CN106227279A - Steam quality modulating system - Google Patents

Steam quality modulating system Download PDF

Info

Publication number
CN106227279A
CN106227279A CN201610801019.5A CN201610801019A CN106227279A CN 106227279 A CN106227279 A CN 106227279A CN 201610801019 A CN201610801019 A CN 201610801019A CN 106227279 A CN106227279 A CN 106227279A
Authority
CN
China
Prior art keywords
steam
branch road
air collector
quality
drimeter
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.)
Granted
Application number
CN201610801019.5A
Other languages
Chinese (zh)
Other versions
CN106227279B (en
Inventor
张大波
吴玉生
邓国栋
罗靖
秦晓柯
周跃飞
王永庆
古新
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.)
Zhengzhou University
Zhengzhou Tobacco Research Institute of CNTC
Xiamen Tobacco Industry Co Ltd
Original Assignee
Zhengzhou University
Zhengzhou Tobacco Research Institute of CNTC
Xiamen Tobacco Industry 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 Zhengzhou University, Zhengzhou Tobacco Research Institute of CNTC, Xiamen Tobacco Industry Co Ltd filed Critical Zhengzhou University
Priority to CN201610801019.5A priority Critical patent/CN106227279B/en
Publication of CN106227279A publication Critical patent/CN106227279A/en
Application granted granted Critical
Publication of CN106227279B publication Critical patent/CN106227279B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D27/00Simultaneous control of variables covered by two or more of main groups G05D1/00 - G05D25/00
    • G05D27/02Simultaneous control of variables covered by two or more of main groups G05D1/00 - G05D25/00 characterised by the use of electric means
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00Preparing tobacco in the factory
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D22/00Control of humidity
    • G05D22/02Control of humidity characterised by the use of electric means

Landscapes

  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Automation & Control Theory (AREA)
  • Drying Of Gases (AREA)

Abstract

A kind of steam quality modulating system, including steam generator, air collector and be connected between both three branch roads in parallel way, in branch road I, steam generator and air collector are joined directly together as normally open, branch road II is provided with humidifying device, being provided with dehydrating unit in branch road III, the escape pipe of air collector connects with gas utilization unit and is provided with drimeter.Feature of the present invention is, the steam of each branch road converges in air collector, according to the steam quality value of drimeter actual measurement, handoff leg II and branch road III, and by valve regulated steaming amount, can realize dry, the moist steam mixing of different proportion.It addition, the interpolation of signal controller can realize detection automatically and the regulation and control of steam quality.Online for association type pipeline steam drimeter is applied in native system, the on-line real-time measuremen of primary processing line key workshop section quality of steam can be realized.Good steam quality is possible not only to ensure tobacco shred crudy, improves capacity usage ratio, can effectively extend the service life of valve member and equipment.

Description

Steam quality modulating system
Technical field
The present invention relates to steam detection and regulation and control, specifically a kind of steam quality modulating system, utilize this modulating system can Realize on-line checking and the regulation and control of pipeline steam mass dryness fraction on primary processing line.
Background technology
Steam, as a kind of important clean energy resource, is widely used in commercial production and daily life.Tobacco cutting Process is widely used saturated vapor has pole as machining medium, properly functioning, the product quality of apparatus for production line with steam quality Important Relations.Steam quality is the mass percent in every kilogram of wet saturated steam containing dry saturated steam, and saturated vapor dryness is Needed for weighing the important parameter of steam quality, different operations, steam quality is different.At cut tobacco cylinder dry operation, saturated vapor As heating medium, by septate heat transfer heating barrel and hot blast, provide thermal source for tobacco shreds drying dehydration, therefore, if used There is the superheated steam of certain degree of superheat, more satisfied treatment effect can be obtained;In loosening and gaining moisture, leaves moisting, HT moisture regain, charging Etc. operation, saturated vapor injects as PROCESS FOR TREATMENT medium, directly contacts with at goods, provides high humiture moisture regain to process for it Environment, therefore uses saturated vapor to be more suitable for.Water content of steam is unstable, for equipment operating condition, equipment can be caused to imitate Rate can not get effectively playing, controlling the safety problems such as instability, and water hammer;For product quality, process consumption can be brought Increasing, physical quality, aesthetic quality are unsatisfactory for the problems such as technological standards requirement.
Summary of the invention
The purpose of the present invention is just for solving potential safety hazard and the product quality ripple that primary processing line is brought by steam quality Dynamic, start with, by jet chimney configuration optimization, steam dehumidifying and increasing from setting up pipeline steam water capacity efficient easy detection method The design of wet device and comprehensive matching application, propose a kind of steam quality modulating system, steam quality is effectively measured and Accurately control.Good steam quality is possible not only to ensure tobacco shred crudy, improves capacity usage ratio, also can effectively extend valve Part and the service life of equipment
It is an object of the invention to be achieved through the following technical solutions:
A kind of steam quality modulating system, including steam generator, air collector and be connected between both in parallel way Three branch roads, the break-make of three branch roads all by valve realize freely switch;Branch road I passes through with air collector for steam generator Pipeline is joined directly together, and for normally open, is provided with humidifying device and check-valves, is provided with dehydrating unit in branch road III in branch road II And check-valves, the escape pipe of air collector connects with gas utilization unit, and is provided with drimeter on this steam outlet pipe road.This drimeter can be real The existing pressure of wet saturated steam, flow, temperature, density and the associating of mass dryness fraction and real-time online detection.
In the present invention, described humidifying device selects attemperator that steam carries out desuperheat humidification, and described dehydrating unit is selected Steam is dehumidified by steam-water separator.
This system is additionally provided with the signal controller being electrically connected with drimeter, for realizing the detection automatically of steam quality and adjusting Control, is equipped with the regulation valve controlled by signal controller on each branch road.
In particular, the specific works mode of the present invention and process are as follows: include three branch roads altogether, from steaming in branch road I Vapour generator steam out is directly entered air collector;From steam generator steam out first via humidifying device in branch road II Carry out desuperheat humidification, then lead to air collector;Branch road III first removes via dehydrating unit from steam generator steam out Wet, then lead to air collector.Branch road I is normally open, and branch road 2 and branch road 3 freely can be switched by valve, survey according to drimeter Steam quality value, signal controller, by regulation related valve steaming amount, can realize steam humidification, steam dehumidifying, the most on year-on-year basis Example dry and wet steam, it is achieved the detection automatically of steam quality and regulation and control.
The present invention can reach to provide the benefit that:
1, the present invention can freely switch because of branch road 2 and branch road 3, and according to the steam quality value of drimeter actual measurement, control valve leads to Vapour amount, can realize steam humidification, steam dehumidifying, different proportion dry and wet steam, improves steam quality.
2, association type online pipeline steam drimeter, can realize the pressure of wet saturated steam, flow, temperature, density and do The combined measurement of degree, and primary processing line key workshop section pipeline steam quality is carried out on-line real-time measuremen.
3, native system is because with the addition of signal controller, can realize detection automatically and the regulation and control of steam quality.
4, native system is reaching effectively to carry out the metering of saturated vapor, while the Reasonable Regulation And Control steam zone water yield, it is also possible to Realize improving equipment operating efficiency and stability, improve tobacco shred product quality and stability, reduce process consumption of raw materials and the energy The purposes such as consumption.
Accompanying drawing explanation
Fig. 1 is the structure connection diagram of the present invention.
Fig. 2 is that the structure of the present invention connects and control system overall schematic.
Fig. 3 is branch road I and path one schematic diagram of branch road II composition.
Fig. 4 is branch road I and path two schematic diagram of branch road III composition.
In figure: 1 is steam generator, 2 is air collector, and 3 is humidifying device (i.e. attemperator), and 4 is dehydrating unit (i.e. soda pop Separator), 5 is drimeter, and 6 is signal controller.
Detailed description of the invention
Its structure and annexation and control are described further by the present invention below in conjunction with accompanying drawing:
As shown in Figure 1, 2: a kind of steam quality modulating system, including steam generator 1, air collector 2 and be connected to both Between three branch roads in parallel way, the break-make of three branch roads all realizes freely switching by valve;Branch road I is steam generation Device 1 is joined directly together by pipeline with air collector 2, for normally open, is provided with humidifying device 3(i.e. attemperator in branch road II) and only Return valve, branch road III be provided with dehydrating unit 4(i.e. steam-water separator) and check-valves, the escape pipe of air collector and gas utilization unit phase Connect, and on this outlet pipe, be provided with drimeter 5.This drimeter can realize the pressure of wet saturated steam, flow, temperature, density Associating with mass dryness fraction and real-time online detection.This system is additionally provided with the signal controller 6 being electrically connected with drimeter 5, is used for realizing Automatically the detection of steam quality and regulation and control, be equipped with the regulation valve controlled by signal controller on each branch road.
Its duty is described further by the present invention below in conjunction with accompanying drawing:
Embodiment 1:
As it is shown on figure 3, this path is made up of branch road I and branch road II, main purpose is to reduce steam quality, steam generator go out The steam part come carries out desuperheat humidification via attemperator, and another part is directly communicated to air collector and from attemperator steaming out Vapour converges.From air collector steam out, first measure through drimeter, subsequently enter gas utilization unit.
Embodiment 2:
As shown in Figure 4, this path is made up of branch road I and branch road III, and main purpose is to improve steam quality, and steam is partly into Steam-water separator, makes steam quality improve, and converges in air collector with steam generator steam out.From air collector Steam out, first measures through drimeter, subsequently enters gas utilization unit.
By pipeline steam mass dryness fraction regulation and control each equipment of measurement system, pipeline, pipe fitting and valve are selected, establish Detailed pipeline steam mass dryness fraction Modulation Measurement System, as shown in Figure 1.This system is by steam generator, attemperator, steam-water separation Device, air collector, drimeter, signal controller and supporting jet chimney composition.
By technique scheme, the detection of steam quality can be realized and effectively control.When steam is sent to loosening and gaining moisture etc. When steam quality requires low operation, open branch road I and branch road II, close branch road III, pipeline steam is carried out humidification process, from And obtain relatively moist steam.It is sent to the steam quality such as cut tobacco cylinder dry when steam when requiring high operation, opens branch road I and branch road III, close branch road II, pipeline steam is carried out dehumidification treatments, thus obtains relatively dry saturated steam.In a word, branch road I is in normally open, Steam quality value according to drimeter actual measurement compares with mass dryness fraction value needed for gas utilization unit, continuous handoff leg II and branch road III, and By valve regulated steaming amount, it is achieved the mixing of different proportion steam quality.Dry, moist steam is sufficiently mixed slow in gas collecting tank Punching, enters gas utilization unit via steam calorimeter after measuring.The outlet conduit of air collector is provided with drimeter, can measure full With pressure, flow, temperature, density and the mass dryness fraction of steam, the mass dryness fraction after processing, flow, the signal such as temperature is sent to signal control Device processed, by comparing with pre-set mass dryness fraction, flow, temperature signal, sends feedback signal respectively, controls motorized adjustment Valve, regulates each bypass flow size, makes the mass dryness fraction of output steam, flow, and temperature reaches to specify requirement, thus realizes steam quality Automatically detection and regulation and control.Table 1 and table 3 obtain after modulating via branch road I and branch road II for the steam that steam generator produces Data, table 2 is the cooling water parameter that in branch road I, attemperator is passed through.Understanding, after steam is humidified via branch road I, steam quality can drop Low by 10.0% ~ 11.0%;After steam dehumidifies via branch road II, steam quality can promote 15.0% ~ 22.9%.
Table 1 inlet steam
    Flow (kg/s) Temperature (K) Pressure (MPa) Mass dryness fraction x
  1 90 432.01 0.6 1.00
Branch road I 2 90 453.15 0.5 1.00
  3 90 425.00 0.5 0.90
4 100 433.15 0.638 0.70
Branch road II 5 100 423.15 0.491 0.80
  6 100 413.15 0.374 0.75
Table 2 cools down water
  Flow (kg/s) Temperature (K) Pressure (Mpa)
1 10 293.15 0.1
Branch road I 2 10 293.15 0.1
  3 10 293.15 0.1
Table 3 outlet vapor
    Flow (kg/s) Temperature (K) Pressure (MPa) Mass dryness fraction x
1 100 399.15 0.249 0.89
Branch road I 2 100 418.15 0.433 0.90
  3 100 403.15 0.279 0.81
4 81.1 428.15 0.294 0.86
Branch road II 5 87.4 418.15 0.433 0.92
  6 84.25 413.15 0.374 0.89

Claims (4)

1. a steam quality modulating system, it is characterised in that include steam generator, air collector and be connected to both it Between three branch roads in parallel way, the break-make of three branch roads all realizes freely switching by valve;Branch road I is steam generator It is joined directly together by pipeline with air collector, for normally open, branch road II is provided with humidifying device and check-valves, branch road III sets Being equipped with dehydrating unit and check-valves, the escape pipe of air collector connects with gas utilization unit, and is provided with mass dryness fraction on this escape pipe pipeline Meter, this drimeter can realize associating and the real-time online of the pressure of steam, flow, temperature, density and mass dryness fraction in escape pipe pipeline Detection.
Steam quality modulating system the most according to claim 1, it is characterised in that described humidifying device selects attemperator pair Steam carries out desuperheat humidification.
Steam quality modulating system the most according to claim 1, it is characterised in that described dehydrating unit selects steam-water separation Steam is dehumidified by device.
Steam quality modulating system the most according to claim 1, it is characterised in that be additionally provided with in this system and drimeter electricity Signal controller even, for realizing detection automatically and the regulation and control of steam quality, is equipped with by signal controller on each branch road The regulation valve controlled.
CN201610801019.5A 2016-09-05 2016-09-05 Steam quality modulating system Active CN106227279B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610801019.5A CN106227279B (en) 2016-09-05 2016-09-05 Steam quality modulating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610801019.5A CN106227279B (en) 2016-09-05 2016-09-05 Steam quality modulating system

Publications (2)

Publication Number Publication Date
CN106227279A true CN106227279A (en) 2016-12-14
CN106227279B CN106227279B (en) 2018-04-17

Family

ID=58074671

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610801019.5A Active CN106227279B (en) 2016-09-05 2016-09-05 Steam quality modulating system

Country Status (1)

Country Link
CN (1) CN106227279B (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107389747A (en) * 2017-07-04 2017-11-24 东北石油大学 Gas-liquid two-phase dryness measurement system
CN109632354A (en) * 2018-12-03 2019-04-16 中国舰船研究设计中心 U-tube steam generator steam (vapor) outlet external characteristics simulator and analogy method
CN110096083A (en) * 2018-01-31 2019-08-06 中国辐射防护研究院 A kind of temperature and humidity accurate control device
CN110848657A (en) * 2019-11-21 2020-02-28 河南中烟工业有限责任公司 Device and method for controlling moisture content of steam for drying
CN110850836A (en) * 2019-12-11 2020-02-28 中国烟草总公司郑州烟草研究院 Quantitative control method for water content of outlet material of tunnel type heating and humidifying equipment
CN113088400A (en) * 2021-04-13 2021-07-09 康荍生物技术(上海)有限公司 Device for extracting aroma substances from aromatic plants
CN114003067A (en) * 2021-10-25 2022-02-01 河北白沙烟草有限责任公司 Tobacco shred moisture constant control method and system based on environmental humidity influence analysis
CN114082282A (en) * 2021-10-23 2022-02-25 河南中烟工业有限责任公司 Saturated steam dryness online regulation and control system

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009024358A2 (en) * 2007-01-30 2009-02-26 Siemens Aktiengesellschaft Method for operating a gas and steam turbine plant and a gas and steam turbine plant for this purpose
CN202870660U (en) * 2012-10-18 2013-04-10 北京朝阳高科应用技术研究所有限公司 Temperature and humidity automatic control system of diesel oil lubricity testing machine
CN203812121U (en) * 2014-04-02 2014-09-03 中国石油集团长城钻探工程有限公司工程服务公司 Heat source system device adjustable in steam parameters
CN204042442U (en) * 2014-08-18 2014-12-24 山东新华医疗器械股份有限公司 Vapo(u)rous degree automatic control tegulatingdevice
CN206058017U (en) * 2016-09-05 2017-03-29 中国烟草总公司郑州烟草研究院 Steam quality modulating device

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009024358A2 (en) * 2007-01-30 2009-02-26 Siemens Aktiengesellschaft Method for operating a gas and steam turbine plant and a gas and steam turbine plant for this purpose
CN202870660U (en) * 2012-10-18 2013-04-10 北京朝阳高科应用技术研究所有限公司 Temperature and humidity automatic control system of diesel oil lubricity testing machine
CN203812121U (en) * 2014-04-02 2014-09-03 中国石油集团长城钻探工程有限公司工程服务公司 Heat source system device adjustable in steam parameters
CN204042442U (en) * 2014-08-18 2014-12-24 山东新华医疗器械股份有限公司 Vapo(u)rous degree automatic control tegulatingdevice
CN206058017U (en) * 2016-09-05 2017-03-29 中国烟草总公司郑州烟草研究院 Steam quality modulating device

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107389747A (en) * 2017-07-04 2017-11-24 东北石油大学 Gas-liquid two-phase dryness measurement system
CN107389747B (en) * 2017-07-04 2020-12-29 东北石油大学 Gas-liquid two-phase dryness measuring system
CN110096083A (en) * 2018-01-31 2019-08-06 中国辐射防护研究院 A kind of temperature and humidity accurate control device
CN109632354A (en) * 2018-12-03 2019-04-16 中国舰船研究设计中心 U-tube steam generator steam (vapor) outlet external characteristics simulator and analogy method
CN109632354B (en) * 2018-12-03 2020-12-29 中国舰船研究设计中心 Device and method for simulating external characteristics of steam outlet of U-shaped pipe steam generator
CN110848657A (en) * 2019-11-21 2020-02-28 河南中烟工业有限责任公司 Device and method for controlling moisture content of steam for drying
CN110848657B (en) * 2019-11-21 2021-04-16 河南中烟工业有限责任公司 Device and method for controlling moisture content of steam for drying
CN110850836A (en) * 2019-12-11 2020-02-28 中国烟草总公司郑州烟草研究院 Quantitative control method for water content of outlet material of tunnel type heating and humidifying equipment
CN113088400A (en) * 2021-04-13 2021-07-09 康荍生物技术(上海)有限公司 Device for extracting aroma substances from aromatic plants
CN114082282A (en) * 2021-10-23 2022-02-25 河南中烟工业有限责任公司 Saturated steam dryness online regulation and control system
CN114003067A (en) * 2021-10-25 2022-02-01 河北白沙烟草有限责任公司 Tobacco shred moisture constant control method and system based on environmental humidity influence analysis
CN114003067B (en) * 2021-10-25 2022-06-10 河北白沙烟草有限责任公司 Tobacco shred moisture constant control method and system based on environmental humidity influence analysis

Also Published As

Publication number Publication date
CN106227279B (en) 2018-04-17

Similar Documents

Publication Publication Date Title
CN106227279A (en) Steam quality modulating system
CN105605910B (en) A kind of operational mode and structure of recycle heat formula heat pump drying device
CN102292459B (en) Method for producing pulverized coal
CN111947952B (en) Fuel cell humidifier test system and test method
CN206058017U (en) Steam quality modulating device
CN203687533U (en) Tea dryer
CN110044145A (en) A kind of high voltage electric field and heat pump united drying system
CN203812121U (en) Heat source system device adjustable in steam parameters
CN102132950A (en) Process method for utilizing waste heat in tobacco shred airflow drying and special flow heating device
CN204041130U (en) The brown coal drying power generation system of Water Sproading in a kind of coal
CN114046449B (en) Steam compression system with inlet steam parameter control function
CN208860029U (en) A kind of heat pump enclosed dehumidification system with volume adjusting apparatus
CN201238593Y (en) Low-temperature tobacco oven heated by hot-water system
CN201131298Y (en) A humidifying device for a tobacco dryer
CN209763716U (en) Energy-saving drying system
CN201399906Y (en) Packing base material curing device
CN103948159B (en) Tobacco drying drum liquid phase heating circulation system
CN110850836A (en) Quantitative control method for water content of outlet material of tunnel type heating and humidifying equipment
CN103940208B (en) Plasterboard industrial exhaust heat drying system
CN114376254B (en) Device and method for measuring air moisture content in tobacco conditioning cylinder and conditioning cylinder
CN203494184U (en) High-speed centrifugal spraying drier
CN208526233U (en) A kind of generator hydrogen drying system for hydrogen that can be automatically controled
CN111248477A (en) Novel steam drying device
CN220987624U (en) Quantitative control system for water content of outlet material of heating and humidifying equipment
CN106958495B (en) Method for generating power by using low-concentration gas of coal mine

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant