CN110207146A - A kind of high-precision Industrial Boiler Temperature-controlled appliance - Google Patents

A kind of high-precision Industrial Boiler Temperature-controlled appliance Download PDF

Info

Publication number
CN110207146A
CN110207146A CN201910488264.9A CN201910488264A CN110207146A CN 110207146 A CN110207146 A CN 110207146A CN 201910488264 A CN201910488264 A CN 201910488264A CN 110207146 A CN110207146 A CN 110207146A
Authority
CN
China
Prior art keywords
shell
admission line
boiler
controlled appliance
flour mill
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.)
Withdrawn
Application number
CN201910488264.9A
Other languages
Chinese (zh)
Inventor
张海苗
赵川
乔如春
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.)
Jiaxing Yingman Trading Co Ltd
Original Assignee
Jiaxing Yingman Trading 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 Jiaxing Yingman Trading Co Ltd filed Critical Jiaxing Yingman Trading Co Ltd
Priority to CN201910488264.9A priority Critical patent/CN110207146A/en
Publication of CN110207146A publication Critical patent/CN110207146A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/02Regulating fuel supply conjointly with air supply
    • F23N1/025Regulating fuel supply conjointly with air supply using electrical or electromechanical means

Abstract

The present invention relates to field of boilers, and disclose a kind of high-precision Industrial Boiler Temperature-controlled appliance, including flour mill, the top of the flour mill is connect with feed hopper, the flour mill is connected to by feed pipe with the shell of cavity structure, driving motor is provided with above the shell, the inside of the shell is equipped with screw rod, the top of the screw rod passes through the top surface of shell and is fixedly connected with the shaft for being located at driving motor lower end, the inside bottom of the shell is equipped with the discharge port of funnel-shaped structure, the bottom end of the shell is connected to admission line, the admission line and be located at shell on the right side of corresponding position be provided with gas flowmeter, the admission line and corresponding position in left side for being located at shell is provided with poweder flowmeter, the left end of the admission line is connected to the inside of boiler.By the supply amount of control coal dust or oxygen, i.e., the amount for the thermal energy that controllable coal dust firing generates, and then realize and the high-precision of boiler temperature is regulated and controled.

Description

A kind of high-precision Industrial Boiler Temperature-controlled appliance
Technical field
The present invention relates to field of boilers, specially a kind of high-precision Industrial Boiler Temperature-controlled appliance.
Background technique
Industrial Boiler includes steam boiler, coal-burning boiler and gas fired-boiler, and current Industrial Boiler is still with coal-fired pot Furnace is in the great majority, and in boiler system, the device for controlling boiler temperature is of crucial importance, such as in the hair of Thermal generation unit In electric process, the coal of burning, which heats water, generates steam, will be so that water quickly generates steaming if the heat that coal combustion generates is excessive Vapour and steam maintain that the higher temperature time is longer, this meeting so that the metallic conduit of guidance steam flowing intensity decline, seriously Can even burn the temperature end of superheater, bring hidden danger to safety in production.
The product that patent document CN108800102A is provided at the steam end of boiler by being arranged for detecting vapor (steam) temperature Device, and estimate temperature by look-ahead device preset algorithm, but the generation of steam is to have at detection device to being moved to Certain distance, it is therefore desirable to a period of time, and it is also to need that the heat that coal combustion generates, which makes water generate the steam of excessive temperature, The time is wanted, therefore is adjusted again after predictive algorithm has estimated temperature, is there are a time difference, this will lead to adjust It is whole not prompt enough, in addition, inhibit vapor (steam) temperature by way of desuperheating water is added into boiler after estimating temperature raising, Although effect can be reached, can also make water temperature drop, in a period of time, water is vaporized into steam conversion ratio can under Drop, and then cause the power generation of generating set to be affected, therefore this cooling method is worthless.
Summary of the invention
In view of the above-mentioned problems, the purpose of the present invention is to provide a kind of high-precision Industrial Boiler Temperature-controlled appliance, solution The device of the control boiler temperature certainly proposed in background technique, it is biggish that temperature adjusts not prompt enough and cooling method defect Problem.
The present invention is to realize that technical purpose adopts the following technical scheme that
A kind of high-precision Industrial Boiler Temperature-controlled appliance, including flour mill, the top of the flour mill and feed hopper Connection, the flour mill are connected to by feed pipe with the shell of cavity structure, are provided with driving motor above the shell, The inside of the shell is equipped with screw rod, and the top of the screw rod passes through the top surface of shell and turns with positioned at driving motor lower end Axis is fixedly connected, and the inside bottom of the shell is equipped with the discharge port of funnel-shaped structure, the bottom end of the shell and admission line Connection, the admission line and the corresponding position being located on the right side of shell are provided with gas flowmeter, the admission line and are located at The corresponding position in the left side of shell is provided with poweder flowmeter, and the left end of the admission line is connected to the inside of boiler, described Part between admission line and boiler is provided with heating tube.
Preferably, the admission line uses heat resistant and wear resistant material.
Preferably, the admission line and boiler outside is provided with air extractor.
Preferably, thermal insulation layer is enclosed on the outside of the heating tube.
The present invention have it is following the utility model has the advantages that
The high-precision Industrial Boiler Temperature-controlled appliance is converted to water by the thermal energy for generating coal dust firing in boiler After the conversion ratio of the interior energy of steam determines, warm of the coal dust before kindling is put into outside furnace and is carried out, warm is avoided to inhale The heat in furnace is received, therefore the thermal energy that coal dust firing generates in furnace is by (extraneous environment is identical, heat in the ratio according to conversion ratio The natural loss of amount is constant) be converted to vapor it is interior can, therefore the raising of steam temperature depend on coal dust full combustion production Raw thermal energy increases, then by the supply amount of control coal dust or oxygen, i.e., the amount for the thermal energy that controllable coal dust firing generates, And then it realizes and the high-precision of boiler temperature is regulated and controled.
Detailed description of the invention
Fig. 1 is the schematic diagram of each device connection relationship of the present invention;
Fig. 2 is the schematic diagram of internal structure of shell in the present invention;
Fig. 3 is one of the connection relationship diagram of admission line in another embodiment;
Fig. 4 is two of the connection relationship diagram of admission line in another embodiment.
In figure: 1, flour mill;2, feed hopper;3, feed pipe;4, shell;5, driving motor;6, screw rod;7, discharge port; 8, admission line;9, gas flowmeter;10, poweder flowmeter;11, heating tube;12, air extractor;13, heat exchanger tube;14, first Escape pipe;15, the second escape pipe;16, third escape pipe;17, control valve.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other Embodiment shall fall within the protection scope of the present invention.
A kind of high-precision Industrial Boiler Temperature-controlled appliance that embodiment according to the present invention provides referring to FIG. 1-2, Including flour mill 1 (brand: sensible, model: 1510, the granularity of finished product can be adjusted arbitrarily within the scope of 100-1250 mesh), milling The top of machine 1 is connect with feed hopper 2, and flour mill 1 is connected to by feed pipe 3 with the shell 4 of cavity structure, the top of shell 4 It is provided with driving motor 5 (brand: three open up, model: GW90W, peak torque 410N/M), the inside of shell 4 is equipped with screw rod 6, The top of screw rod 6 passes through the top surface of shell 4 and is fixedly connected with the shaft for being located at 5 lower end of driving motor, the inside bottom of shell 4 The bottom end of discharge port 7 equipped with funnel-shaped structure, shell 4 is connected to admission line 8, admission line 8 and is located at the right side of shell 4 Corresponding position is provided with gas flowmeter 9, and (title: turbine flowmeter, scale of precision ± 0.5%R carry lithium battery power supply, adopt Transmitted with two-wire system signal, degree of protection IP65), the admission line 8 and corresponding position in left side for being located at shell 4 is provided with powder Flowmeter 10 (brand: Hua Delin, model: HDLDG-06, working principle: measuring principle is to be based on Faraday's electromagnetic induction law, The non-magnetic alloy short tube of the measurement pipe insulation liner material of flowmeter, electrode are fixed on measurement pipe along caliber direction break-through tube wall On, electrode is substantially flush with lining inner surface, magnet exciting coil by both party wave impulse excitation when, will be vertical with measurement pipe axis Direction on the magnetic density that generates be B operating fields.At this point, if fluid flows through measurement pipe.By cutting magnetic line with Electromotive force E is induced, magnetic density B is inversely proportional to, how much magnetic density is just inversely proportional with the powder for flowing through measurement pipe at this time, And it directlys proportional to internal diameter d to the product of mean flow rate v.Electromotive force E (flow signal) detected by electrode and pass through cable send to turn Parallel operation.Converter can show fluid flow, and can export pulse for after flow signal enhanced processing, the signals such as analog current), The left end of admission line 8 is connected to the inside of boiler, and the part between admission line 8 and boiler is provided with heating tube 11.
Wherein, admission line 8 uses heat resistant and wear resistant material.
Wherein, admission line 8 and boiler outside is provided with air extractor 12.
Wherein, the outside of heating tube 11 is enclosed with thermal insulation layer.
Working principle: in general, burning of the coal dust in burner hearth is broadly divided into three phases:
1) preparation stage before catching fire: need to be preheating to the temperature of ignition point before coal powder ignition, this is an endothermic phase;
2) combustion phases: when coal dust temperature reaches ignition point, and coal powder density is suitable, initial burning burning, and it is right Coke directly heats, therefore coke also burns at high temperature, this stage is the very exothermic stage;
3) the after-flame stage: uncombusted a small amount of carbon burns away until after-flame, this stage is also exothermic phase.
It follows that other stages are heat release other than preparation stage of the coal dust before kindling is endothermic phase, and it is single The heat that position coal dust completely burned generates is constant, is carried out if the process for absorbing heat before coal powder ignition is put into outside furnace, It is it is believed that and the heat generated that burns is converted to that so using how many coal dust, completely burned, which generates how many heat, in furnace The conversion ratio of the interior energy of vapor can be determined according to boiler, therefore, in order to avoid ascending to heaven occurs in the temperature of vapor Abnormal conditions, as long as the heat that control coal dust full combustion generates can be realized.Coal cinder is worn into properly by flour mill 1 first The coal dust of partial size, then coal dust is transported to inside shell 4 by feed pipe 3, due to the effect of air extractor 12, so that air inlet It is in negative pressure state at the right end and discharge port 7 of pipeline 8, to avoid coal dust passive type from sucking, causes pulverized coal consumption can not Control, therefore feed is squeezed using screw rod 6, the cavity inside shell 4 is blocked during pressurization, avoids coal dust quilt Dynamic sucking is realized and is actively fed, while gas flowmeter 9 is used to measure the infeed amount of oxygen, avoids oxygen supply is very few from causing Not exclusively, the infeed amount of the further precise measurement coal dust of poweder flowmeter 10 guarantees that the infeed amount of coal dust is in optimal for reaction, when When coal dust reaches 11 position of heating tube, heating tube 11 carries out preceding preheating of catching fire to coal dust, is blown into furnace finally by air extractor 12 It can directly burn when body, the accurate control of vapor (steam) temperature can be realized by the amount of feeding of control coal dust and oxygen.
Referring to Fig. 3, in another embodiment, for saving heat energy, while realizing the cooling to boiler discharge exhaust gas, also It can be arranged with a heat exchanger tube 13 on admission line 8 between poweder flowmeter 10 and air extractor 12, be used from boiler It is connected in the first escape pipe 14 of discharge high-temp waste gas with the left end of heat exchanger tube 13, the right end of the second escape pipe 15 and heat exchanger tube 13 Connection, high-temperature gas transfers heat to during flowing through heat exchanger tube 13 inside admission line 8, for the preheating of coal dust, Realize the recycling of thermal energy.
Referring to Fig. 4, in another embodiment, the utilization rate of the high-temperature gas of boiler discharge can also be further increased, Third escape pipe 16 is provided on first escape pipe 14, third escape pipe 16 is directly connected to admission line 8, and is connected to and is located at powder Between later and decadent stage of a school of thought meter 10 and air extractor 12, control valve 17 is additionally provided on third escape pipe 16, for controlling third escape pipe 16 Circulation so that part high-temperature gas is directly entered inside admission line 8, under conditions of guaranteeing that oxygen supply is sufficient, coal The pre-heat effect of powder is more preferable.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with A variety of variations, modification, replacement can be carried out to these embodiments without departing from the principles and spirit of the present invention by understanding And modification, the scope of the present invention is defined by the appended.

Claims (4)

1. a kind of high-precision Industrial Boiler Temperature-controlled appliance, including flour mill, it is characterised in that: the top of the flour mill It is connect with feed hopper, the flour mill is connected to by feed pipe with the shell of cavity structure, is provided with above the shell Driving motor, the inside of the shell are equipped with screw rod, and the top of the screw rod passes through the top surface of shell and drives electricity with being located at The shaft of machine lower end is fixedly connected, and the inside bottom of the shell is equipped with the discharge port of funnel-shaped structure, the bottom end of the shell Be connected to admission line, the admission line and be located at shell on the right side of corresponding position be provided with gas flowmeter, the air inlet The pipeline and corresponding position in left side for being located at shell is provided with poweder flowmeter, the left end of the admission line and the inside of boiler Connection, the part between the admission line and boiler is provided with heating tube.
2. a kind of high-precision Industrial Boiler Temperature-controlled appliance according to claim 1, it is characterised in that: the air inlet Pipeline uses heat resistant and wear resistant material.
3. a kind of high-precision Industrial Boiler Temperature-controlled appliance according to claim 1, it is characterised in that: the air inlet Pipeline and boiler outside is provided with air extractor.
4. a kind of high-precision Industrial Boiler Temperature-controlled appliance according to claim 1, it is characterised in that: the heating Thermal insulation layer is enclosed on the outside of pipe.
CN201910488264.9A 2019-06-05 2019-06-05 A kind of high-precision Industrial Boiler Temperature-controlled appliance Withdrawn CN110207146A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910488264.9A CN110207146A (en) 2019-06-05 2019-06-05 A kind of high-precision Industrial Boiler Temperature-controlled appliance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910488264.9A CN110207146A (en) 2019-06-05 2019-06-05 A kind of high-precision Industrial Boiler Temperature-controlled appliance

Publications (1)

Publication Number Publication Date
CN110207146A true CN110207146A (en) 2019-09-06

Family

ID=67791164

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910488264.9A Withdrawn CN110207146A (en) 2019-06-05 2019-06-05 A kind of high-precision Industrial Boiler Temperature-controlled appliance

Country Status (1)

Country Link
CN (1) CN110207146A (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2480059Y (en) * 2001-04-13 2002-03-06 任炳志 Positive/negative pressure conveying type low power consumption powder mill
CN201078698Y (en) * 2007-08-24 2008-06-25 邰钦召 Industry furnace coal dust firing system apparatus
CN201443753U (en) * 2009-08-28 2010-04-28 宿长恕 Boiler system for burning coal powder
CN102032590A (en) * 2010-12-31 2011-04-27 北京华电天仁电力控制技术有限公司 Boiler combustion optimizing control system and optimizing control method based on accurate measurement system
CN201823583U (en) * 2010-09-26 2011-05-11 安徽晋煤中能化工股份有限公司 Coal mill dehumidification device
CN103075741A (en) * 2013-01-31 2013-05-01 佛山市沛沣科技有限公司 Negative pressure delivery powder combustion system
JP2014074570A (en) * 2012-10-05 2014-04-24 Nippon Steel & Sumitomo Metal Pulverization plant exhaust gas control device, pulverization plant exhaust gas controlling method and computer program
CN206746693U (en) * 2017-05-16 2017-12-15 湖南洛普节能技术服务有限公司 A kind of coordination control conveying device of coal-grinding machine-made egg-shaped or honey-comb coal briquets amount

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2480059Y (en) * 2001-04-13 2002-03-06 任炳志 Positive/negative pressure conveying type low power consumption powder mill
CN201078698Y (en) * 2007-08-24 2008-06-25 邰钦召 Industry furnace coal dust firing system apparatus
CN201443753U (en) * 2009-08-28 2010-04-28 宿长恕 Boiler system for burning coal powder
CN201823583U (en) * 2010-09-26 2011-05-11 安徽晋煤中能化工股份有限公司 Coal mill dehumidification device
CN102032590A (en) * 2010-12-31 2011-04-27 北京华电天仁电力控制技术有限公司 Boiler combustion optimizing control system and optimizing control method based on accurate measurement system
JP2014074570A (en) * 2012-10-05 2014-04-24 Nippon Steel & Sumitomo Metal Pulverization plant exhaust gas control device, pulverization plant exhaust gas controlling method and computer program
CN103075741A (en) * 2013-01-31 2013-05-01 佛山市沛沣科技有限公司 Negative pressure delivery powder combustion system
CN206746693U (en) * 2017-05-16 2017-12-15 湖南洛普节能技术服务有限公司 A kind of coordination control conveying device of coal-grinding machine-made egg-shaped or honey-comb coal briquets amount

Similar Documents

Publication Publication Date Title
CN202709171U (en) Combustion control system for coal-fired steam boiler
CN208296580U (en) A kind of greasy filth pyrolysis rotary furnace
CN105605609B (en) A kind of power plant boiler burning oxygen amount optimization method
CN102385356A (en) Optimizing control method for sintering waste heat power generation system
CN108679640A (en) The fuel control method that Boiler Metallic accumulation of heat changes during consideration thermal power plant peak regulation
CN105484815B (en) Combustion and steam association system and its progress control method
CN106705034B (en) A kind of supercritical circulating fluidized bed boiler unit quick load change control method
CN1987058B (en) Combustion machine and steam turbine combined circulation system for gas boiler
CN202166034U (en) Vapor generator for heat pipes
CN110207146A (en) A kind of high-precision Industrial Boiler Temperature-controlled appliance
CN203298342U (en) Combustion control system of heat treatment furnace
CN201914929U (en) Chloride process titanium dioxide energy-saving preheater
CN103673650A (en) Steel mill surplus gas and sanitary steam comprehensive utilization system and method
CN203489482U (en) Heat transfer fluid fluidization-and-suspension coal slime combustion boiler
CN107420940B (en) A kind of vertical type square fire door observation door for boiler assembling
CN204324899U (en) Active carbon production equipment process furnace
CN109654736A (en) It is horizontal coal-fired to change gas fired-boiler
CN204665343U (en) The oxygen content control system of coal-burning boiler
CN211502862U (en) Supercritical W flame boiler water wall pipe joint seat device
CN106524141A (en) Quick load change control method of subcritical circulating fluidized bed boiler unit
CN108486303B (en) A kind of technique and device of heating gas-based shaft kiln also Primordial Qi
CN202216415U (en) Moving grate type energy-saving constant temperature automatic control device for furnace
CN207214122U (en) Gas boiler burns furnace control system automatically
CN203615773U (en) Comprehensive recycling system of surplus coal gas and saturated steam of steel plant
CN205824986U (en) A kind of gas fired-boiler

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WW01 Invention patent application withdrawn after publication

Application publication date: 20190906

WW01 Invention patent application withdrawn after publication