation in dissolver, extraction element and water glass concentrating unit is the water circle device of melting granulating unit, the water outlet of the water tank 12 of water circle device establishes an arm, this arm establishes three secondary arms, wherein a secondary arm is positioned at directly over hybrid reaction groove 21, other two secondary arms are connected with the water-in of autoclave 16 and the water-in of rinse bath 23 respectively, and secondary arm is provided with valve 36.
Workshop ceiling arranges gas treating system, and this gas treating system comprises exhaust duct 32, condenser 33 and gas-cleaning installation 34, and the exhaust outlet of exhaust duct 32 connects condenser 33, and condenser 33 is connected with gas-cleaning installation 34.Exhaust duct 32 is arranged on the ceiling of workshop, the blast inlet of this exhaust duct is provided with several extraction hood, for absorbing the waste gas produced in operation process, waste gas successively enters condenser 33 through exhaust duct 32 and gas-cleaning installation 34 processes, and is then disposed in air.
In the present embodiment, can adopt and manually send in shredding unit by leaded cullet, so only need establish material loading stair 4 on shredding unit side, operator can take the stairs up, and are poured in shredding unit by leaded cullet.Also can feeding unit be set, as lift, conveying belt etc., leaded cullet be sent in shredding unit.
Workshop ceiling is also arranged means of illumination and camera 2, means of illumination is used for providing illumination to workshop if desired, and the effect of camera is used to Real Time Observation workshop operation state, conveniently finds problem fast when production line breaks down and keeps in repair.
Online component detection apparatus 37 is connected with intelligent controlling device 1.Intelligent controlling device 1 controls operation and the stopping of each device, composition in online component detection apparatus 37 detection slag charges or solution, detected result is delivered to intelligent controlling device 1, intelligent controlling device 1 controls the charging capacity of material and chemical reagent in dosing case 9, dosing case 15, hybrid reaction groove 21 according to detected result.
The utility model can be summarized with other the specific form without prejudice to spirit of the present utility model or principal character.Above-mentioned embodiment of the present utility model all can only be thought explanation of the present utility model instead of restriction, therefore every above embodiment is done according to flesh and blood of the present utility model any trickle amendment, equivalent variations and modification, all belong in the scope of technical solutions of the utility model.
Claims (10)
1. a leaded cullet resource utilization remanufacture line, is characterized in that, comprise shredding unit, melting granulating unit, dissolver and meticulous extraction element, described shredding unit, melting granulating unit, dissolver are connected successively with meticulous extraction element.
2. leaded cullet resource utilization remanufacture line according to claim 1, it is characterized in that, described shredding unit is two cover shredding units, comprise primary mill and type fine disintegrating machine, between described primary mill and type fine disintegrating machine, lift is set, the discharge port of described type fine disintegrating machine is connected with described melting granulating unit by lift, the material through fine crushing process is delivered to the process of melting granulating unit.
3. leaded cullet resource utilization remanufacture line according to claim 1, it is characterized in that, described melting granulating unit comprises dosing case, molten bath, shrend discharge device and water circle device, the bottom of described dosing case is provided with discharge port, and described molten bath is positioned at immediately below the discharge port of dosing case, material dosing after fine crushing process drops in molten bath and carries out melting by described dosing case, discharge gate is established in the bottom in described molten bath, described shrend discharge device comprises water quenching box, opening for feed is established in the bottom of this water quenching box, water-in and water port, top is provided with the discharge gate for being connected with dissolver, the top of described water circle device sets out the mouth of a river, be connected with the water-in of shrend discharge device, its underpart is then provided with water-in, for being connected with the water port of described shrend discharge device, described water circle device constantly send water toward shrend discharge device, shrend is carried out to the liquation entering water quenching box, liquation meets cold formation frit, frit is discharged from discharge gate, enter dissolver.
4. leaded cullet resource utilization remanufacture line according to claim 1, it is characterized in that, described dissolver comprises frit pulverizer, dosing case, autoclave and water supply installation, lift is provided with between described frit pulverizer and dosing case, frit powder after pulverizing is sent in dosing case by lift, described autoclave is positioned at the below of dosing case discharge port, its opening for feed is connected with the discharge port of dosing case, quantitative frit powder is sent in autoclave and processes, described water supply installation is connected with autoclave, for supplying water in still, the dissolving of hydro-thermal high pressure is carried out to material.
5. leaded cullet resource utilization remanufacture line according to claim 1, it is characterized in that, described meticulous extraction element comprises the first separating centrifuge, there is the hybrid reaction groove of stirring rake, water supply installation and the second separating centrifuge, opening for feed established by described first separating centrifuge, liquid outlet and discharge port, described opening for feed is connected with the discharge gate of autoclave, material from autoclave is separated in the first separating centrifuge, described liquid outlet connected drainage pipe, the leakage fluid dram of liquid discharge pipe is positioned at the top of hybrid reaction groove, the liquid that first separating centrifuge is separated is entered in hybrid reaction groove to react with chemical reagent and generates sulfuration lead, the slag charge that first separating centrifuge is separated then is discharged from discharge port, described water supply installation is connected with hybrid reaction groove, for reaction provides solvent, described second separating centrifuge establishes opening for feed, liquid outlet and discharge port, the opening for feed that the discharge gate of described hybrid reaction groove is connected with the second separating centrifuge connects, sent in the second separating centrifuge by the material that reaction generates and carry out centrifugation, the liquid of gained and solid are discharged from liquid outlet and discharge port respectively.
6. leaded cullet resource utilization remanufacture line according to claim 5, it is characterized in that, ball mill is provided with between described first separating centrifuge and hybrid reaction groove, filter vat and pressure filter, described ball mill, filter vat is connected along Flow of Goods and Materials direction successively with pressure filter, the described discharge port of the first separating centrifuge is connected with the opening for feed of ball mill, the liquid outlet of pressure filter is connected with hybrid reaction groove, filter screen is provided with in wherein said filter vat, described filter screen tilts to liquid flow direction, slag charge from the first separating centrifuge enters grinding in ball grinder, then enter filter vat filtering separation slurry and ball-milling medium, slurry out enters pressure filter afterwards from filter vat and carries out press filtration, liquid enters in hybrid reaction groove, filter residue is disposed to the tailings receiving tank of slag-drip opening placement from the slag-drip opening of pressure filter as tailings.
7. leaded cullet resource utilization remanufacture line according to claim 6, it is characterized in that, also comprise water glass concentrating unit, this water glass concentrating unit is the open container being provided with well heater, described well heater is arranged on container outer wall, and fluid inlet and liquid outlet are established in the bottom of described open container, the liquid outlet connected drainage pipe of described second separating centrifuge, the outlet end of described liquid discharge pipe is positioned at the top of described open container, the liquid separated is entered heating in open container concentrated.
8. leaded cullet resource utilization remanufacture line according to claim 7, it is characterized in that, rinse bath and pressure filter is provided with between described second separating centrifuge and water glass concentrating unit, described rinse bath is a casing, opening for feed and water-in are established in its top, bottom sets out the mouth of a river, described opening for feed is connected with the slag notch of the second separating centrifuge, water-in is then connected with water supply installation, add water in rinse bath and solid lead sulfide cleaned, water after cleaning and solid lead sulfide flow into press filtration in pressure filter, in influent liquid stream glass concentrating unit, solid lead sulfide is then disposed to from the slag-drip opening of pressure filter in the lead sulfide receiving tank of slag-drip opening placement.
9. the leaded cullet resource utilization remanufacture line according to any one of claim 4 ~ 8, it is characterized in that, water supply installation in described dissolver, extraction element and water glass concentrating unit is the water circle device of melting granulating unit, its water outlet establishes an arm, this arm establishes three secondary arms, these three secondary arms are connected with autoclave, hybrid reaction groove and rinse bath respectively, and secondary arm is provided with valve.
10. leaded cullet resource utilization remanufacture line according to claim 9, it is characterized in that, also comprise gas treating system, this gas treating system comprises exhaust duct, condenser and gas-cleaning installation, the exhaust outlet of exhaust duct connects condenser, condenser is then connected with gas-cleaning installation, described exhaust duct is arranged on the ceiling of workshop, the blast inlet of this exhaust duct is provided with several extraction hood, for absorbing the waste gas produced in operation process, waste gas successively enters condenser and gas-cleaning installation process through exhaust duct, is then disposed in air; Also comprise means of illumination and camera, described means of illumination and camera are arranged on the ceiling of workshop; Also comprise online component detection apparatus and intelligent controlling device, described online component detection apparatus is connected with control device, described intelligent controlling device controls operation and the stopping of each device, described online component detection apparatus detects the composition in slag charge or solution, detected result is delivered to control device, and control device calculates material throwing amount according to detected result.
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| CN201420838662.1U CN204454657U (en) | 2014-12-25 | 2014-12-25 | A kind of leaded cullet resource utilization remanufacture line |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104649313A (en) * | 2014-12-25 | 2015-05-27 | 中国电器科学研究院有限公司 | Lead-containing waste glass resource recovering production line |
| CN109226203A (en) * | 2018-10-22 | 2019-01-18 | 湖南机电职业技术学院 | Powder processing system and processing method are discarded in a kind of machine-building |
-
2014
- 2014-12-25 CN CN201420838662.1U patent/CN204454657U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104649313A (en) * | 2014-12-25 | 2015-05-27 | 中国电器科学研究院有限公司 | Lead-containing waste glass resource recovering production line |
| CN104649313B (en) * | 2014-12-25 | 2016-05-18 | 中国电器科学研究院有限公司 | A kind of leaded cullet resource remanufacture line |
| CN109226203A (en) * | 2018-10-22 | 2019-01-18 | 湖南机电职业技术学院 | Powder processing system and processing method are discarded in a kind of machine-building |
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