CN203615308U - Glass kiln waste heat-oil heat conduction generating device - Google Patents
Glass kiln waste heat-oil heat conduction generating device Download PDFInfo
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- CN203615308U CN203615308U CN201320517481.4U CN201320517481U CN203615308U CN 203615308 U CN203615308 U CN 203615308U CN 201320517481 U CN201320517481 U CN 201320517481U CN 203615308 U CN203615308 U CN 203615308U
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Abstract
The utility model relates to a glass kiln waste heat-oil heat conduction generating device comprising a pipeline, a case body, an expansion groove, a first circulating pump (4-1), a second circulating pump (4-2), a third circulating pump (4-3), an energy storing tank, an oil temperature tank and a heat supplying body. By the use of a heat source of a glass kiln waste heat pipeline and characteristics of a high boiling point and specific heat of conduction oil, the conduction oil can be circulated and transmitted, so the heat supplying body can be heated and advantages are achieved with obvious energy conversancy, high safety coefficient, environment protection, free of emission, concentrated water and incrustation, free of water softening process and large water saving amount; steam is produced via air heating and speed for air heating is times quicker than liquid water heating; and the glass kiln waste heat-oil heat conduction generating device breaks through a traditional mode utilized for hundreds of years, so production cost of cement is effectively reduced.
Description
Technical field
The utility model relates to the UTILIZATION OF VESIDUAL HEAT IN of glass industry, specifically a kind of glass furnace waste heat oil heat conduction electricity generation system.
Background technology
We know, the exhausted air quantity that glass furnace is discharged is very large, and temperature is lower, and utilization rate, between 30～40%, have a large amount of complementary energy and produce, and most of complementary energy exists with the form of waste gas residual heat.If waste gas residual heat resource fully not recycled, not only waste the waste heat energy, but also contaminated environment is destroyed nature.
The glass furnace of glass industry uses heavy oil, natural gas, coal gas etc. as fuel conventionally, fuel in stove, burn form flue gas be discharged from outside kiln, produced waste gas residual heat resource.Glass furnace waste gas belongs to middle temperature waste gas residual heat, and temperature is 450～550 ℃, and exhaust gas flow is less, and hot grade is lower, and recuperation of heat cost is larger; The parameter (temperature, flow, pressure) of waste gas residual heat has certain fluctuation, and fluctuation range is large; The construction scale of most glass factories wall scroll glass production line is little, and the waste heat of glass furnace is more limited comparatively speaking, and the investment of cogeneration project relative unit is large, and investment cycle is long; The scale of glass furnace waste gas residual heat resource is relatively more less than cement industry.At present, glass industry mainly adopts the recovery approach of heat utilization both at home and abroad, and heat pipe waste heat boiler is set, recovery section heat energy from waste gas, and flue gas major part is partly passed through.Waste heat boiler is only for generation of saturated vapor, offer heavy oil heating or bear Heating Load, or the low-temp low-pressure device for generating power by waste heat of supporting small-scale, its efficiency of utilization and TRT efficiency are low, the stability of a system is poor, conventionally the exhaust gas temperature of waste heat boiler is at 230～250 ℃, and utilization rate of waste heat only has 30～40%.And in fact, the smoke discharging residual heat utilization rate of glass furnace can reach 65～80%.
Summary of the invention
The purpose of this utility model is that in order to solve, the UTILIZATION OF VESIDUAL HEAT IN efficiency existing in traditional glass kiln waste gas heat utilization is low, generating efficiency is low, the stability of a system is poor, recuperation of heat cost is large, waste gas residual heat parameter fluctuation scope is large, environmental pollution serious, one-time investment high in cost of production technical problem.To provide, a kind of utilization rate of waste heat is high, generating efficiency is high, the stability of a system is good, recuperation of heat cost is low, simple structure, environmental protection, zero-emission, of many uses, long service life, glass furnace waste heat oil heat conduction TRT easy to maintenance.
Oil heat conducting and supplying device in glass furnace cogeneration, it is made up of pipeline, casing, expansion slot, first circulating pump, second circulating pump and the 3rd circulating pump, energy storage canister, oil temperature tank and hot body, it is characterized in that: two metallic conduits and insulation material are housed in described casing, and pipeline is connected with two metallic conduits in casing; Described expansion slot is slack tank body, is surrounded by insulation material outward, the conduction oil that inner chamber splendid attire expands; Described energy storage canister is surrounded by insulation material outward, splendid attire Oil Guide heat in tank body, and tank body is respectively equipped with two groups of import and export pipes; Described oil temperature tank is surrounded by insulation material outward, and electrothermal tube is inside housed, the in-built conduction oil of tank body, and tank body has respectively two groups of import and export pipes; Described hot body inner chamber has been installed the oily thermal conductive metal pipe that has import and export; Device for cleaning pipeline is crossed two pipelines in connect box and energy storage canister one group and is connected into and out of hydraulic fluid port, connects on a pipeline of energy storage canister and pipeline connect box first circulating pump and expansion slot are housed; Another group of energy storage canister goes out, inlet pipe road is connected into and out of oil pipe with oil temperature tank, on the tank connected pipeline of oil temperature tank and energy storage, second circulating pump is housed; The going out of oil temperature tank, inlet tube are connected with the import and export of oily thermal conductive metal pipe in hot body by pipeline, on one article of pipeline that oil temperature tank is connected with oily thermal conductive metal pipe in hot body end, the 3rd circulating pump are housed.
The oily heat conduction steam generator of described oil heat conducting and supplying device, it regulates storage tank to form by pipeline, casing, expansion slot, first circulating pump, energy storage canister, water heat exchanger, oil temperature tank, high pressure piston pump, high pressure sprays fog equipment, steam generator and steam, described pipeline is connected with casing, and two metallic conduits and insulation material are housed in casing, described expansion slot is slack tank body, described energy storage canister is surrounded by insulation material outward, tank inner chamber splendid attire Oil Guide heat, and tank body is respectively equipped with two groups of import and export pipes, described water heat exchanger is surrounded by insulation material outward, electrothermal tube is inside housed and has the oily heating of metal coil pipe of import and export pipe, splendid attire water in water heat exchanger, described oil temperature tank is surrounded by insulation material outward, and electrothermal tube is inside housed, tank inner chamber dress conduction oil, and tank body is respectively equipped with two groups of import and export pipes, described steam generator is some layers of annular seal pipeline, Article 1, oil guide pipe, Article 2 oil guide pipe, Article 3 oil guide pipe and Article 4 oil guide pipe, Article 1, steam pipe, Article 2 steam pipe and Article 3 steam pipe, at front end steam pipe and Article 2 steam pipe, Article 2 oil guide pipe and Article 3 oil guide pipe are respectively equipped with tube connector, Article 1, oil guide pipe is connected with pipeline, Article 3 steam pipe is connected with pipeline, Article 4 oil guide pipe is connected with pipeline, at rear end Article 1 oil guide pipe and Article 2 oil guide pipe, Article 2 steam pipe and Article 3 steam pipe, Article 3 oil guide pipe and Article 4 oil guide pipe are respectively equipped with tube connector, it is slack tank that described steam regulates energy storage canister, is provided with steam import and export pipe, being connected to of the described each parts of oily heat conduction steam generator: device for cleaning pipeline is crossed entering of two pipelines in connect box and energy storage canister, oil-out connects, on a wherein pipeline of connection energy storage canister and connect box, first circulating pump and expansion slot are housed, going out of energy storage canister, inlet pipe road respectively with the entering of the oily heating of metal coil pipe of water heat exchanger, flowline and oil temperature tank enter, flowline connects, on the tank connected wherein one article of pipeline of the oily heating of metal coil pipe of water heat exchanger and energy storage, the 4th circulating pump is housed, on the tank connected wherein pipe of oil temperature tank and energy storage, second circulating pump is housed, hot water exchanger is connected with high pressure piston pump inlet tube by another pipeline, high pressure piston pump outlet conduit connects high pressure sprays fog equipment, high pressure sprays fog equipment is connected with the rear end steam pipe of steam generator again, the front end steam pipe of steam generator regulates storage tank inlet tube to be connected by pipeline and steam, the outlet of oil temperature tank is connected with the front end oil guide pipe 20 of steam generator by pipeline, inlet tube is connected with the front end Article 4 oil guide pipe of steam generator by pipeline, circulating pump is housed in connecting pipe.
The utility model has the advantages that:
The utility model adopts modular steam generator can expand at any time increase-volume; Obvious energy conservation, without stop production maintenance, can adjust at any time vapor (steam) temperature and pressure, moment steams at any time, safety coefficient is high, environmental protection, zero-emission, without condensed water, Non-scale, without soft water processing, water-saving amount is large, of many uses, by heated air producing steam, than high several times of the liquid aquatic products vapour speed of heating, break through century-old traditional mode.
Accompanying drawing explanation
Fig. 1 is the utility model oil heat conducting and supplying device structural representation.
Fig. 2 is the utility model oil heat conduction steam generator structural representation.
Fig. 3 is the utility model steam generator front-end architecture schematic diagram.
Fig. 4 is the utility model steam generator rear end structure schematic diagram.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail:
As shown in Figure 1, pipeline of the present utility model (1), casing (2), expansion slot (3), first circulating pump (4-1), second circulating pump (4-2), the 3rd circulating pump (4-3), energy storage canister (5), oil temperature tank (6) and hot body (8) composition, it is characterized in that, in described casing (2), two metallic conduits and insulation material are housed, the two ends of pipeline (1) are connected with two metallic conduits in casing (2) respectively; Conduction oil in pipeline (1) is recurrent state in sealing.When waste heat, treat that the maximum temperature that oil temperature in oil temperature tank (6) reaches waste heat and can provide closes first circulating pump, open electrothermal tube (9), give the conduction oil additional heat of oil temperature tank (6), conduction oil in electrical heating oil temperature tank (6) reaches temperature required, by oily thermal conductive metal pipe (7), heat energy is offered to hot body (8).
As shown in Figure 2, pipeline of the present utility model (1) is connected into and out of hydraulic fluid port by two pipelines in connect box (2) and energy storage canister (5), energy storage canister (5) has insulation material, tank inner chamber is empty, for splendid attire Oil Guide heat, connect on the wherein pipeline of energy storage canister (5) and pipeline and have first circulating pump and be connected expansion slot (3).Going out of energy storage canister (5), oil-in enters with water heat exchanger (10) respectively by pipeline, oil-out and oil temperature tank (6) enter, oil-out connects, water heat exchanger (10) has insulation material and metal coil pipe (7-1), for heating water, casing (2) inner chamber is empty, for splendid attire water, on the wherein one article of pipeline being connected with energy storage canister (5), the 4th circulating pump is housed, water heat exchanger (10) is connected with high pressure piston pump (11) by pipeline, high pressure piston pump (11) connects high pressure sprays fog equipment (12) by pipeline and is connected with the rear end Article 1 steam pipe (21) of steam generator (13), the front end Article 3 steam pipe (25) of steam generator (13) regulates storage tank (14) to be connected by pipeline and steam, oil temperature tank (6) has insulation material, tank inner chamber is empty, for splendid attire conduction oil, the oil-out of oil temperature tank (6) is connected with the front end Article 1 oil guide pipe (20) of steam generator (13) by pipeline (16), oil-in is connected with the front end Article 4 oil guide pipe (26) of steam generator (13) by pipeline (15).Conduction oil is injected to energy storage canister (5), oil temperature tank (6) and steam generator (13) oil guide pipe.Open first circulating pump between pipeline (1) and energy storage canister (5), make conduction oil circulating, by the transmission of pipeline waste heat, be stored in energy storage canister (5) between the two; Open the 4th circulating pump between energy storage canister (5) and water heat exchanger (10), make conduction oil at second circulating pump between the two, open the 3rd circulating pump between oil temperature tank (6) and steam generator (13), conduction oil is circulated between three; Treat that the oil temperature in oil temperature tank (6) and steam generator (13) reaches stripping temperature processed, hot water in water heat exchanger (10) is passed through to high pressure sprays fog equipment (12) again through high pressure piston pump (11), hot water is sprayed into the vaporific formula of high pressure in the rear end Article 1 steam pipe (21) of steam generator (13), the vaporific hot water of high pressure is heated in the steam generator (13) of high temperature, and very fast degree is converted into steam; Steam is discharged by the front end Article 3 steam pipe (25) of steam generator (13), enter into steam and regulate storage tank (14), and oily heat conduction is played very large effect to boiler steam temperature fast lifting, especially for the preheating of glass kiln residual heat power generation project saturated vapor, can make the generated energy of whole power generating system by glass-kiln waste heat significantly promote, for making client.
As shown in Figure 3,4, the outlet conduit (18) of the high pressure piston pump (11) of the utility model steam generator, high pressure sprays fog equipment (12), Article 1, oil guide pipe (20), Article 2 oil guide pipe (22), Article 3 oil guide pipe (24) and Article 4 oil guide pipe (26), Article 1, steam pipe (21), Article 2 steam pipe (23) and Article 3 steam pipe (25), pipeline (15), pipeline (16), pipeline (17).
Claims (2)
1. the oil heat conducting and supplying device in a glass kiln residual heat oil heat conduction TRT, it is characterized in that: it is made up of pipeline (1), casing (2), expansion slot (3), first circulating pump (4-1), second circulating pump (4-2), the 3rd circulating pump (4-3), energy storage canister (5), oil temperature tank (6) and hot body (8), in described casing (2), two metallic conduits and insulation material are housed, pipeline (1) is connected with two metallic conduits in casing (2); Described expansion slot (3) is slack tank body, is surrounded by insulation material outward, the conduction oil that inner chamber splendid attire expands; The outer insulation material that is surrounded by of described energy storage canister (5), splendid attire Oil Guide heat in tank body, tank body is respectively equipped with two groups of import and export pipes; Described oil temperature tank (6), is surrounded by insulation material outward, and electrothermal tube (9-1) is inside housed, the in-built conduction oil of tank body, and tank body is respectively equipped with two groups of import and export pipes; Described hot body (8) inner chamber has been installed the oily thermal conductive metal pipe of import and export (7); By two pipelines in connect box (2), a group with energy storage canister (5) is connected into and out of hydraulic fluid port pipeline (1), connects on a pipeline of energy storage canister (5) and pipeline (1) connect box (2) first circulating pump and expansion slot (3) are housed; Another group of energy storage canister (5) goes out, inlet pipe road is connected into and out of oil pipe with oil temperature tank (6), on the pipeline that oil temperature tank (6) is connected with energy storage canister (5), second circulating pump is housed; The going out of oil temperature tank (6), inlet tube are connected with the import and export of oily thermal conductive metal pipe in hot body (8) by pipeline, on one article of pipeline that oil temperature tank (6) is connected with the interior oily thermal conductive metal pipe (7) of hot body end, the 3rd circulating pump are housed.
2. the oil heat conducting and supplying device in a kind of glass kiln residual heat oil heat conduction TRT according to claim 1, it is characterized in that, oil heat conduction steam generator, it regulates storage tank (14) to form by pipeline (1), casing (2), expansion slot (3), first circulating pump, energy storage canister (5), water heat exchanger (10), oil temperature tank (6), high pressure piston pump (11), high pressure sprays fog equipment (12), steam generator (13) and steam, described pipeline (1) is connected with casing (2), two metallic conduits and insulation material are housed in casing (2), the described slack tank body that is expanded to, described energy storage canister is surrounded by insulation material outward, tank inner chamber splendid attire Oil Guide heat, tank body is respectively equipped with two groups of import and export pipes, described water heat exchanger (10) is outer is surrounded by insulation material, electrothermal tube (9-1) is inside housed and has the oily heating of metal coil pipe (7-1) of import and export pipe, the interior splendid attire water of water heat exchanger (10), described oil temperature tank (6) is outer is surrounded by insulation material, and electrothermal tube (9) is inside housed, tank inner chamber dress conduction oil, and tank body is respectively equipped with two groups of import and export pipes, described steam generator (13) is some layers of annular seal pipeline, Article 1, oil guide pipe (20), Article 2 oil guide pipe (22), Article 3 oil guide pipe (24) and Article 4 oil guide pipe (26), Article 1, steam pipe (21), Article 2 steam pipe (23) and Article 3 steam pipe (25), at front end Article 1 steam pipe (21) and Article 2 steam pipe (23), Article 2 oil guide pipe (22) is respectively equipped with tube connector with Article 3 oil guide pipe (24), Article 1, oil guide pipe (20) is connected with Article 4 oil guide pipe (26), Article 2 steam pipe (23) is connected with Article 3 steam pipe (25), Article 3 oil guide pipe (24) is connected with Article 4 oil guide pipe (26), at rear end Article 1 oil guide pipe (20) and Article 2 oil guide pipe (22), Article 2 steam pipe (23) and Article 3 steam pipe (25), Article 3 oil guide pipe (24) is respectively equipped with tube connector with Article 4 oil guide pipe (26), being connected to of the described each parts of oily heat conduction steam generator: pipeline (1) enters by two pipelines in connect box (2) and energy storage canister (5), oil-out connects, on a wherein pipeline of connection energy storage canister (5) and connect box (2), first circulating pump and expansion slot (3) are housed, going out of energy storage canister (5), oily heating of metal coil pipe (7-1) of inlet pipe road difference water heat exchanger (10) enters, flowline and oil temperature tank (6) enter, flowline connects, on wherein one article of pipeline that the oily heating of metal coil pipe (7-1) of water heat exchanger (10) is connected with energy storage canister (5), the 4th circulating pump is housed, on the wherein pipeline that oil temperature tank (6) is connected with energy storage canister (5), second circulating pump is housed, water heat exchanger (10) is connected with high pressure piston pump (11) inlet tube by another pipeline, high pressure piston pump (11) outlet conduit connects high pressure sprays fog equipment (12) and is connected with rear end the 2nd pipe of steam generator (13), front end the 6th pipe of steam generator (13) regulates storage tank (14) inlet tube to be connected by pipeline (17) and steam, the outlet of oil temperature tank (6) is connected with the front end oil guide pipe (20) of steam generator (13) by pipeline (16), inlet tube is connected with the front end Article 4 oil guide pipe (26) of steam generator (13) by pipeline (15), the 3rd circulating pump is housed in connecting pipe (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320517481.4U CN203615308U (en) | 2013-08-23 | 2013-08-23 | Glass kiln waste heat-oil heat conduction generating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320517481.4U CN203615308U (en) | 2013-08-23 | 2013-08-23 | Glass kiln waste heat-oil heat conduction generating device |
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| Publication Number | Publication Date |
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| CN203615308U true CN203615308U (en) | 2014-05-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201320517481.4U Expired - Fee Related CN203615308U (en) | 2013-08-23 | 2013-08-23 | Glass kiln waste heat-oil heat conduction generating device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110953030A (en) * | 2019-11-19 | 2020-04-03 | 深圳市凯盛科技工程有限公司 | Method and device for generating electricity by using waste heat of glass kiln |
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2013
- 2013-08-23 CN CN201320517481.4U patent/CN203615308U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110953030A (en) * | 2019-11-19 | 2020-04-03 | 深圳市凯盛科技工程有限公司 | Method and device for generating electricity by using waste heat of glass kiln |
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| 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: 20140528 Termination date: 20210823 |
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| CF01 | Termination of patent right due to non-payment of annual fee |