CN86104731A - The production method of glass sphere and equipment - Google Patents
The production method of glass sphere and equipment Download PDFInfo
- Publication number
- CN86104731A CN86104731A CN86104731.1A CN86104731A CN86104731A CN 86104731 A CN86104731 A CN 86104731A CN 86104731 A CN86104731 A CN 86104731A CN 86104731 A CN86104731 A CN 86104731A
- Authority
- CN
- China
- Prior art keywords
- combustion chamber
- air
- flow
- production method
- equipment
- 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.)
- Expired - Lifetime
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/10—Forming beads
- C03B19/1005—Forming solid beads
- C03B19/102—Forming solid beads by blowing a gas onto a stream of molten glass or onto particulate materials, e.g. pulverising
- C03B19/1025—Bead furnaces or burners
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Melting And Manufacturing (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
- Pre-Mixing And Non-Premixing Gas Burner (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
A kind of method and apparatus of producing glass sphere, wherein material fuel and oxidizer spray into combustion chamber 20 from combustion furnace assembly I, and in combustion chamber 20, raw material is subjected to the effect of flame 26 and is heated the formation glass sphere.Glass sphere is discharged from the combustion chamber then.Non-flammable gas is by sending into combustion chamber 20 around the conduit 25 of combustion furnace assembly I, flows and form the air-flow of a gas ring around flame along flame 26 tracks to keep one.
Description
The present invention relates to a kind of method of producing glass sphere, in this method, raw material is subjected to the effect of flame in a combustion chamber, so that this raw material is heated and makes said glass sphere, and is taken out from said combustion chamber.The invention still further relates to the equipment of making glass sphere, comprising a combustion chamber, fuel and oxidizer are provided for said combustion chamber so that produce the equipment of flame and add raw material in the flame so that heat and change into glass sphere, and the equipment that the ball of making is taken out from the combustion chamber.
The whole bag of tricks and the equipment of production that is used for the production of solid glass ball and multicellular glass ball is known.
For example, in the manufacturing processed of solid ball, the known glass particle raw material that will deliver fragmentation in the air-flow of people is given the combustion chamber, and in the combustion chamber, glass particle flows by flame heating, thereby makes broken glass become spherolite.Similarly, for the manufacturing of foam ball, people are known to be to provide a kind of coccoid raw material to the combustion chamber.In the combustion chamber, because the effect of flame, these beads are heated, and change into the multicellular glass ball.A kind of like this raw material is normally by spraying-dry a kind of solution (for example a kind of based on the silicate hydrate sodium solution, but also contain the solution of a kind of foaming agent (for example urea)) and make.
The mode of heating raw to the quality of shaping ball and output cause close important, especially when those balls will be made the multicellular glass ball.Simultaneously, the economy to production process also is very important.Rapid heating to form spherolite and (or) vitrifying of raw material is favourable, and this needs the good thermo-contact of flame and stock yard.In order to obtain the product of a homogeneous quality, importantly in the combustion chamber, should be processed equably by the made ball of this kind production method, reduce simultaneously between solid material bonding and (or) tendency that adheres on the sidewall of combustion chamber also is important, above-mentioned bonding and adhesion situation, may be that over-heating causes during the feedstock conversion balling-up.
An object of the present invention is to satisfy above-mentioned ask for something at least in order to help.
A kind of method of producing glass sphere that proposes according to the present invention, in this method, raw material is subjected to the effect of flame in the combustion chamber, and this raw material is heated, and makes said glass sphere, and after this, these balls are taken out from said combustion chamber.The raw material that it is characterized in that above-mentioned said supply combustion chamber is diffused in the delivery air-flow, this delivery stream is a kind of mixture, comprising giving burning fuel gas and oxygen that interior flame provides, non-flammable gas also offers the combustion chamber simultaneously, in order to keep an air-flow, this air-flow is along the flame track, and flows around flame, to form a gas ring.
By various overall characteristics provided by the invention, guarantee raw material is carried out all even processing well, to increase the output of gained high quality ball.Owing to adopted this method that raw material and gas is offered the combustion chamber, each unfashioned ball is surrounded fully by a stable flame, they are heated rapidly in the gas ring, this gas ring is passed to raw material and ball to additional kinetic energy, transfer out the combustion chamber so that the ball that processes collected, and ball is remained under the state of abundant diffusion, thereby avoided ball bonding or adhered on the side wall of combustion chamber.A prior advantage of the method applied in the present invention is, people find, are effectively making in the ball process, and side wall of combustion chamber is than cold under other situation, and help like this improving hot worked economy, and help to prolong the useful working life of combustion chamber.
In preferred forms of the present invention, said gas ring is formed by the air that offers the combustion chamber, and this all is favourable to improving economy and accessibility, and because the result that nitrogen exists provides a favourable ballast.This gas ring can provide one deck screen efficiently, with stop glass or can vitrified material impacts side wall of combustion chamber.Equally, this airborne additional oxygen that is provided has promoted the perfect combustion of fuel gas, has further improved the economy of fuel.Owing to similar reason, the oxygen that replenishes in the preferably said non-flammable gas can guarantee that the oxygen in the combustion chamber surpasses and keep the required amount of oxygen of said fuel perfect combustion.
If the air of providing preferably for said gas ring is three times for the said fuel required air of perfect combustion at least, this will make advantage of the present invention more remarkable.
Except that the bonding of ball and they adhere to the problem of sidewall of combustion chamber, if over-heating some further problem also can occur, especially with regard to foam ball.If foam ball is heated excessively, the bubble wall is softened such degree and produces the trend of damaging to cause them, thereby causes the qualification rate of good moulding ball to reduce.
Therefore, wish the flame temperature of heat balls in the restriction combustion chamber.People know that regulating flame temperature has three kinds of methods, and each method is used in the sort of production method involved in the present invention, all can show the disadvantage of oneself.At first, flame temperature can be regulated by suitable selection fuel.In fact, should be local piped gas supply because consideration economically requires fuel used usually, i.e. town gas, or more common natural gas.Certainly, other fuel also can use, but this certainly will disproportionately increase production cost.When the fuel provided was provided, flame temperature can be regulated by too much fuel or too much air are provided to flame.If too much fuel is provided, because be used for the oxygen deficiency of perfect combustion, the flame that is produced will reduce greatly, thereby when production method of the present invention is implemented under these conditions, the ball of the being produced blackening that is bound to, this has just caused the serious limitation of they use aspects.Otherwise in order to limit flame temperature, if too much air is provided, flame will can not keep stable, thereby cause the inhomogeneous of ball processing.Use too much air, be disadvantageous to the perfect combustion of fuel, and can reduce flame transmission speed greatly.When a kind of meticulous substantially material that is divided into during at the flame internal diffusion, the repressed trend of flame will increase, and it must be in the enforcement of a kind of production method of the above-mentioned type certainly.In brief, previously known production method is not satisfied.
Adopt some preferred forms of the present invention, no matter the size of fuel used heat release in gas region, these problems can both be resolved.
In preferred forms more of the present invention, the thermal value that said fuel gas has is at least 6000 kilocalories/Where
3For example, can use and have about 8000 kilocalories/Where
3The Sweet natural gas of thermal value.People find, use a kind of like this delivery air-flow (it is surrounded by a gas ring, and this gas ring provides too much supplemental oxygen to the combustion chamber) in the fuel of oxygen mix, particularly when offering the combustion chamber, use a large amount of too much air the sort of fuel, can produce advantageous effect aspect reduction flame temperature and the prolongation flame, thereby improved the output good, the uniform ball of processing that is shaped, and do not had the danger of restraining flame or making the ball blackening.In this embodiment, best said delivery air-flow is a kind of very easily incendiary mixture, and this has further reduced to restrain any danger of flame.Especially advantageously, the ratio that comprises oxygen in the delivery air-flow accounts for 1/4～3/4 of the interior perfect combustion aequum of said fuel chambers, and preferable ratio is to account for 1/3～2/3 of said fuel perfect combustion aequum.The oxygen that comprises such ratio in the delivery air-flow has promoted the stable of flame and has helped fuel combustion.For example, the required amount of oxygen of Sweet natural gas (can think methane) perfect combustion is slightly less than the twice of volume of himself oxygen or 10 times of himself volume of air: the suitable proportion that the delivery air-flow that is provided is provided is the air of the Sweet natural gas of a volume than 5 parts of volumes, is half of perfect combustion aequum.
In other preferred forms of the present invention, the thermal value that said fuel gas has is no more than 5000 kilocalories/Where
3For example can use town gas.When being used for production method of the present invention, this obtains extraordinary result equally.
When using a kind of gas with such lower calorific value, preferably manage to increase the high-temperature residence time of unshaped ball, therefore it is favourable using embodiments of the invention, in the present embodiment, the polynary air-flow that contains fuel gas and oxygen offers the combustion chamber at least along length of flame direction in an annular zone band, and several strands of air-flows are concentrated mutually, and intersect with said flame.Advantageously in such annular zone band, have three strands of air-flows of concentrating like this at least, so that promote the homogeneity of processing.Preferably should have 2 said annular zone bands at least, in this annular zone band, the air-flow of concentrating offers the combustion chamber so that further increase the time that high temperature continues, perhaps advantageously, at least one such annular zone band is set, and the spacing of it and flame root is 1/3 of combustion chamber length at least.
The fuel that preferably this concentrated air-flow contains and the ratio of oxygen are enough to satisfy the perfect combustion of the sort of fuel.This has promoted flame quite firmly to assemble, and when using a kind of like this gas of lower calorific value with box lunch, obtains the good required temperature of shaping ball, and the convergence of flame helps to concentrate heat in the annular zone band of this focused airflow.
Supply with identical substantially gaseous mixture with said delivery air-flow especially preferably for said convergence air-flow.
No matter what fuel gas is used in the enforcement of production method of the present invention,, it would be desirable that the delivery air-flow should comprise the raw material in the direct mixture that fully is diffused in a kind of inflammable and combustion-supporting gas in order to promote the homogeneity of raw material processing.For this reason, the first kind of composition that preferably has a delivery air-flow of transported raw material advances along a passage that leads to the combustion chamber.Second gaseous constituent of this delivery air-flow is compelled to laterally compress into that passage by at least one hole on the passage perisporium, and the mixing delivery air-flow that wherein has the raw material that is transferred was subjected to further promoting direct blended reactive force there before arriving the combustion chamber.
After leaving flame, the ball of advantageously making still is diffused among the air-flow before being collected, and passes through a cooling zone with gas stream.This just makes the ball of making after leaving flame, unlikely bonding.
The present invention also provides the equipment of making glass sphere, it comprises a combustion chamber, give said combustion chamber provide fuel and oxidizer to produce flame equipment and add raw material in the flame so that heat and change into glass sphere, and the equipment that the ball of making is taken out from the combustion chamber.According to the present invention, wherein said equipment comprises and is used for supplying raw materials to the combustion chamber that (this raw material is to be spread in a carrier gases that comprises said fuel and oxidizer, and be transferred with it) the burning boiler tube, round this roasting kiln pipeline equipment with keep non-flammable gas stream by this pipe-line equipment, and the direction identical with the material stream that sprays from the roasting kiln aperture enters the combustion chamber, so that form the equipment of a gas ring round described material stream.
A kind of like this equipment is particularly suitable for use in the enforcement of method of the present invention.When using by this method, the production method that these equipment adopt just embodies its superiority, and particularly these equipment have long useful working life and reduced the advantage of maintenance.
In order to keep an airflow to flow through above-mentioned pipe-line equipment, blower equipment is set preferably.Air is a kind of dog-cheap gas resource that is used to form above-mentioned gas ring, and has to fuel chambers and provide additional oxygen to help the advantage that production process is carried out.
Advantageously at least one the annular zone band on the length direction of combustion chamber, a plurality of pilot jets are set, comprise that with guiding the multiply air-flow of fuel gas and oxygen enters the combustion chamber and assembles mutually, and with crossing from the material stream of burning boiler tube ejection.Adopt these pilot jets, play a part a kind of favourable increasing the heat that produces in the combustion chamber.This has special value when adopting the combustion gases (as town gas) of quite low thermal value.
For the homogeneity that promotes to process, be preferably in each annular zone band, 3 pilot jets will be arranged at least.
Ideal method is along the combustion chamber, will have 2 this sets that the annular zone band of pilot jet is arranged at least, so that further increase the heat that the combustion chamber produces.Be that benchmark makes progress preferably perhaps,, at least one this annular zone band that pilot jet is arranged be set at least at 1/3 place of combustion chamber length with the outlet of burning boiler tube.To promote the prolongation of the length of flame that in the combustion chamber, produces like this, thereby prolong the high-temperature residence time of raw material and unshaped ball.Like this, when obtaining best result and allow to adopt lower temperature; This helps to prolong the useful working life of equipment again and reduces maintenance.
Below by means of with a particular example preferred forms of the present invention being described in more detail with reference to the accompanying drawings.In the accompanying drawings:
Fig. 1 is a burner apparatus side partial sectional view;
Fig. 2 be one along cross-sectional view that II among Fig. 1-the II line is analysed and observe;
Fig. 3 is a synoptic diagram that is used to produce the equipment of circular glass ball.
In Fig. 1 and Fig. 2, burner apparatus (normally among the figure sequence number 1 indication) comprises a burning boiler tube 2 that ends at roasting kiln top 3.The transport pipe equipment of providing for roasting kiln top 3 comprises a first channel 4 that ends at volute 5, volute 5 is around burning boiler tube 2, and by an eyelet 6(Fig. 2) with the internal communication of burning boiler tube 2, and eyelet 6 is enough big, so that unlikely obstruction system ball passes through with particulate.System ball particle is to transmit with a gas stream, along first channel 4 flows into combustion boiler tubes 2.
Be used to provide the second passage 7 of second gaseous constituent to end at second volute 8, volute 8 is around first volute 5, and is communicated with first volute 5 by a plurality of apertures 9, and the many apertures of sequence number 9 indications are arranged on the periphery wall of first volute 5 among the figure.Sense of rotation that it should be noted that volute 5,8 is opposite.
The end of burning boiler tube 2, is with covering 10 sealings.
At two volutes 5,8
The top, the collar 11 be installed in the burning boiler tube 2 on, with fixed outer aid burning boiler tube 12.Aid burning boiler tube 12 ends at aid burning furnace roof portion 13, and the assist gas supply arrangement is housed.In this embodiment, except for adapt to external firing boiler tube 12 than major diameter, outside the size of the volute of assist gas supply arrangement need change, these equipment were the same with above-described those equipment.The reference number of each parts of additional gas supply arrangement is that the sequence number of aforesaid device adds 10.
Because second gaseous constituent is by aperture 9,19, laterally enter first channel, when all gases enters burning boiler tube 2,12 o'clock, these gases mix well, and because of the geometrical shape of gas supply system, along with these mixtures flow to the roasting kiln top at 3,13 o'clock along burning boiler tube 2,12, make these mixtures form swirling motion, thus each gas before igniting by thorough mixing.
Because aperture 9 is on the periphery wall of the first main volute 5, second gaseous constituent enter the system ball material particle generation effect that certainly will carry another gaseous constituent so that they are during by volute, compensating action centrifugal force thereon at least in part.
In Fig. 3, combustion chamber 20 have one as the described burner apparatus 1 of Fig. 1 and 2 stretch into its bottom 21.Burner apparatus 1 is supplied raw materials by supply line 4, and the raw material that is used for producing glass sphere is diffused in air, provides inflammable gas by supply line 7, comprises the delivery air-flow of fuel and air with formation.Air offers supply line 4 by gas blower 22, and raw material injects supply line 4 from hopper 23.Second air-blaster 24 and air supply pipe line 14 and fuel feed pipeline 17 gives the aid burning furnace roof 13(of portion shown in Figure 1) a kind of flammable mixture is provided.
In said embodiment, the bottom 21 of combustion chamber is opened wide, so that combustion chamber 20 absorbs the air in the external world that upwards flows into by pipeline 25 naturally, pipeline 25 is limited between the bottom of burner apparatus and combustion chamber 20.In an embodiment (not shown) that derives from, provide the 3rd gas blower, air is provided for the bottom 21 of combustion chamber 20 along a supply line.This supply line tangentially enters combustion chamber 20 under the horizontal plane at roasting kiln top 3, so that make the air that is blown into produce a kind of eddying motion of rising, thereby make air keep contacting with the wall of combustion chamber 20.Under arbitrary both of these case, because airflow rises to the upper position of a broad, so it is round the flame 26 of ejection from burner apparatus 1.The upper position of this broad forms a cooling zone 27 above combustion chamber 20, the ball of shaping can therefrom take out by a pipeline 28, so that further process or choose and store.
Each annular zone band place in leave three annular zone bands at interval each other on the length direction of combustion chamber 20 all provides a plurality of pilot jets 29, in order that the guiding multiply comprises that the air-flow of fuel gas and oxygen enters combustion chamber 20 and assembles mutually, and with roasting kiln 1 in crossing as the material stream of flame 26 ejection.In said layout, 4 pilot jets are all arranged on each annular zone band, the annular zone band is the top from roasting kiln 1, is arranged on 1/4,2/4,3/4 place of the length of combustion chamber.
This pilot jet is chosen wantonly, but when the thermal value of used fuel gas was relatively low, they were useful especially.The pilot jet of the top annular zone band in some embodiments of the present invention has been removed.
Example 1
A kind of boric acid aqueous solution and sodium hydroxide react, and mix with hydrated sodium silicate, are the solution of 35% solute by weight to obtain a kind of containing.Add be approximately solute by weight 2% urea as foaming agent.And this primary solution is with a kind of known method, and self spraying drying is so that form a kind of spherical raw material.It is fit to form the only bead in 40～60 micrometer ranges of average particle size particle size, and particle size depends on desired the finished product.About ratio of dried raw material composition weight is expressed as follows:
SiO
267.34%
Na
2O 25.51%
B
2O
37.05%
The spherical raw material that is become like this is 250 Where in speed
3/ hour Sweet natural gas and speed be 1250 Where
3/ hour the delivery air-flow of air in, supply with roasting kiln with 150 kilograms/hour speed, this air-flow is lighted subsequently.One replenishes airflow with 12000 Where
3/ hour speed deliver to the bottom of combustion chamber, it surrounds the flame that sprays from roasting kiln.By the ratio of the air that provides of delivery air-flow approximately is half of perfect combustion aequum, almost is 10 times of the sort of aequum and be provided for surrounding the required air of delivery air-flow.Do not adopt pilot jet 29 in the embodiment.This method can obtain glass sphere high yield, that moulding is good.The particle size determination of moulding ball is that all balls all are 250 microns mesh screen by a mesh size, the mesh size that passes through that accounts for weight 75% is 150 microns a mesh screen, it is 5 microns mesh screen that weight only accounts for 5% the mesh size that passes through, and it is 100 microns mesh screen that weight accounts for 50% the mesh size that passes through.
In the embodiment that this embodiment derives from, in fact the original solution of identical composition replaces boric acid to make with borax.
The example II
As the spherical raw material of making in the example I, along with the delivery air-flow of coal gas and air is supplied with roasting kiln with 150 kilograms/hour speed.Coal gas is with 300 Where
3/ hour absolute speed supply with roasting kiln.And air is with 600 Where
3/ hour absolute speed supply with roasting kiln, then, this strand air-flow is lighted.The thermal value that used coal gas has is 4550 kilocalories/Where
3, its about composition is following listed: CO6.9%, H
252.9%, CH
429.7%, shiner 0.8%, O
20.8%, CO
22.1%, N
26.8%.In order to form an air ring around the flame 26 that leaves roasting kiln, air is with 4000 Where
3/ hour speed supply with pipeline 25 round the roasting kiln top.Two groups of pilot jet 29(are 4 pilot jets for every group) fueling/air mixture.Speed is 150 Where
3/ hour coal gas and speed be 200 Where
3/ hour air be supplied to each this sets of auxiliary blowers.First this set of nozzles is set on the annular zone band of 1 meter of 3,13 top, main burning furnace top, and second this set of nozzles is set on the annular zone band at first 1 meter, set of nozzles top.
This method can obtain high yield, the glass sphere that moulding is good equally.
Claims (24)
1, produces the method for glass sphere, in this method, raw material is subjected to the effect of flame in the combustion chamber, raw material is heated and makes said glass sphere, the ball of making takes out from said combustion chamber, it is characterized in that the said raw material that offers the combustion chamber is diffused in the delivery air-flow, this delivery air-flow is a kind of mixture that comprises fuel gas and oxygen, this mixture is used for producing flame in the combustion chamber, and non-flammable gas offers the combustion chamber and flows and form the air-flow of a gas ring around flame along the flame track to keep one.
2, according to the production method of claim 1, wherein said gas ring is to be formed by the air that offers the combustion chamber.
3, according to the production method of claim 1 or 2, wherein said non-flammable gas comprises additional oxygen, and the amount of supplemental oxygen makes the oxygen in the combustion chamber surpass the needed amount of said fuel perfect combustion that guarantees.
4, according to the production method of claim 3, the air capacity of wherein supplying with said gas ring is 3 times of said fuel perfect combustion required air quantity at least.
5, according to the production method of claim 3 or 4, the thermal value that wherein said fuel gas has is at least 6000 kilocalories/Where
3
6, according to the production method of claim 5, wherein said delivery air-flow is a kind of very easily mixture of combustion.
7, according to the production method of claim 6, wherein delivering the oxygen proportion that air-flow comprises is 1/4～3/4 of said fuel perfect combustion aequum.
8, according to each the production method in the claim 5～7, wherein delivering the oxygen proportion that air-flow comprises is 1/3～2/3 of said fuel perfect combustion aequum.
9, according to each the production method in the claim 1～4, the thermal value that wherein said fuel gas has is not more than 5000 kilocalories/Where
3
10, according to the production method of claim 9, wherein at least one annular zone band of length of flame direction, the multiply air-flow that is comprising fuel gas and oxygen is provided for the combustion chamber and assembles mutually, and intersects with said flame.
11, according to the production method of claim 10, wherein in this annular zone band, have three strands of such convergence air-flows at least.
12, according to the production method of claim 10 or 11, wherein have two said annular zone bands at least, in the annular zone band, assemble air-flow and offer the combustion chamber.
13, according to each the production method in the claim 10～12, wherein or at least one such annular zone band is set, it is 1/3 of a combustion chamber length from the spacing of flame root at least.
14, according to each the production method in the claim 10～13, the fuel that wherein this convergence air-flow comprises and the ratio of oxygen are enough to satisfy the needs of the sort of fuel perfect combustion.
15,, wherein assemble air-flow and said delivery air-flow and supply with by substantially the same gaseous mixture according to each production method in the claim 10～14.
16, the production method that requires according to any aforesaid right, the wherein said another kind of composition that has the delivery air-flow of the raw material that is transferred is advanced by the passage that leads to the combustion chamber along, second gaseous constituent of this delivery air-flow is by at least one hole on the passage perisporium, be compelled to laterally compress into described passage, and the mixing delivery air-flow that wherein has the raw material that is transferred was subjected to further promoting well-mixed reactive force before arriving the combustion chamber.
17, according to the production method of above-mentioned arbitrary claim, wherein leave flame after, newly formed glass sphere still is diffused in the air-flow before being collected, and crosses a cooling zone with air communication.
18, the equipment of manufacturing glass sphere comprises a combustion chamber, give said combustion chamber provide fuel and oxidizer to produce flame equipment and in flame, add raw material from the combustion chamber so that the equipment that heats and change into glass sphere and the ball of making is taken out, it is characterized in that described this equipment comprises is used for the burning boiler tube of supplying raw materials to the combustion chamber, raw material is to be diffused in the delivery stream that comprises said fuel and oxidizer and to be transferred with it, round the pipe-line equipment of this burning boiler tube and keep one not gas-flow by these pipe-line equipments, and the direction identical with the material stream that ejects from the roasting kiln aperture enters the combustion chamber, so that form the equipment of a gas ring round described material stream.
19, according to the equipment of claim 18, wherein be provided with blower equipment for keeping airflow to flow through above-mentioned pipe-line equipment.
20, according to the equipment of claim 18 or 19, wherein a plurality of pilot jets are arranged on along at least one the annular zone band on the roasting kiln length direction, comprise that with guiding the multiply gas stream of fuel gas and oxygen enters the combustion chamber and can intersect with the material stream that goes out from the roasting kiln pipe inspection by coalescence mutually.
21, according to the equipment of claim 20, wherein in this annular zone band, have three pilot jets at least.
22, according to the equipment of claim 20 or 21, wherein have at least 2 this sets that the annular zone band of pilot jet is arranged along the combustion chamber length direction.
23,, wherein or from the outlet of burning boiler tube,, a this annular zone band that pilot jet is arranged is set at least at least at 1/3 place of combustion chamber length according to each the equipment in the claim 20～22.
24, according to each the equipment in the claim 18～23, the second kind of composition that wherein comprises the first channel of first kind of gaseous constituent that is used to provide the said delivery air-flow that has transferring raw material for the pipe-line equipment of supplying with burning boiler tube gas and be used to force said delivery air-flow laterally enters the second passage of this another passage by the one or more holes on the first channel perisporium, said second kind of composition with enter said burning boiler tube after the first kind of composition that is loaded with raw material mixes.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB8518680 | 1985-07-24 | ||
| GB8518680A GB2178024B (en) | 1985-07-24 | 1985-07-24 | Process of and apparatus for producing vitreous beads |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN86104731A true CN86104731A (en) | 1987-01-21 |
| CN1017888B CN1017888B (en) | 1992-08-19 |
Family
ID=10582776
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN86104731A Expired CN1017888B (en) | 1985-07-24 | 1986-07-17 | Process and apparatus for producing vitreous beads |
Country Status (10)
| Country | Link |
|---|---|
| CN (1) | CN1017888B (en) |
| AU (1) | AU581328B2 (en) |
| BE (1) | BE905136A (en) |
| CS (1) | CS271337B2 (en) |
| ES (2) | ES8800569A1 (en) |
| FR (1) | FR2585348B1 (en) |
| GB (1) | GB2178024B (en) |
| HU (1) | HU212474B (en) |
| SU (1) | SU1611215A3 (en) |
| ZA (1) | ZA865478B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113754252A (en) * | 2021-09-28 | 2021-12-07 | 陕西科技大学 | Preparation method and production device of large-particle spherical glass |
| CN115023409A (en) * | 2020-01-24 | 2022-09-06 | 巴斯夫欧洲公司 | Method for producing hollow spherical glass particles |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB8914639D0 (en) * | 1989-06-26 | 1989-08-16 | Shell Int Research | Heat processing of particulate material and apparatus therefor |
| JPH09512781A (en) * | 1994-04-25 | 1997-12-22 | ミネソタ マイニング アンド マニュファクチャリング カンパニー | Composition containing melted particles and method for producing the same |
| US6254981B1 (en) | 1995-11-02 | 2001-07-03 | Minnesota Mining & Manufacturing Company | Fused glassy particulates obtained by flame fusion |
| AU742345B2 (en) * | 1997-05-22 | 2001-12-20 | Siren Jian | A method and apparatus for recovering energy of waste classification incineration |
| US6813902B2 (en) * | 2000-11-01 | 2004-11-09 | American Air Liquide, Inc. | Systems and methods for increasing production of spheroidal glass particles in vertical glass furnaces |
| CN101633551B (en) * | 2009-09-09 | 2011-08-24 | 中材科技股份有限公司 | Glass ball manufacturing device |
| CN103553304B (en) * | 2013-10-31 | 2016-03-09 | 河北勇龙邦大新材料有限公司 | A kind of method and apparatus of inorganic microspheres Fast Sintering |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE521556A (en) * | 1953-07-18 | |||
| NL232500A (en) * | 1957-10-22 | |||
| US3190737A (en) * | 1960-07-07 | 1965-06-22 | Flex O Lite Mfg Corp | Glass bead furnace and method of making glass beads |
| BE627719A (en) * | 1962-03-27 | |||
| GB1060234A (en) * | 1964-05-16 | 1967-03-01 | Cataphote Corp | Method and apparatus for manufacturing glass beads |
| US3579720A (en) * | 1968-01-04 | 1971-05-25 | Glaverbel | Apparatus for subdividing fluid mass into grains |
| IE51461B1 (en) * | 1980-08-15 | 1986-12-24 | Redland Technology Ltd | Method and apparatus for the production of glass beads |
| EP0086599A1 (en) * | 1982-02-12 | 1983-08-24 | Redland Technologies Limited | Method and apparatus for the heat processing of particulate materials |
| GB2121782B (en) * | 1982-06-08 | 1986-10-22 | Glaverbel | Manufacture of rounded vitreous beads |
-
1985
- 1985-07-24 GB GB8518680A patent/GB2178024B/en not_active Expired
-
1986
- 1986-06-21 ES ES556391A patent/ES8800569A1/en not_active Expired
- 1986-06-23 ES ES556402A patent/ES8706580A1/en not_active Expired
- 1986-07-03 CS CS865039A patent/CS271337B2/en not_active IP Right Cessation
- 1986-07-10 AU AU60036/86A patent/AU581328B2/en not_active Expired
- 1986-07-17 CN CN86104731A patent/CN1017888B/en not_active Expired
- 1986-07-18 BE BE1/011520A patent/BE905136A/en not_active IP Right Cessation
- 1986-07-21 FR FR868610658A patent/FR2585348B1/en not_active Expired - Lifetime
- 1986-07-23 ZA ZA865478A patent/ZA865478B/en unknown
- 1986-07-23 SU SU4027856A patent/SU1611215A3/en active
- 1986-07-23 HU HU863001A patent/HU212474B/en not_active IP Right Cessation
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115023409A (en) * | 2020-01-24 | 2022-09-06 | 巴斯夫欧洲公司 | Method for producing hollow spherical glass particles |
| CN113754252A (en) * | 2021-09-28 | 2021-12-07 | 陕西科技大学 | Preparation method and production device of large-particle spherical glass |
Also Published As
| Publication number | Publication date |
|---|---|
| ES556402A0 (en) | 1987-07-01 |
| HU212474B (en) | 1996-07-29 |
| ES556391A0 (en) | 1987-11-01 |
| ZA865478B (en) | 1987-03-25 |
| FR2585348B1 (en) | 1992-12-04 |
| SU1611215A3 (en) | 1990-11-30 |
| ES8706580A1 (en) | 1987-07-01 |
| FR2585348A1 (en) | 1987-01-30 |
| CS503986A2 (en) | 1990-02-12 |
| AU581328B2 (en) | 1989-02-16 |
| HUT45464A (en) | 1988-07-28 |
| GB2178024B (en) | 1989-08-02 |
| CS271337B2 (en) | 1990-09-12 |
| CN1017888B (en) | 1992-08-19 |
| GB8518680D0 (en) | 1985-08-29 |
| AU6003686A (en) | 1987-01-29 |
| BE905136A (en) | 1987-01-19 |
| ES8800569A1 (en) | 1987-11-01 |
| GB2178024A (en) | 1987-02-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4487620A (en) | Method and apparatus for manufacturing rounded vitreous beads | |
| CN1144013C (en) | Process and apparatus for drying and heating | |
| US5558822A (en) | Method for production of spheroidized particles | |
| CN1022233C (en) | Method and apparatus for heat processing glass batch materials | |
| CN1035239C (en) | Fluidized bed system and a fluidization and cooling nozzle for use therein | |
| CN1125308A (en) | Polverized coal combustion burner | |
| US4337032A (en) | Device for mixing gaseous fluids by turbulence | |
| CN102597629B (en) | Method of combusting particulate solid fuel with a burner | |
| CN86104731A (en) | The production method of glass sphere and equipment | |
| CN100449239C (en) | Mixing high temp. gas i nmineral kilns | |
| US4229109A (en) | System for producing bituminous paving mixtures | |
| US4249892A (en) | Method and apparatus for the thermal treatment of pulverulent material particularly for the calcining of cement | |
| US20110232333A1 (en) | Process and apparatus for making mineral fibres | |
| CN85104420A (en) | Produce the method and apparatus of white cement clinker | |
| KR100414472B1 (en) | Method and apparatus for melting recycled silicate starting material | |
| WO1995020544A1 (en) | Annular batch feed furnace and process | |
| JP2549635B2 (en) | Method for heat treating glass batch material and method for producing glass products | |
| US4477251A (en) | Process and apparatus for calcining pulverulent material | |
| US3337669A (en) | Apparatus and methods for producing panels of mineral fibers | |
| US6813902B2 (en) | Systems and methods for increasing production of spheroidal glass particles in vertical glass furnaces | |
| CN1030396A (en) | The melting method of glass batch and equipment | |
| US6244860B1 (en) | Apparatus and process for producing perlite | |
| EP0149881B1 (en) | Method and apparatus for combusting ash producing solids | |
| CN1142249A (en) | Apparatus for melting fine particles containing carbon and method thereof | |
| US4110064A (en) | Air-jet 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 | ||
| C13 | Decision | ||
| C14 | Grant of patent or utility model | ||
| C17 | Cessation of patent right |