CN107721144A - Glass factory's integrated energy system - Google Patents
Glass factory's integrated energy system Download PDFInfo
- Publication number
- CN107721144A CN107721144A CN201711047696.3A CN201711047696A CN107721144A CN 107721144 A CN107721144 A CN 107721144A CN 201711047696 A CN201711047696 A CN 201711047696A CN 107721144 A CN107721144 A CN 107721144A
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- China
- Prior art keywords
- module
- electricity generation
- annealing
- generation module
- cleaning
- 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
- 239000011521 glass Substances 0.000 title claims abstract description 40
- 230000005611 electricity Effects 0.000 claims abstract description 58
- 238000000137 annealing Methods 0.000 claims abstract description 49
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 45
- 238000004140 cleaning Methods 0.000 claims abstract description 36
- 239000007789 gas Substances 0.000 claims abstract description 36
- 239000002826 coolant Substances 0.000 claims abstract description 28
- 238000001035 drying Methods 0.000 claims abstract description 22
- 239000003345 natural gas Substances 0.000 claims abstract description 22
- 238000002844 melting Methods 0.000 claims abstract description 11
- 230000008018 melting Effects 0.000 claims abstract description 11
- 239000012530 fluid Substances 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims abstract description 5
- 230000008569 process Effects 0.000 claims abstract description 5
- 230000004927 fusion Effects 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000003949 liquefied natural gas Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 8
- 230000008016 vaporization Effects 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 5
- 230000000505 pernicious effect Effects 0.000 claims description 5
- 238000002485 combustion reaction Methods 0.000 claims description 4
- 238000012545 processing Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims 2
- 239000000110 cooling liquid Substances 0.000 claims 1
- 239000000446 fuel Substances 0.000 abstract description 7
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 239000003245 coal Substances 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 5
- 230000008859 change Effects 0.000 description 3
- 238000004134 energy conservation Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 230000007812 deficiency Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B25/00—Annealing glass products
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C23/00—Other surface treatment of glass not in the form of fibres or filaments
- C03C23/0075—Cleaning of glass
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C23/00—Other surface treatment of glass not in the form of fibres or filaments
- C03C23/0085—Drying; Dehydroxylation
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)
Abstract
The present invention discloses a kind of glass factory's integrated energy system, supplying module, for providing natural gas；Module is founded, module is founded and is connected with supplying module, melting furnace is carried out using natural gas to heat fusion cast glass material；Electricity generation module, electricity generation module are connected with supplying module, are generated electricity using natural gas；Annealing module, blast pipe of the annealing module respectively with supplying module and electricity generation module are connected, and process annealing is carried out to glassware using the heat of tail gas institute band caused by electricity generation module and natural gas；The coolant duct connection of cleaning module, cleaning module and electricity generation module, is heated using the heat of the coolant of electricity generation module to cleaning fluid；Drying module, the coolant duct of drying module and electricity generation module connects, the glassware after cleaning is dried using the heat air of coolant, electricity consumption or the fuel consumption of annealing module, cleaning module and drying module can be reduced, the utilization rate of resource is improved, reduces the wasting of resources and environmental pollution.
Description
Technical field
The present invention relates to integrated energy system technical field, more particularly to a kind of glass factory's integrated energy system.
Background technology
In industrial enterprise, glass factory belongs to high energy consumption, high pollution enterprise, is the key object of energy-saving and emission-reduction, and glass produces
The energy consumption cost accounting of product is higher, main reason is that the passing energy resource structure based on coal in China, from industry development initial stage just
Affect the characteristic of glass factory's energy system design.
Substantial amounts of electric energy is needed to use in the production of glass factory, when regional power grid is powered, due to local power network with
Based on thermal power plant, generate electricity dependent on coal charge consume, burn coal charge when, substantial amounts of CO can be produced2、NOX、SO2, PM particulate matters
Deng the discharge of polluter, high power consumption has encouraged the generation of high pollution, maximum discharge.Simultaneously in net electric system, the hair in region
The electric energy that power station is sent is transported to enterprise's high pressure entry by boosting, by high pressure netting twine, and is used after being depressured, and electric energy have passed through far
The conveying of distance, and multiple energy transformation, primary energy ratio very, generally 40%~50% or so.
In addition, also need to set up in the glass factory using coal as main energy consumption resource gas generator coal charge is handled plus
The supply needs that water-gas meets melting furnace and annealing kiln are made after work, equally can produce substantial amounts of CO because of the burning of coal charge2、
NOX、SO2, the polluter such as PM particulate matters, so as to directly contribute poor, high pollution the environmental issue of discharge.
The content of the invention
It is an object of the invention to：A kind of glass factory's integrated energy system is provided, it can improve the utilization rate of resource, subtract
The few wasting of resources and environmental pollution.
To use following technical scheme up to this purpose, the present invention：
A kind of glass factory's integrated energy system is provided, including：
Supplying module, for providing natural gas；
Module is founded, for heating fusion cast glass material, the module of founding is connected with the supplying module；
Electricity generation module, the electricity generation module are connected with the supplying module；
Annealing module, blast pipe of the annealing module respectively with the supplying module and the electricity generation module are connected, profit
Hot exhaust gas and the heat energy caused by natural gas that burns carry out process annealing to glassware caused by the electricity generation module；
Cleaning module, the cleaning module are connected with the coolant duct of the electricity generation module, utilize the electricity generation module
The heat of coolant cleaning fluid is heated；
Drying module, the drying module are connected with the coolant duct of the electricity generation module, utilize the coolant
Heat air is dried to the glassware after cleaning.
As a kind of preferable technical scheme of this programme, the annealing module includes annealing kiln, is set in the annealing kiln
It is equipped with the combustion gun being connected with the supplying module and the radiating tube being connected with the blast pipe.
As a kind of preferable technical scheme of this programme, some heat emission holes, the radiating are provided with the radiating tube
Pipe is arranged at the bottom of the annealing kiln.
As a kind of preferable technical scheme of this programme, it is provided between the cleaning module and the coolant duct
Heat exchanger, for being heated to the cleaning fluid of the cleaning module.
As a kind of preferable technical scheme of this programme, between the blast pipe of the electricity generation module and the annealing module
Tail gas filter is provided with, for filtering particle and harmful gas in the electricity generation module running in caused tail gas
Body.
As a kind of preferable technical scheme of this programme, it is provided between the drying module and the coolant duct
Fan water tank type radiator, for being heated to the air in drying module.
As a kind of preferable technical scheme of this programme, the connection of the power network of the electricity generation module and glass factory, for pair
The electrical equipment of glass factory is powered.
As a kind of preferable technical scheme of this programme, the air exit end of the melting furnace for founding module sets tail
Flash Gas Compression Skid System, heat exchanger tube and water circulation system.
As a kind of preferable technical scheme of this programme, the supplying module includes zone duct natural gas and liquefaction day
Right gas gasification station.
As a kind of preferable technical scheme of this programme, water bath type gasifier is set in the LNG Vaporizing Station
Liquefied natural gas is gasified.
Beneficial effects of the present invention are：Glass factory is powered using electricity generation module, caused by power generation process
Exhaust heat and coolant heat can provide heat for annealing module, cleaning module and drying module, can reduce annealing module, clearly
The electricity consumption of mold cleaning block and drying module or fuel consumption, the utilization rate of resource is improved, reduce the wasting of resources and environmental pollution.
Brief description of the drawings
The present invention is described in further detail below according to drawings and examples.
Fig. 1 is glass factory's integrated energy system dimensional structure diagram described in embodiment.
In figure：
1st, zone duct natural gas；2nd, LNG Vaporizing Station；3rd, module is founded；4th, electricity generation module；5th, annealing module；
6th, cleaning module；7th, drying module；8th, heat exchanger；9th, fan water tank type radiator；10th, electrical equipment.
Embodiment
Further illustrate technical scheme below in conjunction with the accompanying drawings and by embodiment.
As shown in figure 1, in the present embodiment, a kind of glass factory's integrated energy system of the present invention, including：
Supplying module, for providing natural gas；
Module 3 is founded, for heating fusion cast glass material, the module 3 of founding is connected with the supplying module, to pass through
The supplying module provides the burning energy to the module 3 of founding；
Electricity generation module 4, the electricity generation module 4 are connected with the supplying module, to give the hair by the supplying module
Electric module 4 provides the burning energy and then realized and generates electricity；
Annealing module 5, blast pipe of the annealing module 5 respectively with the supplying module and the electricity generation module 4 are connected,
Process annealing is carried out to glassware using heat energy caused by hot exhaust gas caused by the electricity generation module 4 and burning natural gas；
Cleaning module 6, the cleaning module 6 are connected with the coolant duct of the electricity generation module 4, utilize the generating mould
The heat of the coolant of block 4 heats to cleaning fluid；
Drying module 7, the drying module 7 are connected with the coolant duct of the electricity generation module 4, utilize the coolant
Heat air the glassware after cleaning is dried.
The melting furnace natural gas that directly burns for founding module 3 carries out heating and can ensure the normal working temperature of melting furnace, and
And the product after the burning of natural gas is less with respect to pollution of the coal to air, can reduce air pollution.
Electricity generation module 4 is generated electricity using natural gas, can is that the electrical equipment 10 of glass factory provides electric energy, can be reduced region
The load of power network, good peak load shifting effect is served to regional power grid, enhances operational reliability and the storage of regional power grid
Standby ability.
Module 5 of annealing carries out low temperature using the heat and natural gas of tail gas institute band caused by electricity generation module 4 to glassware
Annealing, the fuel consumption of annealing module 5 can be effectively reduced, so that annealing module 5 reaches energy-conservation, the purpose of emission reduction.
Cleaning module 6 and drying module 7 cool down the heat of institute's band after electricity generation module 4 using the coolant in electricity generation module 4
Heated, the use of electric energy and fuel can be reduced, and the work radiating efficiency of the coolant in electricity generation module 4 can be strengthened,
Incidental heat in coolant can be effectively utilized to be used for cleaning module 6 while ensure that the cooling of electricity generation module 4
With the heating of drying module 7, the resource utilization of glass factory is improved, reduces the wasting of resources, reduces the fuel in production process
Cost.
Preferably, the annealing module 5 includes annealing kiln, is provided with what is be connected with the supplying module in the annealing kiln
Combustion gun and the radiating tube being connected with the blast pipe.
Further, some heat emission holes are provided with the radiating tube, the radiating tube is arranged at the bottom of the annealing kiln
Portion.
Annealing kiln in the annealing module 5 of glass factory is required typically from 350-600 DEG C annealing temperature, and electricity generation module 4
The delivery temperature of the middle gas engine to be generated electricity using natural gas is at 350 DEG C~500 DEG C or so, therefore using generating mould
Caused high-temperature exhaust air carries out heat supply to annealing kiln in gas engine running in block 4.
Specifically, the bottom in annealing kiln installs a row or multi-row radiating tube for setting length additional, by gas engine
High-temperature exhaust air is uniformly dissipated after being linked into radiating tube, is discharged to flue gas greatly by high temperature exhaust blower in annealing kiln low-temperature zone
In gas.Combustion gun is additionally provided with annealing kiln simultaneously, when temperature deficiency in annealing kiln, heat is carried out by burning gun burner natural gas
Amount supplement, so as to realize to the heat recovery and utilization of the high-temperature exhaust air institute band of gas engine into annealing kiln, can effectively be reduced
The fuel consumption of annealing kiln, so that annealing kiln reaches energy-conservation, the purpose of emission reduction.
Preferably, heat exchanger 8 is provided between the cleaning module 6 and the coolant duct, for described clear
The cleaning fluid of mold cleaning block 6 is heated.Cleaning module 6 is connected to adding for heat exchanger 8 with the coolant duct
Hot junction and heat energy end.
The heat of institute's band is transferred to after using heat exchanger 8, the coolant in coolant duct is cooled down to electricity generation module 4
In the relatively low cleaning fluid of temperature, the secondary use to the heat of institute's band in coolant is realized, ensure that the cooling of electricity generation module 4
While can effectively utilize incidental heat in coolant to be used for the heating to cleaning module 6 and drying module 7, improve
The resource utilization of glass factory, the wasting of resources is reduced, reduce the fuel cost in production process.
Preferably, tail gas filter is provided between the blast pipe of the electricity generation module 4 and the annealing module 5, used
Particle and pernicious gas in the filtering running of electricity generation module 4 in caused tail gas.
Blast pipe and annealing module 5 between set tail gas filter can to exhaust in institute's band particle and pernicious gas
Filtered, avoid particle and pernicious gas from entering in annealing kiln the quality of production for influenceing glassware, and reduce final row
Pollution of the tail gas gone out to air.
Preferably, fan water tank type radiator 9 is provided between the drying module 7 and the coolant duct, is used for
Air in drying module 7 is heated.
Baking stage after glassware cleaning, using fan water tank type radiator 9 by gas engine cooling water
Heat energy is converted into hot blast, can be achieved to blow bakings to glassware after cleaning, so as to effectively substitute or reduce the heating of drying module 7
Power consumption, baking operation is set to realize energy-conservation, the purpose of emission reduction.
Preferably, the electricity generation module 4 is connected with the power network of glass factory, for supplying the electrical equipment 10 of glass factory
Electricity.
Glass factory powers by the electricity generation module 4 of itself, can meet the power demand of oneself, is supplied without regional power grid
Electricity, local power network coal electricity expenditure is considerably reduced, local power network heat power station Coal-fired capacity has been greatly lowered, so as to effectively drop
The discharge of the polluters such as low CO2, NOX, SO2, PM particulate matter, the energy-saving and emission-reduction career development for locality provide strong branch
Support.
Preferably, the air exit end of the melting furnace for founding module sets exhaust gas processing device, heat exchanger tube and water to follow
Loop system.
Install at the air exit of melting furnace exhaust gas processing device can to the melting furnace course of work in caused tail gas enter
Row processing, reduces dust granules and pernicious gas enters and atmosphere pollution is caused in air, and heat exchanger tube and water circulation system can profits
Water in the tail gas heating water circulation system discharged with melting furnace is transported to the place for needing hot water, improves the resource profit of melting furnace
With rate, the wasting of resources is reduced.
Preferably, the supplying module includes zone duct natural gas 1 and LNG Vaporizing Station 2.
Further, water bath type gasifier is set to gasify liquefied natural gas in the LNG Vaporizing Station 2.
Using area pipe natural gas 1 and LNG Vaporizing Station 2 are supplied simultaneously, can avoid liquefied natural gas gas
Changing 2 amount deficiencies of station causes production to be delayed.Setting up for LNG Vaporizing Station 2 can be sharp while natural gas is provided for glass factory
Heated up with liquefied natural gas and absorb the characteristic of substantial amounts of heat energy in gasification, using water bath type gasifier by liquified natural gas gas
Cold energy during change, cold and hot exchange is carried out using water as heat transferring medium, more than 0 DEG C of low-temperature frozen water can be obtained, be transported to
Need to be used with cold place, such as the refrigerator in dining room or freezer are used for the fresh-keeping of food, or for air-conditioning heat exchange pair
Office cools.
It is to be understood that above-mentioned embodiment is only that presently preferred embodiments of the present invention and institute's application technology are former
Reason, in technical scope disclosed in this invention, change that any one skilled in the art is readily apparent that or
Replace, should all cover within the scope of the present invention.
Above by specific embodiment, the present invention is described, but the present invention is not limited to these specific implementations
Example.It will be understood by those skilled in the art that various modifications, equivalent substitution, change etc. can also be made to the present invention.But this
A little conversion, all should be within protection scope of the present invention without departing from the spirit of the present invention.In addition, present specification and power
Some terms used in sharp claim are not limitation, it is only for are easy to describe.In addition, " one described in above many places
Individual embodiment ", " another embodiment " etc. represent different embodiments, naturally it is also possible to which its all or part is incorporated in into one
In embodiment.
Claims (10)
- A kind of 1. glass factory's integrated energy system, it is characterised in that including：Supplying module, for providing natural gas；Module is founded, for heating fusion cast glass material, the module of founding is connected with the supplying module；Electricity generation module, the electricity generation module are connected with the supplying module；Annealing module, blast pipe of the annealing module respectively with the supplying module and the electricity generation module are connected, and utilize institute Heat energy caused by stating hot exhaust gas caused by electricity generation module and burning natural gas carries out process annealing to glassware；Cleaning module, the cleaning module are connected with the coolant duct of the electricity generation module, utilize the cold of the electricity generation module But the heat of liquid heats to cleaning fluid；Drying module, the drying module are connected with the coolant duct of the electricity generation module, utilize the heat of the coolant Heating air is dried to the glassware after cleaning.
- 2. glass factory's integrated energy system according to claim 1, it is characterised in that the annealing module includes annealing Kiln, the combustion gun being connected with the supplying module and the radiating tube being connected with the blast pipe are provided with the annealing kiln.
- 3. glass factory's integrated energy system according to claim 2, it is characterised in that be provided with the radiating tube some Heat emission hole, the radiating tube are arranged at the bottom of the annealing kiln.
- 4. glass factory's integrated energy system according to claim 1, it is characterised in that the cleaning module and the cooling Liquid pipe is provided with heat exchanger between road, for being heated to the cleaning fluid of the cleaning module.
- 5. glass factory's integrated energy system according to claim 1, it is characterised in that the blast pipe of the electricity generation module with Tail gas filter is provided between the annealing module, for filtering in the electricity generation module running in caused tail gas Particle and pernicious gas.
- 6. glass factory's integrated energy system according to claim 1, it is characterised in that the drying module and the cooling Fan water tank type radiator is provided between liquid pipe road, for being heated to the air in drying module.
- 7. glass factory's integrated energy system according to claim 1, it is characterised in that the electricity generation module and glass factory Power network connects, for being powered to the electrical equipment of glass factory.
- 8. glass factory's integrated energy system according to claim 1, it is characterised in that the melting furnace for founding module Air exit end sets exhaust gas processing device, heat exchanger tube and water circulation system.
- 9. glass factory's integrated energy system according to claim 1, it is characterised in that the supplying module is managed including region Road natural gas and LNG Vaporizing Station.
- 10. glass factory's integrated energy system according to claim 9, it is characterised in that the LNG Vaporizing Station Middle setting water bath type gasifier gasifies to liquefied natural gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711047696.3A CN107721144A (en) | 2017-10-31 | 2017-10-31 | Glass factory's integrated energy system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711047696.3A CN107721144A (en) | 2017-10-31 | 2017-10-31 | Glass factory's integrated energy system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107721144A true CN107721144A (en) | 2018-02-23 |
Family
ID=61202524
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711047696.3A Pending CN107721144A (en) | 2017-10-31 | 2017-10-31 | Glass factory's integrated energy system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107721144A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000205530A (en) * | 1999-01-13 | 2000-07-25 | Babcock Hitachi Kk | Waste gasifying fusing power-generating system |
| CN202902797U (en) * | 2012-09-17 | 2013-04-24 | 上海新奥能源科技有限公司 | Combined heat and power hot air drying system |
| CN204417322U (en) * | 2015-01-05 | 2015-06-24 | 山东金晶科技股份有限公司 | Annealing furnace electrically heated electric supply installation |
| CN105347656A (en) * | 2015-11-27 | 2016-02-24 | 东旭（营口）光电显示有限公司 | Glass kiln, natural gas supply system and heating system thereof and temperature stabilization method |
| CN205907177U (en) * | 2016-06-28 | 2017-01-25 | 信义玻璃（营口）有限公司 | Glass apparatus for producing |
| CN207552169U (en) * | 2017-10-31 | 2018-06-29 | 佛山市派能机电有限公司 | Glass factory's integrated energy system |
-
2017
- 2017-10-31 CN CN201711047696.3A patent/CN107721144A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000205530A (en) * | 1999-01-13 | 2000-07-25 | Babcock Hitachi Kk | Waste gasifying fusing power-generating system |
| CN202902797U (en) * | 2012-09-17 | 2013-04-24 | 上海新奥能源科技有限公司 | Combined heat and power hot air drying system |
| CN204417322U (en) * | 2015-01-05 | 2015-06-24 | 山东金晶科技股份有限公司 | Annealing furnace electrically heated electric supply installation |
| CN105347656A (en) * | 2015-11-27 | 2016-02-24 | 东旭（营口）光电显示有限公司 | Glass kiln, natural gas supply system and heating system thereof and temperature stabilization method |
| CN205907177U (en) * | 2016-06-28 | 2017-01-25 | 信义玻璃（营口）有限公司 | Glass apparatus for producing |
| CN207552169U (en) * | 2017-10-31 | 2018-06-29 | 佛山市派能机电有限公司 | Glass factory's integrated energy system |
Non-Patent Citations (1)
| Title |
|---|
| 兰州企业管理协会: "《工业企业管理简明词典》", 甘肃人民出版社, pages: 465 - 466 * |
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Application publication date: 20180223 |
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