CN103486870A - Smoke waste heat refrigeration and heating supply system of industrial kiln stove - Google Patents
Smoke waste heat refrigeration and heating supply system of industrial kiln stove Download PDFInfo
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- CN103486870A CN103486870A CN201310457536.1A CN201310457536A CN103486870A CN 103486870 A CN103486870 A CN 103486870A CN 201310457536 A CN201310457536 A CN 201310457536A CN 103486870 A CN103486870 A CN 103486870A
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- smoke
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- flue gas
- chimney
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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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
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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
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Abstract
The invention relates to a smoke waste heat refrigeration and heating supply system of an industrial kiln stove. The system comprises the industrial kiln stove (1), a forced draught blower (5), a kiln stove smoke exhaust channel (3) and a kiln stove chimney (4), and is characterized in that a smoke waste heat type lithium bromide absorption type refrigerating machine, an induced draft fan (10), a bromine refrigerator smoke inlet pipe (6) and a bromine refrigerator smoke exhaust pipe (9) are additionally arranged in the system, the smoke inlet end of the bromine refrigerator smoke inlet pipe (6) is connected to the kiln stove smoke exhaust channel (3), a smoke valve (7) is arranged on the bromine refrigerator smoke inlet pipe (6), the induced draft fan (10) is arranged on the bromine refrigerator smoke exhaust pipe (9) , and the smoke outlet end of the induced draft fan (10) is provided and connected with an induced draft fan smoke exhaust chimney (11). According to the smoke waste heat refrigeration and heating supply system, the fuel heat utilization rate of the industrial kiln stove can be greatly improved.
Description
Technical field
The present invention relates to a kind of industrial furnace smoke utilizing waste heat for refrigeration heating system.Belong to air conditioner technical field.
Background technology
Industrial Stoves are widely used in the industries such as pottery, cement, glass, metallurgy, iron and steel and metal processing.Most burning fuel oils (heavy oil, fuel oil), combustion gas (natural gas, coal gas) operation.Exhaust gas temperature higher (up to 500 ℃~600 ℃), heat loss due to exhaust gas is large, and energy consumption is high.The energy consumption rich and influential family who belongs to industrial circle.Industrial Stoves manufacturer and application enterprise all pay much attention to the efficiency that improves Industrial Stoves all the time.To save the energy and to increase economic efficiency.The large-sized industrial kiln of the sector application such as cement and glass generally all disposes waste heat boiler simultaneously, utilizes the fume afterheat heating waste heat boiler of Industrial Stoves to produce steam.This steam can be used for generating, technique heating or life vapour.But the medium and small Industrial Stoves of majority of the sector applications such as metallurgy, iron and steel and metal processing, due to the exhaust smoke level less, be not suitable for configuring waste heat boiler, mostly adopt the fume afterheat shown in Fig. 1 to utilize mode, air preheater 2 is set in kiln exit flue 3, utilize the fume afterheat of kiln discharge to carry out preheating to combustion air, to reduce exhaust gas temperature, improve the air themperature that enters kiln simultaneously, reduce fuel consumption, energy utilization rate and performance driving economy all are improved.But this UTILIZATION OF VESIDUAL HEAT IN technology is limited to the recovery utilization rate of fume afterheat, the flue-gas temperature that enter kiln chimney 4 after air preheater, finally enters atmosphere still up to 300 ℃~400 ℃, fume afterheat still is underutilized.
Summary of the invention
The object of the invention is to overcome above-mentioned deficiency, the industrial furnace smoke utilizing waste heat for refrigeration heating system that provides a kind of fuel heat utilization ratio that makes Industrial Stoves to be greatly improved.
The object of the present invention is achieved like this: a kind of industrial furnace smoke utilizing waste heat for refrigeration heating system, this system comprises Industrial Stoves, pressure fan, kiln exit flue and kiln chimney, it is characterized in that: described system has additional fume afterheat type lithium-bromide absorption-type refrigerating machine, air-introduced machine, bromine cooling machine smoke-intake pipe and bromine cooling machine smoke exhaust pipe, wherein, the gas approach end of bromine cooling machine smoke-intake pipe is connected on the kiln exit flue, be provided with smoke valve on the bromine cooling machine smoke-intake pipe, air-introduced machine is arranged on the bromine cooling machine smoke exhaust pipe, the smoke outlet of air-introduced machine is installed and is connected with the air-introduced machine chimney.
Industrial furnace smoke utilizing waste heat for refrigeration heating system of the present invention arranges air preheater in described kiln exit flue simultaneously.
Industrial furnace smoke utilizing waste heat for refrigeration heating system of the present invention, described fume afterheat type lithium-bromide absorption-type refrigerating machine is flue gas type lithium bromide adsorption water chilling unit, flue gas type cold/hot water machine of lithium bromide group, flue gas fuel supplementing type lithium bromide adsorption water chilling unit or flue gas fuel supplementing type cold/hot water machine of lithium bromide group.
Industrial furnace smoke utilizing waste heat for refrigeration heating system of the present invention, described flue gas fuel supplementing type cold/hot water machine of lithium bromide group is connected with bromine cooling machine fuel inlet tube and bromine cooling machine afterburning chimney.
Industrial furnace smoke utilizing waste heat for refrigeration heating system of the present invention, described smoke valve adopts motor-driven valve, pneumatic operated valve or hand-operated valve.
Industrial furnace smoke utilizing waste heat for refrigeration heating system of the present invention, the air-introduced machine chimney independently arranges, or is incorporated to kiln chimney.
The invention has the beneficial effects as follows:
The present invention by setting up fume afterheat type lithium-bromide absorption-type refrigerating machine, air-introduced machine, smoke valve and flue gas connecting pipe in the exit flue of Industrial Stoves, utilize the waste heat flue gas of Industrial Stoves discharge to drive fume afterheat type lithium-bromide absorption-type refrigerating machine refrigeration (heat) operation, cold (heat) water for air-conditioning or technique is provided, the flue-gas temperature of Industrial Stoves discharge is reduced to below 170 ℃ simultaneously, the fuel heat utilization ratio of Industrial Stoves is greatly improved, and saves a large amount of air-conditionings or technique cooling (heat) energy consumption.
The accompanying drawing explanation
Fig. 1 is the structural representation of industrial furnace smoke utilizing waste heat for refrigeration heating system in the past.
Fig. 2 is industrial furnace smoke utilizing waste heat for refrigeration heating system embodiment of the present invention 1 structural representation.
Fig. 3 is industrial furnace smoke utilizing waste heat for refrigeration heating system embodiment of the present invention 2 structural representations.
Fig. 4 is industrial furnace smoke utilizing waste heat for refrigeration heating system embodiment of the present invention 3 structural representations.
Fig. 5 is industrial furnace smoke utilizing waste heat for refrigeration heating system embodiment of the present invention 4 structural representations.
Reference numeral in figure:
Kiln exit flue 3
Bromine cooling machine smoke-intake pipe 6
Flue gas type cold/hot water machine of lithium bromide group 8
Bromine cooling machine smoke exhaust pipe 9
Air-introduced machine 10
Air-introduced machine chimney 11
Bromine cooling machine cooling water inlet pipe 12
Bromine cooling machine cooling water outlet pipe 13
Bromine cooling machine cold (heat) water inlet pipe 14
Bromine cooling machine cold (heat) water outlet pipe 15
Bromine cooling machine fuel inlet tube 16
Bromine cooling machine afterburning chimney 17
Flue gas fuel supplementing type cold/hot water machine of lithium bromide group 18.
The specific embodiment
The present invention is industrial furnace smoke utilizing waste heat for refrigeration heating system as shown in Figure 2, and this system is the waste heat flue gas inlet tube of flue gas type cold/hot water machine of lithium bromide group by Industrial Stoves 1, pressure fan 5, kiln exit flue 3, flue gas type cold/hot water machine of lithium bromide group 8, air-introduced machine 10, bromine cooling machine smoke-intake pipe 6(), and bromine cooling machine smoke exhaust pipe 9(be the waste heat smoke outlet tube of flue gas type cold/hot water machine of lithium bromide group) form.Wherein, the gas approach end of bromine cooling machine smoke-intake pipe 6 is connected on kiln exit flue 3, is provided with smoke valve 7 on bromine cooling machine smoke-intake pipe 6, and general motor-driven valve or the pneumatic operated valve of adopting of this smoke valve 7, also can adopt hand-operated valve.Air-introduced machine 10 is arranged on bromine cooling machine smoke exhaust pipe 9, and the smoke outlet of air-introduced machine 10 is installed and is connected with air-introduced machine chimney 11.Air-introduced machine chimney 11 both can independently arrange (shown in Fig. 2), also can be incorporated to shown in kiln chimney 4(Fig. 3), to reduce the chimney magnitude setting.In kiln exit flue 3, can arrange shown in air preheater 2(Fig. 4) simultaneously.
In Fig. 2, Fig. 3, Fig. 4 system, when the Industrial Stoves operation, while having surplus heat flue gas, 8 groups of startup operations of flue gas type cold/hot water machine of lithium bromide, smoke valve 7 is opened, air-introduced machine 10 starts operation, the part or all of waste heat flue gas that in the kiln exit flue, temperature is higher is by induced draft blower withdraws, enter flue gas type cold/hot water machine of lithium bromide group 8 through bromine cooling machine smoke-intake pipe 6, drive 8 refrigeration (heat) operations of flue gas type cold/hot water machine of lithium bromide group, cold (heat) water for air-conditioning or technique externally is provided; Go out the waste heat flue gas after flue gas type cold/hot water machine of lithium bromide group 8, temperature reduce, enter atmosphere through bromine cooling machine smoke exhaust pipe 9, air-introduced machine 10 and air-introduced machine chimney 11, thereby realize flue gas type cold/hot water machine of lithium bromide group and Industrial Stoves coordinated operation, utilize fume afterheat refrigeration, heat supply.Into and out of the waste heat flue gas flow of flue gas type cold/hot water machine of lithium bromide group, by the control system of flue gas type cold/hot water machine of lithium bromide group, according to refrigeration (heat) the required heat that adds of loading, by the operation to air-introduced machine, control to regulate control.Residue flue gas in the kiln exit flue, under the effect of kiln chimney self draft power, enter atmosphere through kiln chimney.
When flue gas type cold/hot water machine of lithium bromide group is stopped transport, the air-introduced machine stall, smoke valve is closed, and the waste heat flue gas in the kiln exit flue, under the effect of kiln chimney self draft power, enters atmosphere through kiln chimney, i.e. the Industrial Stoves independent operating that can do as usual.
If the flue gas type cold/hot water machine of lithium bromide group (shown in Fig. 5) replaced in Fig. 2, Fig. 3, Fig. 4 by flue gas fuel supplementing type cold/hot water machine of lithium bromide group 18, when Industrial Stoves exhaust smoke level deficiency or Industrial Stoves stoppage in transit, flue gas fuel supplementing type cold/hot water machine of lithium bromide group 18 can start combustion-compensating device heating operation, to meet refrigeration, heat demand.Flue gas fuel supplementing type cold/hot water machine of lithium bromide group 18 needs to install connection bromine cooling machine fuel inlet tube 16 and bromine cooling machine afterburning chimney 17.
For only needing cooling, do not need the application places of heat supply, available flue gas type or flue gas fuel supplementing type lithium bromide adsorption water chilling unit replace flue gas type or flue gas fuel supplementing type cold/hot water machine of lithium bromide group (figure is slightly).
Claims (6)
1. an industrial furnace smoke utilizing waste heat for refrigeration heating system, this system comprises Industrial Stoves (1), pressure fan (5), kiln exit flue (3) and kiln chimney (4), it is characterized in that: described system has additional fume afterheat type lithium-bromide absorption-type refrigerating machine, air-introduced machine (10), bromine cooling machine smoke-intake pipe (6) and bromine cooling machine smoke exhaust pipe (9), wherein, the gas approach end of bromine cooling machine smoke-intake pipe (6) is connected on kiln exit flue (3), be provided with smoke valve (7) on bromine cooling machine smoke-intake pipe (6), air-introduced machine (10) is arranged on bromine cooling machine smoke exhaust pipe (9), the smoke outlet of air-introduced machine (10) is installed and is connected with air-introduced machine chimney (11).
2. a kind of industrial furnace smoke utilizing waste heat for refrigeration heating system according to claim 1, is characterized in that: air preheater (2) is set in described kiln exit flue (3) simultaneously.
3. a kind of industrial furnace smoke utilizing waste heat for refrigeration heating system according to claim 1 and 2, it is characterized in that: described fume afterheat type lithium-bromide absorption-type refrigerating machine is flue gas type lithium bromide adsorption water chilling unit, flue gas type cold/hot water machine of lithium bromide group (8), flue gas fuel supplementing type lithium bromide adsorption water chilling unit or flue gas fuel supplementing type cold/hot water machine of lithium bromide group (18).
4. a kind of industrial furnace smoke utilizing waste heat for refrigeration heating system according to claim 3, it is characterized in that: described flue gas fuel supplementing type cold/hot water machine of lithium bromide group (18) is connected with bromine cooling machine fuel inlet tube (16) and bromine cooling machine afterburning chimney (17).
5. a kind of industrial furnace smoke utilizing waste heat for refrigeration heating system according to claim 1 and 2, is characterized in that: described smoke valve (7) employing motor-driven valve, pneumatic operated valve or hand-operated valve.
6. a kind of industrial furnace smoke utilizing waste heat for refrigeration heating system according to claim 1 and 2 is characterized in that: air-introduced machine chimney (11) is independent to be arranged, or is incorporated to kiln chimney (4).
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104089429A (en) * | 2014-06-27 | 2014-10-08 | 双良节能系统股份有限公司 | Overlapped air cooling single effect lithium bromide absorption refrigeration machine |
ES2584172A1 (en) * | 2015-03-23 | 2016-09-26 | Universidad De Extremadura | Refrigerator of residual heats (Machine-translation by Google Translate, not legally binding) |
CN106925765A (en) * | 2017-05-02 | 2017-07-07 | 河北工业大学 | Afterheat of casting recycle device based on radiation heat transfer |
CN107891963A (en) * | 2017-10-25 | 2018-04-10 | 上海新奥新能源技术有限公司 | A kind of Ship Waste Heat utilizes system |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4307577A (en) * | 1980-03-12 | 1981-12-29 | Agency Of Industrial Science & Technology | Air conditioning system making use of waste heat |
JP2002349995A (en) * | 2001-05-22 | 2002-12-04 | Ebara Corp | Heating system |
CN201867081U (en) * | 2010-06-23 | 2011-06-15 | 中冶东方工程技术有限公司 | Waste heat utilization system for low-temperature smoke of heating furnace |
CN102425881A (en) * | 2011-11-30 | 2012-04-25 | 金能科技有限责任公司 | Waste heat utilization method and waste heat utilization system of tail gas in production of carbon black |
CN102456897A (en) * | 2010-10-20 | 2012-05-16 | 上海新奥能源科技有限公司 | Combined electricity-heat-cold supply system based on fuel cell |
CN202973140U (en) * | 2011-12-23 | 2013-06-05 | 北京博奇电力科技有限公司 | Efficient flue gas purification and waste heat utilization system |
CN203011002U (en) * | 2012-12-19 | 2013-06-19 | 双良节能系统股份有限公司 | Direct-fired lithium bromide absorption type heating and refrigerating unit with smoke valve and used for recovering smoke waste heat |
CN203132199U (en) * | 2013-03-27 | 2013-08-14 | 北京京诚泽宇能源环保工程技术有限公司 | Continuous heating furnace high temperature flue gas waste heat recovery air conditioning refrigeration system |
CN203501820U (en) * | 2013-09-30 | 2014-03-26 | 双良节能系统股份有限公司 | Industrial-kiln smoke residual-heat refrigerating and heating system |
-
2013
- 2013-09-30 CN CN201310457536.1A patent/CN103486870A/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4307577A (en) * | 1980-03-12 | 1981-12-29 | Agency Of Industrial Science & Technology | Air conditioning system making use of waste heat |
JP2002349995A (en) * | 2001-05-22 | 2002-12-04 | Ebara Corp | Heating system |
CN201867081U (en) * | 2010-06-23 | 2011-06-15 | 中冶东方工程技术有限公司 | Waste heat utilization system for low-temperature smoke of heating furnace |
CN102456897A (en) * | 2010-10-20 | 2012-05-16 | 上海新奥能源科技有限公司 | Combined electricity-heat-cold supply system based on fuel cell |
CN102425881A (en) * | 2011-11-30 | 2012-04-25 | 金能科技有限责任公司 | Waste heat utilization method and waste heat utilization system of tail gas in production of carbon black |
CN202973140U (en) * | 2011-12-23 | 2013-06-05 | 北京博奇电力科技有限公司 | Efficient flue gas purification and waste heat utilization system |
CN203011002U (en) * | 2012-12-19 | 2013-06-19 | 双良节能系统股份有限公司 | Direct-fired lithium bromide absorption type heating and refrigerating unit with smoke valve and used for recovering smoke waste heat |
CN203132199U (en) * | 2013-03-27 | 2013-08-14 | 北京京诚泽宇能源环保工程技术有限公司 | Continuous heating furnace high temperature flue gas waste heat recovery air conditioning refrigeration system |
CN203501820U (en) * | 2013-09-30 | 2014-03-26 | 双良节能系统股份有限公司 | Industrial-kiln smoke residual-heat refrigerating and heating system |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104089429A (en) * | 2014-06-27 | 2014-10-08 | 双良节能系统股份有限公司 | Overlapped air cooling single effect lithium bromide absorption refrigeration machine |
ES2584172A1 (en) * | 2015-03-23 | 2016-09-26 | Universidad De Extremadura | Refrigerator of residual heats (Machine-translation by Google Translate, not legally binding) |
CN106925765A (en) * | 2017-05-02 | 2017-07-07 | 河北工业大学 | Afterheat of casting recycle device based on radiation heat transfer |
CN106925765B (en) * | 2017-05-02 | 2019-06-04 | 河北工业大学 | Afterheat of casting recycle device based on radiation heat transfer |
CN107891963A (en) * | 2017-10-25 | 2018-04-10 | 上海新奥新能源技术有限公司 | A kind of Ship Waste Heat utilizes system |
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Application publication date: 20140101 |