CN202865101U - Molten diamond bead blank tank pool heat exchange chamber - Google Patents
Molten diamond bead blank tank pool heat exchange chamber Download PDFInfo
- Publication number
- CN202865101U CN202865101U CN2012204725001U CN201220472500U CN202865101U CN 202865101 U CN202865101 U CN 202865101U CN 2012204725001 U CN2012204725001 U CN 2012204725001U CN 201220472500 U CN201220472500 U CN 201220472500U CN 202865101 U CN202865101 U CN 202865101U
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- heat exchange
- pipeline
- exchange pipeline
- combustion air
- intake stack
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- 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
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Abstract
The utility model relates to a molten diamond bead blank tank pool heat exchange chamber. The heat exchange chamber comprises a waste gas pipeline, a combustion air pipeline and a heat exchange chamber, wherein the waste gas pipeline and the combustion air pipeline are connected with a tank pool; the heat exchange chamber comprises more than one layer of heat exchange pipelines, and each layer of heat exchange pipelines is formed by alternate parallel adjacent arrangement of N air inlet pipelines and N-1 air outlet pipelines; waste gas and combustion air are subjected to heat exchange through the heat exchange pipeline, so that the combustion air can be preheated, the energy loss can be reduced, the combustion utilization of fuel in the tank furnace can be improved, the raw material can be molten uniformly, and the final product has stable performance; and the air outlet direction of waste gas and air intake direction of combustion air are kept to be opposite, so that the heat reclamation rate can be further improved.
Description
Technical field
The utility model relates to a kind of tank furnace Heat Room, is a kind of for fusing water brill pearl blank tank furnace Heat Room specifically.
Background technology
Water bores as a kind of ornament, liked by the people.The conventional crucibles stove is produced water and is bored, and its throughput is little, and the color poor consistency is progressively used tank furnace production instead.The combustion air that ortho-water bores pearl base tank furnace directly adopts outside air, and combustion-supporting temperature is not enough, is unfavorable for the abundant burning of fuel, the serious waste energy, and production cost is high; Burn incompletely easily produces large quantity of exhaust gas, and waste gas directly is discharged in the atmosphere, pollutes environment; And the tank furnace internal combustion is insufficient, and it is inhomogeneous that water bores the fusing of pearl base raw material, affects final pearl base product performance.
Summary of the invention
In order to solve tank furnace combustion air temperature deficiency in the prior art, be unfavorable for full combustion of fuel, easily produce large quantity of exhaust gas, raw material melts the inhomogeneous deficiency that affects product performance, and it is a kind of simple in structure that the utility model provides, can effectively utilize tank furnace heat energy from waste gas warm-up combustion-supporting air, be beneficial to the abundant burning of fuel, energy efficient reduces waste gas, dust discharge, reduce environmental pollution, guarantee all fusing water brill pearl blank tank furnace Heat Rooms of even the finished product stable performance of raw material fusing.
The technical solution adopted in the utility model is: a kind of fusing water bores pearl blank tank furnace Heat Room, it is characterized in that comprising exhaust pipe, combustion air pipeline and Heat Room, exhaust pipe is connected with the combustion air pipeline and is connected tank furnace, Heat Room comprises the heat exchange pipeline that one deck is above, every layer of heat exchange pipeline is by N root intake stack and the parallel adjacent setting in N-1 root wind pipe space, intake stack is connected the difference end and is connected respectively combustion air pipeline and exhaust pipe in the first layer heat exchange pipeline with wind pipe, arbitrarily in one deck heat exchange pipeline intake stack terminal with lower one deck heat exchange pipeline in the intake stack same side be communicated with up and down, in lower one deck heat exchange pipeline the head end of intake stack with descend again one deck heat exchange pipeline in the same side of intake stack be communicated with up and down, wind pipe is terminal in one deck heat exchange pipeline arbitrarily is communicated with up and down with the wind pipe same side of lower one deck heat exchange pipeline, in lower one deck heat exchange pipeline the head end of wind pipe with descend again one deck heat exchange pipeline in the same side of wind pipe be communicated with up and down, the intake stack of lowest layer heat exchange pipeline is connected the difference end and is connected respectively outside blast inlet and air outlet with wind pipe.
Further, described exhaust pipe and combustion air pipeline connect respectively end and the head end of tank furnace.
Again further, described combustion air pipeline is arranged between tank furnace and the exhaust pipe.
Adopt above technology, the beneficial effects of the utility model are: Heat Room is recycled the discarded energy in the tank furnace combustion exhaust again, waste gas and combustion air are by carrying out heat exchange by the adjacent heat exchange pipeline that forms with the wind pipe interval of intake stack more than one deck, combustion air is carried out preheating, reduce energy loss, improve tank furnace fuel combustion utilization ratio, guarantee all even the finished product stable performances of raw material fusing, the air-out direction of waste gas and the air intake direction of combustion air always keep in opposite directions simultaneously, can further improve heat energy recovery rate; The raw material dust of carrying secretly in the waste gas, volatile matter are through under the above heat exchange pipeline drag effect of Heat Room one deck, and drop in temperature in the Heat Room, constantly separate out, and are deposited on the Heat Room base plate, have reduced the quantity discharged in the atmosphere, have reduced environmental pollution.
Description of drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is the utility model Heat Room vertical view;
Fig. 3 is A-A view among Fig. 2;
Fig. 4 is B-B view among Fig. 2.
Among the figure: tank furnace 1, combustion air pipeline 2, exhaust pipe 3, Heat Room 4, blast inlet 5, intake stack 6, air outlet 7, wind pipe 8.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
Shown in Fig. 1-4, a kind of fusing water bores pearl blank tank furnace Heat Room and comprises exhaust pipe 3, combustion air pipeline 2 and Heat Room 1, exhaust pipe 3 is connected end and the head end that all connects tank furnace 1 with the combustion air pipeline, the combustion air pipeline is arranged between tank furnace and the exhaust pipe, Heat Room 1 comprises the heat exchange pipeline that one deck is above, every layer of heat exchange pipeline is by N root intake stack 6 and the N-1 root wind pipe parallel adjacent settings in 8 spaces (as shown in Figure 2), intake stack is connected the difference end and is connected respectively combustion air pipeline and exhaust pipe in the first layer heat exchange pipeline with wind pipe, arbitrarily in one deck heat exchange pipeline intake stack terminal with lower one deck heat exchange pipeline in the intake stack same side be communicated with up and down, in lower one deck heat exchange pipeline the head end of intake stack with descend again one deck heat exchange pipeline in the same side of intake stack be communicated with up and down (as shown in Figure 3), wind pipe is terminal in one deck heat exchange pipeline arbitrarily is communicated with up and down with the wind pipe same side of lower one deck heat exchange pipeline, in lower one deck heat exchange pipeline the head end of wind pipe with descend again one deck heat exchange pipeline in the same side of wind pipe be communicated with up and down (as shown in Figure 4), the intake stack of lowest layer heat exchange pipeline is connected the difference end and is connected respectively outside blast inlet 5 and air outlet 8 with wind pipe.
Claims (3)
1. a fusing water bores pearl blank tank furnace Heat Room, it is characterized in that: comprise exhaust pipe, combustion air pipeline and Heat Room, exhaust pipe is connected with the combustion air pipeline and is connected tank furnace, Heat Room comprises the heat exchange pipeline that one deck is above, every layer of heat exchange pipeline is by N root intake stack and the parallel adjacent setting in N-1 root wind pipe space, intake stack is connected same side and is connected respectively combustion air pipeline and exhaust pipe in the first layer heat exchange pipeline with wind pipe, arbitrarily in one deck heat exchange pipeline intake stack terminal with lower one deck heat exchange pipeline in the intake stack same side be communicated with up and down, in lower one deck heat exchange pipeline the head end of intake stack with descend again one deck heat exchange pipeline in the same side of intake stack be communicated with up and down, wind pipe is terminal in one deck heat exchange pipeline arbitrarily is communicated with up and down with the wind pipe same side of lower one deck heat exchange pipeline, in lower one deck heat exchange pipeline the head end of wind pipe with descend again one deck heat exchange pipeline in the same side of wind pipe be communicated with up and down, be provided with arbitrarily a commutation pipeline in one deck heat exchange pipeline in the intake stack, the two ends of commutation pipeline connect, are connected the difference end and connect respectively outside blast inlet and air outlet in the two ends of intake stack in the lower two-layer heat exchange pipeline, the intake stack of lowest layer heat exchange pipeline with wind pipe.
2. a kind of fusing water according to claim 1 bores pearl blank tank furnace Heat Room, it is characterized in that: described exhaust pipe and combustion air pipeline connect respectively end and the head end of tank furnace.
3. a kind of fusing water according to claim 1 and 2 bores pearl blank tank furnace Heat Room, and it is characterized in that: described combustion air pipeline is arranged between tank furnace and the exhaust pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204725001U CN202865101U (en) | 2012-09-17 | 2012-09-17 | Molten diamond bead blank tank pool heat exchange chamber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204725001U CN202865101U (en) | 2012-09-17 | 2012-09-17 | Molten diamond bead blank tank pool heat exchange chamber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202865101U true CN202865101U (en) | 2013-04-10 |
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ID=48031837
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012204725001U Expired - Fee Related CN202865101U (en) | 2012-09-17 | 2012-09-17 | Molten diamond bead blank tank pool heat exchange chamber |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202865101U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102838267A (en) * | 2012-09-17 | 2012-12-26 | 江苏锦程集团科技有限公司 | Heat exchange chamber of diamond bead blank melting tank furnace |
| CN114160053A (en) * | 2022-02-14 | 2022-03-11 | 龙口市化工厂 | Sulfuryl fluoride reaction device |
-
2012
- 2012-09-17 CN CN2012204725001U patent/CN202865101U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102838267A (en) * | 2012-09-17 | 2012-12-26 | 江苏锦程集团科技有限公司 | Heat exchange chamber of diamond bead blank melting tank furnace |
| CN114160053A (en) * | 2022-02-14 | 2022-03-11 | 龙口市化工厂 | Sulfuryl fluoride reaction device |
| CN114160053B (en) * | 2022-02-14 | 2022-05-31 | 龙口市化工厂 | Sulfuryl fluoride reaction device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130410 Termination date: 20200917 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |