CN220366676U - Full-automatic ceramic film sintering shuttle kiln - Google Patents
Full-automatic ceramic film sintering shuttle kiln Download PDFInfo
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- CN220366676U CN220366676U CN202320438464.5U CN202320438464U CN220366676U CN 220366676 U CN220366676 U CN 220366676U CN 202320438464 U CN202320438464 U CN 202320438464U CN 220366676 U CN220366676 U CN 220366676U
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- air
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- kiln
- kiln body
- gas
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- 239000000919 ceramic Substances 0.000 title claims abstract description 21
- 238000005245 sintering Methods 0.000 title abstract description 7
- 239000007789 gas Substances 0.000 claims abstract description 50
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000003546 flue gas Substances 0.000 claims abstract description 42
- 239000000779 smoke Substances 0.000 claims abstract description 32
- 238000007599 discharging Methods 0.000 claims abstract description 28
- 238000002485 combustion reaction Methods 0.000 claims abstract description 17
- 230000001105 regulatory effect Effects 0.000 claims description 18
- 239000003517 fume Substances 0.000 claims description 12
- 238000010304 firing Methods 0.000 claims description 11
- 239000012528 membrane Substances 0.000 claims description 10
- 239000003063 flame retardant Substances 0.000 claims description 6
- 239000002918 waste heat Substances 0.000 claims description 5
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims description 4
- 230000001276 controlling effect Effects 0.000 claims description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 235000021313 oleic acid Nutrition 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Abstract
The utility model discloses a full-automatic ceramic film sintering shuttle kiln, which comprises a kiln body, wherein an automatic operation transfer platform is arranged on the side edge of the kiln body, a product kiln car is arranged on the surface of the automatic operation transfer platform, a furnace pressure automatic control smoke discharging mechanism is arranged outside the side wall of the kiln body, the kiln body and the furnace pressure automatic control smoke discharging mechanism are communicated, a harmful flue gas incineration treatment system is arranged on a pipeline at the top end of the kiln body, a smoke discharging main pipe is arranged at the joint of the kiln body and the harmful flue gas incineration treatment system, smoke discharging branch pipes are arranged on two sides of the smoke discharging main pipe, a flue gas incinerator is arranged on the side edge of the kiln body, the flue gas incinerator is connected with the smoke discharging main pipe through pipelines, a combustion system with accurate gas flow control is arranged on two sides of the kiln body, a plurality of groups of excessive air secondary air combustors are arranged on the combustion system, and the excessive air secondary air combustors are arranged outside the kiln body.
Description
Technical Field
The utility model relates to the technical field of shuttle kilns, in particular to a full-automatic ceramic film sintering shuttle kiln.
Background
The ceramic film sintering shuttle kiln has the advantages that due to the product characteristics of the ceramic film, the components contain substances such as glycerin, oleic acid, soybean oil, silica sol and the like, the substances volatilize in a heating stage, and harmful smoke is discharged along with the harmful discharge of the smoke, and the harmful smoke is required to be burned according to the environmental protection requirement and then discharged outdoors. Kiln furnaces used in the current market have defects of different degrees. If a product kiln car is pushed manually, a kiln door is opened and closed manually, the furnace pressure is controlled by a manual flashboard for adjustment, the operation labor intensity is high, and the degree of automation is low. Because the waste heat recycling mode is not adopted, the heat energy is wasted and discharged, the control accuracy of the combustion air-fuel ratio is poor, the energy consumption of the control mode is relatively high, and the heat energy efficiency is not fully utilized; the incineration treatment of harmful flue gas is insufficient, the flue gas content of NOx is not up to the standard, the environmental pollution is great, and therefore, the full-automatic ceramic membrane sintering shuttle kiln is provided.
Disclosure of Invention
The utility model aims to overcome the defects of the prior art and provides a technical scheme capable of solving the problems.
The utility model provides a full-automatic ceramic membrane burns shuttle kiln, includes the kiln body, kiln body side is provided with the automatic operation change platform, and the automatic operation change platform surface is provided with the product kiln car to the product kiln car is transported through the automatic operation change platform and is carried to inside the kiln body, kiln body side wall outside is provided with the stove pressure automatic control mechanism of discharging fume, and link up between kiln body and the stove pressure automatic control mechanism of discharging fume, kiln body top pipeline is provided with harmful flue gas and burns processing system, and the junction between kiln body and the harmful flue gas burns processing system is provided with the main pipe of discharging fume, and the both sides of main pipe of discharging fume all pipeline is provided with the branch pipe of discharging fume, and carries out the pipe connection between the flue gas burns stove and the main pipe of discharging fume through the flue gas burns stove, kiln body both sides all are provided with the accurate flow control's of gas combustion system, and combustion system is provided with a plurality of groups of excess air overgrate air combustor, and the air overgrate air combustor all sets up outside the kiln body.
Preferably, the side part of the flue gas incinerator is provided with a flue gas incinerator gas control group, an incinerator gas machine and a flue gas incineration air control area, and the flue gas incinerator gas control group is electrically connected with the incinerator gas machine.
Preferably, the outlet pipeline of the flue gas incinerator is provided with a first automatic cold air temperature regulating valve, one end pipeline of the first automatic cold air temperature regulating valve is provided with a gas-gas heat exchanger, the inner pipeline of the flue gas incinerator is provided with a second automatic cold air temperature regulating valve, the junction between the first automatic cold air temperature regulating valve and the flue gas incinerator and the junction between the second automatic cold air temperature regulating valve and the flue gas incinerator are provided with an exhaust smoke fan, and side pipelines of the exhaust smoke fan are provided with a smoke exhaust chimney.
Preferably, the side of surplus air overgrate air combustor all is provided with first interface, second interface and third interface, and first interface connection combustion system to the junction between first interface and the combustion system is provided with the main control group of gas, the second interface pipe connection has the hot-blast fire-retardant system of waste heat utilization, and the junction between second interface and the hot-blast fire-retardant system is provided with combustion-supporting and drives into the fan, the third interface pipe connection has the overgrate air control system that adjusts the temperature, and the junction between third interface and the overgrate air control system that adjusts the temperature is provided with automatic temperature regulating total valve.
Preferably, the gas main control group pipeline is provided with a gas main pipe, the side edge of the gas main pipe is provided with a gas branch pipe, the gas branch pipe is connected with the excessive air secondary air burner through a pipeline, and a gas flow control area is arranged at the joint between the excessive air secondary air burner and the gas branch pipe.
Preferably, the combustion-supporting driving fan pipeline is provided with an air filter, the air filter pipeline is connected with a combustion-supporting air main pipe, the combustion-supporting air main pipe is provided with a low-pressure switch for controlling wind pressure, the combustion-supporting air main pipe is connected with the excessive air secondary air burner through a pipeline, the joint between the excessive air secondary air burner and the combustion-supporting air main pipe is provided with an air flow control area, and the side edge of the air flow control area is provided with a cold air switching valve.
Preferably, the automatic temperature-adjusting main valve pipeline is provided with a secondary air main pipe, the other end of the secondary air main pipe is connected with the excessive air secondary air burner through a pipeline, and an air flow manual adjusting switch is arranged at the connection between the secondary air main pipe and the excessive air secondary air burner.
Preferably, the front inlet of the kiln body is vertically provided with an automatic lifting self-locking kiln door, the automatic lifting self-locking kiln door and the front inlet of the kiln body are in the same vertical plane, and the interior of the kiln body is sealed through the automatic lifting self-locking kiln door.
Compared with the prior art, the utility model has the beneficial effects that: the use amount of fuel gas can be reduced, harmful flue gas can be automatically burnt, the flue gas content of NOx is reduced, the emission reaches the standard, and the environment is improved, so that the energy is saved and the environment is protected. Because the hot air combustion-supporting system for utilizing the waste heat is provided, the fuel gas is saved, the automation degree is high, the operation is stable, and the atmosphere control is accurate. The kiln is also suitable for other industries, various products for firing and producing harmful smoke are produced, the environment protection and energy saving are achieved, the working environment is improved, and the labor intensity is reduced. The method is suitable for wide application industry and is suitable for great popularization and use.
Additional aspects and advantages of the utility model will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the utility model.
Drawings
In order to more clearly illustrate the embodiments of the utility model or the technical solutions of the prior art, the drawings which are used in the description of the embodiments or the prior art will be briefly described, it being obvious that the drawings in the description below are only some embodiments of the utility model, and that other drawings can be obtained according to these drawings without inventive faculty for a person skilled in the art.
FIG. 1 is a schematic diagram of a fully automatic ceramic membrane firing shuttle kiln;
FIG. 2 is another schematic structural view of a fully automatic ceramic membrane firing shuttle kiln;
fig. 3 is a schematic view of still another construction of a fully automatic ceramic membrane firing shuttle kiln.
The figure shows: 1. kiln body, 2, combustion system, 3, hot air combustion-supporting system, 4, temperature-regulating overgrate air control system, 5, harmful flue gas incineration treatment system, 6, product kiln car, 7, automatic lifting self-locking kiln door, 8, gas main control group, 9, gas main pipe, 10, gas branch pipe, 11, gas flow control area, 12, surplus air overgrate air burner, 13, flue gas incinerator gas control group, 14, incinerator burner, 15, combustion-supporting driving fan, 16, air filter, 17, combustion-supporting air main pipe, 18, wind pressure low-pressure switch, 19, air flow control area, 20, cold air switching valve, 21, gas-gas heat exchanger, 22, hot air switching valve, 23, flue gas incinerator air control area, 24, automatic temperature-regulating main valve, 25, overgrate air main pipe, 26, air manual air adjusting switch, 27, smoke discharging branch pipe, 28, smoke discharging main pipe, 29, flue gas incinerator, 30, first automatic cold air valve, 31, second automatic temperature-regulating valve, 32, air discharging fan, 33, smoke stack, 34, furnace pressure automatic control smoke discharging mechanism, 35, automatic operation rotary table.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1-3, in the embodiment of the utility model, a full-automatic ceramic film sintering shuttle kiln comprises a kiln body 1, wherein the kiln body 1 is formed by taking GB profile steel as a main structural frame, a lightweight refractory material for bricklaying and a ceramic fiber module for heat preservation, an automatic operation turning table 35 is arranged on the side edge of the kiln body 1, a product kiln car 6 is arranged on the surface of the automatic operation turning table 35, the product kiln car 6 is transported to the inside of the kiln body 1 through the automatic operation turning table 35, a furnace pressure automatic control smoke discharging mechanism 34 is arranged outside the side wall of the kiln body 1, a furnace pressure automatic control smoke discharging mechanism 34 is communicated with the kiln body 1, a harmful smoke burning treatment system 5 is arranged at the pipeline at the top end of the kiln body 1, a smoke discharging main pipe 28 is arranged at the joint between the kiln body 1 and the harmful smoke burning treatment system 5, a smoke discharging branch pipe 27 is arranged at both sides of the smoke discharging main pipe, a smoke burning 29 and the smoke discharging main pipe 28 are connected through the automatic operation turning table 35, a flue 29 and a secondary air combustion system 12 is arranged at both sides of the kiln body 1, and an excess combustion air system 12 is arranged at the outside of the kiln body 2.
The side part of the flue gas incinerator 29 is provided with a flue gas incinerator gas control group 13, an incinerator gas machine 14 and a flue gas incineration air control area 23, and the flue gas incinerator gas control group 13 is electrically connected with the incinerator gas machine 14, so that the incinerator gas machine 14 is controlled through the flue gas incinerator gas control group 13.
The outlet pipeline of the flue gas incinerator 29 is provided with a first automatic cold air temperature regulating valve 30, one end pipeline of the first automatic cold air temperature regulating valve 30 is provided with a gas-gas heat exchanger 21, the inner pipeline of the flue gas incinerator 29 is provided with a second automatic cold air temperature regulating valve 31, the joints between the first automatic cold air temperature regulating valve 30 and the second automatic cold air temperature regulating valve 31 and the flue gas incinerator 29 are provided with an exhaust smoke blower 32, and the side pipeline of the exhaust smoke blower 32 is provided with a smoke exhaust chimney 33.
The side of the excess air secondary air burner 12 is provided with a first interface (not shown in the figure), a second interface (not shown in the figure) and a third interface (not shown in the figure), the first interface is connected with the combustion system 2, a gas main control group 8 is arranged at the joint between the first interface and the combustion system 2, a hot air flame retardant system 3 utilizing waste heat is connected with the second interface pipeline, a combustion supporting driving fan 15 is arranged at the joint between the second interface and the hot air flame retardant system 3, a temperature-regulating secondary air control system 4 is connected with the third interface pipeline, and an automatic temperature-regulating main valve 24 is arranged at the joint between the third interface and the temperature-regulating secondary air control system 4.
The gas main control group 8 is provided with a gas main pipe 9, the side edges of the gas main pipe 9 are respectively provided with a gas branch pipe 10, the gas branch pipes 10 are connected with an excessive air secondary air burner 12 in a pipeline manner, and a gas flow control area 11 is arranged at the joint between the excessive air secondary air burner 12 and the gas branch pipes 10.
The combustion-supporting driving fan 15 is provided with an air filter 16 through a pipeline, the air filter 16 is connected with a combustion-supporting air main pipe 17 through a pipeline, the combustion-supporting air main pipe 17 is provided with a low-pressure switch 18 for controlling wind pressure, the combustion-supporting air main pipe 17 is connected with the excessive air overgrate air combustor 12 through a pipeline, an air flow control area 19 is arranged at the joint between the excessive air overgrate air combustor 12 and the combustion-supporting air main pipe 17, and a cold air switching valve 20 is arranged at the side edge of the air flow control area 19.
The automatic temperature regulating main valve 24 is provided with a secondary air main pipe 25 in a pipeline manner, the other end of the secondary air main pipe 25 is connected with the excessive air secondary air burner 12 in a pipeline manner, and an air flow manual regulating switch 26 is arranged in the connection between the secondary air main pipe 25 and the excessive air secondary air burner 12.
The front inlet of the kiln body 1 is vertically provided with an automatic lifting self-locking kiln door 7, the automatic lifting self-locking kiln door 7 and the front inlet of the kiln body 1 are in the same vertical plane, and the interior of the kiln body 1 is sealed through the automatic lifting self-locking kiln door 7.
It will be evident to those skilled in the art that the utility model is not limited to the details of the foregoing illustrative embodiments, and that the present utility model may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The present embodiments are, therefore, to be considered in all respects as illustrative and not restrictive, the scope of the utility model being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein.
Claims (8)
1. The utility model provides a full-automatic ceramic membrane burns shuttle kiln, includes the kiln body, its characterized in that, kiln body side is provided with the automatic operation change platform, and the automatic operation change platform surface is provided with the product kiln car to the product kiln car is transported to inside the kiln body through the automatic operation change platform, kiln body side wall outside is provided with the stove pressure automatic control mechanism of discharging fume, and link up between kiln body and the stove pressure automatic control mechanism of discharging fume, kiln body top pipeline is provided with harmful flue gas and burns processing system, and the junction between kiln body and the harmful flue gas burns processing system is provided with the main pipe of discharging fume to the both sides of main pipe of discharging fume all are provided with the branch pipe of discharging fume, the side of kiln body is provided with the flue gas and burns the stove and carry out the pipe connection between the main pipe of discharging fume, kiln body both sides all are provided with the accurate flow control's of gas combustion system, and surplus combustion system is provided with a plurality of groups of air secondary air combustor, and surplus air secondary air combustor all sets up in kiln body outside.
2. The fully automatic ceramic membrane firing shuttle kiln according to claim 1, wherein a flue gas incinerator gas control group, an incinerator gas engine and a flue gas incineration air control area are arranged on the side portion of the flue gas incinerator, and the flue gas incinerator gas control group is electrically connected with the incinerator gas engine.
3. The full-automatic ceramic film firing shuttle kiln according to claim 1, wherein a first automatic cold air temperature regulating valve is arranged at an outlet pipeline of the flue gas incinerator, a gas-gas heat exchanger is arranged at one end pipeline of the first automatic cold air temperature regulating valve, a second automatic cold air temperature regulating valve is arranged at an inner pipeline of the flue gas incinerator, an exhaust smoke blower is arranged at a joint between the first automatic cold air temperature regulating valve and the flue gas incinerator, and a smoke exhaust chimney is arranged at a side pipeline of the exhaust smoke blower.
4. The full-automatic ceramic membrane firing shuttle kiln according to claim 1, wherein the side edges of the excess air overgrate air burner are respectively provided with a first interface, a second interface and a third interface, the first interface is connected with a combustion system, a gas main control group is arranged at the joint between the first interface and the combustion system, the second interface pipeline is connected with a hot air flame-retardant system utilizing waste heat, a combustion-supporting driving fan is arranged at the joint between the second interface and the hot air flame-retardant system, the third interface pipeline is connected with a temperature-regulating overgrate air control system, and an automatic temperature-regulating main valve is arranged at the joint between the third interface and the temperature-regulating overgrate air control system.
5. The full-automatic ceramic membrane firing shuttle kiln according to claim 4, wherein the gas main control group pipeline is provided with a gas main pipe, the side edges of the gas main pipe are respectively provided with a gas branch pipe, the gas branch pipes are connected with the excessive air secondary air burner in a pipeline manner, and a gas flow control area is arranged at the joint between the excessive air secondary air burner and the gas branch pipes.
6. The fully automatic ceramic membrane firing shuttle kiln according to claim 4, wherein the combustion-supporting driving fan pipeline is provided with an air filter, the air filter pipeline is connected with a combustion-supporting air main pipe, the combustion-supporting air main pipe is provided with a low-pressure switch for controlling wind pressure, the combustion-supporting air main pipe is connected with the excessive air overgrate air burner through a pipeline, the joint between the excessive air overgrate air burner and the combustion-supporting air main pipe is provided with an air flow control area, and the side edge of the air flow control area is provided with a cold air switching valve.
7. The full-automatic ceramic film firing shuttle kiln according to claim 4, wherein the automatic temperature-regulating main valve pipeline is provided with a secondary air main pipe, the other end of the secondary air main pipe is connected with a pipeline between the excessive air secondary air burners, and an air flow manual regulating switch is connected between the secondary air main pipe and the excessive air secondary air burners.
8. The fully automatic ceramic film firing shuttle kiln according to claim 1, wherein the front inlet of the kiln body is vertically provided with an automatic lifting self-locking kiln door, the automatic lifting self-locking kiln door and the front inlet of the kiln body are on the same vertical surface, and the interior of the kiln body is sealed by the automatic lifting self-locking kiln door.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320438464.5U CN220366676U (en) | 2023-03-09 | 2023-03-09 | Full-automatic ceramic film sintering shuttle kiln |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320438464.5U CN220366676U (en) | 2023-03-09 | 2023-03-09 | Full-automatic ceramic film sintering shuttle kiln |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220366676U true CN220366676U (en) | 2024-01-19 |
Family
ID=89512877
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320438464.5U Active CN220366676U (en) | 2023-03-09 | 2023-03-09 | Full-automatic ceramic film sintering shuttle kiln |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220366676U (en) |
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- 2023-03-09 CN CN202320438464.5U patent/CN220366676U/en active Active
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