CN207161158U - Reduced ilmenite particle coupled thermomechanics co-feeding system - Google Patents

Reduced ilmenite particle coupled thermomechanics co-feeding system Download PDF

Info

Publication number
CN207161158U
CN207161158U CN201721100029.2U CN201721100029U CN207161158U CN 207161158 U CN207161158 U CN 207161158U CN 201721100029 U CN201721100029 U CN 201721100029U CN 207161158 U CN207161158 U CN 207161158U
Authority
CN
China
Prior art keywords
exchanger
heat
solid
temperature
solid 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.)
Active
Application number
CN201721100029.2U
Other languages
Chinese (zh)
Inventor
杨崇岳
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.)
BEIJING HUAHANG SHENGSHI ENERGY TECHNOLOGY Co Ltd
Original Assignee
BEIJING HUAHANG SHENGSHI ENERGY TECHNOLOGY Co Ltd
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 BEIJING HUAHANG SHENGSHI ENERGY TECHNOLOGY Co Ltd filed Critical BEIJING HUAHANG SHENGSHI ENERGY TECHNOLOGY Co Ltd
Priority to CN201721100029.2U priority Critical patent/CN207161158U/en
Application granted granted Critical
Publication of CN207161158U publication Critical patent/CN207161158U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The utility model provides a kind of reduced ilmenite particle coupled thermomechanics co-feeding system, and system includes solid heat-exchanger, evaporator, turbine power generation unit and cooling tower;The high-temp solid charging aperture of solid heat-exchanger is connected by the high-temp solid discharge gate of the 1st valve and rotary kiln;The low-temperature solid discharge gate of solid heat-exchanger is connected by drainage conduit with warehouse for finished product;The high-temperature-hot-water outlet of solid heat-exchanger is connected with the water inlet of evaporator;The high temperature discharge outlet of evaporator and heat supply pipeline one end of heat supply user connect, and after the pressurized pump of the other end of the heat supply pipeline of heat supply user, are connected to the low-temperature water heating import of solid heat-exchanger.Advantage is:The high temperature sensible heat that reduced ilmenite particle can be reclaimed to greatest extent is converted into electric energy, it can be heated again to heat user, original cooler in reduced ilmenite production technology can also directly be substituted, to reduce energy consumption, reduces energy consumption, tool of increasing economic efficiency is of great significance to enterprise.

Description

Reduced ilmenite particle coupled thermomechanics co-feeding system
Technical field
The utility model belongs to cogeneration technology field, and in particular to a kind of reduced ilmenite particle coupled thermomechanics alliance System.
Background technology
China is TiO in the world2One of reserves country the abundantest, but most TiO2Exist in the form of ilmenite. The rotary kiln production technology of reduced ilmenite has the characteristics that yield is high, environmental pollution is small and product quality is stable therefore this Production technology obtains increasing application and promoted.
At present, high from the reduced ilmenite particle temperature of rotary kiln discharge, a large amount of waste heats can not effectively be utilized, caused always Huge energy dissipation.
Utility model content
The defects of existing for prior art, the utility model provide a kind of reduced ilmenite particle coupled thermomechanics alliance system System, can effectively solve the above problems.
The technical solution adopted in the utility model is as follows:
The utility model provides a kind of reduced ilmenite particle coupled thermomechanics co-feeding system, including solid heat-exchanger (6), steaming Send out device (7), turbine power generation unit and cooling tower (15);Wherein, the turbine power generation unit includes turbine (10) and generator (11);
The high-temp solid charging aperture of the solid heat-exchanger (6) passes through the 1st valve (3) and the kiln head cover (1) of rotary kiln (2) High-temp solid discharge gate connection;The low-temperature solid discharge gate of the solid heat-exchanger (6) passes through drainage conduit and warehouse for finished product (20) Connection;There is the solid heat-exchanger (6) low-temperature water heating import and high-temperature-hot-water to export, the high temperature of the solid heat-exchanger (6) Hot water outlet is connected with the water inlet of the evaporator (7);The high temperature discharge outlet of the evaporator (7) and heat supply user (8) Heat supply pipeline one end connects, and after the pressurized pump of the other end (9) of the heat supply pipeline of the heat supply user (8), is connected to described solid The low-temperature water heating import of body heat exchanger (6);It is consequently formed circulation loop;
The superheated steam outlet of the evaporator (7) is connected to turbine (10) by pipeline and done work, and drives generator (11) electric energy is outwards exported;The afterbody exhaust steam of the turbine (10) is condensed into liquid by condenser (12), and passes through working medium pump (13) it is connected to the organic working medium import of the evaporator (7);It is consequently formed circulation loop;
The recirculated water discharge outlet of the cooling tower (15) is connected to following for the condenser (12) by water circulating pump (14) Ring water inlet;The circulating water outlet of the condenser (12) is connected with the circulating water intake of the cooling tower (15);It is consequently formed Circulation loop.
Preferably, the high-temp solid discharge gate of the kiln head cover (1) of rotary kiln (2) also passes through the 2nd valve (4) and cooler (5) import connection;The outlet of the cooler (5) is connected with the warehouse for finished product (20).
Preferably, the exhanst gas outlet of rotary kiln (2) kiln tail also passes sequentially through air cooler (16), sack cleaner (17) After air-introduced machine (18), it is connected with the gas approach of chimney (19).
Preferably, the solid heat-exchanger (6) is in vertical, and the import of the solid heat-exchanger (6) is provided with turriform cloth Glassware, inside are equipped with level monitoring device, the multiple adapters of exit design of the solid heat-exchanger (6);The solid heat-exchanger (6) heating surface uses multichannel membrane wall structure.
Reduced ilmenite particle coupled thermomechanics co-feeding system provided by the utility model has advantages below:
Reduced ilmenite particle coupled thermomechanics co-feeding system can reclaim the high temperature of reduced ilmenite particle to greatest extent Sensible heat is converted into electric energy, can be heated again to heat user, moreover it is possible to directly substitutes original cooler in reduced ilmenite production technology To reduce energy consumption, energy consumption is reduced to enterprise, tool of increasing economic efficiency is of great significance.
Brief description of the drawings
Fig. 1 is the structural representation of reduced ilmenite particle coupled thermomechanics co-feeding system provided by the utility model;
Fig. 2 is the structural representation of solid heat-exchanger provided by the utility model;
Wherein:1. kiln head cover, 2. rotary kilns, 3. the 1st valves, 4. the 2nd valves, 5. coolers, 6. solid heat-exchangers, 7. steam Hair device, 8. heat supply users, 9. force (forcing) pumps, 10. turbines, 11. generators, 12. condensers, 13. working medium pumps, 14. water circulating pumps, 15. cooling tower, 16. air coolers, 17. sack cleaners, 18. air-introduced machines, 19. chimneys;20. warehouse for finished product;
Fig. 2 is the structural representation of solid heat-exchanger provided by the utility model;
21. ilmenite particle import;22. turriform distributing device;23. import feedwater piping;24. export water return pipeline;25. titanium Iron ores particle conveying device.
Embodiment
In order that technical problem, technical scheme and beneficial effect that the utility model solves are more clearly understood, below With reference to drawings and Examples, the utility model is further elaborated.It should be appreciated that specific implementation described herein Example only to explain the utility model, is not used to limit the utility model.
The utility model provides a kind of reduced ilmenite particle coupled thermomechanics co-feeding system, can fully reclaim reduced ilmenite The waste heat of particle, energy consumption is reduced to enterprise, tool of increasing economic efficiency is of great significance.
Specifically, reduced ilmenite particle coupled thermomechanics co-feeding system can reclaim reduced ilmenite particle to greatest extent High temperature sensible heat be converted into electric energy, can be heated again to heat user, moreover it is possible to directly substitute reduced ilmenite production technology in it is original Cooler does not influence the continuous and steady operation of original production process to reduce energy consumption.Belong to cogeneration technology field.
With reference to figure 1, reduced ilmenite particle coupled thermomechanics co-feeding system includes solid heat-exchanger 6, evaporator 7, turbine hair Group of motors and cooling tower 15;Wherein, turbine power generation unit includes turbine 10 and generator 11;
The high-temp solid charging aperture of solid heat-exchanger 6 is arranged by the high-temp solid of the 1st valve 3 and the kiln head cover 1 of rotary kiln 2 Material mouth connects;The low-temperature solid discharge gate of solid heat-exchanger 6 is connected by drainage conduit with warehouse for finished product 20;Solid heat-exchanger 6 has Low-temperature water heating import and high-temperature-hot-water outlet, the high-temperature-hot-water outlet of solid heat-exchanger 6 are connected with the water inlet of evaporator 7;Steam The high temperature discharge outlet of hair device 7 is connected with heat supply pipeline one end of heat supply user 8, the other end warp of the heat supply pipeline of heat supply user 8 After force (forcing) pump 9, the low-temperature water heating import of solid heat-exchanger 6 is connected to;It is consequently formed circulation loop;Wherein, solid heat-exchanger 6 is in Vertical, the import of solid heat-exchanger 6 are provided with turriform distributing device, it is ensured that reduced ilmenite particle is along the circumferential direction uniform It is distributed each heating surface;Inside is equipped with level monitoring device, the multiple adapters of exit design of solid heat-exchanger 6, it is big to take over the elevation angle In 45 °, ensure that uniform blanking, solve the problems, such as solid heat-exchanger internal particle core pulling, improve equipment service efficiency and Life-span.The heating surface of solid heat-exchanger 6 uses multichannel membrane wall structure, and membrane wall outer wall spacing is not less than 100mm;Each film Formula wall is arranged vertically.
The superheated steam outlet of evaporator 7 is connected to turbine 10 by pipeline and done work, and drives generator 11 outwards to export Electric energy;The afterbody exhaust steam of turbine 10 is condensed into liquid by condenser 12, and is connected to the organic of evaporator 7 by working medium pump 13 Working medium import;It is consequently formed circulation loop;
The recirculated water discharge outlet of cooling tower 15 is connected to the circulating water intake of condenser 12 by water circulating pump 14;Condenser 12 circulating water outlet is connected with the circulating water intake of cooling tower 15;It is consequently formed circulation loop.
In addition, the high-temp solid discharge gate of the kiln head cover 1 of rotary kiln 2 is also connected by the import of the 2nd valve 4 and cooler 5 Connect;The outlet of cooler 5 is connected with warehouse for finished product 20.Set this bypass purpose be:When event occurs for the equipment of cogeneration system During barrier, whole system can exit from reduced ilmenite production technology, and the reduced ilmenite particle of rotary kiln discharge directly passes through Warehouse for finished product 20 is discharged into after cooler 5.
After the exhanst gas outlet of the kiln tail of rotary kiln 2 also passes sequentially through air cooler 16, sack cleaner 17 and air-introduced machine 18, with cigarette The gas approach connection of chimney 19, by being purified to the flue gas that rotary kiln is discharged, then is discharged into air, prevents from causing environment Pollution.
The utility model also provides a kind of method based on reduced ilmenite particle coupled thermomechanics co-feeding system, including following Step:
The high temperature reduction ilmenite particle discharged from rotary kiln 2 enters the inside of solid heat-exchanger 6, with being flowed into solid The low-temperature water heating of heat exchanger 6 carries out heat exchange, and temperature is down to after high temperature reduction ilmenite particle is exchanged heat by solid heat-exchanger 6 Less than 150 DEG C, the reduced ilmenite particle after cooling, which enters in warehouse for finished product 20, to be stored;Low-temperature water heating is changed by solid heat-exchanger 6 Heat is absorbed after heat so as to which temperature raises, obtains high-temperature-hot-water;Then, high-temperature-hot-water flows through evaporator 7, heat is transmitted to organic After working medium, high-temperature-hot-water flows into the heat supply pipeline of heat supply user 8, for being heated to user;The pressurized pump 9 of hot water after heating Afterwards, the low-temperature water heating import of solid heat-exchanger 6 is flowed to, is consequently formed circulation loop;Wherein, R245fa can be used as organic work Matter.
And organic working medium enters absorption heat in evaporator 7 under the driving of working medium pump 13, caused superheated steam passes through Pipeline does work into turbine 10, and drives generator 11 outwards to export electric energy;The afterbody exhaust steam of turbine 10 is condensed by condenser 12 Enter evaporator 7 into liquid, and again by working medium pump 13, be consequently formed a closed circuit;
In addition, the recirculated water that cooling tower 15 is discharged enters condenser 12 under the driving of water circulating pump 14 absorbs heat, inhale Receive the recirculated water after heat and return to the releasing heat of cooling tower 15 again, and start new round circulation.
Reduced ilmenite particle coupled thermomechanics co-feeding system provided by the utility model and method have advantages below:
(1) heating surface of solid heat-exchanger uses multichannel membrane wall structure, forms material channel.On the one hand, titanium is reduced Iron ores particle, uniformly through each heating surface, is not easily blocked, not only heat exchange rate is controllable, and considerably increases along gravity direction Effective heat exchange area;On the other hand, because solid heat-exchanger employs multichannel heated face structure, it is suitable for ilmenite reduction mistake Particle temperature caused by Cheng Bodong and changes in flow rate, ensure the stabilization of solid heat-exchanger outlet parameter, improve coupled thermomechanics The security and stability of co-feeding system.
(2) solid heat-exchanger is embedded into reduced ilmenite production system, directly substitutes the cooler in original production process, makes Solid heat-exchanger combines together with reduced ilmenite production system, realizes that reduced ilmenite particle temperature is down to less than 150 DEG C. During the device fails of cogeneration system, whole system can exit from reduced ilmenite production technology, so as to ensure not Disturb the stable operation of original production process.
(3) by reduced ilmenite production technology whole process research, developing and joining suitable for coupled thermomechanics under variable working condition The high reliability DCS control systems of confession, realize the cooperated integration of reduced ilmenite production technology and coupled thermomechanics co-feeding system And optimization, whole system is improved with respect to running rate and reliability.
Described above is only preferred embodiment of the present utility model, it is noted that for the common skill of the art For art personnel, on the premise of the utility model principle is not departed from, some improvements and modifications can also be made, these improve and Retouching should also regard the scope of protection of the utility model.

Claims (4)

1. a kind of reduced ilmenite particle coupled thermomechanics co-feeding system, it is characterised in that including solid heat-exchanger (6), evaporator (7), turbine power generation unit and cooling tower (15);Wherein, the turbine power generation unit includes turbine (10) and generator (11);
The high-temp solid charging aperture of the solid heat-exchanger (6) passes through the 1st valve (3) and the height of the kiln head cover (1) of rotary kiln (2) Warm solids discharge mouth connection;The low-temperature solid discharge gate of the solid heat-exchanger (6) is connected by drainage conduit with warehouse for finished product (20); There is the solid heat-exchanger (6) low-temperature water heating import and high-temperature-hot-water to export, and the high-temperature-hot-water of the solid heat-exchanger (6) goes out Mouth is connected with the water inlet of the evaporator (7);The high temperature discharge outlet of the evaporator (7) and the heating tube of heat supply user (8) Road one end connects, and after the pressurized pump of the other end (9) of the heat supply pipeline of the heat supply user (8), is connected to the solid heat exchange The low-temperature water heating import of device (6);It is consequently formed circulation loop;
The evaporator (7) superheated steam outlet by pipeline is connected to turbine (10) acting, and drive generator (11) to Outer output electric energy;The afterbody exhaust steam of the turbine (10) is condensed into liquid by condenser (12), and by working medium pump (13) even It is connected to the organic working medium import of the evaporator (7);It is consequently formed circulation loop;
The recirculated water discharge outlet of the cooling tower (15) is connected to the recirculated water of the condenser (12) by water circulating pump (14) Import;The circulating water outlet of the condenser (12) is connected with the circulating water intake of the cooling tower (15);It is consequently formed circulation Loop.
2. reduced ilmenite particle coupled thermomechanics co-feeding system according to claim 1, it is characterised in that rotary kiln (2) The high-temp solid discharge gate of kiln head cover (1) be also connected by the 2nd valve (4) with the import of cooler (5);The cooler (5) outlet is connected with the warehouse for finished product (20).
3. reduced ilmenite particle coupled thermomechanics co-feeding system according to claim 1, it is characterised in that the rotary kiln (2) after the exhanst gas outlet of kiln tail also passes sequentially through air cooler (16), sack cleaner (17) and air-introduced machine (18), with chimney (19) Gas approach connection.
4. reduced ilmenite particle coupled thermomechanics co-feeding system according to claim 1, it is characterised in that the solid changes Hot device (6) is in vertical, and the import of the solid heat-exchanger (6) is provided with turriform distributing device, and inside is equipped with level monitoring device, The multiple adapters of exit design of the solid heat-exchanger (6);The heating surface of the solid heat-exchanger (6) uses multichannel membrane wall Structure.
CN201721100029.2U 2017-08-30 2017-08-30 Reduced ilmenite particle coupled thermomechanics co-feeding system Active CN207161158U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721100029.2U CN207161158U (en) 2017-08-30 2017-08-30 Reduced ilmenite particle coupled thermomechanics co-feeding system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721100029.2U CN207161158U (en) 2017-08-30 2017-08-30 Reduced ilmenite particle coupled thermomechanics co-feeding system

Publications (1)

Publication Number Publication Date
CN207161158U true CN207161158U (en) 2018-03-30

Family

ID=61719803

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721100029.2U Active CN207161158U (en) 2017-08-30 2017-08-30 Reduced ilmenite particle coupled thermomechanics co-feeding system

Country Status (1)

Country Link
CN (1) CN207161158U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107401432A (en) * 2017-08-30 2017-11-28 北京华航盛世能源技术有限公司 Reduced ilmenite particle coupled thermomechanics co-feeding system and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107401432A (en) * 2017-08-30 2017-11-28 北京华航盛世能源技术有限公司 Reduced ilmenite particle coupled thermomechanics co-feeding system and method
CN107401432B (en) * 2017-08-30 2023-05-26 北京华航盛世能源技术有限公司 Reduced ilmenite particle thermoelectric coupling co-supply system and method

Similar Documents

Publication Publication Date Title
CN103644743B (en) Combination system for efficiently using waste heat in iron mine sintering cooling process
CN202768090U (en) Recovery system of dead steam waste heat
CN109826685A (en) A kind of supercritical carbon dioxide coal circulation burning electricity generation system and method
CN107905897A (en) Gas turbine cycle flue gas waste heat recovery and inlet gas cooling association system and method
CN207487425U (en) Reduced ilmenite rotary kiln flue gas coupled thermomechanics co-feeding system
CN106870040B (en) A kind of change system for realizing carbon dioxide recycle power generation using cement plant waste heat
CN204267119U (en) Oil field geothermal tail water is utilized to carry out the equipment of dual-circulation screw expansion machine generating
CN103615908B (en) Combined waste heat recycling system for stepping-type flat-burning sintering machine
CN101539036A (en) Device for generating power from flue gas waste heat of aluminum cells on the basis of organic Rankine cycle
CN207161158U (en) Reduced ilmenite particle coupled thermomechanics co-feeding system
CN202869080U (en) Device for recovering low-pressure steam and cooling water waste heat of waste heat power generation system
CN206440032U (en) A kind of recovery Steam Turbine exhaust steam residual heat system based on heat pump
CN209116822U (en) A kind of residual heat of electric power plant and clean energy resource utilization system
CN209876891U (en) Power plant waste heat recovery system
CN107401432A (en) Reduced ilmenite particle coupled thermomechanics co-feeding system and method
CN102003887B (en) Sintering waste heat utilization system
CN204085207U (en) A kind of afterheat generating system being applied to cement production process
CN207945086U (en) A kind of biomass electric power plant air compressor cooling water heat-exchanger rig
CN206655723U (en) A kind of change system that carbon dioxide recycle generating is realized using cement plant waste heat
CN206037000U (en) Back pressure steam turbine moisturizing is heating system in advance
CN206488677U (en) Aluminium cell low temperature exhaust heat recycling system
CN103060498B (en) Blast furnace cinder flushing water residual heat power generation system
CN203704106U (en) Heating heat supply network circulating water heat exchange system
CN203756246U (en) Novel auxiliary machine cooling water system used for indirect air cooling unit
CN206670330U (en) A kind of carbon dioxide energy storage equipment of accumulation radiant heat of rotary kiln

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant