CN111170619A - Glass bead production system and application thereof - Google Patents
Glass bead production system and application thereof Download PDFInfo
- Publication number
- CN111170619A CN111170619A CN201911376174.7A CN201911376174A CN111170619A CN 111170619 A CN111170619 A CN 111170619A CN 201911376174 A CN201911376174 A CN 201911376174A CN 111170619 A CN111170619 A CN 111170619A
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- pipe
- diffusion chamber
- combustion chamber
- cooling diffusion
- communicated
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- 239000011521 glass Substances 0.000 title claims abstract description 60
- 239000011324 bead Substances 0.000 title claims abstract description 56
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 69
- 238000001816 cooling Methods 0.000 claims abstract description 60
- 238000009792 diffusion process Methods 0.000 claims abstract description 57
- 238000002485 combustion reaction Methods 0.000 claims abstract description 43
- 239000002994 raw material Substances 0.000 claims abstract description 32
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000003546 flue gas Substances 0.000 claims abstract description 26
- 230000002093 peripheral effect Effects 0.000 claims abstract description 11
- 239000000428 dust Substances 0.000 claims description 34
- 238000007599 discharging Methods 0.000 claims description 13
- 239000007789 gas Substances 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 6
- 238000006477 desulfuration reaction Methods 0.000 claims description 4
- 230000023556 desulfurization Effects 0.000 claims description 4
- 239000000446 fuel Substances 0.000 claims description 3
- 239000012535 impurity Substances 0.000 claims description 3
- 239000004005 microsphere Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 230000000630 rising effect Effects 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 2
- 238000012545 processing Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 4
- 238000012546 transfer Methods 0.000 abstract description 2
- 239000004744 fabric Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
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- 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
- C03B19/103—Fluidised-bed furnaces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/008—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases cleaning gases
-
- 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
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Abstract
The invention discloses a glass bead production system and application thereof, and the glass bead production system comprises a base combustion chamber, a cooling diffusion chamber arranged on the base combustion chamber, a plurality of feed inlets arranged on the outer peripheral side of the base combustion chamber, a plurality of discharge bins arranged at the bottom of the cooling diffusion chamber, a heat exchange wall water pipe arranged on the outer peripheral side of the cooling diffusion chamber, a steam tank arranged at the top of the cooling diffusion chamber and communicated with an upper port of the heat exchange wall water pipe, and a circulating water descending pipe communicated with the bottom of the steam tank and communicated with a lower port of the heat exchange wall water pipe. Install steam heat transfer device on the equipment of conventional glass bead production in this application for the high temperature energy of collecting device periphery side and top flue gas, thereby reduce the flue gas temperature effectively, thereby be convenient for utilize the sack cleaner, not only reach the exhaust emission standard, intercept and capture a large amount of glass beads that float escape equipment along with the flue gas moreover, can also play energy-conserving effect of accelerating production efficiency at equipment fixing raw materials preheater tube in addition.
Description
Technical Field
The invention relates to the technical field of glass bead production, in particular to a glass bead production system and application thereof.
Background
The exhaust temperature of the conventional traditional glass bead furnace is over 300-400 ℃, filtered tail gas cannot be treated by using cloth bag dust removal equipment, but the dust removal equipment can only use a cloth bag dust remover to meet the environment-friendly requirement of air emission when dust is treated at present; therefore, the flue of the glass production equipment is cooled by the water heat exchanger to the usable temperature of cloth bag dust removal, so that hot water generated by cooling can be utilized, and the environment-friendly requirement is met. The conventional cyclone dust removal can not meet the environmental protection requirement of air emission, and part of glass beads are not intercepted, so that the material waste is caused.
Disclosure of Invention
The invention aims to provide a glass bead production system and application thereof, and solves the problems that the conventional glass bead production system and application thereof are convenient for low utilization rate of waste heat of conventional glass bead production equipment, so that the flue gas temperature is too high and is inconvenient to treat, and the energy utilization efficiency of the conventional glass bead production system is low.
In order to solve the technical problems, the invention adopts the following technical scheme:
the invention provides a glass bead production system and application thereof, comprising a base combustion chamber, a cooling diffusion chamber arranged on the base combustion chamber, a plurality of feed inlets arranged on the outer peripheral side of the base combustion chamber, and a plurality of discharge bins arranged at the bottom of the cooling diffusion chamber; a circle of heat exchange wall water pipes, a steam tank which is arranged at the top of the cooling diffusion chamber and is communicated with the upper port of the heat exchange wall water pipes and a circulating water descending pipe which is communicated with the bottom of the steam tank and is communicated with the lower port of the heat exchange wall water pipes are arranged on the outer peripheral side of the cooling diffusion chamber; the cooling diffusion chamber is communicated with the bag-type dust collector through a flue pipe, and a cyclone dust collector and a heat exchanger are sequentially arranged on the flue pipe; the top of the steam tank is communicated with a steam pipe; the lower end of the circulating water descending pipe is communicated with the lower end of the heat exchange wall water pipe through the water supply pipe; the upper end of the base combustion chamber extends to the inside of the cooling diffusion chamber, and the upper end of the base combustion chamber is connected with the bottom of the cooling diffusion chamber in a sealing installation mode.
Furthermore, a plurality of fuel inlets and air supply outlets are arranged at the bottom of the base combustion chamber.
Still further, the cooling diffusion chamber and the base combustion chamber are on the same vertical axis.
Still further, a material collecting groove is arranged below the bag-type dust collector.
Still further, the discharge bin is of a cone structure, is provided with an opening at the bottom and is conveyed through the conveying device.
Still further, the feed inlet conveys raw materials through a conveying device.
Still further, be provided with the raw materials preheating pipe of downwardly extending on the inner wall of cooling diffusion room, the upper end intercommunication of raw materials preheating pipe has to be installed the outside feed inlet of cooling diffusion room, the intercommunication is installed to the lower extreme of raw materials preheating pipe the inlet pipe of base combustion chamber, install the feed valve on the inlet pipe.
And a desulfurization and denitrification system is further arranged on the flue pipe and between the cyclone dust collector and the heat exchanger.
And further, the flue gas is cooled in the heat exchanger through a pipeline communicated with a water supply pipe or a steam tank.
A method for processing glass beads, which comprises the following steps,
a. the gas at the bottom of the base combustion chamber is continuously supplied and is combusted for a period of time to preheat the base combustion chamber and the cooling diffusion chamber;
b. then conveying raw materials for producing glass beads to a feeding hole through a conveying device, and then feeding the raw materials into a base combustion chamber, wherein the raw materials for producing the glass beads are diffused and suspended in a cooling diffusion chamber to be heated and melted under the action of gas combustion rising and the suction force of a fan, are changed into glass beads according to the surface tension of the glass beads, then fall into a discharging bin, and receive finished glass beads along with an opening at the lower part of the discharging bin;
c. wherein, the heat exchange wall water pipe on the outer peripheral side of the cooling diffusion chamber forms a natural circulation device through a water supply pipe, a circulating water descending pipe and a steam tank on the top of the circulating water descending pipe, thereby cooling the flue gas in the hearth of the cooling diffusion chamber;
d. the flue gas in the cooling diffusion chamber is continuously cooled to below 180 degrees under the heat exchange of the heat exchange wall water pipe, the service temperature range of the bag-type dust remover is reached, wherein a cyclone dust remover is utilized to remove impurities with larger particle size, so that the flue gas is conveyed into the bag-type dust remover under the action of a draught fan, wherein the flue gas contains a part of fine glass beads, and the bag-type dust remover is utilized to capture, collect and recycle the glass beads.
Compared with the prior art, the invention has the beneficial technical effects that: install steam heat transfer device on the equipment of conventional glass bead production in this application for the high temperature energy of collecting device periphery side and top flue gas, thereby reduce the flue gas temperature effectively, thereby be convenient for utilize the sack cleaner, not only reach the exhaust emission standard, intercept and capture a large amount of glass beads that float escape equipment along with the flue gas moreover, can also play energy-conserving effect of accelerating production efficiency at equipment fixing raw materials preheater tube in addition.
Drawings
The invention is further illustrated in the following description with reference to the drawings.
FIG. 1 is a schematic diagram of a main body of a glass bead production system according to the present invention;
FIG. 2 is a schematic view showing another structure of the glass bead production system according to the present invention;
FIG. 3 is a schematic diagram of the main body of FIG. 2 in the glass bead production system of the present invention;
FIG. 4 is a schematic view of a position main body in which desulfurization and denitrification are installed in the glass bead production system of the present invention.
Description of reference numerals: 1. a base combustion chamber; 2. a feed inlet; 2-1, a raw material preheating pipe; 2-2, a feed valve; 2-3, a feeding pipe; 3. a heat exchange wall water pipe; 4. cooling the diffusion chamber; 4-1, discharging a material bin; 5. a water supply pipe; 6. a steam tank; 7. a circulating water downcomer; 8. a steam pipe; 9. a cyclone dust collector; 10. an induced draft fan; 11. a bag-type dust collector, 11-1 and a discharge bin; 12. a support frame; 13. a material collecting groove; 14. a heat exchanger; 15. and (4) a chimney.
Detailed Description
Example one
As shown in fig. 1, the present embodiment discloses a glass bead production system, which includes a base combustion chamber 1, a cooling diffusion chamber 4 installed on the base combustion chamber 1, four feed inlets 2 installed on the outer peripheral side of the base combustion chamber 1, and four discharge bins 4-1 installed at the bottom of the cooling diffusion chamber 4, wherein a circle of heat exchange wall water pipes 3 are respectively installed on the outer peripheral sides of the cooling diffusion chamber 4 and the base combustion chamber 1, a steam tank 6 installed on the top of the cooling diffusion chamber 4 and communicated with the upper port of the heat exchange wall water pipe 3, and a circulating water down pipe 7 communicated with the bottom of the steam tank 6 and communicated with the lower port of the heat exchange wall water pipe 3; the cooling diffusion chamber 4 is of a cylindrical structure, the structure of the cooling diffusion chamber is the same as that of combustion equipment of a thermal power plant, the discharge bin 4-1 is of a conical structure convenient for collecting glass microspheres, the bottom of the discharge bin is provided with a discharge hole, and the discharge hole can be conveyed by a packing auger or a pneumatic conveying system; the heat exchange wall water pipe 3 is a vertical pipe or a pipe wound around the heat exchange wall water pipe 3; the cooling diffusion chamber 4 is communicated with a bag-type dust collector 11 through a flue pipe, and a cyclone dust collector 9 and a heat exchanger 14 are sequentially arranged on the flue pipe; the top of the steam tank 6 is communicated with a steam pipe 8; the heat exchange wall water pipe 3 is used for conveying a steam make-up water source through a water supply pipe 5, and the lower end of the circulating water descending pipe 7 is communicated with the lower end of the heat exchange wall water pipe 3 through the water supply pipe 5; the upper end of the base combustion chamber 1 extends into the cooling diffusion chamber 4, and the upper end of the base combustion chamber 1 is connected with the bottom of the cooling diffusion chamber 4 in a sealing installation mode. Wherein the bottom of the bag-type dust collector 11 is provided with a support frame 12; the top of the steam tank 6 is communicated with a steam pipe 8; the heat exchange wall water pipe 3 is used for conveying steam to supplement a water source through a water supply pipe 5, a lower header is installed at the bottom of the heat exchange wall water pipe 3, the water supply pipe 5 provides circulating water for the heat exchange wall water pipe 3 through the lower header, the lower end of a circulating water descending pipe 7 is communicated with the lower end of the heat exchange wall water pipe 3 through the water supply pipe 5, and the heat exchange wall water pipe comprises a boiler barrel, a descending pipe, a header, an ascending pipe, a steam-water guiding pipe and the like in a concrete mode, so that the heat exchange wall water pipe 3 is used for exchanging heat on the outer peripheral side of a cooling diffusion chamber 4, the delay temperature is reduced, steam is prepared, and the concrete steam is used for meeting the requirements of industrial production and is used for producing EPS.
In the present embodiment, a plurality of fuel inlets and air supply outlets are installed at the bottom of the base combustion chamber 1; the cooling diffusion chamber 4 and the base combustion chamber 1 are on the same vertical axis, so that the interior of the cooling diffusion chamber 4 is uniformly heated; a material collecting groove 13 is arranged below the bag-type dust collector 11 and is used for collecting the tiny glass beads intercepted by the bag-type dust collector; the discharging bin 4-1 is of a cone structure, the bottom of the discharging bin is open, and the discharging bin is conveyed through a conveying device; the feeding port 4 is used for conveying raw materials through a conveying device, and the feeding port 4 is used for conveying raw materials through a packing auger, so that the conveying efficiency is improved; the inner wall of the cooling diffusion chamber 4 is provided with a raw material preheating pipe 2-1 extending downwards, the upper end of the raw material preheating pipe 2-1 is communicated with a feed port 2 arranged on the outer side of the cooling diffusion chamber 4, the lower end of the raw material preheating pipe 2-1 is provided with a feed pipe 2-3 communicated with the base combustion chamber 1, and the feed pipe 2-3 is provided with a feed valve 2-2, so that the control of the feed speed of the raw materials is facilitated. And a desulfurization and denitrification system is also arranged on the flue pipe and between the cyclone dust collector 9 and the heat exchanger 14, so that the cleanness of the flue gas is ensured. And the heat exchanger 14 cools the flue gas through a pipeline communicated with a water supply pipe 5 or a steam tank 6.
The production method in the embodiment:
a. the gas at the bottom of the base combustion chamber 1 is continuously supplied and is combusted for a period of time to preheat the base combustion chamber 1 and the cooling diffusion chamber 4;
b. then, conveying raw materials for producing glass beads to a feeding hole 2 through a conveying device, and then feeding the raw materials into a base combustion chamber 1, wherein the raw materials for producing the glass beads are diffused and suspended in a cooling diffusion chamber 4 to be heated and melted under the action of gas combustion rising and the suction force of a fan, are changed into glass beads according to the surface tension of the glass beads, then fall into a discharging bin 4-1, and receive finished glass beads along with an opening at the lower part of the discharging bin 4-1;
c. wherein, the heat exchange wall water pipe 3 at the peripheral side of the cooling diffusion chamber 4 forms a natural circulation device through a water supply pipe 5, a circulating water descending pipe 7 and a steam tank 6 at the top of the circulating water descending pipe, thereby cooling the flue gas in the hearth of the cooling diffusion chamber 4;
d. the flue gas in the cooling diffusion chamber 4 is continuously cooled to below 180 degrees under the heat exchange of the heat exchange wall water pipe 3, the service temperature range of the bag-type dust remover is reached, wherein a cyclone dust remover 9 is utilized to remove impurities with larger particle size, so that the flue gas is conveyed into the bag-type dust remover 11 under the action of an induced draft fan 10, wherein the flue gas contains a part of fine glass beads, and the bag-type dust remover 11 is utilized to capture, collect and recycle the flue gas.
Example two
As shown in fig. 2 and 3, the difference between the embodiment and the implementation is that a raw material preheating pipe 2-1 extending downward is installed on the inner wall of the cooling diffusion chamber 4, the upper end of the raw material preheating pipe 2-1 is communicated with a feed port 2 installed on the outer side of the cooling diffusion chamber 4, a feed pipe 2-3 communicated with the base combustion chamber 1 is installed at the lower end of the raw material preheating pipe 2-1, and a feed valve 2-2 is installed on the feed pipe 2-3, wherein the raw material for producing glass beads through the raw material preheating pipe 2-1 is preheated, so that not only the energy-saving effect is achieved, but also the raw material for producing glass beads can be pretreated by using the flue gas in the cooling diffusion chamber 4, and the glass beads can be rapidly formed in the subsequent production of the glass beads.
In the description of the present invention, it is to be understood that the terms "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like, indicate orientations or positional relationships based on those shown in the drawings, and are used for convenience of description only, and do not indicate or imply that the referenced devices or elements must have a particular orientation, be constructed and operated in a particular orientation, and thus, are not to be construed as limiting the present invention.
The above embodiments are only for describing the preferred mode of the present invention, and do not limit the scope of the present invention, and various modifications and improvements of the technical solution of the present invention by those skilled in the art should fall within the protection scope defined by the claims of the present invention without departing from the spirit of the present invention.
Claims (10)
1. A glass bead production system which characterized in that: the device comprises a base combustion chamber (1), a cooling diffusion chamber (4) arranged on the base combustion chamber (1), a plurality of feed inlets (2) arranged on the outer peripheral side of the base combustion chamber (1), and a plurality of discharge bins (4-1) arranged at the bottom of the cooling diffusion chamber (4); a circle of heat exchange wall water pipes (3), a steam tank (6) which is arranged at the top of the cooling diffusion chamber (4) and is communicated with the upper port of the heat exchange wall water pipes (3), and a circulating water descending pipe (7) which is communicated with the bottom of the steam tank (6) and is communicated with the lower port of the heat exchange wall water pipes (3) are arranged on the periphery of the cooling diffusion chamber (4); the cooling diffusion chamber (4) is communicated with a bag-type dust collector (11) through a flue pipe, and a cyclone dust collector (9) and a heat exchanger (14) are sequentially arranged on the flue pipe; the top of the steam tank (6) is communicated with a steam pipe (8); the heat exchange wall water pipe (3) is used for conveying a steam make-up water source through a water supply pipe (5), and the lower end of the circulating water descending pipe (7) is communicated with the lower end of the heat exchange wall water pipe (3) through the water supply pipe (5); the upper end of the base combustion chamber (1) extends to the inside of the cooling diffusion chamber (4), and the upper end of the base combustion chamber (1) is connected with the bottom of the cooling diffusion chamber (4) in a sealing and installing mode.
2. The glass bead production system according to claim 1, wherein: the bottom of the base combustion chamber (1) is provided with a plurality of fuel inlets and air supply outlets.
3. The glass bead production system according to claim 1, wherein: the cooling diffusion chamber (4) and the base combustion chamber (1) are on the same vertical axis.
4. The glass bead production system according to claim 1, wherein: and a material collecting groove (13) is arranged below the bag-type dust collector (11).
5. The glass bead production system according to claim 1, wherein: the discharging bin (4-1) is of a cone structure, the bottom of the discharging bin is open, and the discharging bin is conveyed through the conveying device.
6. The glass bead production system according to claim 1, wherein: the feeding hole (4) is used for conveying raw materials through a conveying device.
7. The glass bead production system according to claim 1, wherein: the inner wall of the cooling diffusion chamber (4) is provided with a raw material preheating pipe (2-1) extending downwards, the upper end of the raw material preheating pipe (2-1) is communicated with a feed inlet (2) arranged at the outer side of the cooling diffusion chamber (4), the lower end of the raw material preheating pipe (2-1) is provided with a feed pipe (2-3) communicated with the base combustion chamber (1), and the feed pipe (2-3) is provided with a feed valve (2-2).
8. The glass bead production system according to claim 1, wherein: and a desulfurization and denitrification system is also arranged on the flue pipe and between the cyclone dust collector (9) and the heat exchanger (14).
9. The glass bead production system according to claim 8, wherein: and the flue gas is cooled in the heat exchanger (14) through a pipeline communicated with a water supply pipe (5) or a steam tank (6).
10. The method for processing glass microspheres by the glass microsphere production system according to claim 1, wherein:
a. the gas is continuously supplied through the bottom of the base combustion chamber (1) and is combusted for a period of time to preheat the base combustion chamber (1) and the cooling diffusion chamber (4);
b. then conveying raw materials for producing glass beads to a feeding hole (2) through a conveying device, and then feeding the raw materials into a base combustion chamber (1), wherein the raw materials for producing the glass beads are diffused and suspended in a cooling diffusion chamber (4) to be heated and melted under the action of gas combustion rising and the suction force of a fan, are changed into glass beads according to the surface tension of the glass beads, then fall into a discharging bin (4-1), and receive finished glass beads along with an opening at the lower part of the discharging bin (4-1);
c. wherein the heat exchange wall water pipe (3) at the peripheral side of the cooling diffusion chamber (4) forms natural circulation equipment through a water supply pipe (5), a circulating water descending pipe (7) and a steam tank (6) at the top of the circulating water descending pipe, so that the temperature of the flue gas in the hearth of the cooling diffusion chamber (4) is reduced;
d. the flue gas in the cooling diffusion chamber (4) is continuously cooled to below 180 degrees under the heat exchange of the heat exchange wall water pipe (3), the service temperature range of the bag-type dust remover is reached, wherein impurities with a certain particle size are removed by using the cyclone dust remover (9), so that the flue gas is conveyed into the bag-type dust remover (11) under the action of the induced draft fan (10), wherein the flue gas contains a part of fine glass beads, and the bag-type dust remover (11) is utilized to capture, capture and collect and recycle the flue gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911376174.7A CN111170619A (en) | 2019-12-27 | 2019-12-27 | Glass bead production system and application thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911376174.7A CN111170619A (en) | 2019-12-27 | 2019-12-27 | Glass bead production system and application thereof |
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| Publication Number | Publication Date |
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| CN111170619A true CN111170619A (en) | 2020-05-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911376174.7A Pending CN111170619A (en) | 2019-12-27 | 2019-12-27 | Glass bead production system and application thereof |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113336424A (en) * | 2021-07-02 | 2021-09-03 | 潜江菲利华石英玻璃材料有限公司 | Quartz glass's combustor automatic water supply device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113336424A (en) * | 2021-07-02 | 2021-09-03 | 潜江菲利华石英玻璃材料有限公司 | Quartz glass's combustor automatic water supply device |
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