SU518232A1 - The method of regulating the flotation process - Google Patents

The method of regulating the flotation process

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Publication number
SU518232A1
SU518232A1 SU1992520A SU1992520A SU518232A1 SU 518232 A1 SU518232 A1 SU 518232A1 SU 1992520 A SU1992520 A SU 1992520A SU 1992520 A SU1992520 A SU 1992520A SU 518232 A1 SU518232 A1 SU 518232A1
Authority
SU
USSR - Soviet Union
Prior art keywords
foam
flotation process
regulating
density
mineralization
Prior art date
Application number
SU1992520A
Other languages
Russian (ru)
Inventor
Вячеслав Борисович Канунников
Юрий Петрович Уваров
Original Assignee
Предприятие П/Я В-2413
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 Предприятие П/Я В-2413 filed Critical Предприятие П/Я В-2413
Priority to SU1992520A priority Critical patent/SU518232A1/en
Application granted granted Critical
Publication of SU518232A1 publication Critical patent/SU518232A1/en

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Description

(54) СПОСОБ РЕГУЛИРОВАНИЯ ПРОЦЕССА ФЛОТАЦИИ(54) METHOD OF REGULATING THE FLOTATION PROCESS

33

iiocTH двухфазной пены, высоте перелива ми горалноованной пены косвенно поддерживают горч зонтальную скорость движени  пенного нродукта и врем  флотации, В таком режиме работы флотомашины минерализгнш  пены зависит от качества обработки флотируемых минералов реагентом-коллектором в кондиционере 1 и имеет экстремальный характер. Эта зависимость положена Б основу действи  экстремального регул тора.iiocTH biphasic foam, the height of the overflow of the foam foam indirectly supports the bitter speed of the foamy product and the flotation time. In this mode of operation, the mineralization foam machine depends on the quality of the processing of the floated minerals by the collector agent in the air conditioner 1 and has an extreme character. This dependence is based on the basis of the action of the extreme regulator.

Минерализацию цены измен ют блоком 17 разности ппотноетей, к которому подключен датчик 14 плотности двухфазной пены и весовой датчик 18 плотности трехфазной пены, установленный на сливе пенного продукта. Выходные сигналы с этого блока поступают на экстремальный регул тор 19, воздействующий на питатель 20 реагента-коллектора. Экстремальный регу9 5 9Price mineralization is changed by unit 17 of the difference in the flow of power to which the two-phase foam density sensor 14 and the three-phase foam density weight sensor 18, mounted on the discharge of the foam product, are connected. The output signals from this block are fed to an extreme regulator 19, acting on the feeder 20 of the collector reagent. Extreme regulation9 5 9

л тор обеспечивает поиск и поддержание максимума минерализации пены в услови х действи  неконтролируемых или трудноучитываемых параметров исходной пульпы, к которым относитс  количество и крупность флотируемьрс мР1нералов, наличие шламов или же других возмущающих факторов.The torus ensures the search for and maintenance of the maximum mineralization of the foam under the conditions of uncontrolled or difficult-to-read parameters of the initial pulp, which include the number and size of the pulp, the presence of sludge or other disturbing factors.

Claims (1)

Формула изобретени Invention Formula Способ регулировани  процесса флотации путем дозировки реагента пенообразовател  по плотности двухфазной пены, о тл и ч а ю щ и и с   тем, что, с целью стабилизации максимального значени  минерализации пены, дополнительно измер ют плотность трехфазной пенЫ; и в зависимости от разности значений измеренных плотностей измен ют подачу реагента коллектора .The method of controlling the flotation process by dosing the foaming agent reagent according to the density of the two-phase foam, about 10 and so on, so that, in order to stabilize the maximum value of the foam mineralization, the density of the three-phase foam is additionally measured; and depending on the difference in the values of the measured densities change the flow of the collector reagent. nn JOJO lo flo f о о о о t с оо oh oh oh t with oo -is о t о о о о о-is о t о о о о о о : ° nn „ ° о о о о °, «о ° с, о о о "° o o o o o °," o ° s, o o o o «о °оооо"O ° oooh о ° о о о (,0 о ° о о о (, 0 р ° ° о о о р ° ° о о о о о.about oh. о о oh oh о о е оabout o e o О о О f ОO o o f f o „ ° о о Р . о «„° о о Р. about " о « о о о с о о оo "oh oh oh oh oh I II I сГ SG II
SU1992520A 1974-02-01 1974-02-01 The method of regulating the flotation process SU518232A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU1992520A SU518232A1 (en) 1974-02-01 1974-02-01 The method of regulating the flotation process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU1992520A SU518232A1 (en) 1974-02-01 1974-02-01 The method of regulating the flotation process

Publications (1)

Publication Number Publication Date
SU518232A1 true SU518232A1 (en) 1976-06-25

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Family Applications (1)

Application Number Title Priority Date Filing Date
SU1992520A SU518232A1 (en) 1974-02-01 1974-02-01 The method of regulating the flotation process

Country Status (1)

Country Link
SU (1) SU518232A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4552651A (en) * 1983-11-14 1985-11-12 Conoco Inc. Control of froth cell performance through the use of differential bubbler tubes
US4559134A (en) * 1984-11-30 1985-12-17 Conoco Inc. Control of froth flotation separation
US5062964A (en) * 1989-04-07 1991-11-05 J. M. Voith Gmbh Process for control of a flotation system
DE4113861A1 (en) * 1991-04-27 1992-10-29 Gat Handelsgesellschaft Fuer I Device for cleaning waste layer from printing operations - consists of storage vessel linked to reaction vessel by transfer pump with level switches in reaction vessel control agitator, filling, emptying and reagent dosing

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4552651A (en) * 1983-11-14 1985-11-12 Conoco Inc. Control of froth cell performance through the use of differential bubbler tubes
US4559134A (en) * 1984-11-30 1985-12-17 Conoco Inc. Control of froth flotation separation
US5062964A (en) * 1989-04-07 1991-11-05 J. M. Voith Gmbh Process for control of a flotation system
DE4113861A1 (en) * 1991-04-27 1992-10-29 Gat Handelsgesellschaft Fuer I Device for cleaning waste layer from printing operations - consists of storage vessel linked to reaction vessel by transfer pump with level switches in reaction vessel control agitator, filling, emptying and reagent dosing

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