SU800219A1 - Method of agglomeration charge pelletizing control - Google Patents

Method of agglomeration charge pelletizing control Download PDF

Info

Publication number
SU800219A1
SU800219A1 SU782621949A SU2621949A SU800219A1 SU 800219 A1 SU800219 A1 SU 800219A1 SU 782621949 A SU782621949 A SU 782621949A SU 2621949 A SU2621949 A SU 2621949A SU 800219 A1 SU800219 A1 SU 800219A1
Authority
SU
USSR - Soviet Union
Prior art keywords
charge
signal
charge pelletizing
agglomeration charge
input
Prior art date
Application number
SU782621949A
Other languages
Russian (ru)
Inventor
Анатолий Степанович Капусткин
Виктор Валентинович Манион
Виктор Павлович Таран
Original Assignee
Научно-Производственное Объеди-Нение "Тулачермет"
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 Научно-Производственное Объеди-Нение "Тулачермет" filed Critical Научно-Производственное Объеди-Нение "Тулачермет"
Priority to SU782621949A priority Critical patent/SU800219A1/en
Application granted granted Critical
Publication of SU800219A1 publication Critical patent/SU800219A1/en

Links

Landscapes

  • Furnace Details (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

(54) СПОСОБ РЕГУ/ШРОВАНИЯ (ЖСЙМКОВАНИЯ АГЛОНИХТЫ(54) REGUAL / DRIVING METHOD (LIFTING AGLONICHTA

.3S.3S

Поставленна  цель достигаетс  тем, что поддерживают посто нным расход шихты на входе в окомкователь по сухому весу, .а подачу воды на увлажнение регулируют в зависимости от начальной влажности шихты.This goal is achieved by maintaining a constant consumption of the charge at the entrance to the pelletizer on a dry basis, and the water supply to the humidification is adjusted depending on the initial moisture content of the charge.

На чертеже показана блок-схема устройства .The drawing shows a block diagram of the device.

Устройство содержит бункер 1 шихты, датчик 2 влагомера с усилителем-преобразователем 3, источник 4 ионизирующего излучени , конвейер 5, приемник 6 излучени , привод 7 тарельчатого питател , регул тор 8 расхода аглошихты, задатчик 9 расхода агпошихты, вычислитель ный блок 1О, регул тор 11 подачи воды с задатчиком 12, трубопровод 13, барабан-окомковатепь 14, исполнитепьный механизм 15 и датчик 16 грансостава.The device contains a charge hopper 1, a moisture meter sensor 2 with an amplifier converter 3, an ionizing radiation source 4, a conveyor 5, a radiation receiver 6, a disk feeder 7, a charge charge controller 8, an aglow charge setpoint 9, a computing unit 1O, a controller 11 of the water supply with the setting device 12, the pipeline 13, the drum-type stage 14, the operating mechanism 15 and the sensor 16 of the composition.

Устройство работает следующим обра- зом. .The device works as follows. .

Сигнал с выхода усилвтеп  преобразовател  3, пропоравонаиьный начальной влажности швхты, изьлер емой датчиком 2, поступает на вход вычислительногоThe signal from the output of the amplifier converter 3, the propagating initial moisture of the screw removed by sensor 2, is fed to the input of the computational

блока Ю, на второй вход которс го поступает сигнал, пропорцнонага ный мгновениому весу шихты, с приемника 6 излучени . С выхода блока 10 сигнал, пропорввонаньный сухому весу шихты, поступает наunit Yu, to the second input of which a signal, proportional to the instantaneous weight of the charge, is received from the radiation receiver 6. From the output of block 10, the signal, proporvonvany dry weight of the charge enters

вход регул тора 8, на второй вход которого поступает сигнал с задатчвка 9 оптимального расхода шихты. Разность между заданным и текущим значением расхода шихты управлйет приводом 7 тарепьча- того питател  так, чтобы расход шихты по сухому весу оставалс  посто нным. Сигнал с блока 3, пропорциональный на-the input of the regulator 8, to the second input of which receives a signal from the setting point 9 of the optimal charge flow. The difference between the set and the current value of the charge flow is controlled by the drive 7 of the tapped feeder so that the charge flow of the dry weight remains constant. The signal from block 3 is proportional to

194194

чальной влажности, поступает параллельно на вход регул тора 11, на второй вхо которого поступает сигнал с задатчика 12 задающего оптимальную конечную влажность . Сигнал разбаланса с выхода регул тора 11 управл ет исполнительным механизмом 15, измен ющим подачу вс ды на увлажнение.the initial humidity arrives in parallel to the input of the controller 11, the second input of which receives a signal from the setting unit 12 which sets the optimal final humidity. The imbalance signal from the output of the regulator 11 controls the actuator 15, which changes the feed rate for humidification.

Дл  коррекции изменений качества окомковани , вызванных различными технологическими возмущени ми, служит датчик грансостава 16, сигнал с которого корректирует задание конечной влажности через задатчик 12, измен ющий задание при отклонении грансостава от заданных пределов.To correct changes in the quality of pelletizing caused by various technological disturbances, there is a sensor of grain composition 16, the signal from which adjusts the target humidity through setpoint 12, which changes the task when the grain composition deviates from the specified limits.

Использование предлагаемого способа приводит к увеличению выхода годного агломерата.The use of the proposed method leads to an increase in the yield of sinter.

Claims (2)

1.Авторское свшдетельство СССР № 298646, кл. С 22 В 1/16, 1969.1. Authors svdedellstvo USSR № 298646, cl. From 22 to 1/16, 1969. 2.Авторское свидетельство СССР J 441281, кл, С 22 В 1/16, 1972..2. USSR author's certificate J 441281, class, C 22 V 1/16, 1972 ..
SU782621949A 1978-05-30 1978-05-30 Method of agglomeration charge pelletizing control SU800219A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU782621949A SU800219A1 (en) 1978-05-30 1978-05-30 Method of agglomeration charge pelletizing control

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU782621949A SU800219A1 (en) 1978-05-30 1978-05-30 Method of agglomeration charge pelletizing control

Publications (1)

Publication Number Publication Date
SU800219A1 true SU800219A1 (en) 1981-01-30

Family

ID=20767313

Family Applications (1)

Application Number Title Priority Date Filing Date
SU782621949A SU800219A1 (en) 1978-05-30 1978-05-30 Method of agglomeration charge pelletizing control

Country Status (1)

Country Link
SU (1) SU800219A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015092137A1 (en) * 2013-12-17 2015-06-25 Outotec (Finland) Oy Method and equipment for preparing ore concentrate for pelletizing

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015092137A1 (en) * 2013-12-17 2015-06-25 Outotec (Finland) Oy Method and equipment for preparing ore concentrate for pelletizing

Similar Documents

Publication Publication Date Title
SU800219A1 (en) Method of agglomeration charge pelletizing control
US5011088A (en) Control method for a chip refiner
SU1763831A2 (en) Method of automatic control of drying loose material
SU426701A1 (en) METHOD OF MANAGING THE LOADING GRINDER UNIT
SU837414A1 (en) Method of automatic control of drum mill filling by ore
SU814463A1 (en) Apparatus for regulating mill charge with source materials
ZA83648B (en) Method of regulating the air excess in furnances and regulating apparatus for performing the method
SU916925A1 (en) Spray drying process automatic control method
SU928154A1 (en) Drying process automatic control apparatus
SU1266563A1 (en) Method of controlling flotation
SU656660A1 (en) Method of automatic control of loading a mill with ore
SU1121041A1 (en) Device for automatic control of dry magnetic separation process
GB1371110A (en) Device for the regulation of the operational conditions in drying plants particularly for agricultural crops
SU400362A1 (en) AUTOMATIC REGULATION METHOD
SU1142713A1 (en) Method of automatic control of drying process
SU1012987A1 (en) Method of automatic control of ventilated mill
SU710640A1 (en) Method of automatic regulation of the process of disintegrating ore in mill operated jointly with classifier
SU837416A1 (en) Method of automatic control of fine dry grinding process in ball-type mills
SU896599A1 (en) Device for regulating moisture-content of clay rod of single-motor press
SU722534A1 (en) Unit for electroplasmolysis of vegetable raws
SU822895A2 (en) Method of automatic control of jigging machine
SU844967A1 (en) Apparatus for automatic control of process of raw slime feed into rotary furnace
SU666519A1 (en) Device for regulating loose material rate-of-flow
SU494188A1 (en) Crusher capacity control device
SU975086A1 (en) Method of automatic control of grinding process in ball cement mill