CN1916134A - Solid liquid mixing fuel in use for melt kiln for founding glass - Google Patents
Solid liquid mixing fuel in use for melt kiln for founding glass Download PDFInfo
- Publication number
- CN1916134A CN1916134A CN 200610069803 CN200610069803A CN1916134A CN 1916134 A CN1916134 A CN 1916134A CN 200610069803 CN200610069803 CN 200610069803 CN 200610069803 A CN200610069803 A CN 200610069803A CN 1916134 A CN1916134 A CN 1916134A
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- CN
- China
- Prior art keywords
- fuel
- solid
- oil
- glass
- liquid mixed
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- 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.)
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- 239000000446 fuel Substances 0.000 title claims abstract description 54
- 239000007788 liquid Substances 0.000 title claims abstract description 27
- 239000011521 glass Substances 0.000 title claims abstract description 26
- 239000007787 solid Substances 0.000 title claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000002006 petroleum coke Substances 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 4
- 239000000203 mixture Substances 0.000 claims description 9
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 239000006185 dispersion Substances 0.000 claims description 3
- 238000002844 melting Methods 0.000 abstract description 12
- 230000008018 melting Effects 0.000 abstract description 12
- 239000007789 gas Substances 0.000 abstract description 7
- 239000000295 fuel oil Substances 0.000 abstract description 6
- 239000003245 coal Substances 0.000 abstract description 2
- 239000002270 dispersing agent Substances 0.000 abstract 1
- 239000000843 powder Substances 0.000 abstract 1
- 238000005728 strengthening Methods 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 25
- 238000004519 manufacturing process Methods 0.000 description 11
- 239000002817 coal dust Substances 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 230000005855 radiation Effects 0.000 description 4
- 239000007790 solid phase Substances 0.000 description 4
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000004945 emulsification Methods 0.000 description 3
- 239000004533 oil dispersion Substances 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000003911 water pollution Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000011280 coal tar Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000010742 number 1 fuel oil Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000010913 used oil Substances 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- 235000009508 confectionery Nutrition 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
Abstract
This invention relates to a solid-liquid mixed fuel for glass melting furnace. The solid-liquid mixed fuel is mixed from petroleum coke powder 5-80 wt.% and fuel oil 20-95 wt.%. In addition, according to the weight of the solid-liquid mixed fuel, water less than 30 wt.%, emulsifier less than 3 wt.% and dispersant less than 3 wt.% can also be added. This invention uses petroleum coke powder as a substitute for coal powder in the traditional solid-liquid mixed fuel, thus increasing the content of three-atom gases in the flame, improving the flame radiance, and strengthening the radial heat transfer from the flame to the glass liquid. Besides, the solid-liquid mixed fuel can be used in conventional glass melting furnace, thus having a high profit.
Description
Technical field:
The present invention relates to propellant combination and application thereof, specifically a kind of solid liquid mixing fuel in use for melt kiln for founding glass.
Background technology:
We know, at present in glass industry, the used fuel of melting furnaces fusion cast glass is nothing more than following several: heavy oil, residual oil or other oil fuel, Sweet natural gas, producer gas or coke-oven gas, because the related products price of oil and coal is constantly soaring in recent years, makes above-mentioned fuel cost proportion in the glass manufacturing cost significantly improve.
Summary of the invention:
The objective of the invention is to overcome above-mentioned the deficiencies in the prior art, a kind of solid liquid mixing fuel in use for melt kiln for founding glass is provided, on original melting furnaces of making fuel with fuel oil, utilize original firing system equipment, under not increasing pollutant emission and not increasing prerequisite to the refractory corrosion of kiln body, reduce fuel cost significantly, thereby reduce the manufacturing cost of glass widely.
The present invention can reach by following measure:
A kind of solid liquid mixing fuel in use for melt kiln for founding glass is characterized in that being mixed by petroleum coke powder, oil fuel, and the weight percent of petroleum coke powder and oil fuel is petroleum coke powder 5%～80%, oil fuel 20%～95%.
The used oil fuel of the present invention can be crude oil, heavy oil, residual oil, coal tar or various vegetable and animals oils.
Since in the liquid fuel all in various degree contain moisture content, when acting as a fuel use, to carry out processed to it in the past, thereby produced harmful sewage that oil-containing contains phenol etc., polluted environment, the present invention does not only carry out the processed of oil fuel, avoided the water pollution, and can be less than 30% water by the weight percent adding of each composition.
The present invention can also be less than 3% emulsifying agent by the weight percent adding of each composition and be less than 3% dispersion agent in addition, by emulsification and stirring moisture is entered equably and formed water in oil dispersion state in the oil, when high-temp combustion, produce " microexplosion " effect, further disperseed oil droplet, feasible burning is more abundant, improve thermo-efficiency, reduced smoke pollution.
In addition, be superheated vapour, increased the content of three atomic gas in the flame, improved the flame radiation rate, thereby strengthened the radiative transfer of flame, further improved thermo-efficiency metal level owing to water is vaporized into.
Advantageous effect of the present invention is:
First characteristics are: replaced in the Solid-liquid Mixed Fuel in the past coal dust as solid phase with petroleum coke powder.Its reason is as follows: our home-made refinery coke mean calorie is 2022KJ/kg (8453kcal/kg), and typical component is 90% carbon; 4% hydrogen; 2.1% nitrogen; 1.9% sulphur; 1.82% oxygen; 0.18% ash content.But ash oontent is mostly 8%～20% in coal dust usually, and the calorific value of coal dust has only 1435～1674KJ/kg (6000～7000kcal/kg).So big ash oontent and lower calorific value make that Solid-liquid Mixed Fuel in the past, that with the coal dust be solid phase can't be as directly entering the glass melter burnt fuel, a large amount of ash contents not only makes defectives such as the glassy product generation is painted, fault, but also can stop up the regenerator and the flue of melting furnaces, make melting furnaces normally to move.In addition, lower calorific value also can make the melting rate of melting furnaces reduce, thereby has reduced the output of whole production line glass.
Second characteristic is: since in the liquid fuel all in various degree contain moisture content, to carry out processed to it when using acting as a fuel in the past, thereby produce harmful sewage that oil-containing contains phenol etc., polluted environment.The present invention does not only carry out the processed of oil fuel, avoided the water pollution, but also to mix an amount of moisture, by emulsification and stirring moisture is entered equably and formed water in oil dispersion state in the oil, when high-temp combustion, produce " microexplosion " effect, further disperseed oil droplet, make that burning is more abundant, improve thermo-efficiency, reduced smoke pollution.In addition, be superheated vapour, increased the content of three atomic gas in the flame, improved the flame radiation rate, thereby strengthened the radiative transfer of flame, further improved thermo-efficiency metal level owing to water is vaporized into.We use coal oil mixture and above-mentioned novel Solid-liquid Mixed Fuel to do type approval test respectively on large-scale floatation glass production line.Owing to use novel Solid-liquid Mixed Fuel under the prerequisite that does not influence quality and output, reduce achieving noticeable achievement of fuel cost, so we still use this kind fuel ordinary production on two large-scale floatation glass production lines so far.
In addition, the present invention has utilized the firing system equipment of original fuel oil glass melter as much as possible, makes glass works just can use this novel Solid-liquid Mixed Fuel instead under the state that does not stop production, and obtains very considerable economic.
Embodiment:
Below in conjunction with the present invention is further described:
A kind of solid liquid mixing fuel in use for melt kiln for founding glass, mix by petroleum coke powder, oil fuel, the weight percent of petroleum coke powder and oil fuel is petroleum coke powder 5%～80%, oil fuel 20%～95%, the used oil fuel of the present invention can be crude oil, heavy oil, residual oil, coal tar or various vegetable and animals oils, and the present invention has replaced in the Solid-liquid Mixed Fuel in the past coal dust as solid phase with petroleum coke powder.Its reason is as follows: our home-made refinery coke mean calorie is 2022KJ/kg (8453kcal/kg), and typical component is 90% carbon; 4% hydrogen; 2.1% nitrogen; 1.9% sulphur; 1.82% oxygen; 0.18% ash content.But ash oontent is mostly 8%～20% in coal dust usually, and the calorific value of coal dust has only 1435～1674KJ/kg (6000～7000kcal/kg).So big ash oontent and lower calorific value make that Solid-liquid Mixed Fuel in the past, that with the coal dust be solid phase can't be as directly entering the glass melter burnt fuel, a large amount of ash contents not only makes defectives such as the glassy product generation is painted, fault, but also can stop up the regenerator and the flue of melting furnaces, make melting furnaces normally to move.In addition, lower calorific value also can make the melting rate of melting furnaces reduce, thereby has reduced the output of whole production line glass.
Since in the liquid fuel all in various degree contain moisture content, to carry out processed to it when using acting as a fuel in the past, thereby produce harmful sewage that oil-containing contains phenol etc., polluted environment.The present invention does not only carry out the processed of oil fuel, avoided the water pollution, and can be less than 30% water by the weight percent adding of each composition, the present invention can also be less than 3% emulsifying agent by the weight percent adding of each composition and be less than 3% dispersion agent in addition, by emulsification and stirring moisture is entered equably and formed water in oil dispersion state in the oil, when high-temp combustion, produce " microexplosion " effect, further disperseed oil droplet, feasible burning is more abundant, improve thermo-efficiency, reduced smoke pollution.Second characteristic of the present invention are: be superheated vapour owing to water is vaporized into, increased the content of three atomic gas in the flame, improved the flame radiation rate, thereby strengthened the radiative transfer of flame to metal level, further improved thermo-efficiency.We use coal oil mixture and above-mentioned novel Solid-liquid Mixed Fuel to do type approval test respectively on large-scale floatation glass production line.Owing to use novel Solid-liquid Mixed Fuel under the prerequisite that does not influence quality and output, reduce achieving noticeable achievement of fuel cost, so we still use this kind fuel ordinary production on two large-scale floatation glass production lines so far.In addition, be superheated vapour, increased the content of three atomic gas in the flame, improved the flame radiation rate, thereby strengthened the radiative transfer of flame, further improved thermo-efficiency metal level owing to water is vaporized into.
Claims (3)
1, a kind of solid liquid mixing fuel in use for melt kiln for founding glass is characterized in that being mixed by petroleum coke powder, oil fuel, and the weight percent of petroleum coke powder and oil fuel is petroleum coke powder 5%～80%, oil fuel 20%～95%.
2, a kind of solid liquid mixing fuel in use for melt kiln for founding glass according to claim 1 is characterized in that being less than 30% water by the weight percent adding of each composition.
3,, it is characterized in that weight percent by each composition adds and be less than 3% emulsifying agent and be less than 3% dispersion agent according to claim 1, one of 2 described a kind of solid liquid mixing fuel in use for melt kiln for founding glass.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100698038A CN100376659C (en) | 2006-08-02 | 2006-08-02 | Solid liquid mixing fuel in use for melt kiln for founding glass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100698038A CN100376659C (en) | 2006-08-02 | 2006-08-02 | Solid liquid mixing fuel in use for melt kiln for founding glass |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1916134A true CN1916134A (en) | 2007-02-21 |
| CN100376659C CN100376659C (en) | 2008-03-26 |
Family
ID=37737201
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100698038A Active CN100376659C (en) | 2006-08-02 | 2006-08-02 | Solid liquid mixing fuel in use for melt kiln for founding glass |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100376659C (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 |
| CN101362972B (en) * | 2007-08-08 | 2012-06-20 | 金晶(集团)有限公司 | Technology for oil coke slurry for float glass tank furnace |
| CN104694192A (en) * | 2014-12-30 | 2015-06-10 | 株洲醴陵旗滨玻璃有限公司 | Diversified composite fuel for glass kiln |
| CN110845119A (en) * | 2019-12-06 | 2020-02-28 | 武汉理工大学 | Method for co-firing petroleum coke powder and heavy oil in float glass kiln |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62232495A (en) * | 1986-04-03 | 1987-10-12 | Nikka Chem Ind Co Ltd | Fuel composition |
| AU612127B2 (en) * | 1986-12-26 | 1991-07-04 | Ube Industries, Ltd. | Solid fuel-water slurry composition and process for the preparation of the same |
| CN1858164A (en) * | 2006-06-06 | 2006-11-08 | 程汝林 | Oil used as industrial fuel |
-
2006
- 2006-08-02 CN CNB2006100698038A patent/CN100376659C/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101362972B (en) * | 2007-08-08 | 2012-06-20 | 金晶(集团)有限公司 | Technology for oil coke slurry for float glass tank furnace |
| 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 |
| CN104694192A (en) * | 2014-12-30 | 2015-06-10 | 株洲醴陵旗滨玻璃有限公司 | Diversified composite fuel for glass kiln |
| CN110845119A (en) * | 2019-12-06 | 2020-02-28 | 武汉理工大学 | Method for co-firing petroleum coke powder and heavy oil in float glass kiln |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100376659C (en) | 2008-03-26 |
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Legal Events
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|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 264200 -516-37, chess Hill Road, Cao Miao zi Town, Lingang Economic and Technological Development Zone, Weihai, Shandong Patentee after: WEIHAI CNG COATED GLASS Co.,Ltd. Address before: 264200 No. 98 Qingdao Middle Road, Weihai Economic and Technological Development Zone, Shandong Province Patentee before: WEIHAI BLUE STAR GLASS GROUP Co.,Ltd. |
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| CP03 | Change of name, title or address | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190402 Address after: 264200 -516-39, chess Hill Road, Cao Miao zi Town, Weihai port economic and Technological Development Zone, Shandong Patentee after: WEIHAI ZHONGBO NEW MATERIAL TECHNOLOGY R & D CO.,LTD. Address before: 264200 -516-37, chess Hill Road, Cao Miao zi Town, Lingang Economic and Technological Development Zone, Weihai, Shandong Patentee before: WEIHAI CNG COATED GLASS Co.,Ltd. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240119 Address after: Room 202, Building 1, No. 66 Sibo Road, Sijing Town, Songjiang District, Shanghai Patentee after: China Glass New Energy (Shanghai) New Materials Technology Development Co.,Ltd. Address before: 264200 -516-39, chess Hill Road, Cao Miao zi Town, Weihai port economic and Technological Development Zone, Shandong Patentee before: WEIHAI ZHONGBO NEW MATERIAL TECHNOLOGY R & D CO.,LTD. |
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| TR01 | Transfer of patent right |