CN1986462A - Using method and apparatus for petroleum coke powder fuel for smelting glass - Google Patents
Using method and apparatus for petroleum coke powder fuel for smelting glass Download PDFInfo
- Publication number
- CN1986462A CN1986462A CN 200610098033 CN200610098033A CN1986462A CN 1986462 A CN1986462 A CN 1986462A CN 200610098033 CN200610098033 CN 200610098033 CN 200610098033 A CN200610098033 A CN 200610098033A CN 1986462 A CN1986462 A CN 1986462A
- Authority
- CN
- China
- Prior art keywords
- fuel
- petroleum coke
- coke powder
- transfer lime
- burner
- 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
Images
Abstract
The present invention discloses one kind of petroleum coke powder fuel for smelting glass and its using method and apparatus. The using method includes the steps of screening fuel, crushing, grinding, eliminating iron, drying and burning. The apparatus includes one feeding machine, one powder feeder, one mixer, one first conveying pipe, one first burner, one gas storage tank and one kiln connected successively. The present invention can reach the technological requirement of smelting glass and has lowered production cost.
Description
Technical field
The present invention relates to a kind of using method and equipment of fuel, relate in particular to a kind of using method and equipment that is used for the petroleum coke powder fuel of melten glass.
Background technology
At present, the tank furnace that China glass manufacturing works fusion cast glass is used, annealing furnace and the used fuel of baking flower stove have following a few class: heavy oil, coal tar, Sweet natural gas, producer gas, the burnt slurry of water etc., heavy oil, incendiary calorific value height, national most glasswork all is the main fuel of fusion cast glass and annealing baking flower with heavy oil before 3 or four years, but in recent years along with the continuous rising of International Crude Oil, factory changes one after another burns the cheap coal tar of price comparison, the output of coal tar declines to a great extent now, price rises, about 1400 yuan per ton from June, 2005 have risen to about 3000 yuan per ton up till now, fuel accounts for about 1/3 in the production cost of glasswork, and therefore many glasswories stop production or dwindle industrial scale.Producer gas is because calorific value is low, and the glass melting rate is low, and general glasswork near the coal-producing area uses more.Easy to use and the cleaning of Sweet natural gas, but price height, factory can't bear.The producer that also has imitates the burning way of coal water slurry boiler in order to reduce fuel cost, converts water with the refinery coke of pulverizing, and add thickening stabilizer and make water Jiao slurry as tank furnace, annealing furnace, the fuel of baking flower stove, but consume greatly, and influence the whiteness of glass.
Summary of the invention
The invention provides a kind ofly as seen reduce cost, the using method and the equipment of petroleum coke powder fuel simple to operate.
The present invention adopts following technical scheme:
A kind of using method that is used for the petroleum coke powder fuel of melten glass, this method may further comprise the steps:
1. fuel screening of step: the foreign material in the refinery coke are removed,
Step 3. fuel is ground: the refinery coke coarse grain is ground, and obtaining granularity behind the mill is 150~1000 purpose petroleum coke powders,
4. fuel deironing of step: the petroleum coke powder that 3. step is obtained carries out deironing by magnetic field to be handled, obtain iron-holder less than ten thousand/ petroleum coke powder,
Step is the fuel drying 5.: petroleum coke powder fuel carried out drying treatment, makes the water-in-fuel amount less than 8%,
Step is transport of fuel 6.: the petroleum coke powder transport of fuel is arrived the powder feeding machine,
Step is the pre-mixing of fuel and air 7.: carry out pre-mixing at mixing tank PetroChina Company Limited. coke powder fuel and air,
Step 8. fuel is carried: utilizes the pressurized air in first transfer lime, petroleum coke powder fuel and air is transported to first burner,
Step is fuel combustion 9.: petroleum coke powder that sprays from first burner and air admission kiln also burn in kiln.
A kind of use equipment that is used for the petroleum coke powder fuel of melten glass, comprise feeding machine, powder feeding machine, mixing tank, first transfer lime, first burner, gas-holder, kiln, wherein the discharge port of feeding machine links to each other with the opening for feed of powder feeding machine, the discharge port of powder feeding machine links to each other with the opening for feed of mixing tank, first transfer lime is connected on the gas-holder, first transfer lime is provided with opening for feed and this opening for feed communicates with the discharge port of mixing tank, first burner is located at the exit of first transfer lime, the discharge port of first burner and the feeding inlet of kiln.
Compared with prior art, the present invention has the following advantages:
1, the present invention can reduce cost.The employing petroleum coke powder acts as a fuel, compare with fuel such as heavy oil, coal tar, Sweet natural gas, producer gas, the burnt slurries of water, can reduce production costs, with the fuel of petroleum coke powder as melten glass, compared with other fuel,, has good price advantage as heavy oil, coal tar, Sweet natural gas etc., reduce the cost of fuel, also just made the manufacturing cost of glass reduce greatly; If directly petroleum coke powder is burnt, then because the iron-holder in the petroleum coke powder is higher, can directly have influence on the whiteness of glass, do not reach the processing requirement of melten glass, since the iron-holder of the petroleum coke powder fuel that obtains of the technical solution used in the present invention less than ten thousand/, so not only can reduce cost when being used for melten glass but also can reach the processing requirement of melten glass, kept the whiteness of glass.
2, the present invention can make the petroleum coke powder full combustion of fuel, has improved utilization ratio of raw materials.Petroleum coke powder fuel can evenly be stirred the screw feeder from feeding machine, after fuel enters the powder feeding machine, after evenly being screened, powder feeding machine PetroChina Company Limited. coke powder fuel enters in the mixing tank, in mixing tank, finish the pre-mixing of fuel and gas, by transfer lime, petroleum coke powder fuel mixes once more with the mixture and the gas of gas, just makes the ratio of mixture of fuel and gas reach optimum value, help the abundant burning of petroleum coke powder fuel, improved the utilization ratio of fuel.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the structural representation of first burner, second burner.
Fig. 3 is that the A-A of Fig. 2 is to sectional view.
Fig. 4 is the structural representation of magnetic filter.
Embodiment
A kind of using method that is used for the petroleum coke powder fuel of melten glass, this method may further comprise the steps:
1. fuel screening of step: the foreign material in the refinery coke are removed,
Step 3. fuel is ground: the refinery coke coarse grain is ground, and obtaining granularity behind the mill is 150~1000 purpose petroleum coke powders,
4. fuel deironing of step: the petroleum coke powder that 3. step is obtained carries out deironing by magnetic field to be handled, obtain iron-holder less than ten thousand/ petroleum coke powder,
Step is the fuel drying 5.: petroleum coke powder fuel carried out drying treatment, makes the water-in-fuel amount less than 8%,
Step is transport of fuel 6.: the petroleum coke powder transport of fuel is arrived powder feeding machine 4,
Step is the pre-mixing of fuel and air 7.: carry out pre-mixing at mixing tank 5 PetroChina Company Limited.'s coke powder fuel and air,
Step 8. fuel is carried: utilizes the pressurized air in first transfer lime 10, petroleum coke powder fuel and air is transported to first burner 6,
Step is fuel combustion 9.: the petroleum coke powder of ejection and air admission kiln 20 and burn for 20 li at kiln from first burner 6.
Wherein step transport of fuel 6. can be finished by screw feeder.
A kind of use equipment that is used for the petroleum coke powder fuel of melten glass, comprise feeding machine 3, powder feeding machine 4, mixing tank 5, first transfer lime 10, first burner 6, gas-holder 7, kiln 20, wherein the discharge port of feeding machine 3 links to each other with the opening for feed of powder feeding machine 4, the discharge port of powder feeding machine 4 links to each other with the opening for feed of mixing tank 5, first transfer lime 10 is connected on the gas-holder 7, first transfer lime 10 is provided with opening for feed and this opening for feed communicates with the discharge port of mixing tank 5, first burner 6 is located at the exit of first transfer lime 10, the feeding inlet of the discharge port of first burner 6 and kiln 20, on the opening for feed of feeding machine 3, be provided with feed bin 1, top at the discharge port of feed bin 1 is provided with variable valve 2, on gas-holder 7, be connected with second transfer lime 15, the exit of second transfer lime 15 is provided with second burner 18, and the feeding inlet of the discharge port of second burner 18 and kiln 20, on first transfer lime 10, be provided with the first pipeline pressure table 12 and first pipe break valve 13, the end that is provided with the second pipeline pressure table 16 and second pipe break valve, 17, the first transfer limes 10 on second transfer lime 15 is provided with magnetic filter 21.
In the present embodiment, can be by regulating the outer air-valve 22 on first burner and second burner, eddy flow air-valve 23 and center air-valve 24, the length of flame that forms after the petroleum coke powder fuel combustion of feasible ejection remains on about 2/3 of molten pool length, and the flame juxtaposition neither that makes the ejection of adjacent burner, can form maximum coverage rate to metal level again, the consumption of petroleum coke powder fuel can be regulated by the rotating speed of screw feeder, in addition, the caliber of first transfer lime can be selected according to the size of petroleum coke powder flow fuel, because swiftly flowing petroleum coke powder is bigger to the wearing and tearing of tube wall, therefore first transfer lime should be selected posted sides pipeline, and reduce elbow as far as possible, particularly 90 degree are straight curved, therefore can remove irony owing to be provided with magnetic filter because of pipe wear band people at the end of first transfer lime, reduced coloration effects to a greater extent, kept the whiteness of glass, thereby reached the processing requirement of melten glass glass metal.
Claims (8)
1, a kind of using method that is used for the petroleum coke powder fuel of melten glass is characterized in that this method may further comprise the steps:
1. fuel screening of step: the foreign material in the refinery coke are removed,
Step 2. fuel is pulverized: with crusher refinery coke pulverized, obtained the refinery coke coarse grain of granularity less than 25mm,
Step 3. fuel is ground: the refinery coke coarse grain is ground, and obtaining granularity behind the mill is 150~1000 purpose petroleum coke powders,
4. fuel deironing of step: the petroleum coke powder that 3. step is obtained carries out deironing by magnetic field to be handled, obtain iron-holder less than ten thousand/ petroleum coke powder,
Step is the fuel drying 5.: petroleum coke powder fuel carried out drying treatment, makes the water-in-fuel amount less than 8%,
Step is transport of fuel 6.: the petroleum coke powder transport of fuel is arrived powder feeding machine (4),
Step is the pre-mixing of fuel and air 7.: carry out pre-mixing at mixing tank (5) PetroChina Company Limited.'s coke powder fuel and air,
Step 8. fuel is carried: utilizes the pressurized air in first transfer lime (10), petroleum coke powder fuel and air is transported to first burner (6),
Step is fuel combustion 9.: petroleum coke powder and the air admission kiln that sprays from first burner (6) also burns in kiln.
2, the using method that is used for the petroleum coke powder fuel of melten glass according to claim 1 is characterized in that step transport of fuel 6. can be finished by screw feeder.
3, a kind of use equipment that is used for the petroleum coke powder fuel of melten glass, it is characterized in that comprising feeding machine (3), powder feeding machine (4), mixing tank (5), first transfer lime (10), first burner (6), gas-holder (7), kiln (20), wherein the discharge port of feeding machine (3) links to each other with the opening for feed of powder feeding machine (4), the discharge port of powder feeding machine (4) links to each other with the opening for feed of mixing tank (5), first transfer lime (10) is connected on the gas-holder (7), first transfer lime (10) is provided with opening for feed and this opening for feed communicates with the discharge port of mixing tank (5), first burner (6) is located at the exit of first transfer lime (10), the feeding inlet of the discharge port of first burner (6) and kiln (20).
4, the use equipment that is used for the petroleum coke powder fuel of melten glass according to claim 3 is characterized in that being provided with feed bin (1) on the opening for feed of feeding machine (3).
5, the use equipment that is used for the petroleum coke powder fuel of melten glass according to claim 4 is characterized in that being provided with variable valve (2) on the top of the discharge port of feed bin (1).
6, the use equipment that is used for the petroleum coke powder fuel of melten glass according to claim 5, it is characterized in that on gas-holder (7), being connected with second transfer lime (15), the exit of second transfer lime (15) is provided with second burner (18), and the feeding inlet of the discharge port of second burner (18) and kiln (20).
7, the use equipment that is used for the petroleum coke powder fuel of melten glass according to claim 6, it is characterized in that on first transfer lime (10), being provided with the first pipeline pressure table (12) and first pipe break valve (13), on second transfer lime (15), be provided with the second pipeline pressure table (16) and second pipe break valve (17).
8, the use equipment that is used for the petroleum coke powder fuel of melten glass according to claim 7 is characterized in that the end of first transfer lime (10) is provided with magnetic filter (21).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200610098033 CN1986462A (en) | 2006-11-28 | 2006-11-28 | Using method and apparatus for petroleum coke powder fuel for smelting glass |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200610098033 CN1986462A (en) | 2006-11-28 | 2006-11-28 | Using method and apparatus for petroleum coke powder fuel for smelting glass |
Publications (1)
Publication Number | Publication Date |
---|---|
CN1986462A true CN1986462A (en) | 2007-06-27 |
Family
ID=38183424
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200610098033 Pending CN1986462A (en) | 2006-11-28 | 2006-11-28 | Using method and apparatus for petroleum coke powder fuel for smelting glass |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1986462A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101948708A (en) * | 2010-10-12 | 2011-01-19 | 张家港华汇特种玻璃有限公司 | Solid fuel composition and application thereof in glass melting |
CN102060430A (en) * | 2010-12-02 | 2011-05-18 | 上海福莱特玻璃有限公司 | Combustion method for solar super-white embossed glass melting furnace and fuel distribution system |
CN102311826A (en) * | 2011-08-18 | 2012-01-11 | 内蒙古霍煤通顺碳素有限责任公司 | Substituted fuel and apparatus of carbon furnace |
CN102765867A (en) * | 2012-07-30 | 2012-11-07 | 安徽凤阳玻璃有限公司 | Process using petroleum coke for modified synthesis of carbon powder as float glass furnace fuel |
-
2006
- 2006-11-28 CN CN 200610098033 patent/CN1986462A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101948708A (en) * | 2010-10-12 | 2011-01-19 | 张家港华汇特种玻璃有限公司 | Solid fuel composition and application thereof in glass melting |
CN101948708B (en) * | 2010-10-12 | 2013-01-16 | 张家港华汇特种玻璃有限公司 | Solid fuel composition and application thereof in glass melting |
CN102060430A (en) * | 2010-12-02 | 2011-05-18 | 上海福莱特玻璃有限公司 | Combustion method for solar super-white embossed glass melting furnace and fuel distribution system |
CN102311826A (en) * | 2011-08-18 | 2012-01-11 | 内蒙古霍煤通顺碳素有限责任公司 | Substituted fuel and apparatus of carbon furnace |
CN102311826B (en) * | 2011-08-18 | 2016-05-04 | 内蒙古霍煤通顺碳素有限责任公司 | Carbon baking furnace alternative fuel and equipment |
CN102765867A (en) * | 2012-07-30 | 2012-11-07 | 安徽凤阳玻璃有限公司 | Process using petroleum coke for modified synthesis of carbon powder as float glass furnace fuel |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101955824B (en) | Complete two-stage slurry production equipment of water-coal-slurry and gasified water-coal-slurry by using low-rank coal fuel | |
CN201068344Y (en) | Petroleum coke breeze combustion transmission device for industrial furnace | |
CN101636357B (en) | Process and apparatus for making a mineral melt | |
CN100560519C (en) | On glass melter, use the processing method of petroleum coke fuel | |
CN1986462A (en) | Using method and apparatus for petroleum coke powder fuel for smelting glass | |
CN101280203A (en) | Anthracite carbon casting formed coke | |
CN101956992B (en) | Low rank coal fuel coal water slurry and gasified coal water slurry complete production unit | |
CN201762299U (en) | Complete set of equipment for producing coal water slurry fuel and gasification coal water slurry by low rank coal | |
CN100532590C (en) | Method for producing fine iron sand powder by using ferro-sulphur ore as raw material and equipment thereof | |
CN102311826B (en) | Carbon baking furnace alternative fuel and equipment | |
CN102357420A (en) | Decarburizing method for high-carbon stone coal navajoite | |
CN1986464A (en) | Glass smelting process | |
CN201762298U (en) | Complete set of equipment for producing coal water slurry fuel and gasification coal water slurry by low rank coal in two stages | |
CN102676722B (en) | Smelting method for melting gasifier | |
CN201078698Y (en) | Industry furnace coal dust firing system apparatus | |
CN101362972A (en) | Oil coke slurry for float glass tank furnace and technology thereof | |
CN102901089A (en) | Pulverized coal co-combustion system of industrial boiler | |
CN105776904A (en) | Combustion method of fuel in shaft kiln | |
CN106090978B (en) | A kind of method improving solid fuel utilization rate and its application in sinter production | |
CN201526957U (en) | Industrial furnace fuel pneumatic conveying and blowing burning device | |
CN200958072Y (en) | Petroleum fine coke fuel conveyor | |
CN100545247C (en) | A kind of fuel-oil coking slurry | |
CN201496983U (en) | High-efficiency high-concentration high-rheology coal water slurry device | |
CN1079455A (en) | Adopt the technology of coal water slurry burning ceramics | |
CN201314776Y (en) | Silicon residue sintering furnace |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20070627 |