CN206409344U - Recuperation of heat TRT - Google Patents

Recuperation of heat TRT Download PDF

Info

Publication number
CN206409344U
CN206409344U CN201720007882.3U CN201720007882U CN206409344U CN 206409344 U CN206409344 U CN 206409344U CN 201720007882 U CN201720007882 U CN 201720007882U CN 206409344 U CN206409344 U CN 206409344U
Authority
CN
China
Prior art keywords
ammonia
generation tank
recuperation
tourie
heat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201720007882.3U
Other languages
Chinese (zh)
Inventor
张杰平
张杰明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201720007882.3U priority Critical patent/CN206409344U/en
Application granted granted Critical
Publication of CN206409344U publication Critical patent/CN206409344U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/10Geothermal energy
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers
    • Y02E10/46Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines

Landscapes

  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

The utility model discloses a kind of recuperation of heat TRT, including ammonia generation tank, gas pipeline, Turbo-generator Set and ammonia tourie, ammonia generation tank is placed at thermal source, the higher ammoniacal liquor of lower storage initial concentration in ammonia generation tank, leave space in top, the space of ammonia generation tank internal upper part is connected by gas pipeline with the air inlet of Turbo-generator Set, the gas outlet of Turbo-generator Set is connected with the space of ammonia tourie internal upper part, lower storage water or the relatively low ammoniacal liquor of initial concentration in ammonia tourie, ammonia tourie is placed at low-temperature receiver, Turbo-generator Set is sequentially connected with by gas outlet and air inlet by the steam turbine generator of more than two and formed, the air inlet of same steam turbine generator and the axial direction of gas outlet are vertical with the same diameter of its steamer, and positioned at the same side of the diameter.The utility model, which solves existing heat-energy utilizing device applicable situation limitation, causes the problem of a large amount of heat energy scatter and disappear in vain, with simple in construction, easy to install and use, the wide advantage of applicable situation.

Description

Recuperation of heat TRT
Technical field
The utility model is related to recuperation of heat TRT.
Background technology
In the Nature and our production, there are heat energy (heat energy of such as sunshine, geothermal energy, the factory's discharge of many thermals source Flue gas, heat energy in cooling waste water etc.) be not fully utilized, these thermals source contain substantial amounts of heat energy, energy utilization Value is very high, but (such as solar water heater is only suitable for utilizing sunshine due to the limitation of existing heat-energy utilizing device applicable situation Heat energy carry out hot-water supply;Existing Industry Waste heat utilization device mostly complicated, cost it is higher and install, it is inconvenient for use, therefore Its application scenario is also extremely limited), these heat energy all scatter and disappear in vain mostly.
Utility model content
Cause the problem of a large amount of heat energy scatter and disappear in vain to solve existing heat-energy utilizing device applicable situation limitation, this practicality is new Type provides a kind of applicable situation wide recuperation of heat TRT.
In order to solve the above technical problems, the technical scheme that is used of the utility model for:
A kind of recuperation of heat TRT, including ammonia generation tank, gas pipeline, Turbo-generator Set and ammonia tourie, Left for storing the higher ammoniacal liquor of initial concentration, top in space, ammonia generation tank bottom in the ammonia generation tank The space in portion is connected by gas pipeline with the air inlet of Turbo-generator Set, and gas outlet and the ammonia of Turbo-generator Set absorb Bottom in the space connection of tank internal upper part, ammonia tourie is used to store water or the relatively low ammoniacal liquor of initial concentration, the steamer Generating set is sequentially connected with by gas outlet and air inlet by the steam turbine generator of more than two and formed, previous steam turbine generator Gas outlet is connected with the air inlet of latter steam turbine generator, the air inlet of same steam turbine generator and the axial direction of gas outlet and its vapour The same diameter of wheel is vertical, and positioned at the same side of the diameter, the ammonia generation tank is placed at thermal source during work, the ammonia Tourie is placed at low-temperature receiver.
To improve the service behaviour of the recuperation of heat TRT, it is preferable that non-liquid storage space is first in work in the device It is in vacuum state during the beginning.
To prevent from sucking water or ammoniacal liquor in steam turbine generator, it is preferable that the water or ammoniacal liquor of storage in the ammonia tourie The volume sum of ammoniacal liquor with being stored in ammonia generation tank is less than the volume in ammonia tourie.
For ease of being vacuumized to the non-liquid storage space in the recuperation of heat TRT, it is preferable that the ammonia generation tank, It is provided with gas pipeline, the steamer accommodating cavity of steam turbine generator or/and ammonia tourie and vacuumizes interface and corresponding valve.
For ease of filling ammoniacal liquor into ammonia generation tank, it is preferable that be provided with that fluid injection is special to be connect on the ammonia generation tank Mouth and corresponding valve.
For ease of filling water or ammoniacal liquor into ammonia tourie, it is preferable that be provided with fluid injection on the ammonia tourie special With interface and corresponding valve.
To realize the self-loopa of ammonia, enable this recuperation of heat TRT autonomous working, it is preferable that in the ammonia tourie Bottom connected by liquid-transport pipe-line with the bottom in ammonia generation tank.
To improve the ammonia luminous efficiency of ammonia generation tank to greatest extent, it is preferable that under in the ammonia generation tank Portion stores the ammoniacal liquor of initial concentration saturation.
To improve the ammonia absorption efficiency of ammonia tourie to greatest extent, it is preferable that under in the ammonia tourie Portion stores water.
To improve the heat absorption efficiency of ammonia generation tank, it is preferable that the outer surface of the ammonia generation tank is provided with heat absorption and applied Layer.
The utility model is highly soluble in water (1 volume water dissolvable, 700 times of volume ammonia under normal temperature and pressure), ammoniacal liquor using ammonia It is heated it is volatile go out ammonia, different temperatures under different solubility of the ammonia in water principle, by the way that initial concentration is higher Ammoniacal liquor is stored in the bottom in ammonia generation tank, and ammonia generation tank is placed at thermal source, so that bottom in ammonia generation tank Ammoniacal liquor can absorb the heat of thermal source and substantial amounts of ammonia is volatilized in the space of ammonia generation tank internal upper part, and then promote vapour The steamer of turbine generator group rotates, generated electricity, when ammonia is flowed into through Turbo-generator Set and is placed in the ammonia tourie at low-temperature receiver, The relatively low ammoniacal liquor of the water or initial concentration of lower storage absorbs rapidly this part ammonia in ammonia tourie, so that turbine generator The air inlet of unit and gas outlet keep pressure difference, and the steamer of such Turbo-generator Set just can continue to rotate, generate electricity.
The utility model is simple in construction, cost is relatively low, easy to install and use, both using the heat energy of sunshine, underground heat It can generate electricity, and the heat energy power-generating in the flue gas of factory's discharge, cooling waste water can be utilized, applicable situation is very wide, solves existing heat The problem of a large amount of heat energy scatter and disappear in vain can be caused using device applicable situation limitation.
Brief description of the drawings
Fig. 1 is the structural representation of the recuperation of heat TRT of the embodiment of the utility model one;
In figure:1st, ammonia generation tank;2nd, gas pipeline;3rd, steam turbine generator;4th, ammonia tourie;5th, liquid-transport pipe-line;6、 Vacuumize interface;7th, fluid injection special purpose interface.
Embodiment
Specific embodiment of the utility model is described further below in conjunction with the accompanying drawings.
As shown in figure 1, the recuperation of heat TRT of the present embodiment includes ammonia generation tank 1, gas pipeline 2, turbine generator Space is left in bottom in unit and ammonia tourie 4, ammonia generation tank 1 for storing the higher ammoniacal liquor of initial concentration, top, The space of the internal upper part of ammonia generation tank 1 is connected by gas pipeline 2 with the air inlet of Turbo-generator Set, Turbo-generator Set Gas outlet is connected with the space of the internal upper part of ammonia tourie 4, the bottom in ammonia tourie 4 be used for store water or initial concentration compared with Low ammoniacal liquor, Turbo-generator Set is sequentially connected with by gas outlet and air inlet by the steam turbine generator 3 of more than two and formed, preceding The gas outlet of one steam turbine generator 3 is connected with the air inlet of latter steam turbine generator 3, the air inlet of same steam turbine generator 3 and The axial direction of gas outlet is vertical with the same diameter of its steamer, and positioned at the same side of the diameter, ammonia generation tank 1 is placed in during work At thermal source, ammonia tourie 4 is placed at low-temperature receiver.
To improve the service behaviour of above-mentioned recuperation of heat TRT, it is preferable that non-liquid storage space is first in work in the device It is in vacuum state during the beginning.
To prevent suction water or ammoniacal liquor in steam turbine generator 3, it is preferable that in ammonia tourie 4 water or ammoniacal liquor of storage with The volume sum of the ammoniacal liquor of storage is less than the volume in ammonia tourie 4 in ammonia generation tank 1.
For ease of being vacuumized to the non-liquid storage space in the recuperation of heat TRT, it is preferable that ammonia generation tank 1 and ammonia It is provided with aspiration closed cans 4 and vacuumizes interface 6 and corresponding valve.
For ease of filling ammoniacal liquor into ammonia generation tank 1, it is preferable that be provided with fluid injection special purpose interface 7 on ammonia generation tank 1 And corresponding valve.
For ease of filling water or ammoniacal liquor to ammonia tourie 4, it is preferable that be provided with fluid injection on the ammonia tourie 4 special With interface 7 and corresponding valve.
To realize the self-loopa of ammonia, enable this recuperation of heat TRT autonomous working, it is preferable that in ammonia tourie 4 Bottom is connected by liquid-transport pipe-line 5 with the bottom in ammonia generation tank 1.
To improve the heat absorption efficiency of ammonia generation tank 1, it is preferable that the outer surface of ammonia generation tank 1 is provided with heat absorbing coating.
Special instruction:In the utility model, described " the higher ammoniacal liquor of initial concentration " is meant:In the ammoniacal liquor of a variety of concentration In the case of optional, as far as possible from the higher ammoniacal liquor of concentration, the preferably ammoniacal liquor of saturated concentration, to improve ammonia hair to greatest extent The ammonia luminous efficiency of raw tank;Described " the relatively low ammoniacal liquor of initial concentration " is meant:In the optional situation of the ammoniacal liquor of a variety of concentration Under, as far as possible from the relatively low ammoniacal liquor of concentration, preferably ammonia density close to water ammoniacal liquor, to improve ammonia tourie to greatest extent Ammonia absorption efficiency.
The utility model using ammonia is soluble in water, ammoniacal liquor is heated it is volatile go out ammonia, different temperatures under ammonia in water Different solubility principle, by the bottom being stored in initial concentration higher ammoniacal liquor in ammonia generation tank, and by ammonia Generation tank is placed at thermal source, so that the ammoniacal liquor of bottom can absorb the heat of thermal source and in ammonia generation tank in ammonia generation tank The space of internal upper part volatilizes substantial amounts of ammonia, and then promotes the steamer of Turbo-generator Set to rotate, generate electricity, in ammonia through steamer When generating set inflow is placed in the ammonia tourie at low-temperature receiver, the water or initial concentration of lower storage are relatively low in ammonia tourie Ammoniacal liquor absorb this part ammonia rapidly so that the air inlet of Turbo-generator Set and gas outlet keep pressure difference, such steamer The steamer of generating set just can continue to rotate, generate electricity.
The utility model is simple in construction, cost is relatively low, easy to install and use, both using the heat energy of sunshine, underground heat It can generate electricity, and the heat energy power-generating in the flue gas of factory's discharge, cooling waste water can be utilized, applicable situation is very wide, solves existing heat The problem of a large amount of heat energy scatter and disappear in vain can be caused using device applicable situation limitation.
Embodiment of the present utility model is explained in detail above in conjunction with accompanying drawing, but the utility model is not limited to Embodiment is stated, in the knowledge that those of ordinary skill in the art possess, the utility model objective can also not departed from On the premise of make obtaining various change, also should be regarded as protection domain of the present utility model.

Claims (10)

1. a kind of recuperation of heat TRT, it is characterised in that:Including ammonia generation tank, gas pipeline, Turbo-generator Set and ammonia Space, ammonia hair are left for storing the higher ammoniacal liquor of initial concentration, top in bottom in aspiration closed cans, the ammonia generation tank The space of raw tank internal upper part connect by gas pipeline with the air inlet of Turbo-generator Set, the gas outlet of Turbo-generator Set and Bottom in the space connection of ammonia tourie internal upper part, ammonia tourie is used to store water or the relatively low ammoniacal liquor of initial concentration, The Turbo-generator Set is sequentially connected with by gas outlet and air inlet by the steam turbine generator of more than two and formed, previous steamer The gas outlet of generator is connected with the air inlet of latter steam turbine generator, the air inlet of same steam turbine generator and the axle of gas outlet To vertical with the same diameter of its steamer, and positioned at the same side of the diameter, the ammonia generation tank is placed at thermal source during work, The ammonia tourie is placed at low-temperature receiver.
2. recuperation of heat TRT according to claim 1, it is characterised in that:Non- liquid storage space is first in work in the device It is in vacuum state during the beginning.
3. recuperation of heat TRT according to claim 1, it is characterised in that:In the ammonia tourie water of storage or The volume sum of ammoniacal liquor and the ammoniacal liquor of storage in ammonia generation tank is less than the volume in ammonia tourie.
4. recuperation of heat TRT according to claim 1, it is characterised in that:The ammonia generation tank, gas pipeline, vapour It is provided with the steamer accommodating cavity or/and ammonia tourie of turbine generator and vacuumizes interface and corresponding valve.
5. recuperation of heat TRT according to claim 1, it is characterised in that:Fluid injection is provided with the ammonia generation tank Special purpose interface and corresponding valve.
6. recuperation of heat TRT according to claim 1, it is characterised in that:Fluid injection is provided with the ammonia tourie Special purpose interface and corresponding valve.
7. recuperation of heat TRT according to claim 1, it is characterised in that:Bottom in the ammonia tourie passes through Liquid-transport pipe-line is connected with the bottom in ammonia generation tank.
8. recuperation of heat TRT according to claim 1, it is characterised in that:Lower storage in the ammonia generation tank The ammoniacal liquor of initial concentration saturation.
9. recuperation of heat TRT according to claim 1, it is characterised in that:Lower storage in the ammonia tourie Water.
10. recuperation of heat TRT according to claim 1, it is characterised in that:The outer surface of the ammonia generation tank is set It is equipped with heat absorbing coating.
CN201720007882.3U 2017-01-04 2017-01-04 Recuperation of heat TRT Expired - Fee Related CN206409344U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720007882.3U CN206409344U (en) 2017-01-04 2017-01-04 Recuperation of heat TRT

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720007882.3U CN206409344U (en) 2017-01-04 2017-01-04 Recuperation of heat TRT

Publications (1)

Publication Number Publication Date
CN206409344U true CN206409344U (en) 2017-08-15

Family

ID=59553919

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720007882.3U Expired - Fee Related CN206409344U (en) 2017-01-04 2017-01-04 Recuperation of heat TRT

Country Status (1)

Country Link
CN (1) CN206409344U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111089039A (en) * 2019-11-07 2020-05-01 吴嘉鹏 Normal-temperature heat energy generator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111089039A (en) * 2019-11-07 2020-05-01 吴嘉鹏 Normal-temperature heat energy generator

Similar Documents

Publication Publication Date Title
CN201650630U (en) Device generating electricity by solar energy and terrestrial heat
CN104913364B (en) A kind of solar energy soil source hot water type absorption heat pump heating system
CN205445916U (en) Super supercritical carbon dioxide brayton cycle power generation system
CN205940249U (en) Enthalpy exchanger is stored up in phase transition and system thereof
CN203857679U (en) Efficient solar air source heat pump all-in-one machine
CN206409344U (en) Recuperation of heat TRT
CN205744023U (en) High-temperature high pressure water accumulation of energy steam generating system
CN206514353U (en) A kind of warm normal-pressure hot-water boiler of cooking a meal of energy-conserving and environment-protective
CN206368723U (en) A kind of electricity generation system of utilization biomass energy
CN206129340U (en) Organic rankine cycle device
CN207262395U (en) Disc type solar energy electricity generation system
CN102721033A (en) Non-metallic energy oil steam generation method and generation device of no-pressure container
CN205783806U (en) A kind of novel air Teat pump boiler
CN206581994U (en) A kind of middle low temperature heat energy combined generating system of utilization two-phase pipe airlift pump
CN204730508U (en) A kind ofly apply the energy-conservation device of lithium bromide
CN206221186U (en) A kind of solar energy quadri-generation system
CN204175508U (en) Alcohol gasification liquefaction electricity generating device
CN203893140U (en) Superconducting solar energy steam generator
CN103542602B (en) Based on solar absorption refrigeration system and the solar energy refrigerator car of engine
CN209523849U (en) A kind of solar energy water turbine generation apparatus
CN208635363U (en) A kind of novel terrestrial hot dry rock heat-exchanger rig
CN206656506U (en) A kind of solar heat absorber
CN206801623U (en) A kind of organic Rankine bottoming cycle Turbo-generator Set cooling system
CN205048760U (en) Vacuum tube section mould massing heat -retaining solar energy boiler
CN109441743A (en) A kind of solar energy water turbine generation apparatus

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170815

Termination date: 20180104

CF01 Termination of patent right due to non-payment of annual fee